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Reactor Containment Bldg Integrated Leak Rate Test.
	ML17321A182
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Site:	Cook
Issue date:	06/30/1984
From:	; INDIANA MICHIGAN POWER CO. (FORMERLY INDIANA & MICHIG
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REACTOR CONTAINMENT BUILDING INTEGRATED LEAK RATE TEST DONALD C. COOK PLANT UNIT NO. 2 INDIANA AND MICHIGAN ELECTRIC COMPANY 1984 84i0290032, 84i0i9 PDR ADOCK 05000316.

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D. C. COOK PLANT - UNIT TWO CONTAINMENT INTEGRATED LEAK RATE TEST JULY. l984 TABLE OF CONTENTS Section Title

1.0 INTRODUCTION

2.0 LEAKAGE RATE, MEASUREMENT SYSTEM 3.0 TEST CHRONOLOGY 3.1. Introduction 3.2 Pressurization 4a5 3.3 Stabilization 6@7 3.4. Type- A Test, Sa9 3.5 Supplemental 10 3.6 Depressurization 4.0 ANALYSIS AND INTERPRETATION OF TEST RESULTS 4.1 Penalty Leakages 4.1.1 As-Left. Undrained System 12 Leakage Penalty 4.1.2 Repaired Valves Leakage Penalty 4.2 Sump Level Changes 14 4.3 Conclusion 15

Appendix A ILR Program Zisting Appendix B ILR Program Verification Appendix C Undrained System Penalty Leakage Calculation Appendix D Repaired Valves Penalty Leakage Calculation Appendix E Summary of 1984 Types, A, B, and C Leakages Appendix F Supplemental Test Flow Correction Appendix G Summary of Types B and C Testing Appendix H Sump Level Change Calculation Figure I Test Instrumentation Figure II Instrumentation Schematic Figure III Containment Structure and RTD Location Figure IV Personnel Schematic Figure V Containment Airlock Door Sealing Mechanism Figure VI Supplemental Test Instrumentation Installation Figure VII Tabulation of Test Results

1.0 Introduction The third periodic containment Integrated Leak Rate Test (ILRT) for the Donald C. Cook Nuclear Plant Unit 2 reactor containment was successfully completed on July 30, 1984.

The ILRT was performed as specified in surveillance test procedure ~*12 THP 4030 STP.202, Rev. 4 in accordance with the requirements of American National Standard ANSI N45.4-1972, the Code of Federal Regulations 10 CFR 50 Appendix J, the plant PSAR, and Technical Specification 4.6.1.2.

The absolute method of testing was employed on the three compartment containment model developed for both the Unit One and Unit Two Preoperational Integrated Leak Rate Tests.

Data was collected at half hour intervals and was used to calculate the normalized weight of the initial dry air mass remaining in the containment at each half hour interval. The measured Type A leak rate, Lam, is the slope of a straight line determined for a linear least-squares the calculated normalized weight vs. time.

fit of Temperature measurements were taken at 46 locations inside the containment building, pressure and humidity readings at three locations. Leakage was measured at 12.4 psig (design basis accident pressure being 12 psig, +0.5, -0.0 psig ).

A measured induced leak was used to verify the test results.

Interpretation and final analysis of the test data show results well within the specified limits for this containment, which has a maximum allowable leak rate (La) of 0.75 La or 0.1875 weight percent, of the containment atmosphere per day of design basis accident pressure.

4 PAGE 1

2.0 Leaka e Rate Measurement S stem Measurement of overall containment pressure and leak rate was accomplished using the test instrumentation listed in Figure I, in conjunction with the ILR computer program for averaging and weighting of data, correction to standard conditions, and statistical calculation of the leak rate. A copy of the ILR program listing is found in Appendix A, and verification of program accuracy is contained in Appendix B. Changes were made.to ILR software to permit.

terminal interface. The body of the program, containing the leak rate calculation, was not changed.

The measurement instrumentation used was arranged such that humidity and temperature transducers were located inside the containment building, with external recording capability of the transducer output.

Pressure measuring equipment was located outside the containment building, utilizing permanently installed pressure sensing lines open to containment atmosphere.

Redundant instrumentation was used, to allow failure of one channel while still providing data aquisition capability. With the redundant instrumentation use, an average of the two values obtained was used for calculations performed by the ILR Program.

Recording of humidity and temperatue data was performed automatically by the programmed data logging system referenced in Figure I. Pressure measurements were obtained via direct reading of quartz manometers test personnel, at the direction of the Official by Test Timekeeper. Data was then compiled and transferred to data processing personnel, who entered the data into the ILR program and verified data entry accuracy.

For the duration of the test period, the reactor coolant system was at half loop operation, iwith constant level maintained by Operations Personnel.

A schematic arrangement of the leakage rate instrumentation system is shown in Figure II, with a detailed arrangement of the containment structure and temperature measurement system shown in Figure III. A schematic arrangement of the test personnel is contained in Figure IV.

PAGE 2

.0 TEST ORGANIZATION

3.1 INTRODUCTION

Performance of the containment Integrated Leak Rate Test was broken into five distinct segments, beginning with the pressurization period, 'followed by the required stablization period, the Type A test, the supplemental test, and the de-pressurization period. Each segment was documented with respect to date, time, and acceptance criteria. Test data was plotted throughout the duration of the test in order to disclose any gross variation that could indicate equipment failure.

Prior to the beginning of the pressurization period, an inspection of the containment structure was conducted to uncover any visible evidence of structural deterioration.

None was evident. Valve line-ups were completed per procedure specification to isolate the containment structure, and pressurization began at 1300 hours0.015 days 0.361 hours 0.00215 weeks 4.9465e-4 months on June 12, 1984.

Several items were not able to be removed from the containment building, but were determined to be of insignificant volume to affect the test. A list of these items follows:

guuanti~ r Item Size (4) Miller welders 3'. z 22.5>> z 23>>

Hydrolasing Equipment 3 tanks and piping Wood box on steam generator- 17>> x 8' doghouse 4'ood boz on steam generator 4'2>> x 6' 20>>

doghouse Steel boz on steam generator 44>> z 44>> X 14" doghouse Green steel box 18>> x 32>> x 14 Various cables and lifting Equipment An error analysis was performed at the end of each test period, when all data for that period was available to calculate the mazimium error.

3.2 PRESSURIZATION At 1200 hours0.0139 days 0.333 hours 0.00198 weeks 4.566e-4 months on June 12, 1984, the Unit 2 reactor containment building was cleared of all personnel, sump level measurements were taken, the lights were extinguished, and the access doors locked. At 1205 hours0.0139 days 0.335 hours 0.00199 weeks 4.585025e-4 months , the pressurization air dryer was placed in service and the control valve to containment was opened at 1255 hours0.0145 days 0.349 hours 0.00208 weeks 4.775275e-4 months to begin pressurization . Data aquisition for the pressurization period began with Run Ol at 1300 hours0.015 days 0.361 hours 0.00215 weeks 4.9465e-4 months .

Two containment lower ventilation units were placed in service without cooling water flow to aid in 'air mixing inside containment. These units were run throughout the .

durati'on of the test, rotating two of the eight fans back into service as they tripped out on thermal overload due to high air density.

After one hour of pressurization, an ice condenser pressure sensing device was removed from service due to inconsistent readings. It was replaced by a quartz manometer formerly used to measure atmospheric pressure, and a mercury manometer was substituted for atmospheric pressure measurement.

Suspected leaks on the ice condenser air handler units

, drain line and the containment. ventilation drain line, both at CPN-31, were investigated during pressurization. Airflow could not be verified on the vented side of the isolation valves on either line, and no maintenance or adjustments were made.

At 0933 hours0.0108 days 0.259 hours 0.00154 weeks 3.550065e-4 months on June 13, 1984, the control air dryer was taken out of service and the isolation valve to containment was closed. Containment was entered at approximately 1045 hours0.0121 days 0.29 hours 0.00173 weeks 3.976225e-4 months to clean hygrometers and to adjust sampling flowrates which were elevated due to high pressure. On exit from containment, personnel remarked that the airlock had been pressurized on entry.

Investigation revealed that o-rings on the inner door had dislodged from the equalizing valve on door operation due to the high air velocity and subsequent lowered static pressures near the o-rings during the pressure equalization phase of door operation.

PAGr 4

Upon investigation of the door sealing mechanism (see attached Figure V), two members were found bent (¹1 and

¹2), and a broken pin was replaced (¹3). An attempt to straighten the bent member using the bolt adjustment (¹4) failed, and the bolt was broken in the process. Because the lower airlock door could not, be used, the entire sealing assembly was removed through upper containment.

Subsequent dislodging of the upper airlock o-rings due to containment exit necessitated replacement of the o-rings on that airlock also.

Measurement of the inner door leakage prior to repairs was not necessary, as leakage out of containment is determined by outer door leakage. A Type B test performed on the outer door just prior to the Type A test verified that there was no leakage through its seals.

Entry and exit of the containment structure necessitated re-pressurization, which commenced at 1450 hours0.0168 days 0.403 hours 0.0024 weeks 5.51725e-4 months on June 14, 1984. At 1835 hours0.0212 days 0.51 hours 0.00303 weeks 6.982175e-4 months on June 14, 1984, pressurization was stopped. An average containment pressure of 12.415 was recorded at 1900 hours0.022 days 0.528 hours 0.00314 weeks 7.2295e-4 months .

PAGE 5

3.3 STABILIZATION At 1900 hours0.022 days 0.528 hours 0.00314 weeks 7.2295e-4 months on June 14, 1984, the required stabilization period was begun. At 0000 hrs. on June 15, 1984, the stabilization period was complete. Acceptance criteria to verify stability are as follows:

1) . Stabilization period has exceeded the maximum of four hours.

2) Containment pressure has been maintained at a pressure of 12.0 ( +0.5, -0.0 ) psig for a minimum of the last two consecutive hours of the stabilization period.

3) The weighted average temperature in the upper, lower, and ice condenser compartments has not varied more than O.l'F/hr. over the last four hour period of the stabilization.

4) No single upper, lower, or ice condenser containment temperature reading has changed more than 0.5'F during the last hour of the stabilization period.

Due to the cyclic defrost operation of the ice condenser air handling units, however, and the higher than normal heat "

load in the ice condenser compartment while under pressure, temperature criteria as they apply to the ice condenser may not be met. In this case, and only after all other stabilization criteria are met,, it is specified by procedure that the specifications of criteria 3) and 4) may be waived as they apply to the ice condenser. This was done for the 1984 test.

All other criteria for stabilization was met as tabulated on the following page.

PAGE 6

STABILIZATION CRITERIA Time Containment Pressure hours Run Numbers Pressure si 2200-2300 6-8 12.4049 2300-2400 8-10 12.4098 Criteria: Avg. Cont. Pressure = 12.0 (+0.5, -0.0)

'psig for last two consecutive hours of stabilization Run Wei hted Avera e hT Time Numbers hT U er bT Tower bT Ice 2000-2100 2-4 -0.0516 +0.0258 +0.1521 2100-2200 4-6 -0.0514 +0.0629 +0.1983 2200-2300 6-8 -0.0310 +0.0285 +0.0018 2300-2400 8-10 -0.0637 +0.0281 +0.2237 Criteria: Weighted average temperature of each compartment has not varied more than 0.1'F over the, last four hour period of the stabilization period.*

Hi hest indicated bT - Runs 8-10 2300-2400 hrs.

hT U er hT Iower hT Ice ETRE 108 135 118 0.20 -0.14 -1.94 Criteria: No single upper, lower, or ice condenser containment temperature reading has changed more than 0.5'F during the last hour.*

Ice condenser criteria waived per **12 THP 4030 STP.202.

PAGE 7

3.4 TYPE A TEST The Type A test of the Unit 2 reactor containment building commenced on June 15, 1984 at 0000 hours0 days 0 hours 0 weeks 0 months . During the conduct of the Type A test, dewpoint hygrometers went into normal defrost, cycles as listed below. The defrost cycle is necessary for proper functioning of the hygrometers, but as no output is available at that time, hygrometer data was deleted for the following:

Data Runs Lower Containment> 9 through 12 38 through 60 Upper Containment>

Upper Containment2 10 through 32 51 through 60 Because both humidity detectors in upper containment were in the defrost mode, all data for run 554 was not used in the ILR Program.

At 1055 on June 15, 1984, test personnel were contacted to investigate a "lower airlock door unlatched" annunciator that was discovered during an Operations tour. Concerned that an airlock door leak may be present if a door was not fully closed, a local leak test was conducted on the outer door seal and indicated that there was no leakage. It was also verified that the inner door seal was not leaking, due to absence of pressure inside the airlock, as indicated on an existing pressure gage. As there was no exhibited leakage through the airlock, the Type A test was not affected and limit switch adjustments were made following test completion.

Total elapsed time of the type A test was 29.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months , fulfillingthe requirement that the test exceed 24 hours2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months .

The measured overall containment leak rate was determined to be -0.03404 wt. %/day (-0.1362 La) for the containment structure as left following repairs to containment isolation valves during the preceding surveillance period.

PAGE 8

Containment leak rates amended for the as found condition of containment follow in Section 4.0.

Acceptance criteria for the Type A test stipulates that the leak rate as determined by the linear regression 95%

upper confidence limit has converged to a value below the acceptance criteria for the actual measured leakage. At type A test completion, the 95% upper containment leak rate was determined to be -0.03874 wt %/day, or -0.155 La, which meets the acceptance criteria of > -0.75 La.

PAGE '9

0 3.5 SUPPLENENTAL TEST In order to verify the validity of Type A leak test data, a measured leak was induced in the containment structure, and measurement parameters used to quantify the containment overall leakage as determined in the Type A test were compared with the supplemental measuring system.

Configuration of the supplemental test instrumentation is shown in Figure VI.

Data acquisition for the supplemental test began at 0700 hours0.0081 days 0.194 hours 0.00116 weeks 2.6635e-4 months on June 16, 1984. This allowed the minimum thirty minute stabilization period to elapse following leak imposition, which occured at 0630 hours0.00729 days 0.175 hours 0.00104 weeks 2.39715e-4 months .

The supplemental test began with the number two upper containment hygrometer out. of service due to defrost, and remained out for the duration of the test. At 1500 hours0.0174 days 0.417 hours 0.00248 weeks 5.7075e-4 months on it June 16, 1984, the number one upper containment dewpoint hygrometer (VPU-1) also went into defrost, and due to lack of humidity sensing capability for the 1500 hrs. run, the entire data set was rejected. At 1530 hours0.0177 days 0.425 hours 0.00253 weeks 5.82165e-4 months , with VPU-1 restored, data entry into the ILR program was resumed.

Total elapsed time for the supplemental test was 14.5 hours5.787037e-5 days 0.00139 hours 8.267196e-6 weeks 1.9025e-6 months , meeting the minimum period requirement of six hours.

During performance of the supplemental test, an error in calculation of the rotometer correction factor caused the induced leak to be greater than that specified by the procedure. This error was detected through corporate review of the procedure. Although the induced leak was above that specified, the correlation between the leak rate measured at the rotometer and the leak rate measured by the Type A test equipment was within the specified range of

+ 0.25 Ia. Details of the independent review and subsequent calculations are contained in Appendix F.

PAGE 10

3.6 DEPRESSURIZATION Following completion of the supplemental test, depressurziation commenced at 0050 hours5.787037e-4 days 0.0139 hours 8.267196e-5 weeks 1.9025e-5 months on June 17, 1984 at an initial containment pressure of 26.808 psia. Personnel were permitted to enter containment at 0800 hours0.00926 days 0.222 hours 0.00132 weeks 3.044e-4 months , when pressure had decreased below 1.5 psig. Depressurization ended at 0930 hours0.0108 days 0.258 hours 0.00154 weeks 3.53865e-4 months , when Patm of 14.34 psia had been reached.

PAGE 11

4.0 Anal sis 8 Inter retation of Results:

Results of the third periodic integrated leak rate test demonstrating the acceptability of the Unit 2 containment structure are tabulated in Figure VII. Acceptance criteria and test values within the specified limits to demonstrate an acceptable containment leak rate are listed in chronological order of performance.

Explanation of acceptance criteria are given by footnote where necessary, and penalties to correct the criteria are calculated in the sections which follow.

4.1 Penalt Leaka es Measurement of the overall containment leak rate must meet two sets of acceptance criteria based on the as-found and as-left condition of containment isolation valves for the period just prior to the test. Determination of the leak rate acceptance criteria is accomplished via the following equality for two sets of penalty leakages:

Acceptable leakage limit = -0.75 La - Penalty Leakage.

Two penalties assessed on the acceptable leak rate limit are defined as follows:

4.1.1 As-Left Undrained S stems Leaka e Penalt This penalty takes into account the volume of air that would escape through a given volume of piping and its associated isolation valves were the system in a drained state during the test.

based on the known condition of the piping and It 's values quantified during the final Type C tests performed just prior to the Type A test.

Calculation of this penalty leakage is contained in Appendix C.

Leakage Limit = -0.75 La - Penalty*

Leakage Limit = -0.75 La -(-867 sccm X La 110,220,74 sccm Leakage Limit = -0.75 La -(-0.00787 La)

Leakage Limit = -0.7421 La

Requires conversion factor: 110,220.74 sccm = 1 La, per D. C. Cook Plant Surveillance Test Procedure (**12 THP 4030 STP.202, Rev. 4, Page 37 of 55).

PAGE 12

0 4.1.2 Re aired Valves Leaka e Penalt Isolation valves on several system were repaired during the period prior to the type A test as a result of Types BSC leak testing. To more accurately reflect the as-found condition of the containment structure prior to these repairs, a penalty was assessed to correct the acceptable leakage limit. A list of the repaired systems and their associated penalty leakages is itemized in Appendix D.

Leakage Limit2 = -0.7421 La - Penalty* 2 Leakage Limit> = 0.7421 La (-34,941.8 SCCM Z Leakage Limit2 = -0.4251 La This yields a stricter criteria for measured allowable leakage.

Requires conversion factor: 110,220.74 sccm Plant Surveillance Test Procedure (**12

= l La, THP 4030 per D. C.

STP.202, Rev.

Cook 4, Page 37 of SS)

PAGE 13

4.2 SUMP LEVEL CHANGES Prior to pressurization of the containment structure,and immediately susbsequent to depressurization, sump levels were measured to determined whether a change in containment volume would result due to sump level change. As-found and as-left values for each sump are tabulated below. The measurements were taken from the top of the sump to the water level.

Sump Sump As-Found As Left Volume Name Size Level Level Change (ft )

Reactor 2'6"x4'6" 2 ft. 1 in 2 ft. 1 in.

Cavity Lower Containment 2'4"x4'10" 7 ft. 8.5 in. 7 ft. 8 in. -0.47 Pipe 2 I 6 II x4 I 6 'll 5 ft. 8 in. 4 ft. 0.5 in. +18.28 The above represents a total volume change of 17.81 cubic feet, or 504,000 cubic centimeters. Assuming that the volume changed at a constant rate between the initial and final mesurements, this would correspond to a positive volume change of 504,000 cubic centimeters over a 116 hour0.00134 days 0.0322 hours 1.917989e-4 weeks 4.4138e-5 months period, or 73 cubic centimeters per minute.*

A positive change in volume over the duration of the Type A test would effectively mask an equivalent leakage out of containment. A penalty must be assessed on the measured containment leakage, therefore, to compensate for the small positive volume change. This results in a final leakage rate, considering an additional -73 ccm (-0.0002% wt/day),

of -0.03424% wt/day, well within the acceptance criteria as listed in Figure VII.

Rounding conservatively, based on smallest possible time elapsed between measurements - from June 12, 1984 at 1200 hours0.0139 days 0.333 hours 0.00198 weeks 4.566e-4 months when the airlock gates were locked, until June 17, 1984 at 0800 when personnel were allowed in containment.

PAGE 14

4.3 CONCLUSION

All acceptance criteria outlined in Figure VIE being met as specified, and testing being accomplished in accordance with the required codes and standards, the leakage rate for the D.

C. Cook Unit Two containment building is considered acceptable., The next scheduled test of the Unit Two containment is November 1987.

PAGE 15

APPENDIX A ILR PROGRAM ZISTING

II DATE AND TIHE OF LISTING'9/21/84 09.49.i6 DATA SET NAMEI FROM AHS t f 00000000011111111112222222222333333333344444444445555555555666666666677777777778 12345678901234567890i23456789012345678901234567890123456789012345678901234567890 100 C INTEGRATED LEAK RATE TEsT PRDGRAH 200 C ZLRTEST t3 400 C

C DEVELOPED. BY'SD-NEH YORK 500 C HAIHTAINED BY: EHGXNEERING INFORHATIOH SYSTEMS 600 C LAST UPDATE: 060184 BY J. PROBST> EIS COHPUTElt SYSTEM) CANTON 800 C LOAD HODULE. ILRTEST t LIB.PEP )

900 C PROCS: PZLR tSINGLE OUTPUT LCTtt);

C, Qq 1100 1000 12oO C

C USERS! ~

PILR2 tTERHINAL 8 PRINT OUTPUT)

USER. INTERFACE'LR ROSCOE INTERFACE - CANTON ROSCOE COOK PLANT PERFORMANCE SECTZON tUSED DVRXHG EVERY 1300 C LEAK RATE TEST - EVERY 3YRS PER UNIT)

'500 1400 1600 C

C C

VARIABLE LXST

-, 17oo c ATUcti2oi - HEIGHTEn AvG TEMPs; UiPER CAPT 1800 t: APUCtl20) - AVG CORRECTED PRESSURES> UPPER CltPT 1900 C AVP0Ct 120)- AVG.VAPOR PRESSURES>, UPPER CHPT 2000 C ATLCt120f - )tEZGIITED. AVG TEMPS> LONER CMPT, 2100 C APLCt 120 f '-'VG CORRECTED PRESSURES LO)IER CMPT 8 -'300 -: '- . 2200 C AVPLCt120) AVG VAPOR PRESSURES> LONER CMPT C ATICt120) = )IEXGHTED AVE, TEMPS'CE CHPT 24oo C APICt12bf -'VG CORRECRED PRESSURES3 XCE CMPT

., 2500 c AYPIct120)" AYG YAP0R PREssUREsp xcE cHPT 26oo C ACPA AVG COHTAIRIENT PRESSURE J PSIA 2700 C ACFG - AVG COHTAINttEHT PRESSURE) PSIG O. = '800 C A - INTERCEPT OF H VS T ).INE tANUM/ADEtt) 2900 C ANUH, ~ ",'tUMERATOR OF IHTERCEPT VALUE tA)- ~ .

3000 c ADEH - -"'ENDMINATDR 0F INTERcEPT VALUE tAi k,sLofE tBf C bt120) HEASlJRED LEAK RATE tSLOPE OF H VS T LXHEf

:;".c 5200 c.BUt12of

'.'300 3500 C BNUH

-, 3400 C Ct 6 f yeoo C tS CA ', .

~

'TD

'AS 95% UPPER coNFIDEftcE LIttIT LEAK RATE NUMERATOR OF SLOPE tB).

CONVERSIOH COEFFICIENTS HAS VA1.UE OF

'thICATES VALUE OF

~A'OR IS'OR bOMPARXSOti PURPOSES COHPARISON PURPOSES 3700 C CC . , ~

NSOII C '. ::,'A',>> TYPE A Ht)XC)t COMPLETIOtt CHECK TO NERFORlt .;. ~

'S~ 'UPPLEMENTAL, C6i k ICE VALUES USED XH, B}lECkIHG FOR TEST COttPLETIOA -I'.

9 -"-'":, -'."- . 3900 C bPth).

~

~ DEN POINTS, tDEGREESF) 4100 DPctlltth). INDxcATDR FoR iNvAiio DER PoxttTs

. 4200 C DEL,. - - DIFF BE1WEEH UPPER LIHIT AttD HEAS LEAk RATE

'= = VALUE .FROH TABLE FOR N-2DEGREES OF FREEDOM 4300 C EKk .

44oo C HYGtef -;" HYGROMETER MILLIVOLTREADINGS 45Oo C IBYP , - Z)tDICATOR TO BYPASS DATA FOR PROCESSING

',--'"-.,~4600 C I)AS "-,.-,,'RUNNUMBER AT Hl)IClt PROCESSIHG BEGIttS

"~;",'..'700 L XXE -';; ~ hUH QNBEIt AT HHICH PROCESSING.ENDS C IPR,. ' HUHfIUMBER OF FIRST RUH TO, BE PRIHTEt),

.-; -'-."~.",49od C kt12);.-',"-'tYGROMETER t:ONVERSIOH COEFFICIENTS 5000 C ).UC ~ ~ TOTAL Ndo OF UPPER CHPT TEMPS

.,"-'.: 5ioo C t.LC 'OTAL NO. OF l.OHER CHPT TEMPS t: t.IC., " TOTAL Noi OF.XCE CHPT TEHPS

-'OG10 VAPOR PRESSURE ARRAY

, 5300 , C LVPthi

0 LRI.

' XHPOSED l.EAK RATE IH SCFtt,,

~ :;~;,~i':,".'~ 5500 C LitIR" iHPOSEDLRAk RATE, I)t,/ltT/DAY . ~

56tID C.ttltAti20) P ARRAY. OF AI.L RUN 4S USED.IH PROCESSING

.~r ..'&45678'30i2345678901234567890i234567t) 901234567890012~901234567s90ih34547890

9 II DATE AND TIME OF LISTING: 09/21/84 09.49.16 DATA SET NAMEt FROM ANS t )

0000000001111llllll2222222222333333333344444444445555555555666666666677777777778 12345678901234567890123456789012345678901234567890123456789012345678901234567890 5700 C NRD - RUN NUHBER READ FROH XNPUT DATA 58OO C NRO - CURRENT RUN NUMBER

~ 5900 C NR - COUNTER OF RUNS USED IN PROCESSING Qc 6000 C PRES(7) - UNCORRECTED PRESSURES'SIA 6100 C PRESCt?) - CORRECTED PRESSURES'SIA 6200 C PRESCU - AVG CORRECTED PRESSURE) 'UPPER 6300 C PRESCL - AVG CORRECTED PRESSUREp LONER O 6400 C PRESCZ - AVG CORRECTED PRESSURE> ICE 6500 C -

RTDLlt32) LITERAL ARRAY> INTEGERS 66OO C RTDL2148) - LITERAL ARRAY> INTEGERS 6700 C RTOL3t14) -'ITERAL ARRAY> INTEGERS 6800 C SRt70) - HAfKNETER CORRECTION COEFFICIENTS 6900 C SIGHAB - VARIANCE OF MEAN

?000 C TCLP TYPE C LEAKAGE PENALTY> SCCH

'200 7100

?300 C

C C

TCLP2 'YPE C LEAKAGE PENALTY) WT/DAY TALR -; lYPE A MEASURED LEAK RATE> /NT/DAY TZHEt 120) - ELAPSED, TZffE SINCE INITIAL RW 7400 C TIMERtl20) - TIME READ FROH DATA TIHEST - TIHE OF INITIAL RUN 9 . 7500 7600 C

C TEMPUCt16) -

UPPER TEMP RDGSs HILLIVOLTS 7700 C TEHPLCt24) LONER TEHP ROOSE HILLIVOLTS 7800 C TEHPICt7) - ICE TEMP. ROOSE HZLLIVOLTS 9 . 7900 8000 C

C TEHPUt16)

TEHPLt24)

- CONVERTED UPPERS TEMPS> F CONVERTED LONER TEMPS'

'300 8100 TEJ1PIt?) CONVERTED ICE TEIIPSj F C

8200 C THSMUC - UPPER VOLUHE NEIGHTED AVG TEHP 6 F C) C THSMUR - tJPPER VOLUHE NEIGllTED AVG TEHP> R 840o C THSHLC = LONER VOLUME NEZGHTED AVG TENPIN F 8500 C THSHLR LONER VOLUHE NEIGHTED AVG TEHPj R 8600 C THSHIC ICE VOLUME NEIGHTED AVC TEMP F j

'. "-'8700 C THSHIR ICE VOLUHE NEIGHTED AVG TEMP) R 8800 C TSS - SUH OF.TIHE SQUARED 8900 C TS.- SUH OF TIHE, /

9001) C T2S)I - SUH OF tTIHE % ItI

.': :; .--; 9iOO C TAB!.Et 118) -'. VALUES,FROH CONFIDENCE LIHZV TABLE 9200 . C VNFl = UPPER COHPARTHENT VOLUHE NEIGHTINC FACTOR

c,,'..'-" 9300 . " C VNF2 -:LONER COMPARTMENT VOLUMENEIGHTING FACTOR 9400 C VNF3 -" ZCE COJJPARTHENT tJOLUME l'JEIGHTIAS FACTOR 9 ';i; "-'~e'-

9500 9600

, C C

VNAC VPAtJC USED IN NEIGJITED AVG TEHP CALCULATIONS

-'VO VAPOR PRESSURE -" UPPER 9700 C VPALC ~ AVG VAPOR PRESSURE !.ONER 9800

'0900 ioooo C

C C

VPAIC ftoUP -

AVG.VAPOR, PRESSURE LITERAL ARRAY ICE VPRt6) -'lAPOJt PRESSURES CELC FRY DhH.POIItTS . ".,', . ,'" A

- 4, =,...," 10100 C NDLO -'ITERAL ARRAY

' ItDXC '.LITERAL ARRAY 9 ';-,;"~ji~-"~'=1D300

'".';"j". xo4oO

..~'=.,".

, C C

ItTUP t 46) .-'PPEJI RTD IfEIGHTINO FACTORS ItfLOJtt24) " LONER,ItTD NEIGJJTINO.FACTORS = . ". : - ." '",, ~ ',

,: C NTICEt?)

> 10500 ICE RTD NEXGHTING FACTORS

, --"--'; "-, ioboo C NUCDEH = XAITIAL RUN UPPER NEXGHT RE)IAINiNO i,,','..~." 10700 C NLCDEg - INITIAL RLRI LONEJt,)tEIGHT REHAINZNO

' ItICDEH -'XNITIAL RUJI ICC HEIGHT REHAININC

,~~-;.'-~.10900

..;-'";, -'.;:->iiO1) C

~ C NDEH -; INITIAL RUN-TOTAL,HEIGHT, REFRAINING .'

NUC)ltWI, '0RRENT Rl@,UPPElt )thXG}0 REMAINIAO NUCt 126)

UPPER IthICHT FlfACTIO)I IkEItAiNINO' '

~ ',s '

6'::"",'; -.i, Ot) ~

C NLCNUJI ='IJRRENT RUN LONE)t NEX6Hf.REHAININO

~

J c~~'~~ -~ '=

i2345678tJOik5456?HOikk4N?890i234567890i23454759t)10345 234547890i234557890 9

DATE AND TIME OF LISTXNG'- 09/21/84 09.49.16 DATA SET NAME! t'ROH AHS ( )

000000000llllllll1122222222223333333333444444i44445555555555666666666677777777778 12345678901234567890123456789012345678901234567890123456789012345678901234567890 11300 C t(LC(120) LONER HEIGHT FRACTION REMAINING 11400 C HICNUjt - CURRENT RUN ICE VOL HEIGHT REMAINING 11500 C HICtl20) - ICE VOL HEIGHT FRACTION REMAINING 11600 C HNUM - CURRENT RUN TOTAL HEIGHT REHAINING 11700 C H(120) - TOTA(. HEIGHT FRACTXON REMAINING li800 C 11900 C 12000 C 12100 IHPLICIT REALw8(A-H>P-Z) 12200 REALw8 K>LVPpLRI~LRI2 12300 INTEGER OPCHK(6) 060184 12400 DIMENSION B(120) pBU(120) 12500 DIHENSION TEHPUC(16) >TEHPLC(24) pTEHPICt 7) 12600 DXHENSION TEHPU(16)p TEHPL(24) TEMPI(7) j 12700 DATA LUCjLLCjLIC/16>24>7/

12800 DIHENSION RTOLl(16) pRTDL2t 24) pRTDL3(07) rHYG(6) 12900 DATA RTDLl/'ETR-101 'p ETR-102 'j'ETR-103 'j'ETR-104 jp'ETR-105'j 1300d 'hTR-106 p'ETR"107 'p'ETR"108 'p'ETR-109 'ETR-110'j 13ioo 13200 kTR lil j ETR 112 i p ETR 114 e p ETR 128 i p ETR 133 ETR 113 DATA RTDL2/'ETR 122 j'ETR 123 >'ETR 124 jiETR 125 o,'ETR 126 i j 13300 'ETR-127 'p'ETR-129 'j'ETR-130 'ETR-131 'ETR-132 'p 13400 13500 ETR-134 'p'ETR-135 'j'ETR-136 'j'ETR-137 'ETR-138

'ETR-139 j 'ETR-140 j 'ETR-141 ' 'ETR-142 ' 'ETR-143

'j 13600 'ETR-i44 'j'ETR-145 j ETR-146 ETR-113 '/i.

13700 DATA RTDL3/iETR115 i,'ETR 116 i j'ETR 117 'ETR 118 'ETR 119 13800 'ETR-120 ETR-121 '/

139OO 14000 -DIHENsIDN Sic(120)TALC(120),HIC(120)gH(120)pTIHE(120)iNRA(120)j ATUC(120),APUC(120) AVPUC(120) jATLC(120)iAPLC(120) AVPLC((i20)~

141oo - ATXCt 120) jAPIC(120) pAVPIC(120) 1420o bIHENSION K(i8)jSR(70) >DP(6) >LVP(6) jPRESl 7) jPRESCt 7) jVPRt 6 )

14300 DIHENSIO(t NTlJP ( l6 ) >HTLOH( 24) jkTXCE( 7) p TABLE( 118) i44oo 145do C Tl(ESE T DISTRIBUTION VALUES HERR OBTAINED FROM THE HANDBOOK OF STATISTICAl. TABLES - VA(.UES 97 Tl(RU 118 HERE ADDED 6/1/84 JAP

, i46oo DATA TABLE /6.314 2.92b 2.353 2.132j2.015 1.943 1.895jl'860j1.833 147oo "1.812jl 796 1 782j1.77lji 76ijl.753ji 746 1.740 1.734 1.729j1.725>

14800 -'1.72i ji+717ji.714>i.7iIjli708iIs706 jl+703pl.701 j1.699ji.697)1.695 j 14900 1 '94>1 692}1 69lpi 689jl 688plo687jl 686pla685yl 684jla683slo682j

~ ~

i5ood -1.6blj1.680j1.679ji.679 1.678j1.677j1.676j1.676ji.675>1.675>1.674j i5ioo 15200 1 673ii 673pl 672ji 672 i 67iji 671ji 67$ jl 670ji;670)1,669 1'.669j ii'669s3jji 668j3<li667j3jila666j4jjia665j4+1+664j5>1@663@5>lo662j

~

i5300 "6j(1.66ip7%1.660j7jji.659 6jji.655/

i5400 DATA HDUPpHOLO HDIC/'UPPER 'j'LONER 'j(ICE 15500 DATA CApCS/'A'i'S'/

156bo C START OF PROGRAH 15700 )(RXTE (6j310) 15800 Sio FORMAT(lt(lj44l(jj)Htwjjjij(iHHH(%FIXEd INP(ft.DATA jijiwaijiijjfiijiVHj'/l) 15900 kaTE tib)32d) 16000 Hd 'ORMATtittlj44)(jib H.R ERRolt AND NklMHG MESSAGES jjjHtV/)

.16100 l(RITE t 9j330)

" 16200 33O FORMAT(1Hij44Rj 'jinni) ILR PROGRAH RESULTS tijijt ir /)

i63oo I>X 16400 DLGIOO + Dt OGlot 1013 ~ 246DO )

.'65ao Dl.GO < DLOGlbt 6'1071DO)

=-i66oo HOEH = 0.0 16700 READ t5j300jhttR=kkjNd-12f Ci jCkjC3)C4 jC5 jC6)X)(8 jibjlfRpTCLt jTAN 168 0 <<jLRIjCC i2545678901234567890i234567590ik3455785di234hh789bi234S67~84Ã7890i234M iaed

II Q>>.

DATE AND TIME OF LISTING) 09/21/84 09>>49.16 DATA SET NAME'ROM AWS ( )

0000000001lllllllllR222222222333333333344444444445555555555666666666677777777778 123456789012345678901234567890123456789012345678901R3456789012345678901234567890 16900 300 FORMATl 6F6 3)13)I3)13)FS 0)F7 0)F6 ~ 0)AI)

~ 02/22/78 17000 I= 2 Q~ 17100 REAb t5)30l)ERR-"22>END-"IRi K 17200 30i FORMAT( 6FII. 6/6FII. 6/6FII o 6 )

17300 X=3 17400 READ (5)302>ERR=RR>END"-IR) SR .

17500 3o2 FoRMAT(IOF8.5/IOF8.5/IOFS.S/loF8.5/IOFS.S/ioFS.S/ioF6.5) 17600 X=4 17700 READ (5 )303)ERR=RR jEND IR) WTUP>I(TLOW)ENTICE 17800 303 FORMAT( IDF4.5/6F6.5/IIF6.5/13F6.5/7F6.5)

Q 17900 X=5 18000 READ (5)304)ERR=RR)END=IR) VWFI>VWFR)VWF3 18100 304 FORl(AT( 3F7.5) 18200 WRITE t6)305) IXS)IXE)CI)CR>C3)C4)CS>C6jKtl))K(2))K(3))K(7i>K(8)j S 18300 Kt 9))K( I'3) jKt 14))K( 15) )K(4))K(5))K( 6) yK( 10))K( 11) )Kt 1R) j 18400 ~ kt16)>Kt17) )K(18)>SR 18500 305 FORMAT( IH )

18600 TEST START RUN 8 o)13,5X,1TEST END ~ RUN O,I3,/IH I87od hTD i(ILLI-VOLTTO FAHRENHEIT CONVERSION COEFFICIENTS'/IH )6Xj 1880d UPPER )IRX) LOWER j13X> ICE /IH )FS 2)3X>FS 2)4X)FS R)3X) i8900 FS>>2)4'k)FS 2)3X)FS>>2////IH j HYGROMETER MILLI VOLT TO j 19000 'FAHRENHEIT CONVERSION COEFFICIENTS'/ll{ )T16)'UPPER-1')T52) 6 19100 19200

'LOWER"I'T88 'ICE-I /IH 3($ (F10.5 IX))3X)//1H 'T16 lUPPER-2 j T52 j LDWER-2 ~;-Tss )ICE-2'nH )3t3iFI0.5 jix),3xi/i//iH j 't(ANDMET

.. - i93od hk PRESSURE CORRECTION COEFFICIENTS)/IH )T4) 1Wls )6X ) iRll )SXj iW21 j 19400 6X 'RR'SX 'W3'6X'R3'BX 'W4'6X 'R4'X 'W5'6X'R5' i950d i/T4o,'PU-I'ilH '5(2tF7)4 Ix))2x)/IH )38x) 19600 'PU-2 /IH jS(2t P7.4 IX))2X)//1(t )38X 'PL-I )lk 5t HF7.4'iXi 2Xii

.=.= 1970o /lll phSX) )PL-2'/IH )St Rt F7.4)IX)) 2X)//lit )38X) 'PI-1'i.

10800 IH )5(2(F7.4)IX) jRX)/IH )38Xj'PI-2'/iH )5(2(F7.4)iX) )2X)))

9 ..;,- '9900

~ 2'dooo

. I( ., IH )38X)'P-ATtt /Itt j5(2tF7)4)I)t) )RX))

)(RITE l 6)306) )(TUP)WTLOW)WTXCEjV)(FI)VWl'2)V)tF3

=-,. 20100 406 FORMATtlH"j'RTD I(EIGHTING FACTORS'/lit jR7Xj'UPPER(/itt )9(FSc4jIX) j

.*" 20200 F5>>4/iH )5(FN>>4jIX)tFS>>4//IH j'27X) LOWER /I(t jib(FS>>4)iX) j O '-" . Rb30o F5>>4/iH jiRtF5>>4)IX))FS>>4//l(t j28X) ICE /IH j6tF5>>4ji)() jl'5>>4/i

-.'-; 204oo //iH 'WLUME WEIGHTING FACTORS)iiH $ 1X)(UPPER')(j'LOWERj 3X) 20500 --o;- )) -. 'ICE /i(t )2(F6(4)IX) jF6>>4)

. '.",-"::,-,2o6oo I(RiTE tf')7id) TcLP)TALR)LRI 9 .".':,=,o; 20700

- ." 20800

)i6 FORMAT()). TY(?E C LEAKAGE PENALTY6))Fi5okjtthCCHII TYPh 4 I(ESUREb BLEAK RATE,B ) jk9 5) j t)b(T/DAY)I IHPOSED LEAK RATE 5 j )09'3$

2d90o tSCFM).) I o Riooo XF tIXS>>LhoO).i& > 1 Q .

.-.':-'IRuo

':,-;"','.," Rllbd ,XF (IXE.LE>>de IXE E XF lt(llJP.(16).LE>0.(hi 5k',70i GO TO 52/22/76

'.,~,- ; Ri3OD

" "-"; ..i2i4(Jo -GO TO 70k

.215bb '7oi LUc 5 IS "1.'.=-.-

21600 Td2NR= o '-

'."", =-.: ,i .21700 .NRd-"0 -., -. - .- --. -- - ---= o6dle4 NIsod t.xcPI ~ t.xc. 4 i,

',~~~-

'~1 -'i900 -

t.Ucr I - LUC4 1

-.'22ood IS C ",

NR STORAGE.INDE)f)tjROGRAM DATA )(CCESh LOOP STARTS I(ERE) 22100 '..Dd PO Itt < I')i25 o

22300 '.-', IBYP < 0 I(EAn IS;IO6)Ekt=@,(Nb>>='32) I(tu))Txi(El

.". iot) I'DR((AT(f3;Ix)FS) i, i2345(17890123456789di25454'td90123456789bi845678)bi230

', . ... . o2)26'7e 123454789(Ii234567890 g)

9 ll (Q DATE AND TIME OF 22500 LISTING: 09/21/84 00000000011111111112222222222333333333344444444445555555555666666666677777777778 C

12345678901234567890123456789012345678901234567890123456789012345678901234567890 INPUT SEQUENCE CHECK I

09.49.16 bATA SET NAHE: FROM AHS ( f 226do IF (NR.EQ.O.OR.NRD.GT.NRO) GO TO 703 22700 HRITE (10>901) NRDpNRO 22800 901 FORHAT ('0'p2Xj'ILR005I D>><<INCORRECT DATA SEQUE)(CE - RUN 8'p13p'2/24/78 22900 <<ENTERED FOLLOHS RUN 8'pl3j'>><<')

23000 GO TO 23 23ioo 32 IF (IPR.NE.O) CO TO 40 23200 IPR = 120 23300 GO TO 55 23400 703 NRO = NRD 23500 IF (NRO.GT.IXE) GO TO 32 23600 IF (NRO.CE.IXS) GO TO 705 23700 IBYP -" I 23800 GO TO 707, 23900 705 IF (NRO.EQoIXS) TIHEST = TIHER 24000 NR "-NR 4 I 241bo 'IME(NR) = TIHER - TIHEST 24200, ARA(t(R) = f(RD 24300 200 FORMAT(IHIj 'RU)t tSMBER'4k j13/IH j 'ELAPSED TIME'2X>F5.2//IH I 02/22/78 244bo>> 'coNTAINMENT TEMPERATURES DATA cHEGK'//IH j7X)'UPPER VDLUME~ g 24500 21Xp i ONER VOLUME ) I 19X ICE CONDENSER /IH p3X j RTD p2X j 24600 'MILLI-'VbLTS'2Xj 'DEG. N; '7X j 'RTO'&p 'HILLI-VOLTS'2Xp 247oo DEG F" p7)(p RTO p2Xj HILI I Vdi TS j 2X 4 DECo F 24800 707 RkAD (SjioljhRR-"42jEND-"62) TEHPUC 24900 iol FORHATtIO(F5.2jIX)/6tFSc2yi)t))

25000 READ t 5 jlD2jERR=42 jEND=62) TEHPLC 25Iob ib2 FORMAT( Ilt FS'2>IX)/i3t F5'2) IX))

25260, 25300 READ t 5>103>ERR"-42>END=62) TEMPIC iD3 FDRHATl7(F5.2jlX))

25400 IF, (IBYP.EQ.I) GO TO 45 Nsoi) THsHt)c ='.o 600 -

VHAC, -" 1-.0 25700 - - - bd 400 JAHI;-ljLUC 258od A TEHPUC( JAWI),,

25900 IF tA.I.Eo()i()) Gd 8bi war" ~w"-:>

24000 26100 k 8 'ci>>A C2 i

=')(SHUC TO S A<<HTUPt JA'Hi)

- ~ '6200 Cd,TO 406 ...

9,,", ". '.;: 26300 N400 t)I)i to(Ac ~ vHAc -'aiti t JAHi) .

)(RITE (ibj902) t(RDpWDUPy JAWi 26500 - .905 FORHAT l ~0'SX ~TEMPERATURE fkSSIHl) -"'t)N 4(513ytj))SjNj - =" =-

5kA2/7()

'I3) 9 .~, '.; 26600 2670()

26800

>>~CONTAINMENT ENTRY NUMBER 400 TEMPUl JAHI) =-A ADJUSTMENT kbR MISSXI(() TE)HEI(ATUA' dh

=:;.=-;=. 269oo

'-,-.=: 27OOO

..;,; =27ioo IF tVHAC'EQ.i.o) GO TO 709 Tt(SHUC = THSHUC/VHAC,

.,V'HAC, "- i.b

'"'- s-.

'.'-',-', -.-'- '272bo -'... to9 T)tsHLb jl b.b

.',.~ ". 273oo 'O 9 .

',. '.-- -274eo 27500 27eoo 401 JAH2-"ijt.t.C

,A ='Efa l.ctJAH2).

IF tA<LE.O;0). Go T6 803 A + b3aA i c4,

~

., - ~." .:.~; 27700 T)isHLc ~ T')tsHLc 4 A<<)(T'i.oH(JAA2) ~

27800 GO TO 4(ii 9 ".';:.';-. p: 27900 . hot VHAC =..v'Hid

'=

Vir'L6ittJA)tP.).,

)titITE tlbj902) NRDpHDLOjJAH2 ',

- i64566f89bi234567896i2345678901234567690&345678501434 123k$ 475)oi 234567895 9

Cp DATE AND TINE OF LISTING: 09/Rl/84 09.49.16 DATA SET NAME! FROM AWS ( )

Q> 000000000111111111122222RR2RR333333333344444444445555555555666666666677777777778 12345678901234567890123456789012345678901234567890123456789012345678901234567890 28100 401 TEHPL(JAHR) " -A 28200 IF (VHAC.Eq.l.o) Go To 711 28300 TMSMLC = 'PtSHLC/VWAC Qg" 28400 Vl'(AC -"1.0 28500 711 TMSHIC = 0.0 28600 DO 402 JAW3=lplXC 28700 A = TEHPIC(JAW3)

Q IF (A.LE.O.O) 28800

-"C5vA i C6 Go iTO 805 28900 A 29000 THSHIC = THSMIC AIWTICE(JAH35 R9100 GO TO 402 29200 805 VWAC "- VHAC - HTICE(JAW3) 29300,,

29400 4b2 WRITE (10>902) NRD>HDICpJAH3 TEMPI( JAH3) "-

6 29500 29600 C IF (VHAC.NE.1.0)

CONVERT TO ABSOLUTE THSHIC = THSHIC/VWAC 29700 29800 THSMUR -TMSHUC THSHLR = TttSHLC + 459.7 t 459'7 R9900 TMSHIR = XMSHXC j 459.7 30000 C PRINT CONTROL IPR 0"-LAST ONLYj ¹tj TKR0 LAST

.. IF (IPR.EQ.O.OR.IPR.GT.NRD) Go TO 30100 45 30200 55 HRITE t 6>200) NRDpTIHER 30300 Db 50() IHRT=lpLiC 30400 500 WRITE tbj501) RTDLl(XHRT)sTEMPUC(IHRT)>TEHP()(IWRT)j 30500 .

'- = = RTDL2lIHRT)jTEMPLC(IHRT)jTEHPL(IHRT)3 30600, 30700 30800

'6i 'O-', 502 IHRT=LICPijl.UC RTDL3(IHRTi jTEHPIC(IHRT) 'EMPI t IHRT)

FORMAT t 1)t )AS j2X)2( F6 2 35X) jAS>RX 3 R( F6( 2p5X) sA8pRX jF6 2>@ jF6 2 )

~ ~ ~

.'.. -'., 3o9oo 5oR HRiTE tbjso3i RTDLitiHRTijTEHPUcti3@TijTEHPuixHRri, 51000 ' RTDL2tIHRT)jTEMPLC(IHRT)~TEHPL(XHRT)

. ', '-* '.- 3iio(5 Rbg FORHAT t fk jAS j2Xj2(F6i Rp5X)jAS jRXjF6.2>5xpF6;25 Q

=

"' 3120(5 DO 504 IWRT"-Lt)CPXjf.l.C Si300 . 504 )tltITE t 63505) RtOLR(IHRT) jTEHPLCt kktT) jTEHPLt IHRT)

-3i4oo SoS FoRMAT (xtt j32xjAsjRxjF6;2,5xjF6.2), ',--

- =. -! 816DO

,',.31700, 3i500,

~ HRXTE 't 4 j507) THSHUCpTHSHLC jTHSHIC jTftfitJRjTHSHLk36$ HIR

50) FORHAT t 1K.", 317X j j

SUMMARY

OF l(EiGKTEO AVERAGE TEHPERATU5(ES //lH 3

-'ppER VOLU((E tDEG. Fa) 3F5.2j4Xj'LOWER VoLUME (DEGAS I:3 ),,- 'g

.:-"'",'i800 '6(Rj4xy

', -" UPPER VolUHE tDEG. Ra )

.=

ICh CONDENSER tDEGt Ft) jF542/1(t

>f6tRj4kj'LO)(ER V't50)t(E tDEO'T( .

~ -..'".',;-",'31900.

hh -,; ~

' - -" F7 Rj4X3'XCE CONDEMN(SER

=.-

tbEG hc) , '3F7'2)

.;. 'F, (IPRiE(t'1205

.3R()00

-'=..'c: ~ . 322bo

~

'-P. :"'~323DO 32100

~,45 hEAD

..Sb9 FORHAT, t6F6'3/7F8.5) .

GO TO (lj009jERR=423END-60) ttYGjPREb 35-.

'- ', ~ 060184

-.j 55400,. * ..; IF (IBYPhEQai) Go TO 20

~

,.y," =~a32500 ".,~,, bP(15 -" Ktl)jtKYG(l)it(YG(h,)4 k(k)NHYG(i) 4- k(3) -,;,-'" -- -;--- 050184

~ . ~

,. ~'/.'",",~-'~,'326bo . --..'., DP(R) -" k(4)j(HYGt2)<HYG(25 4 kthij(HYG(55 4 K(6), = " *., 060184

~ --..

'~"-'. -'g"-32700 -',

~.=

DPt3) < Kt7i<ttYG(3)<kVGt3i k,kte5~MYGt3) 4 K(9)

!~3~~.-,'-.'2800-- .*='. DPt4) -k(iO)iKYGt4)NMYGt4) 6 ktll)IkYG(4) 4 32900:.:";~'-'"~-DP(55,=K(i3)NKYG(5&ttYG(S) 4 kti4)jjKYG(55 4 k(155 K(iR)'60184 -','-'

. - 060184 060184

...,,, '6oi84

" 33000 ,"- '- DPt 6),-k) 16)I)tYGt 5)jtkYG('6). 4 kt i7)S)tvbt 6) i.k(idi

'.;-'iCKK iS - l)"-VALID, -"" 060184

~ =;..';'i,~',~ -.a~*. 33XOO INDICATOR FOlt XNVALXD DE)(POINTS 1"-1(NALID

".'--r'i=-'j 353bb.'

~",-h =,:""3340O" 33200 .."

'ik',

. , bo 412 J=ljh 60f4TX)(0E - .'

.'.. DPCKK(J) "- t)s(5 ',; ."., -- .

~ ...'

~,

"='--

,-b60184 060184 060184 '='

=

' :,;:j ." ..., DO,403,J6ij4; ";:.',-.::" *. .,:...;...--- *-

.";" 33500 586bo".', -':=...ii tbb(J);-ti;3k~ i )(RitE'ibj4o9i lfIJjphR5

~

.'. ',,'.,;...:.tI60$

. - - ~.~,.

4, I':-' .

1594h678trb123456789biU454789biR34tI67()9di23456789t5i f34 'i23454A'6i234567890

o i)ATE AND TIHE OF (.ISTING: 09/21/84 09.49.16 DATA SET NAHE( FROW AWS t) 000000000llllllllll2222222222333333333344444444445555555555666666666677777777778 12345678901234567890123456789012345678901234567890123456789012345678901234567890 3370O 409 FORHAT('ONVERTED DEW POINT '>F6.2>'UN NUHBER ')I3>'S OUT OF 060184 33800 + RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED') 060184 33900 IF (DPt J).LT.32.0.OR.HYG(J) ~ EQ.O.O) DPCHK(J) = 1 060184 34000 IF (DPtJ)oLTc32.0.OR.HYG(J).EQ.O.O) GO To 403 060184 34100 CIOOC -"373.16/((DP( J)"32. )/1.8 4 273.16),

3420o LVP(J)>> -7c90298%(CIOOC - leo) + 5.02808<DLOGIO(cloocf 4 DLGIOO 34300 -1.3816~(io~(-7.0) )~I lo~~(11.344~(l.o-l.o/clooc) ) -.1. )

34400 48c 1328%(low<(-3co) )%(locc<t-3.49149%(CIOOC - 1.0) ) - 1. )

34500 403 CONTINUE 34600 Do 50 J=5p6 34700 IF (DP(J).LE.O.O.OR.DP(J).GT.32') WRITE tlo 410) DP(J)pNRD, -

060184 34800 4i(f FORHAT( CONVERTED DEW POINT '>F6 ~ 2p RUN NUHBER p13> IS OUT OF 060184 34900 RANGE FOR VAPOR PRESSURE CALCULATIO(t AND HAS BEEN IGNORED'), 060184 35000 IF (DP(J).LE.O.O.OR.DP(J).GT.32.OR.HYG(J).EQ.O.O) DPCHK(J) = I 060184 35100 . IF (DP(J).LE.O.O.OR.DP(J).GT.32.0R.HYG(Jf.EQ+0.0) Go TO 50 060184 35200 COC -"273.16/((DP( J)-32.0)/1.8 + 273.16) 3530b Lvdt J) -"-9.097iew(coc-l.of - 3.56654%DLoei0(cocf 35400 40.876793'(1.0 - 1.0/COC) t DLGO 35500 50 CONTINUE 35(loo DO 404 KAY "-lj6 E 35700 IF.(DPCHK(KAY)'EQ.i) VPR(KAV) = Oo(f - 060184 35800 IF(DPCHK(KAY)oEQ.1) Go TO 404 060184 35900 VPR(KAYf " 0.0145038wlo~LVPt0Y) 36000 404 CONTIt(UE

. 56100 36200 34300 L .. -

IF tDPCHk(if.EQci.AND.DPCI(Kt2)cEQ.I) VPAUC =

IF t DPC((k(1).EQ.I.ANO.DPCHK( 2),EQ.i) & To '717 0.6,

.CHECK FOR )tISSI(to VAPOR PRESSURE all) CALCULATE AVERAGE(

060184 060184 Se4OO .IF tDPCHK(lfcEQ.i) Go TO 713 060184

=,.'-.. 365OO IF (DPC)tkt2)ol(Eel) Go TO 715. -, 060184

." -. '-, 366dd VPAUC = VP(ttif 3676O VPR(2) = OcO 36800 . GO TO 7D 36900 .'".'fit V(IAUC "- VPR(2) 37ODO .VPR(1) "- Oc()

37100 . ~ -. Go TO 717

- 7'PAUC "-, Oc5((tVPRfif 4 VPRt2))

~7200

";., 660l84 30300 .-.. 017 IF (DPCHK(3).EQ.icAk).DPCHK(4) E4ci) VikLC - t).a =..'.

c.,',",'. 7500 37400 AND.bPCHKt4f.EQ;1) GO T(f 723,'-", -

060i84 'DPCHk(3)cEQ.i 9 :- 376oa iF tDPCHKt3)cEQcif Go TO 719, -

IF,'DPcHKt4f.NEcif Go To 72f '. , '.

'60i84 06o184

,-.. .. 877OD

" 37800 VPALC - VPRt3)

VPR(4) "-'cb m . '.-".:. -.'.- 379OO , 5O TO 725,.

38000 . =

78 VPALC ~ VPRt4)

'38100 ', VPR(ki ~ O.(f 38200 '- GO TO 723 iti

-",'....,;:,5830(f .," (

38400 ViALC DcR()tt)P)(th) 4 VPR(4i).

-,f03 iF tDPcARts).EQci ANDcDPct(kt6).C4ci) Vi'Aic < oc6 ...", .-.. b6oi84

=',-'~~" .3850b 1F tbPdkktsf.hQci.A)tD.DP'CHKi6f.kQci) bO TO VB ...'.,=-.. -.:-'; . 666184

.'".-"."+'"j"" 38600 IF (DPcHK(5)cEI);1) Go To 725 . '

()60184

-~=.,: ~ 38700 IF tDPCHK(t!).f(Etif GO TO 727 . O6Oi84 Q ~

38800 VPAIC - VPRt5)

O,

-":""-'~.38900

-."~j'

".='.-';.

'! '.i, 39000

",'.3910b -...7th

='",--.'-".",c'3'b "".. -.Vtttt5f VPR(h}

VPAiC,E 6.0 Vithi

().O.

'ik34mb7()90i234478St)H34878c96i84IHe9oB34hife9oi845 i234567e9oii34s57e9o i

I DATE AN0 TIME OF LISTING: 09/21/84 09.49.16 DATA SET NAME<< FROM AHS t f 00000000011111111112222222222333333333344444444445555555555666666666677777777778 12345678901234567890123456789012345678901234567890123456789012345678901234567890 39300 GO TO 729 39400 727 VPAIC = 0.5<<<<(VPR(5) + VPR(6))

39500 C LINEAR INTERPOLATION FOR PRESSURES.

39600 729 DO 405 M=i>70>10 39700 Nl=H>1 39800 N2=H+9 Q>> 39900 HY=( (H-1)/10)+1 40000 PRDG = PRES(HYf 40100 IF (PRDG.EQ.O.O) GO TO 444 40200 DO 406 ¹Nl>N2<<2 8 40300 40400 IF (PRDG.LT.SR(H))

IF, (PRDG.EQ<<SR(N)) GO TO 731 GO TO 406 40500 IF (N.EQ.H1) GO TO 444 40600 PRESC(HY)=SR(N-l) j (PRDG"SR(N) )IfSRtN-3)-SR(H-1) )/(SRtN-2)-SR(N) )

4070<<f GOTO 405 40800 405 CONTXNUE 40900 444 NRiTE tXO,4O7) PRDG<<NRD<<HY , 02/22/78 41000 407 FORMAT(T2j }<<<<<<<<<<MANOMETER READING }F9>>43 NOT Xit CALIBRATIW RANGE 02/22/78 jI3}>>j <<jI3) g . 41100 41200 40S RUN (j>>

PRESC(HY) = 0.0 ENTRY NUMBER 41300 .GO TO 405 41400 ,73i PRESC(HY) = SR(N-lf 41500 4'ONTXiUE .

4ihoo C >>AVERAGING PRESSURES ALLONING FOR ZERO ENTRY.

41700 PRESCU '= b<<5<<<<(PRESCtl) + PRESC(2))

4i800 PRESCL = 0.5<<<<(PRESC(3) + PRESCt4))

41900 PRESCX = 0.5<<I(PRESC(5)+ PRESC(6)),

42000 IF 'tPRESCtl) ~ LE ~ 0 ~ 0 OR>>PRESC(2) ~ LE ~ 0 ~ 0) PRESCU 2 '>PRESCU 42100 XF tPRESCt3)<<LE.O.O.OR.PRESC(4)>>LE.O.O) PRESCL = 2.0<<<<PRESCL 422,00 IF (PRESC(5)}LE<<0 '>>OR.PRESCt6)>>LE>>0 ~ 0) PRESCI - 2 0<<<<PRESCX 42300 ACPA"-(PRESClf}PRESCL}PRESCI)/3

- 4240O ACPG=ACPA"PRESC(7) 42500 . .... IF,.tiPit>>EQ<<0>>OR<<IPR.GT.NRD) GO TO 74$

. 426OO ,. 3S NRITE t6350S) HYGtl)}DPtl)}VPR(i)}PRES[i)>PRESC(1f3

,',= .'- 457OO l(YGI 2 f pbP( 2) }VPRt 2 f jPRESt 2f }PRESCt 2f 3 (y ..., .':-""'2800 . IIYG( 3 f >DP t 3 ) }VPR( 3 ) }P RRS( 3 ) >PRESC( 3 ) 3

",.~.'>>.* .. 42900 l(YGI4 f <<DP( 4 f pVPR( 4 I }PRES(4) jPRESC( 4) 3

'; <<',;:.,',",,'. 43ooO, I(YGt5) }DP(5f}VPRt5)jPRESt5) }PRESCt5) 3 9 43100 HYG( 6) pDP t 6) }VPRt 6 f <<PRESt 6) jPRESCt 6 f >PRESt 7 f jt<<RES6t )

-. --;,!:.,>> '.43200 : <<'":,"-f)VI}AUt."}VALI:}f RESCI)3VPAIC}PRESCL}PRESCI}ACPA}ACPG .

'3300 r.,

'~.

II

", 43400

.. 608 FORHAT t 0 .311k},'CONTAINHEjtl VAPOR PRESSURE bATA CI(ECK 3T833

,'CONTAIHHENT PRESSURES GRATA CHECK )/1H }19Xp 'HILLI-}SX 3 43500- DEN POINT'4X}'VAPOR PRESSURE'. }30X} 'UNCORRECTED'7X3 0366O .

<<CORRECTED(/Ift 32X}'HYGROMETER<<}SXj'VOLTS'BX}'(DEG37Xj

}"': .." . .;, 43SOO--

43760 t PSIA) '23X} 'ltANOHETER'2Xp 'READING t PSIA) '2Xj tPSXA)<</ljt 33X}<<UPPER<< 'pT81} UPPER: /1H '5X}'VPU."I 39X}4+2} .

'READING

".-'-..'.,: >>'; 45900- 9X F6 2}9XjF7(4i25X> PU-i'2(&}F7i4)/T73'VPt)-2'Zt9X'F6'2 f}'

'; '.- ~;~.44io(f.:

.=

44000 . F7. 4 VPL

'83 i 3

' tl-2 ' 2 ( Bjt3 F 7 . 4 Iri 3

' owE R i <<}tsi3 'DHE R I <<]

}2t 9X)F6 2) 39X<<F7>>4 }T83 3 I L' }2(SXpF7>>4)/

'73<<VPL""2 }2(9X F6.2)39X}F7.4}T83}"PL-2 2(8X F7.4fi,

/<<)<<,'-" '" ";.'.-443bO '-. = T5 3'XCEI 'T81} <<ICE'T7 3 'VPX-1<<32t <<j)t306.2 f39)t}F7.4'T833 'PX-i. 3

-;..:-" '44400 2tBX}F7 4)ITT3 (VPI-2<<j2t9>t}F4.2)}9X}F7.4}T83j'PX-2'}2t8MF7.4)/, -'.

.445OD :,.-

T81 3 AHBIENT }T95}F7>>4psX}F7>>4/itt 3T243 AVERAGE VAPOR PRESSURES./

TB6 j <<SUfQIARY bF CORRECTED AVEI(AGE I>REASSURES /1X}T173 'UPPER CONTAX

" '".':-'; .:..- -.'; 4(37OO- ; -:.-QIEHT tPsiAf? }T47}Ft<<4)lk}Ti73<<LOWE% coi(TAINHENT ti Slk) <<3T4t 307<<4 =.';

Q 0 -" "-'-'-, -"}T(fij AVERAGE t)PIIER tIRESSURE tPSXA).)Ti20}F7<<4/lit }

P "1295678901234567890123454789bi234567(390i234567890i23456 234567895123(565'S9(f o

o 9

DATE AND TIME OF LISTING>> 09/21/84 09.49.16 DATA SET NAME:

00000000011111111112222222222333333333344444444445555555555666666666677777777778 12345678901234567890123456789012345678901234567890123456789012345678901234567890 FROH AHS ( )

44900 ICE CONDENSER (PSIA) pT47pF7 4pTSlp AVERAGE LOHER PRESSURE (P 45000 -SIA)'pT120'F7.4/Told'AVERAGE ICE CONDENSER PRESSURE (PSIA)'1203 6 45100 45200

-F7.4/TSlp

'AVERAGE CONTAINMENT PRESSURE

'AVERAGE CONTAINMENT PRESSURE (PSIA) '120>F7.4/TSi>

(PSIG) 'T120pF7.4) 45300 IF (IPR.EQ.120) GO TO 40 45400 C j CALCULATE NORMALIZED HEIGHT FRACTIONS STORE HIT)l PRESSURES' 45500 747 HUCNUH = (PRESCU VPAUC)/TMSMUR 456OO j(LCNUH ~ (PRESCL - VPA(C)/THSHLR

.45700 HICNUH - t PRESCI - VPAIC f/THSHIR 45800 HNUM = VHFl>>>>HUCNUH ( VHF2>>>>HLCt(UH S %IIF3>>>>HICNUH I 45900 ZF (HDEH.GT.O.O) GO TO 749 46060 hfUCDEH = HUCNUH 46100 HLCDEH = HLCNUH 4620(f HICDEH = HICNUM 46300 HDEH = HNUH 464oo t4t HUC(NRi = HUci(UM/HUcbEH 4!t500 . HLC(NR)=f(LCNUH/HLCDEH 46600 HIC(NR)=HICNUH/HICDEH 46700 H(NR)-"HNUH/HDEH

, 46800 ATUC(NR) = THSHUC

,, 47OOO 46900 , ATLC(NR) THSMLC ATZCthRi "- TMSMIC

'7100 'PUC(NR) = PRESC(J Q 47200 A'PLctNR) >>" PRESCL 47300 'PIC(NRf = PRESCZ

. 474OO Avi uCtNR) ='PA(iC 9 47500 ,'VPLC(NRf = VPA(.C

.; 476OO AVPICtNRi = ViAiC 47700 20 CONTIt(UE

.478oo, f(RITE. (ib>F03(

., 47900 '63 ~

FDRHAT t '0>> 3$ (j >>fLR006I D >>>>>>>>>>>>DATA sPkck E)tchk6ED>>>>(t>>(( i , 62/24/78 48000 , GO TO k3,,

.'i,"j; 'i..:48100 El(D t)P.2ILC A)(D t)T(fkk kkROR HEShkGEC 4820(f ',i2 C,

HRITE t103904) I g,,. ", ', " 4(f300 48400 ':. '

~ 904 FDRMAT i '0'>>2xj xl.R002z () (H>>END ok Pi)(Eo bATA f232)(3>>>>>>g>> )

GR0Ui( )

y ok/k4/78 02/24/78

. ',.:, ".. 4S50if .'; 28 HRITN tit)3)OS)

'"."""::. -' 4566O ,()05 NORHAT t>>-')2)tj"flfiO68Z'tf j>>>>>>>>>>A)fftt)iSAt. Ru'(t T'ER)llHAiZOti44(i 62/24AS-

-.'-'--'~;,':-'. 4570o ', bo Ta k4,

" "," ..48866 .: 8 HRITE t i()>>004 f f

",45900 .', $ 04 FORMAT t;b>>jej>>kLt(b>>fii'. B>>>>>>(@Eke hftfOt( fN PZl(E() DATk -'ROUP 3 j = 62/24/7(j

", " Z2>2)(p>>>>>>>>>>) -

02/24/78 '0000 40).00;.', - &,Td 28

-'t. t(RITE.ti6>)bled f85; 9:.::.:,. 49300 492oo

., 07 $

FQRHAT t 'tl j2kj Il.R003I D>>>>>>>>REA(f ERROR fQ AT= DATA 'H 4'>>I338(062(/ls 4)406 j>>3 i)>>>>>>>> )

"-.'".x"'- 49500

" .:-'..~"~"'. "

GO TO 23.'

'Ilk HRiTh

=

@ 49616 tibjbb5f l(RO

49700 .- 90(f FORHAT t 0 32)tj'fL((064i B>>>>>>>>E}(O BF t)ktk ftt fhSt tfiiik tlU)t 4 jH383Q/k427tj

., -.'. "'.-4>>ferro

,i "

499OO 50000 C .

6d Td

- .,8 RhSt)LT PORTION OF PROGRAH

'If tNRoGE>>3) Go To 41,-

'i ~~,.~~50100 ....,40 . . ~ .;*

,",, .,ill.-,,...-f&kik4ilS

-: '-!',,5(f200, f(RITC tibj>>>>(f>>)f

~ =" "",.',"',".'~'.,"S()36t) -" (fb>>)

b(i

.:.-EDGED FOi(fiAl';i >>(f>> j&f'ifUt537iB-t>>>>>>l&3 TflfN k

'i .-; - ..-.:-.

ANOINTS'-. fkRE 84TL 184557(f9>>flk34857M5i855478)OiH454ld9t)iH4557(f9tfi234>>>>1235567895i23456i(390 02/24/7';.".

9

II i LISTING: 09/Rl/84 iw DATE AND TIME OF 09.49.16 DATA SET NAHE: FROH AHS ( )

00000000011111111112222222222333333333344444444445555555555666666666677777777778 12345678901R34567890123456789012345678901234567890123456789012345678901234567890 50500 GO TO 23 50600 41 TSS = TIHE(l)<<TIME((l) + TIME(2)<<TZMEt2) 50?00 Ts ~ TIME(lf 4 TiME(2) 50800 TRSH -"TIME(I)<<H(l) + TIME(2)<<)t(2) 50900 51000 HS =

HRZTE i

H(1) H(2)

(9p201) 51100 201 FORHAT(lM p48Xp'SUHHARY OF AVERAGES'///IH p2Xp'RUN 8'RXp'ELAPSEO 51200 -'RXj3(34HAVG TEHP AVG PRESS AVG V PRESS )/1H iloXp'TIME'p6Xp'0 51300 51400 PPER p6Xi 'UPPER'7Xp 'UPPER p6Xp 'LOHER p6Xi LONER p7Xp LONER j7Xp CE pSXp ICE j9Xp ICE /)

I 51500 DO 43 I=lpNR 51600 43 HRITE t 9p202) BRA(I)p TIME(Z)p ATUC(I)pAPUC(I)jAVPUC(1)pATl.Ctl)I 51700 -APLC(I ) jAVPLC(I) pATIC(Z ) pAPIC(I ) pAVPICl I) 51800 202 FORMAT (1H j2Xi Z3p4XpF6.2p2Xp3iF9.4p2XpF9.4p3XpF9.4p2X))

Q>>

51900 jiRZTE l 9p205) 52000 205 FORHAT(lMlp34Xp 'RESULTS OF THE LIi(EAR REGRESSION ANALYSIS'///

SR100 -lH j2Xp RUN (I pSXp H jllXj LEAKAGE RATE j9Xj LEAKAGEi9Xp

'H UPPER'7Xp 'H LONER'9Xj 'H ICE'/1M ilOXp 'EXPERIMENTAL p 52ROO 52300 -6Xp UPPER LIHIT ' 11X i 'RATE ', i8Xi 'CONTAINMENT'3Xp 52400 CONTAINHENT j5Xp CONDENSER /)

52500 C . REGRESSION LOOP O '2700 SR(poo DO 44 Z=3pNR .

TSS = TSS ~ iZMEti)>>TZMEti) 52800 ., -

iS =- TS TIME(i)I

,;/.'52900 "

Hs, = Hs ~ N(i) .-

53000 TRS)t ~ T2SH 4 TiHEti)<<H(i) .

53100 ANUM = TSS<<HS - TS>>T2SH 53ROO XNRR ii I -

"., 53300 ADAM = XNRR<<TSS TS>>TC

- 53400 A = kNtJH/ADEi(

' --:; . 53S00 B)IUH ~ )d(RR>>TULSA - Ts<<HS 53400 ktl) -

. 53700 II=IO.o,,"

hNUM/ADEII C

.'-=- '., S3eoo HSUH e =, .';-',

530oo

','4oba C ,SUMOF Sgl/AREif t)IEFERENCES DO.46 i.=.i;iZ.

54i00 )(Lti = A S Bli)<<TiHhtLi

, 542bO IF ((fABSik(L)4LR)<Lhji;db-S9) 06 t6 44

..,'-."-,',',,'- 5430d )(slmt > HsUH 4 tNt Lf-I(LI'tfklNL)-'HLtt)-

..'44db . 4h CO)(iiNiiE

.:;..:; .='4soo ,'.- - ..- Az,= fs/)SR'*

.-, 54600

",',, TbT"- ANAT p(D ';-.'.~ ~ 54?00 Do 44 H=Rpti

'.':-'4ha(f 4tl iOT . TOT a tTiMEtH)-ATiktTii(attt)-At) p - .,,.-';.;. 54900 Bti) pj 8400>0<<Bil}

"~.'-';;",'-; Shobo *,,;".' ELK > TABLE(II"Rf pyj -, ','. '.< '.~; 551bo .>>'. -.--. SfGHAS L DSQRT(HSt&(T(lfjit&k-k>5f))

.-'.".";-:;= '. 552bo DSL =" hkk<<slGMAb<<24oo.if

.-., '-"; =,S53od ,; .. BU(I) =,Btl) -'RL

>> i-7 g>, SS400 ARITY t Oj205) fiRAtki);It{it),B0Q)jhfi ) jNUCtii)pNLCtiIi pHiC>>lit) id'bRMAf ti4jiij5XpF9.5j2tj)f(jFO.S)j?ftjf0'5j5XjF0.5j6kjFV.S)

'~-: ~" j-;-.,~; 55500 55600 CONTIN!)E .,

'..',."',~;-~'~55700 .. EAU, bk.khGRESSIb)t L6b)I

)(hltE,t()j503) 5tNiif jA;- *

";.-,kd3 FaRHAAittdtLi&j'NIALLRAitAM k!ik fP PN 6AA 5(,i(i~5j5ftp>$HRCE: '.

O,;;"-", -':;:.",,;::, )l bo ,

'.-,-'.-Pr" j jf() 5),

H$45t'17()95i645575II6HS4N)89oi)3416?(i9diH445956345 12345$ ?890464M?I)90

o. '--"

II Q

DATE AND TIHE OF LISTING: 09/21/84 09.49.16 DATA SET NAME4 FROH AHS i )

00000000011111111112222222222333333333344444444445555555555666666666677777777778 12345678901234567890123456789012345678901234567890123456789012345678901234567890 56100 HRXTE t9p204) BUINR)

C, 56200 204 FORHAT ilHop21Xj'UPPER CNIFIDENCE LIMIT FOR THE RATE IS '>F9.5) 56300 C 56400 C TYPE A TEST COMPLETION CRITERIA 56500 ADDED 040184 JAP 56600 XF tcC.NE.CA) GO TO 25 56700 TCLP2 =TCLP/440882.96 56800 )IRITE t9p898) TCLPpTCLP2 56900 898 FORHATI//'wwTYPE=A TEST COMPLETION CRXTERXA MESSAGES 57000 -%%%'/'YPE C LEAItJBE PENALTY ~>F10 ~ 2j'SCCH) = 'F10.4 'r'OIT/

57100 -DAY)'

57200 IF,tTCI.P2.NE.O.O) GO TO 875 573oo , HRiTE,t 9)876)

. 57400 876 -

FORMATI~ ~wtt HARNING - TYPE C LEAKAGE PENALTY = 0.0 ~~)

57500 875 IF tTIMEINR)oGT.24.00) GO TO 880 Q .

57600, HRITE I 9>890) 57700 89b FORHATt 'EST bURATXON HAS NOT EXCEEDED 24 HRS -"

CotITINUE

=)

TESTING'7800 57900 GO TO 24 58000 880 IF iBUINR)'i.TrO.O.ANO.BINR)aLT.O.b) Gb TO 800 58100,. HRITEt 9>799) 58206 795 FORHATt 'HE LEAK IIATE t)PPEIt LIitIT AND tIEASURED LEAK RATE ARE NOT 58300 -BOTH NEGATIVE - CONTINUE TESTING 58400 Gd TO 24 58500 58600 5s7oo C,.

'ci 500 CCi = =D.1575

= DABsiccf)

- TCLP2 sld 58800 5890d 59000

~; , IFIDABSiBUINR))'-bE.CCff"GOTO HRITEt 9stt9l) 891 FORHATt 'HE Lhkk RATE UPPER LXttif ttASr CONVERGED TO AH ACCEPTABl.Er 59100 - -

-LEVEL) 7

'-"; "'-'.='-.. S92od, GD,TD 82o,.

. 59300 .'-.'io HRITht9)B92f .

59400 t)92 FORHATt ', AE I.EAk ItATE UPPER LIHfT iiAS )IOT CONVERGED TO AH ACCEPTS

,'.;;-=,,- 59Soo . -BLE LEVEf. - CONTINUE TEsTXNGI)

. y",;.."'"'59600 ~. GO 40 24

'- ""-.'.;:; s9sod hko CEk '=

bUiNttf -

-',lF CC2 = DABStcC2) '-

btNR)-'9900;

....,'-'0000 t6C2;GE b"0625) 60 TO 830

'~6010d,;-, -, HQTEt9ib93) .-.

6020b

., - .... ~,"=;.;...

t)53 FOR)tATt i TIIE 61PVEItkffCh t)ET)tEEH THE LEAkRAtE UPPER 11)tIT PHD HEAS =-.

~ = ..:, r--

60300 " -, -URED l.EAk hATE fS ACCEPTABLE FOR COMPLETION)')

GOTO 840, 60400 -.

,. "~.:,'. 40500 835 HRXTEt9)894), .,

--P-.",. 60600 . H4 FORHAtt TIIE 5IFFEREfICE BET)iEE)t Tits Lhkk,lUiTE.t)IIPEh UHIT Akd fkAS

~

.'i:. 6070d ', '*. 'URED LEAk RATE IS TOO LARGE - CONTINUE TESTING'

';j";," 60itdO, "

GO. TO 24.,;,

-" -.::;-~":.et)9oo.'-;

~

6,'- cHEck O'P'iER LiHIT.I.EAKRATE-6ib00 840 .'0 tNR.LTs7),GO TO 24

-.'.;.-~:.6110d .'.

',",, ",z'. 61200, r

'-,"',." "~"613OO .;.;

"r."

'F IF tBUINR)ALT;BUtNR-lf)GO TO.b50 IBUtNR=I)ALT.BUttIR-2))GO Td 85II lF i BU( HR-2).LT;BuitIR-'37) te TO 850 .

- ~ ., "" -61400,'r 'k.tBUINR-3)'LTaBUIW&))GO TO 850

,".,':I"-'-;-*j~-'61500';--..., '.'RITE t9>B95)-

dd'; ~ 5Q FORHA)t.. t.hAk.ttkTkUPPER LIHIT bb55 HOT WHO)i4EGA TREito bVER,L,:.

~ i23I)557890f 234557890f 2@567890f 23456789012345678901234 >1234547890i234567890

II DA)E AND TIME OF LISTING: 09/21/84 09.49.16 DATA SET NAHEI 0

FROH AHS t) 00000000011111111112222222222333333333344444444445555555555666666666677777777778 12345678901234567890123456789012345678901234567890123456789012345678901234567890 6i700 -AST 5 RUNS.')

61800 GO TO 870 ogi 61900 850 NRITE t9>896) 62000 896 FORHATt 'EAK RATE UPPER LIMIT SHOHS NEGATIVE TREND ttITHXN LAST 5 62100 -RUNS - CONTINUE TESTING' 62200 GO TO 24

'62300 C , CHECK MEASURED LEAK RATE 62400 870 IF tBtNR).LT.BtNR-l)) GO TO 860 62500 IF tBtNR-1).LT.BtNR-2)) GO TO 860 62600 IF tBtNR-2).LT.BtNR"3)) GO TO 860 62700 IF tBtNR-3) ALT.BtNRW)) GO TO 860 62800 NRITE t 9)207) 62900. 207 NORHATt 'tEASURED LEAKAGE RATES DD ttOT SHtlt NEGATIVE TREND OVER LA 63000 -ST 5 RUNS'//'YPE A TEST IS COHPLETEt')

63100 GO TO 24 Q 63200 860 ttRITE 't 9j897I 63300 897 FORHATt MEASURED LEAK RATE SHONS NEGATIVE TREfS IH LAST 5

~ RW-63400 -CONTIttUE TESTING' Qp

. 63500 GO TO R4 63600 C 63700 C SUPPLE)tENTARY. TEST COMPLETION CRITERIA ADDED Q '5900 '40bO 63800 C, iS iF, tCC.AE.CSf Go TO 24 LRX2 >> 'LRX/15.57 040184 JAP 64ioo NRXTE t 9j994) TALR<<LRX>LRXk,

'4200 994 FOR)tATt///' N~SUPPLEHENTAL TEST COHPLETIOfl CRXTERIA MESSAGES 64300 -iI4'/ TYPE A LEAK ltATE - "'>09.5j',t/<<MT/DAY) IHPOSED LEAK RATE 6 644oo jF9 47 tSCFH) = jF9 4j t/HT/DAY)

...,. -,. 64500 IF tTALR.)tE.O.D) GO TO 975 646bd NRXTEt 9>976) 64700 -

I)76 NORHATt'~ NARWING TYPE h HEkSUkE6 LEkk ttATE &TIRED AS 5.0 ~

-- '64800 I)

',.',.~. ..- 64900 4)75 XP, tLRXS+ItE<<t)'D) GO T6 976-

'~

~ , ~

65000 HRITEt 9 j 977) 65100 977 FORHATt PAR)tIHG,-,IHPOSED LEER kATE k)tTEREt) AS 0+0 4~')

.-., 65200 . 975 IFtTIHEtNR)oGT+6ibo) GO TO 900

~.:;...'5300 NRITE t9j990),

,, =.

-JJ 65400

'655OO

49<<O FORHATt! TEST bURAtION ttAS

--k, TESTlki" i le NCNbE5 HIE 4 Ifk HIKIHSI -'ONT&i/

"'5600

'": '"..65700 i GO TO 24

'.-: 9Ob NRiTEi 9>9)X 49k FORHATt 'EST btJRATIOtt ttAS EdchE555 THE 5 HOUk HINIHUH i-.;

658OO

'-.."'-'6Oo'o 65)00 . , XF,tBtNR)>LT b.o) GO Td 915 ttttITE t 0>995) 66100 Y)95 . FOJDtATti. HEASUREd LEltK RAN iS ttot Jt NEGATIVE tlAL4E << CONTI)4JE AS i',.-, .';". 6620'6 -TING' I= ,-'-.;-.

'.'-"=',<<p",.i".'6300 ---

66400

AO C0i GO. T6 k4,

< LRXi 4 Tkltt t 6.0625

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APPENDIX B ILR PROGRAN VERIFICATION E.C.P. CALCULATION NO. 12-PI-06

kE.P.S.C. CALCULATION MECHANICAL. ENGINEERING DIVISION INSTRUMENTATION AND'ONTROLS SECTION KJ'.CALCULATIOINo. SHEET 1 OF TYPE PRELlmlNARY OR FINAL PLANTO-C.i~~ UNm ~~ 2 SIIBIECT /+IEIIT4CIATICIoI CDBPANY 2HOSO~ f PLYPIISaM C~Pvs c4 PRo5;Lewd CALCULATED BY N b. IRCBTAA S/EQIPe "Xl R (RSVP" CHECKED BY ~ . 43k'h <-3'/-V SUPERSEDES CALCULATION NO. <<~ '<<46 ~~ APPROVED BY FILE LOCATION" ANO DATE 3)EMONSTTEATC ABcsIrgrPc Y OC Os'orrT~rWm~

PROBLEB DESCRIPTION:

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'E.C.P. I2-PI-06 REV.I PAGEZ. OF O VERIFICATION OF'ILRT COMPUTER PROGRAM 'ILRTEST" INTRODUCTION In an effort to improve our containment Integrated Leak Rate Test (ILRT) program at the D.C.. Cook Nuclear Plant, several revisions to the ILHT Computer. Program originally identified as "CCVDRK"'/

"CCVREPT" have been implemented. I provements to tne new program include:

1. Ability to select any data interval.

2. The addition of a second hygrometric data input for the Upper Volume and Ice Condenser Compartments, thus providing redundant readings for all containment volumes.

3. Ability to "lose" a single hygrometer and/or manometer reading per containment compartment without adverse affect on leak rate calculations.

'+'ddition .of computer error messages and warning messages.

Due to these improvements the computer program has been re-named "ILHTZST" to avoid confusion bet~reen the original and revised program.

In addition to the above changes, the computer calculations for confidence limits on the final leak rate have been revised. The use of a "one-sided," confidence test instead of a "tvo-sided confidence limit test, as used in the past, vill be implemented for future containment ILHT's by the computer program "ILRTEST".

The difference betveen the "one-sided" and "tvo"sided" confidence limit tests is that in the two-sided, confidence test an upper and lover confidence limit is calculated. On that basis there is a 95 per cent confidence level that the final leakage rate (g per day) is vl'thin the upper and lover limits.

I2-PI-06 REV.1 "ILRTEST'E.C.P. PAGE.S OV Zu VERIFICATION OF ILRT COMPUTER PROGRAM than the lower confidence limit but only in the probability of the containment leak rate being greater than an allowable- value. Thus it should be realized that the lower limit is of no consequence in our particular> application and, in fact, a "one-sided" confidence test should be applied in our statistical analysis. Using the "one-sided" confidence test it is said that there exists a 95 per cent confidence level that the final leakage rate does not exceed the upper confidence limit.

It should be noted, however, that the revised program's calculations for a) processing raw data to converted and/or weighted input, b) determination of the normalized air'raction W, and c) the linear analysis are performed on the exact basis as the original n'egression ILRT. Computer program "CCVDMPT'/CC%HPT"-

As required for all AEPSC computer applications, the original ILRT computer program "CCVDHZPT"/CCVREPT", which was used during the

~~

Unit 2 Pre-Operational ILHT, was verified for accuracy by comparison to '-hand calculations." as per "..C.P. Calculation 12-Pl-06; Rev. O.

In light of the above, the verification of accuracy for computer program "ILBTEST" will be demonstrated by direct comparison to the "CCVDREPT"/"CCVRZPT" data processing and regression analysis performed for the Unit 2 Pre-Operational ILRT Supplemental Test.

The verification of the revised calculations for 95 per cent confidence limit using a "one-side" test shall be demonstrated by comparison to hand calculations.

'E.C.P. 12-PI-06 Rp(.y PAGF< OF Eu PROGRAM VERIFICATION As discussed in the Introduction, this computer verification will consist of direct comparison of the Unit 2 Pre-Operational ILRT Supplemental Test data as'calculated by the original program "CCVDBEPT"/"CCVBEPT" and the revised program "ILRTEST". The computer printouts to be used in the comparison shall be identified as reference numbers 1.1, 1.2, 1.3 and 1.4. for the revised program-and reference numbers 2.1, 2.2, 2.3 and 2.4. fo the orig-'nal program.

CONTAINMENT Tr~FZMUBZS DATA CHECK A comparison of reference numbers 1.1 and 2.1 indicated co~piete agreement in aV to F conversions as well as the determination of weighted average temperatures as. computed in in F and B values. It should also be noted that, as an added convenience, all input data on the revised program is printed out on a single page.

COHTAINMZfT VAPOR PRESSURE DATA CHECK As mentioned, in the Introduction, two additional hygrometric inputs have been added to the revised program. In order to use the Unit 2 test data as a basis for comparison the mV values from the VPU-1 and VPI-1, Upper Volume and Ice Condenser hygrometers input for 0- respectively, were repeated programs for vapor pressure as VPI-2. Complete agreement between original can be seen as VPU-2 and and revised illustrated

,in references 1.1 and 2.1.

VERIFICATION OF ILRT. COMPUTER PROGRAM "ILBTEST" CONTAINMENT PRESSURES DATA CHECK The summary of corrected average pressures, found on references 1.1 and 2.1, clearly shows no differences in the conversion of uncorrected readings to corrected as well. as averaging of redundant manometers.

RESULTS OF LINEAR REGRESSION ANALYSIS As indicated. on references 1.2 and 2.2, the revised program is in complete accordance with the original program in determination of fir al. leak rate, 'ntercept and'll calculations of'ndividua" co. partment air fractions (N) 1 as- well. as the total containment ir fraction

( i. exper.imental) .

SUMMARY

OF AVERAGES With re spec t to re fer enc e s l. 3 and 2. 3, the Summary of'verages for- both computer programs prove to be identical.

CHiCK OF INPUT DATA As shown on references 1.4 and 2.4, the "fixed" input data upon which the computer programs use to perform the RTD mV to F conversions, hygrometer mV to F conversions, manometer calibration cor-rections, temperature weighting and volume. weighting are identical.

p c p. y2-P1'-06 REY.1.

pAQE@ 0F 80 VERIFICATION OF'LRT COMPUTER FROGS "ILRTEST" UPPER CONFIDENCE LIMITS The Upper. Confidence Limits were verified by comparison to the hand calculations performed and attached herein.

A summary of the hand calculation is listed below:

RUN W (g. Wt./DAY) PER CENT No *

. HIND COMPUTER DIFFEHKlCE 1 1.00000 N/A N/A 2 1.00005- N/A N/A

. 1 00006 1..00006 0 o 99992 o 99992 0 rounded-off to nearest 10 g Wt./day RUN UPPER CONFIDENCE LIMIT PER CWT NO- HAND COMPUTER DIFFERENCE:

1 N/A N/A N/A 2 N/A. N/A N/A 3 19379 -0.19971 2.96

-0 55509 -0.55381 0-23

.0 y

~ ., yyyyQ

K.C.P. 12-P1-06 aZv,l Pace 7.0F Eo VERIFICATION OF'LRT COMPUTER PROGiM!

'ILRTEST'PPER CONFIDENCE LIMITS CONT'D.

hs can b seen in the tabularization of the hand and computer calculations for the Upper Confidence Lim't. acceptable correlation has been achieved.

CONC LUSIGI'y direct comparison of the revised ILRT computer program "ILRT=ST" to the orig" nal program "CCVDR PZ"/"CCVREPT" ~

"nd the comparison of hand calculations o computer c alculations for the "one-sided" 95 percent upper con" .

f.'dence 'iait 't has been successfully Cenonstrated that the revised progran "ILRTEST" is indeed accurate and by approval of this ".C'.P.. Calculation verified for use in all future containment Integrated Leak Bate Tests.

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E.C.P 12-P1-06 REV.I .

THE YARiA~eg OF'~ L5;. CcvC-w 8 f- ~~'

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UPPER Clm(T' -a. <@doge

AL KLAP5EO TINE S.OO COHTAI)ILEtiT TEHPERATLSES DATA CHECK UPPER VOL(I(E LOWER VOLUHE ICE CONDENSER RTO tiILLI-VOLTS DEB: Fo RTD t(ILLI-VOLTS DEG., F. RTD NILLI-VOLTS DEG F~

KTR-101 36 +99 73.98 ETR-122 45.67 91. 34 ETR-115 11.58 23.16 ETR 102 36.93 73.86 BR-123 45.06 90.12 ETR"116 lb.97 21.94 KTR-103 36. 96 73.92 FTR-124 45.25 90.50 ETR-117 13.92 27.S4 ETR-104 37.21 74.42 ETR-125 45.42 90.S4 ETR-lib 12.73 25ohd KTR-105 36.47 72.94 ETR-126 39.62 79.24 ETR-119 10 o 33 20edd ETR-106 36.88 73.76 ETR-127 38.39 76.78 BR-120 lb. 58 21.16 0 BR "107 36,74 73 hb ETR"129 37.49 74.9S ETR-121 11.51 23.02 A BR-108 36.90 73.80 KTR-130 -39.75 79.50 BR-109 37.tt 74,44 KTR-131 38.54 77+ 08 ETR-110 37.25 lb.50 BR"132 37.13 74.26 Ã ETR-111 37 13 74.26 ETR-134 30.60 77.20 Pl ETR-ut 37.47 75.34 KTR 114 37.11 74.22 KTR-135 KTR-136

38. 84 37.46 77.6b 74 92 0 KTR-ltb 35.55 71.10 BR-137 39.08 7bo16 KTR 133 36.55 73.10 KTR"138 38.11 lb.22 BR-113 38.34 74.6S BR"139 37.20 74.40 ETR-140 33.63 67.26 KTR-141 36.62 73+24 ETR-142 36.32 72.64 BR"143 34.67 49.34 ETR-144 37.11 74.22 KTR-145 38. 14 76.28 ETR-146 36.39 72o7b SQOQRT OF NEIGHTED AVERAGE TEHPERATURKS UPPER VOL(I(E (DKB. F ~ ) 74.00 LONER VOLUHE (DKG. F. 1 78.15 'CE CONDENSER (DEGo F.) 22.44 UPPER VOLLNK (DEG. R ) 533.70 LONER VOLUHE (DEGAS P.) 537.S5 ICE COHOENSER (DEG. Ri 1 482olh COHTAIti(EHT VAPOR PRE55URK DATA CHECK CONTAINMENT PRESSURE5 DATA CHECK 0 Pl t(ILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGR(ILETKR VOLTS (DEG. F. (PSIA) READIHG (PSIA) READING (PSIA) 32.80 30+10 1

0.0820 t(ANOHETER PU-1 26.5778 26.5996 Pl 9

,.vie 32.80 3D.10 0.0820 PU-2 26.0581 26.5914 26.5945 g~

VPL-1 35.74 42.04 0.1317 PL-1 26.4476 VPL-t VPI-1 39.57 29.02 57 41 14.94 0.2335 0.0395 PL-Z PI-1

" 26.6960 26.5991 26.6164 26+5944

~M VPI-t 29.02 lho 94 0+0395 PI"2 25.9021 26.6030 fsa4 AHSIFHT 14.t055 14.5146 AVERAGE VAPOR PRESSURKS UPPER CONTAI)NEHT (PSIA) 0.0820 SUttQRY OF CDRRKCTKD AVKRAGK PRES5URKS oR LOWER COHTAINHENT (PSIA) 0 1826 AVERAGE UPPER PRESSURE (PSIA) 26+5955 ICK CON)ENSER (PSIA) 0+0395 AVERAGE LONER PRESSURE (PSIAl 26.6054 AVERAGE ICE COtw)EHSER PRES5URE (P5IA) 26 5997 AVERAGE CONTAIHLLEHT PRESSURE (PSIA1 26.600Z AVERAGE CONTAIHHENT PRESSURE (PSIG) 12.0S37

l( RESULTS OF THE LINEAR REGRESSION l

TSIS H LEAKAGE RATE LEAKAGE H UPPER H LONER H ICE EXPERINENTAL UPPER LINIT RATE CONTAINHENT CONTAINHENT CONDENSER 3 1 00006 0.19971 0.13844 1.00011 0.99994 1.00006

-5 0.99992 -0.55381 -0. 11720 0.99994 0.99989 0.99985 0.99990 -Oo36695 -0.15681 0.99994 0 '9985 Oo99986 6 0.99988 "O.RS998 -0.16493 0 '9994 0.99982 0.99973 7 0.99982 -0 '6226 -0.17743 0.99989 0.99980 0.99958 8 0.99984 O.RR423 -0.16031 0.99997 0.99980 0,99943 9 0.999S3 "0.19709 -0.14649 0.99994 0.99976 0.99948 nm'A 10 0 99971 -0.20512 ll 1R 0.99965 0.99969

-0.21266 "O.R0061

-0.16210

-0.17532 0.99989 0.99982 0.99972 0.99970 0.99897 0.99888 l0 Vl p

-0.16925 0.99997 0.99969 0.99858 13 14 0.99951 0-99945

-0.2R126

-O.R3537

-0.18836

-0.20341 0.99971 0.99964 0,99964 0.99956 0.99846 0.99849

~

~ CO OO x

15 0.99949 "0+23078 -0.20327 0.99975 0.99951 0.99842 0 Pl 16 17 0.99955 0.99946 O.R1906

-0 R1339

-0.19293

-0.190R9 0+99981 0.99968 0.99950 0.99953 0.99859 0.99845 2 U FINAL LEAKAGE RATE L% PER OAT) > -,0. 1902$ INTERCEPT"-. 1.00007 UPPER CONFIDENCE LINIT FOR THE RATE IS -0+R1339

'E.C.P. 12-Pl-06 REy.l REF NO. I,Z D Q aPg

~ lQ Wo ITT 0

5QtQRf OF AVERAGES RLN ! KLAP5KD TINK AVS TKNP AVS PRK55 AVS V PRE55 AVS TENP AVS PRESS AVQ V PRK55 AVS TENP AVG PRESS, AVS V PRE55 UPPER UPPER UPPER LONER LONER LONER ICE ICE ICE 1 0.0 74. 3561 26.6254 0.0856 78.4707 R6.635R 0.1843 R2.2144 26.6298 0,0408 2 0.50 74.3350 26.6R4d 0 4852 76 4432 R6.6341 Oil838 R2.1365 R6.628S 0.0394 3 1+00 74.2957 26.6R26 O.OS31 76.4376 26.632R 0.1S44 R2.1880 26.6R6$ 0.0373 4 i+50 74.2916 26,6196 0 OS46 7$ 4133 26.6294 0.183$ 22.1995 26.6236 0.0391 5 R.OO 74 2761 26.6171 Oi082$ 76.3895 26.6266 0.1837 22.1671 26.6211 0.0363 Ql 6 74.23t4 26.6156 0.0637 tb.6252 ZR,0954 26.6197 0.0444 7 '.00 2+50 74.16td 26.6140 0.0857 Tbe3760 lb.3563 Reob237 0+1835 0.1S36 2R.1167 26.6181 0.0453 8 3.50 74.1790 tb.d131 0.0831 7$ .3526 tb.et30 0.183R 22.1902 26.6173 0.0446 Ca 9 4.00 74.149$ 26.6107 0.0627 78.316R R6.6ROT 0 ~ 1637 RR.R186 R6.6150 0.0395 Q 4 10 4.50 74o1513 26 6069 0.0823 76.3167 26.6169 0.1829 22.3961 26.6130 0.0413 11 5.00 74.1333 R6 607R 0.063R TS.R694 R6.6172 0.1831 R2.4337 26.6114 0.039S CD 12 5.50 74.0741 26.6060 0.0611 76.2669 R6.616R 0.1634 22.462S 26.6083 0+0433 13 14 6.00 6.50 74.1038 74.0515 Rb+6035 26+6403 0.4839 0.0853 78.2557 78.2331 R6.6137 R6.6145 0.182$

0.182$

22.5664 RR.4$ 3R 26.6476 26.6446 0.0400 0.040S 0

15 7.40 74 0333 R6.5970 0.0799 78.1996 R6.607R 0.1826 22.4475 26.601R 0.0412 16 7.50 74.0031 26.5967 0.0796 78. 1890 R6.6067 0.1828 22.3761 26.6008 0.0402 17 $ .00 74.0003 26+5955 0.0820 78.154T R6.6054 0.1826 RR.4391 R6.5997 0.0395

'E.C.P. I2-PI-06 REV.1 REF NO; /'5 0 ~

~~n Pl Q 0lo cn

i +<<~ THIS IS A CHECK OF~INPUT OATA ++~

RTO tlILLI-VOLTTO FAHREQIKIT CONVERSION COEFFICIENTS UPPER LONER ICE tooo 0~0 Rooo 0 0 2 ~ 00 0~0 HT6ROHETER NILLI-VOLTTO FAHREQIEIT CONVERSION COEFFICIENTS UPPER-1 LONER "1 ICE-1 O.DDRR7 3.87667 99.4'9390 0.00234 3.86672 -99.14546 0.00192 3.90355 -99.95728 UPPER-2 LOHER-2 ICK-2 D.DDR27 3.87667 -99.49390 0.00277 3.83471 -98.67056 0.00192 3 90355 -99.95728 HAHOHKTKR PRESSURE CORRECTION COEFFICIENTS PU-1 t7 9573 t7.9346 t7.458D 27.4347 Rd 9581 R6.9376 26 4596 26.4373 25.9603 R5.9388 PU"2 t7o 9573 R7 4035 27oh580 Rd ~ '9099 Rdo9581 R6e4208 26 ~ 4596 25 9277 25 9603 25o4322 PL-1 t7 9573 27 8136 27,4580 R7 3102 26,9581 26.8110 Rd 4596 26 31Rb R5.9603 25.8090 PL-2 t7 9573 tb.oRbb t7.4580 27.5317 26.9581 27.0359 26.4596 26.5400 2$ .9603 R6.04R7 PI"1 27o9573 R7 9575 27oh580 27e4606 26 ~ '9581 R6 ~ '9630 26+4596 Rd 4614 R5 9603 R5 9613 PI"2 t7 9573 t7.R318 27 4580 26.7394 R6.9581 26.2529 26.4596 25.7604 R5.9603 25.R719 P-ATH 16,4746 lb.1106 14.9769 14.6549 13 4792 13.19R8 11.9815 11.7310 10.4838 lb.2681 RTQ HEI6HTINS FACTORS UPPER

.Odtb .1161 .O831 .O831 .O96O .O96O .O96O .O96O .0296 .O296

~ DR96 ~ DR96 ~ 0740 ~ 0105 ~ 0167 ~ 0513 LONER

,0415 .0415 .0415 .0415 ~ 0102 ~ 0284 ~ 0586 ~ DD86 ~ 0266 ~ 0586 1037

~ 1037 10'37 o 1037 ~ 0500 +0092 .0244 0145 +0170 ~ 0249 .0219 ~ 0240,0423 .0 ICE

~ 0750 ~ 0750 ~ 0725 o0725 .RR13 .R766 ~ 2071 E.C.P. 12-PI-OG BEY.1 VOLQR MKI6HTINB FACTORS aeF NO. l.~

UPPER LONER ICE 2.0144 1 ~ 0000 0.4559

l R 'R KLAPSEO TltlE 17 8.00 CONTAlttttENT TEttPERATURES DATA CHECK UPPER VOLUttE LONFR VOLUt(E ICE CottOEttSER RTO ttILLI "VOLTS DEG. F ~ RTD ttILLI-VOLTS DEG. F. RTD t',ILLI "VOLTS DEG.

KTR"101 36>>99 73.98 ETR" 122 45.67 91.34 ETP.-115 11.58 23.16 KTR 102 36 '3 36.96 73.86 73.92 ETR-12.3 45.06 90.12 ETR-116 BP.-117

10. 97

13. 92

21. 94 27.84 KTR-103 ETR-124 45.25 90.50 ETR-104 37.21 74.42 ETR-125 45.42 90.84 ETH-lib 12.73 25.46 ETR-105 36>>47 72>>94 KTR-126 39.62 79.24 ETR-119 10. 33 20.66 BR-106 36>>88 73.76 BR-127 38>>39 76.70 ETR-120 10.58 21.16 ETR-107 36. 74 73.48 KTR-129 37.49 74.98 KTR-121 11.51 23.02 F TR-108 36. 90 73.80 ETR-130 39. 75 79.50 BR"109 37.22 74.44 BR-)31 38.54 77>> 08 ETR-110 37.25 74.50 ETR-132 37 13

~ 74.26 ETR "111 37. 13 74.26 ETR-134 38>>60 77.20 KTR-112 37>>67 75.34 KTR-135 38.84 77.68 KTR-114 37.11 74.22 ETR-136 37.46 74.92 ETR-128 35.55 71.10 ETP. 137 39.08 78.16 KTR-133 36.55 73>>10 ETR-138 38.11 76.22 KTR-113 38.34 76.68 KTR"139 37.20 74>>40 ETR-140 33.63 67.26 ETR "141 36.62 73. 24 ETR-142 36.32 72.64 ETR-143 34.67 69. 34 BR-144 37.11 74.22 ETR-145 38.14 76.28 KTR-146 36.39 72.78 SUtttQRY OF HEIGt(TED AVERAGE TEttPERATURES

/

UPPER VOLE%K (DEG>> F ~ ) 74 ~ 00 LONER VOL(R(E (DEG>> F ~ ) 78>>15 ICK COttOKttSER (DEG. F.) 22.44 UPPER VOLUttK (OEG R ) 533.70 LOHER VOLUt(E (DEG. R>>) 537.S5 ICE CONDENSER (DEG. R.) 4S2.14 p, E P,g.C.-M.E.D.

PQQ.

any 'j977

~

mL.U U l 8 C SECTION

(7 COHTAIHttEttT VAPOR PRESSURE DATA CHECK COtfTAlttltittf PRESSURES OATA CllECK t)ILLX" OB) POItlT VAPOR PRESSURE UttCORRECTCO CnnRECTEO NYGROttETER VOLTS lOEG. F. ) lPSZA) tlAt10llETER READING lPSIA) REAOIH~ lPSIA)

VPU-1 32.80 30.10 0.0820 FU-1 26.5778 26.5996 VPL-1 35.70 42. 00 0. 1317 PU-2 26.0581 26.591%

VPL-2 39.57 57.41 0.2335 PL-1 26.6%76 26.5995 VPI 1 29.02 1%.9% 0+0395 Pl.-2 26.6960 26.6160 PX-1 26 5991 26.596%

PX-2 25+9021 26.6030 SUttttARY OF VAPOR PRESSURES AttBIEHT 1%. 2055 14.5166 UPPER COHTAItOENT OPSIA) 0 0820 AVERAGE LONER COHTAINttEHT (PSIA) 0 ~ 1826 SUttttART OF CORREC/ED AVERAGE PRESSURES ICE CON)ENSER (PSIA) 0.0395 l AVEPAGE UPPER PRE5Sl!RE lPSZA) 26.5955 AVERAGE LONER PRESSURE lPSZA) 26+605%

AVERAGE ICE COtQE)tSER PRESSURE lPSIA) -26.5997 AVERAGE CONTAIHttENT PRESSIVE lPSIA) 26.6002 CONTAIH11EHT PRESSURE t PSZG), 12.0837

'E.C.P. 12-P1-06 REV.l AVERAGE

.REF No. 2+i

~

~m Pl 0

~l1 lQ0

> a)

~No

( N RESULTS OF THE LINEAR RKGRESSION LEAKAGK RATE

( SIS TEST LKAKAGE LEAKAGE RATE . N UPPER N LONER N ICK EXPERINENTAL LONER LINIT RATE UPPER LINIT CONTAINNENT CONTAINNENT CONDENSER 3 1,00006 0.54203 0.13844 0.61890 1.00011 0.99994 1.00006 4 0 ~ 99992 -o.7eoeo -0.11720 0.52620 0.99994 0 ~ 99989 0.99965 5 0 99990 0.44096 O. 15661 0.12736 0,99994 0.99985 0.99966 4 0 '99968 0.32775 -0 16493 F -0.00212 0.99994 6.99982 0.99973 7 0 ~ 99982 -0.28566 -0. 17743 0.06920 0.99989 0 99980 0 ~ 99956 6 0 '9984 -0.24OSl -0.16031 -0 07981

~ 0 ~ 99997 0.99950 0 ~ 99943 9 0 99983 >>0 20964 "0.14649 -0.08334 0 99994 0.99976 0.99948 10 0.99971 <<0.21543 -0.16210 0.10677 0.99989 0.99972 0.99S97 11 o.999es 0.22139 "0.17532 -0. 12925 0 99962 0.99970 0.94668 12 0.99969 -0.20781 -0.16925 -0 13069 F 0.99997 0.99969 0.9985S 13 0. 99951 -0.22866 -0.16S36 -0 14SO4

~ 0.99971 0.99964 0.99846 14 0.99945- -0.24249 0 ~ 20341 -0.16433 0.99964 0.9995re 0.99849 15 0.99949 "0.23682 -0.20327 0.16973 0.99975 0 99951 0.99842 14 0.99955 -0.22475 -0.19293 -o.lello 0. 99961 0 ~ 99950 0 ~ 99859 17 0.99946 "0.21837 -0.1902$ -o.le222 0 ~ 9996S 0.99953 0.99845 FINAL LEAKAGE RATE (X PER OAT) > -0 ~ 19029 INTERCEPT> 1.00007 FINAL CONFIDENCE LINITS FOR THE RATE ARE 0 ~ 21S37 $ 0 -0.16222 5<('P4wC~Q 7<st .

)coach.Jeicgl 9's get

! Zca CaHaes>ML.

E.C.P. 12-P1-.06 BEY.1 l'EF fio. 2.2 0

~~"nil NrJ< 3 'p7 l 6 C GEUTlOI'f

fh SUktNARY OF AVERAGI (

RUN 0 ELAPSEO AVG TEMP AVG PAE$ 5 AVG V PRESS AVG TENP AVG PRESS AVG V PRESS AVG TRAP AVG PRESS AVG V PRESS TltiE UPPER UPPER UPPER LONER LoffER LoffER ICE ICE ICE 1 0.0 74. 3581 ts.sR54 0.0856 78.4707 26.6'352 0.1843 22.21OO 26.6R98 0.040$

2 0.50 74.3350 26.6246 0.0852 7S.4432 26.6341 0.1838 22.1365 Rs.saee 0.039%

3 1.00 74.R957 26.622S 0+0831 78.4376 26.6322 0.1844 22 lobo Rs.sase 0.0373 4 1.50 74.R916 26.6196 I6 2+00 2.50 74.2781 26.6171 0,08446 0+0828 7S.4133 7S.3S95 26.6290

~ .6.6266 0.183$

0.1037

22. 1995 RR. 1671 RS'6236 26.6ill 0.0391 0.0383 74.t324 26.6156 0.0837 7$ .3780 R6.6252 0.1835 22.0954 26.6197 0.0444 7 3.00 74.18R6 26.6140 0 '857 7$ .3563 26.6237 0 '836 RR.1167 26.6181 0.04453 8 3.50 74.1790 R6.6131 0. 0831 78.3526 as.saio 0.103R 22. 1902 26.6173 O.O4'Is 4.oo 74+1498 26.6107 0.0027 7$ .3162 26.6207 0.1837 22.2)86 26 6150 0.0395 10 4.50 74.1513 26.6089 ll lt 5.00 74.1333 26 '072 O.OSR3 0.0832 78.3167 78.2894 26.61S9 26.6172 0.1829 0.1831 22.3'?61 22.4337 26.6130 26.61 lr4 0.0413 0.0398 5 50 74.0741 26o6060 O.obli 78.2669 26.616R O.1834 R2.4628 26.6083 0.0433 13 6+00 74.1038 R6.6035 0 0839 78 R557 .26.6137 0.18th ERE 5664 26.6076 0.0400 14 6.50 74.0515 R6.6003 0.0853 70.2331 26.6105 0.18RS 22.4S32 26.60416 0.040$

15 7.00 74.0333 a6.597o 0 ~ 0799 78.1996 26 '07R 0.1826 22.4475 26.6012 0.041R 16 7.50 74.0031 26.5967 0 0796 78. 1890 26.6067 0.1828 22.3761 26.6008 0.04 02 17 8.00 74.0003 26.5955 0.0820 ~78.1547 26.6054 0.1826 22.4391 26.5997 0.0395 E.C.P-. I2-PI-06 REV.1 REFyo gp A.E.P.S.C.-+.E.D.

PfjQPPfl g liOv 3 19l?

) K C SEC7~~~>>

%I ~ ~ ~

+>>N THIS IS A CHECK CF'PUT DATA RTO llILLI-VOLTTO FAHRENHEIT CONVERSION COEFFICIENTS UPPER LOWER ICE R 00 0 0 R.OO 0.0 2.00 0.0 NYGWKTER MILLI-VOLTTO FAHRENHEIT CONVERSION COEFFICIENTS UPPER LOWER-I 0.00227 3.87667 -99 49390 0.00234 3.86672 -$ 9.i4546 LOWER-2 ICK 0~00277 3.83471 98.67056 Oo00192 3.90355 -99.95728 NANOHKTER PRESSURE CORRECTION COEFFICIENTS PU-1 27.9573 R7.9346 27.4580 27.4347 Rd.9581 R6.9376 R6.4596 R6.4373 25.9603 25.9388 PU-2 27 9573 27.4035 27.4580 R6.9099 26 '581 26 4208 R6 4596 25.9277 25.9603 25.432R PL-1 27 9573 27.8136 27.4580 27.3102 26 ~ 9581 R6.8110 26,4596 26.3128 25.9603 25.8090 PL-2 27+9573 28.028b 27.4580 R7.5317 26.9581 27.0359 26.4596 26.5400 25.9603 26.0)27 PI-1 R7 9573 t7.9575 R7,4580 27 4606 26.9581 26.9630 26.4596 26.4614 25.9603 R5.9613 PI-2 R7.9573 R7.2318 27.4580 R6.7394 26.9581 25.R529 26.4596 25.7604 25.9603 25.2719 P-ATN ~

16.4746 16.1106 14.9769 14.6549 13.4792 13.19R8 11.9815 11.7310 lb.4838 lb.2681

QTO ! fACTORS UPPER

~ 0620 ~ 1161 o0031 .Ob31 .0960 .0960 .0960 .09&0 .0296 .0296

~ 0296 .0296 0740 .0105 ~ 01&7 ~ 0513 LONER

~ 0415 ~ 0415 .0415 .0415 .0102 .0204 .0506 0086 .0266 .0506 .1037 gl037 1037 .1037 .0500 0092 .0244 .0145 .0170 .0249 .0219 0240 .0423 0 ICE 0750 .0750,0725 0725 2213 .2766 .2071 VOLUtff NKI6HTIHQ FACTORS UPPER LONER ICE ~

2.0144 1.0000 0.4559 A,P.P.S.C;M.E.D.

O'PQQPllfl l1 u iqiJvs in

~ c T=i '1 t~"'

Pl O

Pl 6 5 o CA Pl

12-Pl-06 REV.l PAGESoOF ~0 VERIFICATION OF ILRT CO%'UTER PROGRAM "ILRTEST" E.C.P. 12-Pl-06 Rev. 1 REFERENCE NO. 3 ILRTEST PROGRAM LISTING

ANKRICAH KLKCTRIC PORE) VICK CORPORATION CONPUTER APPLIC)TIONS DIVISION

)SR>>ILRTKST Ol/14/75 LIB*>>>>k>>>>>>>>>> SOURCE LIBRARY OUTPUT 05/R3/70 10 50 45 PAGE ODOR ooolaa ZNPLZCIT REAL>>bt A-H)P>>7) >>>> 01/27/70 000200 REAL>>b K)LVP 02/02/70 000300 DINEHSIOH TENPUC( lb ) e TKNPLCt 24 ) ) TKttPZCl 7) kk 01/RT/78 000400 DZNENSIDH TKNPU( 16 ) i TENPL(24 ) ) TEt(PI(7) kk 01IR7!70 A.E.P.S.C:M.E.D. 000500 DATA LUC ~ LLC) LIC/lb)R4) 7/ 01/RTITS oooeoa DINENSIDH RTDL1(16) )RTDLRt 24) )RTDL3(07) >>>> 01/27/78 000700 DATA RTDLl/'ETR-101 ETR-10R e ETR 103 t ~ ETR-104

! ~ 'ETR 105! >>k 01/27/70 000800 'ETR-106 't'ETR-107 '-t 'ETR-108 ETR-109 ' 'ETR llo!e lilt 01/27/70 blQ'5 l918 000900 'KTR ill ' 'ETR-llR '- ~ 'ETR-114 ' 'ETR-120 ' 'KTR-133 'ETR-113 kit ol/27/70 001000 k DATA RTDLR/ ETR 122 ~ ) ETR 123 .

) ETR 12 t t ETR 125 t 'ETR 126 >>>> 01/27/70 D01100 'ETR-127 'e'ETR-129 'e'OR-130 ')'ETR-131 'ETR-13R 'e 01/27/70 RlhU U 001200 001300 k

! ETR 134 ! t! ETR 135 ! ) 'ETR 136 ! ) 'KTR 137 ! )! ETR13S !

'ETR"13$ ' 'ETR-140 '<<'ETR 141 ' 'KTR 142 ')'KTR"143

>> et 01!R7!70 01'/RT/70

> 8 C SSCnON 001400 FTR 1 t4 ) ETR 1 t5 ) .OR 146 ) KTR 113 / etll 01/27!78 001500 DATA RTDL3/ ETR 115 ~ ETR 116 e ETR 117 ETR llS t ETR 119 >>>> 01/27/70

/

~

OD1600 ETR 120 j KTR 1Rl >>>> Ol/R7/70 001700 DINKHSION HUCt 99) )HLCl 99) )HIC(99) )H(99) e TINE(99) )NRA(99) e k>> 01/27/70 oolbao ATUC('99) )APUC(99) )AVPUC(99) )ATLC(99) <<APLC(99) )AVPLC(99) ~ Dl/27/70 001900 - ATIC(99) )APZC(99) )AVPIC(99) k>> 01/R7!70 DOR000 DZNENSZON K(10))SR(70) )DP(6) )LVP(6) )PRES(7) <<PRESC(7) )VPR(6) Ilk 01/27/70 OOR100 II DINEHSIDH HTUP(16))HTLOH(24) )HTICE(7) )TABLE(97) lt et 05/23/70 002200 k DATA TABLE /6.314)2.9RO)R ~ 353t2.13R)2.015)1.943)l.S95)1.860)l)833) >>ll 05!23!78 002300 1 812tl 796)1,782 1 771)l 761)l 753)l 746)l 740 1,734 ~ 1 729)l 725 >>lt 05/23/78 E.C.P. 12-PI-06 REV 002400 l. l. l. l. l. l.

"1.721 e 717) 714 ) 1 ~ 711 e 70S) 706 ) 703) 701 e 1.699) 1.697) 1.695 >>lt 05/23/78 tt>> 05/R3/70 1 002500 4

'1.694;1.692)1.691)1.689)1.688)1.607)l.ebe)i.e85,1.684,1.603,1.682, REF hfo. 002600 DOR700 lt 1 eblel 680)l 679 1 679)l 67S 1 677)l 676)l 676)1,675 "1.673)1.673)1.672 1.672)1.671)1.671 1.671)1.670 1.670 1.669 1.669 1 675)l 67t ~

>>k 05/R3/78 05/23/78 002000 1 669)3>>1 668)3>>1 667 3>>1 666 $ >>1 665) t>>l 66 t 5>>1 663 5>>1 662) Ilk 05/23/70 002900 "5>>1.661/ >>>> 05/23!78 ao3aaa DATA HDUP !NOLO<<HDIC/'UPPER ' 'ONER ' 'CK '/ II>> Dl/27/TS 003100 >>C START OF PRDGRAN 01/27!78 003200 Z=l 01/27!70 003300 DLGIOO k OLOG10(1013.246DD) 01/27/70 003400 OLGO e<<DLOGlal6.107100 t 01/R7/70 003500 HOKN

0.0 ORIR2/78 003600 READ (5)300 ~ ERR=2R)KND"-12) Cl)CR)C3)C4)C5)C6 ~ IXS ~ IXK)IPR 01IR7/78 003700 30 0 FORNATt6F6.3)4X)I3)7X)I3)7X)I3) 02/RR/78>>k 02/RRITS 0 W 003800 Ik 2 tl>> 01/27/70

~~o 003900 READ (5)301)ERR=RR)END=12) K tl>> 01/27/70 004000 30 1 FDRNAT(6Fll 6/6F11.6/6F11.6) >>>> 01/R7/70 Pl 0 004100 I =3 II>> ol/R7/70 004200 READ (5)302)ERR"-22)END=lR) SR 01/2T/70 004300 >>302 FDRNAT(10FS.S/laFS.S/lOFS.5/10F0.5/1oF8.5/lOF0.5/lOF0.5) kit 10/R4/77 004400 lt I"-4 k>> 01/R7/70 c) IQ 004500 READ t5)303)ERR=2R)END=12) HTUP)HTLOM)HTICE >>It 01/27/70 004600 >>303 FORNAT(10F6.5/6F6.5/11F6.5/13F6.5/7Fb.s) >>lt 10/18!77 004700 I=5 II>> D1/R7/70 OO48OO READ (5,304,ERR>>22,END=lR) VHFl,VHF2 VHF3 >>It 02/DR/70 004900 >>304 FDRNAT(3F7.5) k>> 10/18/77 CA 005000 k HRITK (6 3051 Cl)CR C3 C4)C5)C6 K(l) K(R))K(3) K(7) KtS) K(9) >>>> 01/27/70 m 005100 005200 -

K(13) )K(1 t))K(15) )K(4) )K(5) <<K(6))K(lo))K(ll))K(12) ~

K(16))K(17) <<Kt 10))SR

>>lt 01/27/70 01/R7/78 fll 005300 >>305 FORNAT(lH1)44X) '>>>>>> THIS IS A CHECK OF THE IHPUT DATA>>k>>'/I//1H ~ >>et 10/10/77 005400 'RTD NZLLI"VOLT TO FAHRENHKZT COHVERSZOH COEFFICIKNTS'/1H )6Xt 10/10/77 005500 'UPPKR'lRX) 'LONER')13X 'ICE'/1H F5.R)3X F5.R)4X)F5.R)3X k>> 10/10/77

l 'I

~ST Ol/14/75 LIB<<aaa<<<<<<<<a SOURCE LIBfc OUTPUT 05/23/7S 1Q,58,45 PAGE 0 005600 % F5 t>>4X>>f5 2 ~ 3X>>F5@2 ///1H t HTGRONETER NZLLI VOLT TO t <<,% lo/ld/77 005700 % FAHREHHEIT CONVERSZOH COEFFICIENTS /1H t T15t UPPER 1 >>T48>> aa Ol/27/7S 005800 % LONER 1 t Tdt ~ ICE 1 /1H ~ 9(Flo ~ 5 ~ 1X)//1H>> T15>> UPPER 2 >>T48>> aa 01/27/78 0059QQ LONER 2>>T82 ~ ICE 2 /1H ~ 9(Flo 5tlX)////1H ~ NANONETER PRESSUR <<<< Ol/27/78 006000 % "E CORRKCTIOH COEF('ICIENTS'/T40) 'PU-1'/10(lX>>F7.4)//1H 38X <<a 02/Dt/78 006100 % PU 2 /1H ~ 9(F7.4>>ZX)>>F?.4//IH>>3SX>> PL 1'/1H>>9(F7 4>>lX)t <<a 10/24/77

'E.C.P. 12-Pl-06 REV.l OO620O % F7.4//1H >>3SX,'PL-2'/1H,9(F7.4>>lX),F7.4//1H>>3SX 'PI-1>>/ <<a 10/24/77 006300 tt 1H >>9(F7.4>>lX) >>F7.4//ZH>>38X>> 'Pl-2'/1N>>9(F7.4>>lX)>>F7.4// <<a 10/24/77 REF NO. B OO64OO % 1H t 38X>> 'P-ATN'/1H ~ 9( F7.4>>1X) t F7.4) aa 10/24/77 OO6SOO % NRITE (6>>306) NTUP NTLON ((TICE>>VWFl>>VMF2>>VNF3 <<a 01/27/78 006600 a 306 FORNAT( 1H ~ RTD KEIGHTING FACTORS /1H ~ 27Xt UPPER /1H>>9( F5+4>>lX) ~ aa a

Ql/27/78 006700 F5 4/1H t5( F5A>> 1X) t F5 4//1H ~ 27Xt LONER /1H >>10( FS 4>>lX) ~ 10/18/77 006800 a F5.4/1H>>12(F5.4>>lX)>>F5.4//1H >>28X>>'ICE'/lH >>6(F5 4>>lX)>>F5.4// aa 10/1S/77 006900 a //1H>> 'VOLUNE NEIGHTING FACTORS'/1H>>1X>> 'UPPER'2X>> 'LONER' 3X>> aa 10/18/ll 007000 a 'ZCK'/1H >>2(F6.4>>1X) >>F6.4) <<a 10/1S/77 007100 % IF (IXS.LE.O) IXS > 1 aa Ol/27/78 007200 % IF (IX/.LE.O) IXK = 999 02/22/78<<a 02/22/78 007300 a IF (NTUP(16).LK.O.O) 60 TO 701 <<a Ol/tl/7S 007400 a LLC

23 <<a 01/27/78 007500 a 60 TO 702 <<a Ol/27/78 007600 % 701 LUC < 15 Ma 01/27/75 007700 % 702 NR a 0 <<a 02/02/75 007800 % LICPl -" LIC 0 1

<<a Ql/27/78 007900 % LUCPl "- LUC + 1 aa Ol/27/78 008000 <<C NR IS STORA6E I)E)EX>>PROGRAM DA/A ACCFSS LOOP STARTS HERE. aa Ol/27/78 ODS100 % DO 20 IR < 1 ~ 99 aa Dl/27/75 008200 % IBYP i0 <<a 01/27/78 OOS300 a READ (5>>100 ~ ERR=42>>END=32) NRD>>TINER aa Ol/27/7S 008400 % 100 FORNAT(I3>>1X>>F5.2) 02/22/ 78<<%.02/22/75 008500 <<C IHPUT SE((UENCK CHECK 008600 % IF ()N(.E().O.OR.NRD+GT.NRO) 60 TO 703 008700 a MRITK llD>>901) IR>>NRD 008800 % 901 FORHAT (lHO>>2X>> 'ILR005I D INCORRECT DATA SEQUENCE'2XtI2 ~ 2X>>l3) 02/24 008900 a GO TO 23 <<<<01/27/78 009000 a 32 IF (IPR.NKo0) 60 '$0 40 aa Ol/27/7S 009100 a ZPR -" 99 <<<< Ol/27/7S 009200 % GO TO 55 aa Ol/27/7S 009300 a 703 NRO "NRD- <<a Ol/27/7S 009400 a IF (NRO.GT.IXE) 60 TO 32 <<a Ol/27/78 009500 tt IF (NROoGE IXS) 60 TO 705 <<a Ol/27/78 009600 0097DO a

% IBYP GO TO 707 1 <<a aa Ol/27/78 01/27/78 0 pl 009SOO a 009900 %

010000 %

705 IF (NRO.EQ.IXS) TINEST "

NR "-HR TINE(NR) > TINER

+ 1

-TINKR FINEST aa a<<

aa Ol/27/7S 02/02/75

~p Pl 0 1

Ol/27/7S 010100 % NRA(NR) t>> NRD <<a 01/27/7d Lb 010200 % 200 FORNAT(lHlt'RUN Mt(BKR'X Z3/1H TINE'X>>F5 2///IH re M 010300 %

010400 %

~ 'KLAPSED

'CONTAINNKNT TENPERATURES DATA CHECK'//1H >>7X>>'UPPER VOLUNE' 21X>> LONER VOLUNE >>19X>> ICE CONDENSER'/1H>>3X>> 'RTD>>2X>>

~ 02/22/78<<%

a>>

<<a 02/22/78 10/18/77 10/24/77 gQ 010500 % 'NILLI-VOLTS' 2X>> 'DEG. F ~ '7X>> 'RTO'2X>> 'NILLI VOLTS'2X>> <<a 10/18/77 010600 % 'DEG. F.'X>>'RTO'>>2X 'NILLI-VOLTS'X 'DKG. F.') <<<<10/18/77 010700 a 707 RKAD (5>>lol>>ERR"-42>>END"-62) TENPUC <<a Ql/27/75 010SOO % 101 FORNAT(lo(F5.t tlX)/6(F5.2>>lX) ) <<a 10/18/77 010900 % READ (5>>102>>ERR=42>>END-"62) TENPLC <<a Ol/27/78 011000 % 102 FORNAT(ll(F5.t >>lX)/13(F5.t >>lX) ) <<a 10/24/77 011100 a READ (5>>103>>ERR 42>>K)I 62) TENPIC aa Ql/27/78 OlltDO a 103 FORNAT(7(F5.2>>lX) ) aa 10/18/ll 011300 a IF (IBYP.K().l) 60 TO 45 aa 01/27/75

T 01/14/75 Llb=<<~~~~>> SOURCE LZSh. PUT 05/23/78 10.55.45 PAGE 0 011400 T)ISNJC "-0.0 IIII 01/27/75 011500 VHAC "- 1.0 ll% 01/27/78 011600 DD 400 JAHl=lyLUC Nlf 01/27/78 011700 A = TBIPUC(JANl) NN 01/27/78 011800 IF (A.LE.O.O) 60 TO'801 01/R7/75 011900 A = GINA 0 CR lilt 01/27/78

'E.C.P. 12-PI-06 REV.1 olR000 TtISNJC < TIISNJC + A~HTUP(JAHl) NN 01/27/75 012100 60 TO 400 Nlt 01/27/78 REF NO. OIRROO 801 VMAC < VHAC - HTUP( JANl) Ng 01/R7/75 012300 WRITE (10~902) HRDsHDUPoJAMl NN 01/R7/78 O124OO 902 FOR)(AT tlHO 5X 'TEIIPERATURE t(ISSZHG'yRX I3 RX ASTIR) 02/22/75~a 02/RR/75 01R500 400 TEIIPU(JANl)

A %lt 01/27/75 01R600 NC ADJUSTtlENT FOR tlISSZHG TEtlPERATURE 01/27/75 012700 IF (VHAC.EQ.I.O) GO TO 709 NN 01/27/75 012800 T)ISIIJC > Tt(SNJC/VHAC Nlb 01/27/78 01R900 VHAC ~ 1.0 %If Ol/R7/78 013000 709 Tt(SIILC > 0.0 %lt 01/R7/75 013100 DO 401 JANR=lyLLC 01/RT/75 013ROO A = TEtlPLC(JAHR) 01/27/78 013300 IF (A.LE.O.O) GO TO 803 Nlf 01/27/78 013400 A > C3~A t C4 %lf 01/27/75 013500 TNStlLC " f

-Tt(SIILC A+MTLON(JAM2) 01/27/75 013600 60 TO fol NN 01/27/75 013700 803 VNAC "- VMAC - NTLOM(JAM2) 01/R7/75 013500 WRITE (lo>902) HROyMDLOe JAH2 II% 01/27/78 013900 401 TEtIPL(JAN2) -"A NN 01/27/78 014000 IF (VMAC.EQ.leo) GO TD 711 %II 01/27/75 014100 TtIS)ILC "

-Tt(SIILC/VHAC 01/27/78 014200 VMAC ~ 1.0 NN 01/R7/75 014300 711 TIISIIZC = 0.0 01/27/75 014400 DO 402 JAH3=1iLIC NN 01/R7/75 014500 A -" TEtlPIC(JAN3) tt l0 01/27/75 Illa'I%

014600 IF (A.LE.O.O) 60 TO 805 01/27/78 014700 A > CS<A + C6 NN 01/27/75 014800 TNStlIC = TtlStIIC t A~NTICE(JAH3) Nlt 01/27/78 014900 60 TO 402 IIII 01/R7/75 015000 805 VMAC > VMAC - HTICE(JAH3) 01/R7/75 015100 WRITE (10>902) NRD>HOICK JAN3 01/27/75 015200 402 TEtlPI(JAN3) > A 01/R7/78 015300 015400 +C 015500 IF (VHAC.NE.1.0) TIISIIIC > Tt(SIIIC/VNAC CONVERT TO ASSOI.UTE TIIStlJR -" Tt(S)IUC t 459.7 01/R7/78 01/27/78 01/27/75

~pU 015600 TtlSHLR = T)ISIILC p 459 7 01/RT/75 015700 015800 +C 015900 TIISIIZR TtlStlIC + 459.7 PRIHT CONTROL IPR 0=LAST DHLTo H=H THRU LAST IF (IPR.EQ.O.OR IPR.GT.NRD) 60 TD 45 SIN NN 01/27/78 ol/R7/78 01/R7/75 L~

o>

016000 55 WRITE (6 ~ 200) NRDiTItIER %II 01/27/78 016100 DD 500 IHRT"-1 ~ LIC IIII 01/27/78 016200 500 HRITE (ee501) RTDL1(IMRT)yTEIIPUC(IHRT) sTEIIPU( ZHRT) e NH 01/27/78 016300 RTDL2(IHRT) s TEtlPLC(IHRT) y TEIIPL( IMRT) y 01/27/78 016400 RTDL3(IHRT)iTEtlPIC(IHRT)oTEIIPI(IHRT) NN 01/27/78 016500 501 FDRNAT '(lH tASeRXtR(f6 ~ 2)5X)>AS>RX>2(F6 ~ Ry5X)sAS ~ RXsF6 ~ RI5X>F6 ~ 2) It% 01/27/75 oleeoo DD 50R INRT=LZCPly LUG N1 01/27/78 016700 502 MRITE (6 ~ 503) RTDLl( IHRT) y TEtlPUCt IHRT) i TEI(PU( IMRT)t N% 01/R7/75 olesoo RTDLR(IHRT)y TEIIPLC(INRT)) TEIIPL(INRT) NN 01/27/78 016900 503 FOR)(AT (lN uASyRXsR(F6 ~ Rs5X)sASyRX>F6 ~ 2y5Xyfe R) Ol/R7/78 017000 DO 504 INRT<LUCPlyLLC Nll 01/27/78 017100 504 WRITE (6 >505) RTOLR(INRT) o TEIIPLC(IHRT)iTEIIPL(IWRT) Nlt 01/R7/75

4 Dl/14/75 LI8>>>>>>%%>>>>>><<

'l'OURCE T LIbh. 05/R3/78 10.55.45 PAGE 00 011too 505 FDR((AT (lH 32XsAS,RX,F6.to5XoF6,2) <<>> Ol/27nb 017340 l(RITE (6>507) Tt(S(NC~THS)(LCyTHS(IICyTt(StNRoTHSt(LRsTt(SHIR %>> 02/02/14 411400 547 FORHAT (1H->>17X>'SUNIARf OF WEIGHTED AVERAGK TKHPERATURKS'//1H >>>> 02/DR/15 017500 UPPER VOLUHE (DKG F ) pF5 tyRXy LOWER VOLUHE (DE6 ~ F ~ ) <<>> 02/02/75 O116OO F6.tyRXy'ICK Cott)ENSER (OEG. F.) 'gF5.2/1H >>>> 02/02/75 C/ 017700 'UPPER VOLUt(E (DEG. R.) '.yF6.2>RXy'LOWER VOILNE (DEG. R.) ~

I <<>> OR/OR/75 017500 F7 ~ RyRXy ICE COHOENSER (DEGo Ro l > t F7+2? %>> 02/02/75

'E.C.P. 12-Pl-06 REV.1 017940 IF (IPR.EQ.99) 60 TO 35 <<>>'l/27/78 REF NO. 3 016000 015100 018200 45 READ (Si509eERR~RtsttQ"-62) VPRliVPRtiVPR3gVPRReVPR5~VPR6tPRES 549 FORt(AT (6F6+3/TFS+5)

IF (ISYP.ECt.l) 60 TO Ro 01/27/75 Ol/27/75

>>>> Dl/R7/18 018300 DP(1) i'((X)>>VPRX>>VPRX y K(e)>>VPRl t K(3) %<< 01/27/75 01840 D DP(Rl > K(4)>>VPR2>>VPRR + K(5)>>VPRR t Kl6) %>> 01/27/78 018500 DP(3) < K(1)>>VPR3>>VPR3 t K(S)<<VPR3 t K(9) <<>> 01/RT/78 015600 DP(4) >>K(lo)>>VPRR>>VPR4 g K(ill<<VPR4 KllR) t >>% Ol/27/74 018700 DP(5) <K(l3)>>VPR5>>VPR5 t K(14)>>VPR5 t Kll5) <<>> 01/R7I75 018800 DP(6) <K(16)>>VPR6>>VPR6 + K(11)>>VPR6 t }(lib) <<>> Ol/27/71 015900 D0 403 J>i>4 <<>> Ol/RTITS 019000 IF lDP( J) ~ LK~ 0 ~ 0) 60 TO 403 <<>> 01/2,7/75 019100 CIOOC a 373. 16/l (0 P( J )-32. )/1 o 4 p 273. 16 ) %>> Ol/27/75 019200 LVP(J) i -7.90295%(CIDOC - 1.0) t 5 02808>>DL0610(CIOOC) t DL6IDO

)- %>> 01/R7/75 019300 019400 019500 403 CONTINUE

-1.3516>>(10>>>>(-7.0) )>>(10<<>>(11.344<<(1.0-1.0/CIDOC) tb.1328>>(14%>>(-3.0))>>(10>>>>(-3.49149%(CIODC - 1,0) I- 1.) I 1~ )

<<<<01/RT/74

%>> Ol/27/75

%% 01/27/75 019600 DO 50 J=5)6 %% Ol/27/75 019700 IF lDP(J).LK.O.O) 60 TO 50 <<% Ol/27/76 019600 COC R13.16/((DP(J)-3R,O)/1.5 f 273.16) <<>> Ol/27/75 019900 LVP( J? > 9.09715%(COC-1.0) 3.56654>>DL0610(CDC) 02/02/75 020000 t0.876793%(l.o - 1,0/COC) + DLGO <<>> 01/27/78 020100 50 COHTIHUK M>> 01/27/75 020200 DO RDR KAY ~le6 <<>> 01/27/7S DR0300 IF (DP(KAQ).LE.O.O) GO TO 404 %>> ol/27/75 420400 VPR(KAY) % 0.0145035>>lo>>>>LVP(KAY) <<% Ol/27/75 020500 404 CONTINUE %% 01/R7/75 020600 <<C CHECK FOR t(ISSIHG VAPOR PRESSURE AHD CALCULATE AVERAGE.

'% Ol/27/75 020700 IF (DP(l).LE.D.O) 60 TO 713 01/27/75 020600 IF (DP(2).GT.O.Q) 60 TO 715 <<>> Ol/27/75 020900 VPAUC " -VPR(1) >>% 41/R7/7S OR1444 DR1100 VPR(R) % 0.0 60 TO 717 01/R7/15 01/R7/75 ~ rn ol/27/78- p ORlRDO 713 VPAUC = VPR(2) <<% Ol/RT/78~

Dl/27/75 ~ .a OR1300 VPR(l) > 0.0 OR1400 60 TO 711 421500 715 VPAUC % 0.5>>(VPR(l? t VPR(Rl) %>> ol/R7/78 4l

~

OR1600 717 IF (DP(3).LE;0.0) 60 TO 719 %>> 01/R7/75 0R1700 OR1500 IF (DP(R).GT.O 0) 60 TO 721 VPALC % VPR(3)

>>>> Ol/R7/7S

>>>> ol/RTI14 ~

~

021900 VPR(4) = 4.0 %% 01/21/75 02ROOD GO TO 723 <<>> Ol/R7/75 022104 119 VPALC

VPR(4) 01/2'//78 DRR200 VPR(3) < 0.0 MW

<<>> gl/27/74. Q ED DRR304 60 TO 723 %>> 01/27/15 ORR404 121 VPA(.C % 0.5%(VPR(3) t VPR(4)) %>> ol/R7/75 ORR500 723 IF (DP(5) LE.D.D) 60 TO 725 %% Ol/27/15 02R60D IF lDP(6).GT 0.0) 60 TO 72$ >>>> 01/R7/75 ORR700 VPAIC % VPR(5) <<>> 01/27/75 DR2800 VPR(6) % 0.0 >>>> Ol/R7/74 022900 GO TO 729 <<>> Ol/27/75

/

(

01/14/75 LIBstt>>>>N>>>>%>>H>>ll SOURCE Llbw PUT 05/23/78 l0.55+45 PAGE 0, 023000 725 VPAIC>>>> VPR(6) Ol/27/75 023100 VPR(5) = 0.0 01/27/75 OR3240 GO TO 729 01/R7/78 023300 7R7 VPAIC - "0.5~(VPR(5) + VPR(6)) 01/27/78 023400 t>>C LINEAR It(TERPOLATIOH FOR PRESSURES Ol/27/7S OR3500 7R9 DO 405 t(=1,70,10 II>>t 01IR7/78 E.C.P.. 12-P1-06 REY.1 OR3604 Nl=tltl N>>t 10IRO/77 OR3700 NR-"Nt9 REF VtO. 3 OR3800 023900 NY>>:( l N-1)/10 )

$ %DG ~ PRKS(tlY) tl >>>>II

>>IN t>>N 14/RO/77 10/to/77 41/27/75 OR4000 IF (PROS.KQ.O.O) 60 TO $ 0b N>>t OR/09/75 OR4100 DO 406 N=Nltkt>>e %N 10/20/77 024ROO IF (PRDG.LT.SRlN) 1 GO TO 406 ttlt 01/27/75 OR4340 IF lPRDG.EQ.SR(N)) 60 $ 0 731 tt lt 01/R7/75 ot440o ZF (H.EQ.Nl) 60 TO 444 tttt Ol/R7/75 024500 PRESC(t(T) =SR(N-I) t (PRDG-SR(N) ) tt( SR(H-3) "SR(N-11)/l SR(P-2)-SR(N) ) it It 01/R7/75 OR4600 60TO 445 tt lf 10/RO/77 oe47oo t>>446 CONTINUE >>lit 10/20/77 024S40 444 HRITE (10>>407) tl(D>>NY>>PRDG 02/22/78N>>t 02/2RI75 OR4900 407 FORNAT(TR>> '>>t+~NANONETER READING OFF CALIBRATIOt(".+tt' RXtI3>>RXt 4 2/22/78>>t>>t OR/R2/75 025000 " It>>F9 4) 02/22/78>>t>>t 02/RR/75 025100 405 PRESC(t(Y1 > 0.0 >>>> tt OR/09/75 OR5ROO a 60 TO 405 01/R7/75 OR5300 731 PRKSC(NY) > SR(N-1) 01/27/75 025400 t>>405 025500 +C CONTINUE I N>>t lo/eonr AVERAGING PRESSURES ALLOHING FOR ZERO BfTRT+ ~ ttII ol/27nb OR5600 PRESCU > 0.5>>t(PRKSC(l) t PRESC(R) ) >>t >>t 01/27/75 025700 >>t PRESCL =, 0.5~(PRESC(3) t PRESC(4)1 >>t >>t 01/27/75 025840 PRESCZ = 0.5~(PRESC(5) 0 PRESC(6)1 tt >>t 01/27/75 025900 IF (PRESC(l).LE.O.O.OR.PRESC(2).LK.O 0) PRKSCU = R.ol>>PRESCU t>>N 01/R7/75 026000 IF (PRESC(3)>>LK.O.O.OR.PRESC(4).l.E 0 0) PRESCL>>: R.O<<PRESCL It >>t 01/R7/75 oebloo tt IF lPRESCl5) LK.O.O.OR PRESC(6)+LE ~ 0 0) PRESCI =, R.O>>PRESCI tt >>t Ol/27/75 oe6eoo ACPA=( PRESCUtPRESCLtPRESCI )/3 lilt 10/20/77 026'340 II ACPG>>:ACPA-PRESC( 7) 10/RO/77 OR6400 tt IF (IPR.EQ+O.OR.IPR.GT.HRD I 60 TO 747 tt lf 01/R7/75 oe650o >>t 35 HRITK (6>>505) VPRl>>DP(1)tVPR(l)>>PRES(1)>>PRESCll)>> >>t>>t 01/27/75 OR6600 >>t VPRR>>DPl 2)>>VPR(2) tPRES(2)>>PRESC(2)>> 41/27/75 026700 tt VPR3>>DP(3)>>VPR(3)>>PRES(3)>>PRESC(3)>> tt tt 01/27/75 OR6800 tt VPR4>>DPl 4)>>VPR(4) ~ PRES( 4)>> PRESC(4) M>>t 01/27/75 026900 II VPR5>>DP(5) tVPRl5) tPRES(5) ~ PRESCl5)

~

D IT(

II>>t 01/R7/75 OR7440 027100 It -

~

VPR6,DP(6),VPR(6),PRES(6),PRESC(6),PRES(7)>>PRESC(7) t %>>t 01/27/75 ~~o 027200 VPAUC>>VPALC>>PRESCU>>VPAIC>>PRESCL>>PRESCZ>>ACPA>>ACPG 505 FORNAT (1H->>llX>>'CONTAINNEHT VAPOR PRESSURK DATA CHECK'>>T83 ~

>>I >>t tt tt OR/OR/75 01/27/78 & "0 427300 lt 'ONTAIHNENT PRESSURES DATA CHECK '//1H>> 19X>> 'NILLZ-' SX t >>t>>t 14/21/77 027400 lt DEN POINT>>4Xt VAPOR 'PRESSURE ~ 30X>> UNCORRECTED ~ 7X>> NN 10/21/77 027500 II CORRECTED /1H>>2Xt HYGRONETER>>SXt VOLTS t8Xt (DES+ F ~ ) ~ 7X>> litt 10/21/77 027640 tt (PSZA) ~ 23X>> 'NAHONETER ~ RX>> READING (PSIA) t2X>> 'READING 10/tl/77 OR7740 'lPSIA) '/1H>>5X>> 'VPU-1'10X>>F5 R>>14X>>F5.2>>9X>>F7.4>>RSX 'PU-I' 10/24/77 027500 - R(SX>>F7 4)/T7>>'VPU-2'(10X F5 2) 9X F7 4 T83 'PU-2'>>R(SX F7.4)/

~

l>>>>t 01/27/78 OR7900 II - ~

T7>> 'VPL-1't(lOX>>F5.R)>>')X>>F7.4>> T83 ~ 'PL-1'2l SX>> F7.4)/ 01/27/75 028400 tt - Trt 'VPL-2'>>t(10X>>F5.2)>>9X>>F7.4>>T83 'PL-2' R(8X>>F7 4)/ 01/27/78 025100 tt - T7>> 'VPI-1'>>R(lOX>>F5.2)>>9X>>F7.4 T83 'PI-1'2(BX>>F7.4)/

~

>>Ilf 01/27/75 02SR40 tt - T7>> VPI 2>>R(loX F5 R)>>9X F7 4 TS3 PI-2 2(SX>>F7 4)/

~

If>>t 01/27/75 XI OR8300 - T53>> 'ANBIENT' T95>>F7.4>>SX>>F7.4/1H>>TR4>> 'AVERAGE VAPOR~

PRESSURES'/ 02/02/75 025400 tt - T56>>'S(kt(ARY OF CORRECTED AVKRAGK PRESSURES'/ t>>lt 02/Ot/75 OR8540 tt 1H tT17>> UPPER CONTAItt(ENT (PSIA)>>T47>>Fro4/ >>H>> 02/02/75 028600 lH>>T17t LOkER CONTAIHNENT (PSIA)>>T47>>Fro4>>Tbl>> 01/Rr/75 OR5700 'AVKRAGE UPPER PRESSURE (PSZA)'Tleo>>F7.4/1H>>T17>> tttt 01/erns

l I T Ol/14/75 LIB>NNNNN>>NN SOURCE Llbt P(JT 05/23/75 10.5&.45 PA6E 0 OR8800 -'ICK COtaEHSER (PSIA)'47tF7 RtT&lt'AVERAGE LONER PRKSSURK (P 01/27/78 024900 SIA)'lRO I'7.4/Tbl 'AVERAGE ICK CONOKNSER PRESSURE (PSIA)'lRO Ol/27/7&

OR9000 -F7.4/Tbl, 'AVERAGE CONTAINNENT PRKSSURE (PSIA)'IRQ,F7.4/T&1 01/27/75 029100 'AVERAGE COHTAINNENT PRESSURE (PSIG) ' T120 ~ FjoR) 01/R7/71 029ROQ IF (IPR.EQ.99) 60 TO Ro 01/Rj/7&

OR93OO CALCULATE NORNALIZED MEZGHT FRACTIONSl STORE MITH PRESSURES~ NN 01/27/78

.E C.P. y2-p1-OS REV.1 029400 747 MUCNW P (PRESCU - VPAUC)/TNSNUR 01/27/75 029500 MLCNW N (PRESCL - VPALC)/TNSNLR Ol/27/75

- REF r~o. 3 02960Q OR9700 OR9800

. MICNUN N (PRESCI MNUN N VMFl>>MUCNW IF (MOEN.GTio ~ Ol 60 $ 0 7/9 VPAZC)/TNSNIR t VMFR>>MLCNW t VMF3>>MICNW Nk Nlt 01/Rj/75 OI/Rjn&

02/2R/7&

029900 MUCDEN N MUCt(UN 01/27/75 030000 MLCDEN F MLCNW 01/27/7&

030100 MICOEt( > MICNN Ol/R7/71 030ROQ MDEN t; MNW 01/27/7&

030300 749 MUC(NR) N MUCNW/MUCOEN NN Ol/27/78 030400 MLC(NR ) =MLCNUN/MLCDEN till 03050Q MIC(NR )>>MICNW/MICOEN 030600 M( NR ) =WUN/MOEN 030700 ATUC(NR)>> TNSNUC NN OR/OR/75 030800 PTLC(HR) ~ TNSNLC OR/02/78 030900 ATIC(NR) "- TNSNIC Nlt OR/02/75 031000 APUC(HR) = PRESCU OR/02/78 0311Q0 APLC(NR) 5 PRESCL >>N OR/02/75 031200 APIC(NR) < PRESCI 02/02/7&

031300 AVPUC(NR) = VPAUC >>lt 02/02/7&

031400 AVPLC(NR) = VPALC 02/02/7&

031500 AVPIC(NR) -",

VPAIC ltN 02/02/7&

O31600 Ro CONTINUE 01/27/75 031700 MRITE (10 ~ 903l 01/27/75 031800 903 FORNAT (1Hot2Xt 'ILR006I 0 k>>>>DATA SPACK EXCEEOEO>>N<<' 02/24/7&<< 02/24/75 031900 60 TO 23 01/27/75 O3ROOO ENO OF FILE ANO OTHE/ ERROR NESSAGES Nk 01/27/75 03R100 1R I(RITE (lot904) I Ol/27/78 032200 '904 FORNAT ( 1HO ~ RXt ILR002I 0 N tEND OF DATA IN SYSTKN GROUP ~ 02/24/7&>>k 02/24/75 032300 IRIRXt 'Itlt' 02/24/78>>k 02/RIt/74 032400 23 MRITK (loe905) lt lt 01I'R7/75 03R500 905 FORt!AT (lH"t2Xt'ILROOSI D N>>NABNORNAL RUN TERNINATION<<<<N') 02/24/7S>>N 02/24/7&

>>N 01I'R7/75 03R600 032700 GO TO MRITK RR'R (lot906) I 01/27/75 6 Pl 032500 03R900 906 FORNAT (1Hot2Xt ILR001I

- 12t2Xt'>>N'l D N>>READ KRROR IN SYSTEtt DATA 6ROUP 02/24/78>><< ORIR4/74 02/24/78>>k 02/24/74 Q+

033000 GO TO 23 01/27/75 Pl 0 033100 tR MRITE (lot907) HRD 01/R7/74 M 033200 907 FORNAT (1HO RX 'ZLR003I 0 N>>READ KRROR ZH TKST GROUP t I3 2X loRIRR/75>>k ORIR4/78 oP

'Nk'O 033300 TO R3 Ol/27/78 033400 6R MRITK (lot905) NRD Nk 01/R7/7& Tl 0 033500 908 FORNAT (1HQt2Xt 'ZLR0041 D N>>KND OF DATA. IN TEST GROUP '13e'0

)02/24/78>>k 02/24/78 033600 TO 23 01/27/78 033700 033400 RESULT PORTION OF PROGRAN 40 IF (NR.GE.3) 60 TO 41 Nlt 01/27/75 01/R7/7&

~~o Gm 033900 MRITE (lot909) N<< 01/27/75 034000 909 FORNAT (1HotZXt 'ILR007I 0 NNLESS THAN 3 TEST POINTS - NORE DATA EOR/24/75>><< OR/24/75 XI 034100 -EOEO>>>>') 02/24/78>>k 02/24/78 034200 GO TO 23 >>lt OI/Rjnb 034300 41 TSS = TINE(l)>>TINE(ll + TINE(R)>>TINE(R) 01/27/75 034400 TS>> TINE(1) + TINE(2) 01/R7/74 034500 T2SM < TINE(ll>>lt(l) 0 TINE(R)>>M(R) ltN 01/27/75

+TEST Sl/18/TS 118 ssaasss>> SDNICE L T OUTPUT os/23/7o I

lo.s8.4s PAGK 08 034600 HS

N(l) ~ N(R) <<<

I <<w ol/R7/71 S

~

RF.F VO. 035500 ROR FORI(AT llH>>RX>> I3)4X>>F6.2)RX)3tF9.4iRX>>F959>>3X)F9.4 RX)) <<Ie 01/R7/78 035600 QtZTK t9)205) <<% 01/R7/7S 035700 R05 FDRI(AT(1Nl 34X RESULTS OF THE LIHEAR REGRESSIDH ANALYSZS'/// <<<< ol/27/70 035800 "1N )RX)'RUN I')SX)'H')llX)'LEAKAGERATK'>>9X>>'LEAKAGE')9X) <<>> 05/23/70 035900 H UPPER>>7X) M LOWER ) 9X) H ICE /1N i lOX>> EXPERItIENTAL ~ <<>> 05/R3/7S 036000 "&X>> 'UPPER LItIIT')llX>>'RATE'SX) 'COHTAINIIENT>>) 3Xe <<<< 05/23/70 036100 -'DHTAItw(EHTS ) 5X i 'otKIEHSER '/) w<<ol/27/78 036200 RKGRKSSION LOOP <<% 01/27/71 036300 DO 44 I>>3)HR <<w Ol/27/78 036400 TSS = TSS + TIIIE(Z)>>TZIIE(I) <<w ol/R7/7S 036500 TS = TS + TIIIE(I) w<< Ol/27/78 036600 NS>>i NS i M(I) <<>> Ol/27/70 036700 TRSN )5 T2SH + TIIIE(l)<<N(I) <<<<Ol/27/70 03&boo ANRt w TSS<<HS - TS>>TRSH w>> ol/R7/7S 036900 XNIR w I <<w Ol/27/78 037000 ADEN > XNRR>>TSS TS>>TS w>> Ol/27/70 037100 A = AN(N/ADEtt <<w Ol/27/70 037200 BNUI( < Xt(RR<<TRSH -. TS<<WS <<<< 01/27/78 037300 B > BHUtl/ADEtt <<<<Ol/27/7S 037400 IZ -" I' <<<<Ol/R7/78 037500 NSUtt "- 0.0 <<w Ol/R7/78 037600 SUII OF SI)UARED DIFFERENCES ww ol/R7/70 037700 DD 46 LT)1>>II <<>> ol/R7/78 037800 MLR w A e B>>TItIElL) <<w Ol/27/78 03'7900 ZF (DABSlNlL)-HLR)~LKsl+OD-39) GO TO 46 %% 01/27/78 038000 NSUtl > NSUtl e (H(L)-WLRI<<(N(L)-HLR) >>w 01/R7/78 03S100 46 CDHTINJE <<w 01/27/7S 038200 AT = TS/XNRR <<% 01/27/71 038300 TOT "- AT))AT >>w ol/27/78 038400 DO 48 N=R)II <<% 01/27/70 038500 48 TOT = TOT + (TItIE(tt)-AT)%(TZIIE(t))-AT) %% 02/02/71 0 Pl 038600 B " 2400.0<>% Ol/27/7S 038700 EKK > TABLE(ZI-R) ww Ql/27/7S 038800 SIGI(AB I DSQRT(NSUI(/f TOT<<(XNRR-2,0) ) ) ol/27/7S Pl Q 038900 DEL -"EKK<<SIGI(AB<<2400-0 Iiw 01/27/71 039000 BU > B DEL %>> 05/23/70 039100 WRITE l9>>R06) HRA( IZ ) )H( IZ ) >>BU>>B>>NUC( ZZ ) >>NLC(IZ )>>HIC(II) <<% 05/23/7S 039200 206 FORIIAT (T4)I3)5XiF9.5)2(9X)F9 5)i7X)F9.5i5X>>F9.5i&X)F9.5) <<<< 05/23/75 039300 44 CONTINUE <<% 01/27/78 039400 EHD OF REGRESSIOH LOOP <<% ol/27/71 039500 WRITE (9)203) B)A w>> Ol/27/70 039600 203 FDRt(AT(1HOiR1Xi'FINAL LKAKAGK RATE (%

-PT ' 9.5)

PER DAY) =')F9.5)5XI'IHTERCE <<>> Ol/27/7S '4 cn 039700 f %% 01/27/78 039500 WRITE (9>>R04) BU <<w 05/23/'78 039900 R04 FORtlAT (lNO)21X)'UPPER CDHFIDKNCE LZIIIQ FOR THE RATE IS ')t'9 5) <<w 05/23/78 040000 24 CALL EXIT <<>> Ol/27/7S 040100 Etl)

~pscAN AMERICAN EI.ECTRIC POY'ER SEPYICE CORsPOPATION DATEs March 14, 1978 .

ILR Program' Bad Temperature E.G.P. 12-Pl-06 BEY.1.

Data PAGESFOF Xa liEF I'~0. +

FROMs J.F'. Holbrook Tos M.J. Trezza In the event of. bad temperature data during the integrated leak rate test the coder is first advised to enter a blank or zero for the RTD reading.

Normally the program calculates the average temperature for n zones within a region by the summation ovg

= Ka'T where T.. are the observed temperatures, td~ are the RTD weighting factors, and ~ 4)j. = l. OOOO For K

a blank or zero temperature reading. in zone j the summation .~')<T< will not include Furthermore a denominator VHAC is formed by the relation VWAC=VW:tC" with WiAC initialized to 1.0000 for each test point and region.

The average temperature is therefore calculated as; O,VJ $'>i%~ (i 0j)

YSRC Should zone j contain a tamperature well represented by the the average of the balance of the that is n<<

coder s responsibility to enter a temperaturen,region readin g arrived ived at by other means, such as extrapolation of observed readings or trending from the region average.

E.C.'P. 12-Pl-06 REV.1 Page 2.

F ~r'C.PFOF <

FEF NO. +

0 4 o-0 4 o ob>~~4 44 4c

g. E~+'~<ed CL 0
Ed~plJ-~w ot" 204
': ~" g g 0', Q g 0 ~
'ce~~
a: Qe ~
fly&
Va .p.~~ rag A. g A.
O Obse~ved 4
"a g C,lcwl .lD 4
Apped. Z . W~~. ~ A~i~ 0 ~
Since entering the estimates for zone j will affect the average region temperatures, this becomes a convergence problem. It is therefore recommended that, the regression analysis be performed over the span of test point data utilizing both zero and estimated zonal temperature readings. The final leakage rate and v raia cnes.will indicate the sensitivity 'of the analysis to this particular zonal temperature reading.
~ggQAN E'I Pc AMERICAH ELECTRlC'OSER SERVICE CORPORATlON
+ER SYS~~
DATFt E'C.P. 1'2-Pl-06 REV.1 12, 1978 SllBJECTc May, PAAF~OF ~<
"~E.N@.z.~.~.
FROMM MAY g g )gyp Joe Holbrook TOt M'.. Trezza Mechanical Engineering L3L)U U I & C.SECnON Approximately 25 computer runs were performed in February and March of 1978 to verify the functional design and correctness- of calculation of the Integrated Leak Rate Test program. Only nine of these test run printouts* have been saved, and are currently'on file in my program workbook.
Test run printouts for normal production. programs are not. usually saved because of the sheer volume of. such printouts.. Where important for program documentation, such printouts will be saved providing th'e request. is made beforehand.
My apologies for not informing you that such a request could have been made and followed.
It; was'he intention of program. testing to duplicate the calculations produced by the previous programs operating on the data of Cook Nuclear Plant Unit. $ Z'.: 'This was achieved and printouts of these test runs were forwarded to Engineering.
Additional testing was performed to verify the program's handling of invalid and/or missing data, and to insure that the printed error and warning messages appearing in the Operations
-Guide were being correctly issued. This was done to my satisfac-tion except for error messages la, lc, and lf. Testing for lf was not done because of the difficulty of fabricating the 83 additional sets of test print data; la and lc were not simulated because they are normally caused by hardware faults and not by errors in data.
J.F. Holbrook Computer Applications Division JFH/drc
~ -.--.. cc.. 'S.T..
-7te J.A. Tesoro Ehrmann
E.C.P. 12-Pl-06. REV.l PAGE4 I OF SO OPERATIONS GUIDE'EF'Q,, Q.
FOR REMOTE JOB'NTRY TERMINAL (READER/PRINTER)
INTEGRATED LEAK RATE TEST A. - Job Control Data.
A.EN.S.C;-M.E.D.
~ ~ ~ ~ ~ ~
//ZLRTKST JOB (4990 OyROOnsot sHly
// ~ ~ USLRtiAHE'XEC PILR
//GO. DATA OD fiihP, $ 3 ]9)8 (DATA'S REQUIRED)
I 8: C SECT,ION The, job control. cards (cards whose first character is a.
slash) should be ordered as shown and submitted via the remote terminal for processing. See the attached Job Card Description (form CA-210) for an explanation of codes. in the first. job control card.
B. Machine 0 eratin Instructions Job can be restarted by computer operator.
C'. Pu ose and Descri tion The, Integrated Leak. Rate Test program converts the
.input data readings to temperatures and pressures. and calculates a normalized'eight fraction for the air in the containment, volume. For three or more test points, the program will determine a, leak rate by linear regres--
sion The FSAR and Technical Specifications limit the allow-able leakage rate from containment. To verify that the allowable rate has not been exceeded, a minimum of 48 runs are required at half-hour intervals. Should the initial runs disclose an excessive leak rate, correc-
'tive actions must be taken by plant per onnel and testing continued to complete a 24 hour2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months period. Itforis therefore vital that turnaround time be minimized each run.
JFH:rlh
. 3/S/78
E.C.P. 12-P1-06 REY.1 PAGE4ZOF so OPERATIONS GUIDE REF NQ,,
FOR'EMOTE JOB ENTRY TERMINAL (Rl: ADER/PRINTER) Q INTEGRATED LEAK RESTE TEST D., Fre uenc and Tar et Date of Proceaa~in (cont.)
Since the unit cannot. be returned to service until the leakage rate criteria have been met, it is also necessary to provide redundant paths for op ra~ion of. the computer program. The first. redundant path provides for access to the Canton, Ohio computer should the NY computer not-be available. In the case of failure of the microwave network, telephone dial'up communication has been provided to either the Canton or New York computer.
In the event of failure of, the Data 100 terminal, telephone communication would be used for verbal trans-mission of data from the plant and test results back to the plant..
G'. In ut Data Instructions The data. required for each run consists of fixed informa-tion and test point data., The fixed information appears.
first and consists of seventeen cards containing five types. of data.. The fixed information data form appears as Figure 1 and the punched cards must be assembled in the order given.
I The. indices at the right of card. Al control the range.
of data processed by the program as follows:
Cols. 41<<43 Program'will begin processing test Sta~:5 Index beginning with this run number; blank, program will start at first if data point run number, Cols., 51-53 Program will include the data of.
End Index this test point as the last run number to be processed; if blank, program will accept all data .start-ing from the start index run number.
JFH:rib 3/9/78
l E.t,.P. 12-Pl-06 BEY.l PAGE<30F Ko OPERATIONS GUIDE <~ EF N0e 4 FOR REMOTE JOB ENTRY TERMIIB.L {REAP;.R/PRINTER)
INTEGRATED LEAK RATE T.=,ST G. In ut Data Instructions {cont.)
Cols. 61-63 Program will print data starting Print Index from this run nu:",ber,; i blank, only the last prgccssea run number data is printed.
The test point data of Figure 2 followers the fixed information and, consists of eight data cards containing four types of data.
The temperature measuring devices (ETR-101, ETR-102, etc.)
on, data cards Tl through T5 correspond to the RTD weight-ing factors given on cards Dl through D5 of the fixed information. Please note that device ETR-113 appears in the last field of both cards T2 and T4. Only one of these is to be used per leak test and such use= is to be indicated by the 1ast field of card D2. If is greater than zero, ETR-113 will be expected on card this factor T2,, else ETR-113 will be expected on card T4.
I. Out ut Processin 1.. Error. Messa es
a. ILR001I D **READ ERROR IN SYSTEM DATA GROUP N**
A. data transmission error has occurred in reading the fixed information cards. Number N corresponds to the data type (1 = A, 2 = B, etc.). If a second attempt does not, succeed, repunch the offending card, group and try again. If still unsuccessful contact NY CAD Engineering and Management Section.
b. ILR002I D **END OF DATA IN SYSTEM GROUP N+*
'nfixedend-of-file condition has information been sensed in reading the cards. Usually caused by a misplaced
/* card within the deck. Correct and retry.
JFH:rlh 3/8/V8
E;t'.P; 12-P1.-06 REV.1 Pht E44 OF oo OPERATIONS GUIDE REF NOI, Cn FOR REMOTE JOB ENTRY TERMINAL (READER/PRINTER)
INTEGRATED LEAK RATE TEST I'. Out ut Processin (cont.)
l. Error Messa es c ILR003Z D **READ ERROR IN TEST GROUP N+~
A data transmission, error has occurred in reading the test. point data cards. Number N corresponds to the run n'umber of card. Rl. Retry as in message la.
d<< ILR004I D **END OF DATA IN TEST GROUP N"*
An end-of-file condition has been sensed in reading the test point data cards. See lb.. for corrective action.
e. ILR005I D INCORRECT DATA SEQUENCE Nl N2 A sequence stepdown has occurred. in reading 'the test point- data cards. Nl is the numerical order of the test point data, group and N2 is the run number from card Rl. There are. several possible causes for this error. to occur, but. the three mcrst likely are:
l. Mispunch of Cols. 1-3 in card Rl.'
~ Incorrect number of data cards within the preceedinq r"oup (eight are expected).:
3~ Repeating De sequence number of the pre-.
~ .ceding test. point.
To correct, find the cause of the sequence step-down and then retry.
f. ILR006Z D ***DATASPACE EXCEEDED***
An attempt has been made to process more than 99 test point data groups. This has exceeded the program's capability and car.sot be done.
g. ILR007I D t:*LESS THAiV 3 TEST POINTS MORE DATA NEEDED**
1 Three test points are needed for a linear regression-This message is normal if only two test, points of data exist. After three test points have been obtained the message will persist if the start and end indices of card Al are incorrect.
JFH:rlh 3/9/78
E.C.P. 12-Pl 06'EV'.1 5'o 'ar.E<S'OF OPERATIONS GUXDE REF NO. C FOR REMOTE JOB ENTRY TERMINAL READER/PRXNTER)
INTEGRATED LEAK RATE TEST I. Out ut Processin (cont.)
h'LR008Z D ***ABNOR'GG RUN TERMINATION***
This message appears after. the messages la. thru lg.
and. indicates the need for subsequent, computer runs to achieve successful processing.
i., XHN215I CONVERT - ILLEGAL DECIMAL CHARACTER X This is a system issued error message produced by an attempt to read a non-numeric character within a field defined as numeric.. Unfortunately the card causing the, error is; not listed, and the character X may even not be'rintable. The error, however,, will usually occur in the last test point data group and a recheck of these cards will usually uncover the input data error.
For other system error messages consult NY. CAD.
2.. Narnin -
Messa es
. UPPER a.. TEMPERATURE MISSING Nl L'OWER N2 s XCE A zero or blank field was encountered on the temperature cards of test point group Nl wt the position indicated by N2. For the uppe zone this will. be in cards Tl and T2, for the lower zone in cards T3 and T4, and on card ~5 condenser.
if in the ice The program compensates for missing temperatures by increasing the remaining RTD weight.'ng factors, proportionally.
b. ***MANOMETER READING OFF CALIBRATION***Nl N2 VALUE The manometer reading of run Nl at pos tion N2 of card Pl is outside the calibration ra..>~ of cards.
Cl-C7. The reading is printed as VALQd. The program corrective action sets the reading to zero. Should the reading be correct, then new calibration data will be required.
JFH:rlh 3/9/78
E;C.P., 12-Pl-06 Ray.l.
. 'PAGEOS&,0F 8 OPERATIONS'UIDE, REF NO Cu- .
FOR REMOTE JOB ENTRY TERMINAL (READER/PRINTER)
INTEGRATED LEAK RATE TEST I'. . Out ut Processin (cont.)
20 Warnin Messa es No, warning message 'is issued for a, blank or zero.
pressure reading. If a zonal pressure, reading is, zero or blank,. the program takes the other reading as the average. If both are blank,. zero, or out of. calibration, a zero average will result. At least one non-zero pressure must be present for each zone for successful program execution.. If both zone pres-sures are bad, the entire test point must be deleted'..
A zero ambient reading will only result. in a false ambient pressure indication.
3 ~ ~al
a. Summary'f Averages a one-page listing of average temperatures, pressures, and vapor pressures, for each of the three containment zones, is produced for each test point. data group accepted for. regression. processing.
b.. Results. of Linear Regression a one-page list-ing which follows the Summary of Averages.
Starting with the third processed test data group, the normalized weight fractions. are printedalong with leakage rates calculated from previous test. data points'inclusive. In addition, high and low leakage rate values at; 95% confidence. level are printed. For the last inclusive test point, the 95% confidence leakage rates are separately printed along with. the final leakage rate and intercept value.
4. ~I2
a. System Data Check - a one-page listing of'he fixed information is always produced in the absence of error messages la. or lb.
JFH: rlh 3/97T8"
E.C.'P. 12-Pl-06 REV.I PAGE'70I.'
OPERATIONS GUIDE EF Non
. FOR REMOTE JOB ENTRX TERMINAL (READER/PRINTER)
INTEGRATED LEAK- RATE TEST I. 'ut ut Processin 4;. ~8 (cont.,)
b.. Test Point Data Check a one-page listing of input: data and computed temperatures and pres-sWes will be produced for each test point requested. by the control indices of card Rl. in the absence of error, messages la. or lb. If message lc., ld., or le., appears only the last valid test group will be listed. In the event.
of- system error messages, the current test point. printout. may be partial'ly or completely missing.
E.C.P. L2-P1-06 REV.1
~<<FWSOF a.o OPERATIONS GUIDE BKF KO, 4l FOR REMOTE JOB ENTRY TERMINAL (READER/PRINTER)
INTEGRATED LEAK RATE TEST Ca@alp ued Procedure
//PILP.' PROC FROG ILRTEST) LIB LIB PEP )REG 128K)C A
//GO EXEC PGt t"-tPROG) P EG10t t=tREG
'/STE PLIB DD DStt=t LIB)DISP=SKR
//FTOSF001 DD ODtttttE=DATA
//FT10F001 OD SYSOVT=tC) OCB" (RECFtt=FBA) LRECL-I 33) BLKSIZE=931 )
//FT09F001 DD SYSOUT tC)OCB (RECFtt FOA)LRECL 133)BLKSIZE 931)
//FT06F001 OD SYSOUT-"tC) DCB=(RECF tt-"FBA) LRECL=133) BLKSIZE-"931 )
JFHtrlh s/e/7s
I t'hfdf xATEQKATE'b I-E( R)TE TEST oF
~ 0<<s ~
<<5 ] <<~rgth aivA ey P. c. CooK UNIT PATE
~ ~ 05 1! ll 14 40 li n 50 11 1 11 11 00 01 44 45 00 01 01 10 05 'll 4<< 01 44 41 444110n 1 <<4 1~
V K'. OL I.b yppKR io E.R. "
iClF.
v)5 OLV t-Rcvc R5 PE lO 10 ~0 I~ I~ N l0 ll ll 11 tl 7400
~ \
'11 10 I 00 01 01 00 ~ 1 04 ~ l0 ~ 0 40 00 04 l1 40 40 00 li 1l 11 00 10 ~0 00% $0 Fzt"uRE- i. FxxE'9 IHFoRNATzal E.G.P. 12-Pl-06 REV.I i ArE4q pp wa
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APPENDIX C UNDRAINED SYSTEMS PENALTY LEAKAGE AS-LEFT CONDITION ECP NO. 2-NO-09
A.E;P.S.C; - M.EJL INSTRUMENTATION AND CONTROLS SECTION ADMINISTRATIVE INSTRUCTION AND DESIGN PROCEDURE ENGINEERING CONTROL PROCEDURE' CONTROLLED DISTRIBUTION FOR E.C.P. PACKAGE I, = INITIALISSUE nicaL Coparusene ( ) Cxadcal Sect. (ooc( ~(neer v = REVISED THIS rpoins) tos ( ) .urine Sect. Hanaoer sucaL ( ) SLoctrxcaL Goneratxcn Sect. (oed ISSUE O Stsporfntosdent Q) Esr)isHoer
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X. Ramexy:
Xn order to ccmplete the addition to the As found and IX'm leakage penalty values must be caaputed As left leakage values.
in This calculation is divided into tham sections:
A Type C penalty for systems which axe not vented-duxing the Type A test.
B. The As found minus As left penalty for repaired type.B & C ccxnponents.
C. The overall Type B and C leakage, both As fciund and As Left.
C penalty for unvented systems is generated by applying AEPSC generated guide1irns to the "Type C Penalty Fozm" fran Plant Proceduxe 12 THP 4030 STP.202. This penalty is based on the As left condition. of the valves listed on the above form..
The As found minus As Left generated .guidelines to Type B Type B & C
~ty is generated by applying AEPSC C Cacmnents which were repaired, during performance of Plant Procedure 2 THP 4030 STP.203.
'bee total type. B &, C As fours and As 1'eft leakages are generated by applying AEPSC generated guidelines to all type B & C ccmponent: leakages neasured during perfonnance of Plant Pxccechum 12 THP 4030 SXP.203.
Results:
A. Calculated Values (uncozrected)
Type C Penalty for unvented systems 850.0 sccm Type B & C As found-As left penalty 34256.7 scan Total type B & C Leakage (As found) 37130.1 scan Tot~ type B & C Leakage (As left) 3676.8 sccm B. Cosxacted Values The flaw netexs used for performing the type B & C test are small ball float neters calibrated at: 12 psig and 70'F. Due to '
variations in instnment sizes and nonlinear viscous correction factors, a uniform correction factor is not av~le..'....
Calculations (ECP 12'-07) were performed to st (lcwest recorded test: tenxeratuze) and 12:5 psig (higi~
that at 60'F recorded test: pressure) the correct factor is less than 2% of the irMcated rea9$ ng;. therefore, conservative cor ected values axe 102% of the calculated values:
Type C Penalty for unvented systems 867.0 scan Type B & C As found-As left penalty 34941.8 sccm Total type B and C Leakage (As fcund)" 37872. 7'ccm Total type B and C Leakage (As left) 3750.3 scan
III. Calculations A. Type C'enalty for unvented systems.
From'ppendix D.l in 12 THP 4030 STP.ZOZ there are 11 conditions to review. Test Steps are from 12 THP 4030 STP 203 (Type C):
Leaka e Penalt (sccm) 1.. CPN-40 Valves OCR-205 and OCR-206 Test, Step- 63 No indicated leakage 0.0 2;. CPN-43 Valve ICM-265 Test, Step 81 Ho indicated leakage- 0.0
3. CPH-36 Valves SF-I52, and SF-154 Test Step 71 Ho indicated leakage 0.0
4. CPN-41 Valves OCR-600 and OCR-601 Test'tep 64
'Ho indicated leakage 0.0
5. CPN 17,18,19,20,21,22,23,24',26,27,73,84,85 Valves, MCR-900 to 915, WCR-920 to 935, MCR-941 to 948, MCR-951 to 958, WCR-960 to 967 Test Steps I-Z8
a. Test Steps I 8 2 WCR>>900,901,902,903 Ho indicated leakage 0.0
b. Test Steps 3 5 4 WCR-912,913,914,915 Ho indicated leakage 0.0
c. Test Steps 5 E 6 MCR-920,921,922,923 No indicated leakage 0.0
d. Test Steps 7 5 8 MCR-932,933,934,935 Use guideline C.I (Attachment I)
Use smaller of 0.0 or 280.0 0.0
Leakage Penalt (sccm) e.. Test Steps 9 Ij'0 Valves Wcr -941,945,951,955 No. indicated. leakage 0.0 Test; Steps 11 Ij'2 Valves; MCR-944,948,954,958 No indicated'eakage 0.0 Test Steps 13 5 14 Valves WCR-904,905,906, 8 guideline C'.1 (Attachment 1) 907'se, Use smaller'of 60.0 or 60.0 80.0'est Steps 15 5'6 Yal ves WCR-908,909,910,911 Use guideline C.l (Attachment 1)
Use smaller of 40.0 or 100.0 40.0 i.. Test Steps 17'jl 18 Valves WCR-924,925,926,927 Use guideline C.l (Attachment 1)
Use. smaller of 0.0 or 300.0 0.0
,j;, -Test:"Steps-19 & 20 Valves MCR-928,929,930,931 No indicated 1'eakage- 0.0.
Test; Steps 21 5 22.
Valves MCR-942,946,952,956 No indicated leakage 0;0 Test Steps 23 5 24 Valves MCR-943,947,953,957 No indicated leakage 0.0
m. Test Steps 25 In 26 Va1 ves MCR-960,961,962,963 No indicated leakage 0.0 n Test Steps 27 5 28 Valves WCR-964,965,966,967 No indicated leakage 0.0
Leaka e Penalt (sccm)
6. CPN-11,12,13,14 Valves CS-442-1, CS-442-2, CS-442-3, CS-442-4 Test Steps 46,47,48,49 No indicated leakage 0.0
7. CPN-34,37 Valves QCR-300,301, LCM-250,350 Test Steps 65,66,67 For steps 65 and 66 use criteria E (Attachment')
Use lower of 0.0 or 30.0 0.0 For step 67 No indicated leakage 0.0
8. CPN-81 Valves ICR-5,6 Test Step 78 No indicated leakage 0.0
9. CPN-66 Valves NCR 107,108,109,110 Test Steps 74,75.
No indicated leakage 0.0
10. CPN-35 Valve CS-321 Test Step 55 Note:This valve was repaired.
Use As left value for this calculation.
Use criteria E (Attachment 1)
As left leakage 750.0 750.0
11. CPN 56,86 .Valves VCR 10,11,20,21, R-156,R-I57 Test Steps 57,58,116,117 For Test Steps 57,58 No indicated leakage 0.0 For Test Steps 116,117 Use criteria E Note:Valve R-157 was repaired.
For this calculation use ~
As left leakage value.
No indicated leakage 0.0 Total Type C Penalty for Unvented Systems 850.0 sccm
1
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Attachrrent l t.
r, Guidelizms for Calculation of Type B a C
~ Leak Rates for Inclusion in Type A Test Rem&ts I's t
Assurr @lions:
These guideLines were developed by application of the fallowing pzEru.ses i C P
1) Containment Boundary~ Leakage thxough a given penetration will be no higher than the leakage through, the rrast restrictive ccrrrcanent..
ri
2) Class. I. piping and cartponents foxming a closed loop inside. containnent between two penetzations will remain leak tight.
3) The leak rate far two valves in series will be equal to
~-
ar less than one third, of the leak rate chsezved when pressurization is accanplished between the valves.
'Ihis, pzerrrise is nat to be used when the leak zate 2
I rraasuzed fxnn between the valves exceeds scfm. F 2 P r
Guidelines:
A) Leakage. of 2 scfm or higher for any lccal. test shall. require that the.
valve with the larger leakage be; lccated and only that valve wiLL be repaired. The leakage identified during the first acceptable retest shalI be. attributed to the second valve and shall be the "As Found" leakage for that. line. Thereafter the second valve can be repaired if appropriate o In cases where a leak rate of less than 2 scfm is detezrnined by B) ores suzization he~ two series iso 1aticn valves on the sane penetration. The "As Faund" leak rate penalty shall he one third of the rraasured leak rate or the leak rate rreasrxred after, the repair of one valve; whichever is less.
C) In cases where leak rate is detexmined by pressurization shall he~ tm or aare valves on different penetratians the follcwing apoly:.
C.1 ~~ Essential Sexvice Water (Class IX connecting piping, valves in series an each 'penetzat'i;an) rate for the
'he "As Found" leak combined penetzations shall be the sna1hm of &m leak rates ncaa~ by the testing of eiK~ valve on each penetration.
C.2 anent Cooling Water (Class I canne~g piping single or series valves on each penetration)
'Ihe "As Found" leak rate shall nat be included because the systetn forms a closed leap inside cantainrrant.
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APPENDIX D REPAIRED VALVES PENALTY LEAKAGE CALCULATION AS-FOUND VS. AS-LEFT CONDITION ECP NO.2-NO-09
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INSTRUMENTATION ANO CONTROLS SECTION , 'pr<tit~
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In order to ccmplete'he EIBZ addition to the As found and
~ left ~tyvalues.
As leakage leakage values must be ccmputed This calculation is in i 5i.
divided into tham sections:
A. Type C penalty for systems which axe not vented during the Type A test.
B. The As. found minus As left penalty for repaired
type B' C ccmponents.
C. The ~~
and As Left Type B and C leakage, both As found IPi r
~ty II The type C for unwanted systems is generated by applying guidelines to the "Type C Penalty Foxm" fran Plant Procedure 12 THP AE'enerated 4030 STP.202 This penalty is based on the As left condition. of the valves listed on the above fozm.
r Ci/i Left Type B & C penalty is generated by applying AEPSC
~
'32m As found minus As 'ih:
generated guidelines to Type B & C Ccmconents which wexe repaired during t 1 pexfozmance of Plant Procedure 2 THP 4030 STP.203. i'
%he total. type B & C As found and As 1'eft leakages are generated by applying i
AEPSC generated guidelines to all type B & C ccaxenent leakages naasured
~
i during performance of Plant Pzocechuw 12 THP 4030 STP.203.
II; Results:
4 p
A. Calculated Values (uncozzected)
Type C Penalty for unvented systems 850.0 scan -1 Type B & C As found-As left penalty 34256.7 scan Total type B & C.Leakage (As fours) 37130.1 sccm ~ y, Total type B & C Leakage (As left) 3676.8 sccm % ~ ir Il P B. Corrected Values The flow naters used for performing the type B & C test: are small ball flcat: me4mrs ca1ihrated at 12 psig and 70'F. Due to variations in instant sizes and nonlinear viscous coaction 1 fa,tors,, a uniform correction factor is not available.
Calculations (ECP 12'-07) were perfoznad to show that at 60'F (lowest recorded test tenperatuze) and 12;5 psig (highest xecoxded test pzessuze) the correction factor is less than 2S of the indicated reading;. therefoxe, conservative corrected values axe 102$ of the calculated values: ~ ~
i
Type C Penalty for unvented systems 867.0 scan Type B & C As found-As left penalty 34941.8 scan ~, I' *
/
'Ibtal type B and C Leakage (As found) 37872.7'c'cm ,
"y Total type B and C Leakage (As left) 3750.3 sccm i%
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B. As found vs As left Type B 5 C Penalty Ouring Performance of Plant Procedure 2 THP 4030 STP.203 the following components were repaired to reduce leakage:
Item- Type C Test Step Component 1 33 VCR-105,205
2. 51. SH-1, 3 53 N-159
4. 55 CS-321 59 OCR-207'-160 60.
6 62 OCR-620,621 7 68 ICH-305 8 ECR-33,35'CR-31,32 9 82'01 10 ICH-251 11, 102 ICH>>250 12 108 CCM-243-72.
13 117 R-157 14 120 ECR-416 121 ECR-417 Type B Test Step Component 15 4. Zone 4 Penetration Bellows Penalt sccm)
1. Test Step 33 Valves VCR-105,205 As .found leakage - 20000.0 sccm Ps left. leakage - 80.0 sccm As found leakage is less than 2 scfm (56632 sccm) therefore, apply guideline B (Attachment 1)
Penalty 1/3. '(20000)-1/3 (80)=6640 6640.0
2. Test Step 51 Valve SH-1 and Valve ECR-36 (Test Step 124) are SH-1'alve in series. Valve ECR-36 had no indicated leakage.
Use the smaller of 625.0 or 0.0 . 0.0
3. Test Step 53 Valve N-159 Valve N-159. and Valve GCR-301 (Test Step 85) are in series.
Valve GCR-301 had no indicated leakage. Use the
, smaller of 570.0 or 0.0. 0.0
Penal (sccm) 4~ Test Step 55 Valve CS-321 This is a single isolation valve. Use As found leakage of 24000 minus the As left leakage of 750. 24000.0 750.0 = 23250 scan 23250.0 Test Steps 59,60 Valves DCR-207, N-160 Valves N-160 and DCR-207 are in series. The As found leakages were 1650 and 300 xespectively.',
lower As found nLinus the penalty.
300.0-20.0 ~ 280.0 scan
~
The As left leakages were 260 and 20 xespectively.
Since these- valves were tested separately use the As left for the 280.0
6. Test= Step 62 Valves DCR-620,621 Use guidelizM. B (Attach>ant 1)
Penalty 1/3 As found 1/3 as left
=1/3 (2400) - 1/3 (0)= 800 scan 800.0 7; Test. Step 68 Valve XCH-305 Use guideline D (Attachment 1)
Penalty=l/3 As found - 1/3 As left
~1/3 (6000) 1/3 (0) =. 2000 sccm 2000.0
8. Tlest Step 79 Valves ECR-33,35 Use guide1izm B (Attachrant 1)
Penalty 1/3 As found 1/3 As left
~ 1/3 (2500) 1/3 (1900)=200 200.0 scorn'est
9. Step 82 Valves 1XR-31,32 Use guide3ixm B (Attachment 1)
Pena1tZ=1/3 as found - 1/3 as left
=1/3 (1300) -1/3 (1250) =16.7 scan 16. 7
10. Test Step 101 Valve ZCZ-251 Use guideline D (Attachnont 1)
Penalty=l/3 as found - 1/3 as left 1/3 (700) - 1/3 (40) =220sccm 220.0 Test Step 102 Valve ZCH-250-Use guideline D (Attachment 1)
Penalty=l/3 as found - 1/3 as left
=1/3 (1850) - 1/3 (50) = 600 sccm 600.0
12. Test Step 108 Valve CCH<<243-72 guideline C.2 (Attachnent Use No ~ty 1) 0.0
0 S
Penalt (sccm) 13; Test Step 117 Valve this calculation this valve is R-157'ote:
For-taken to be in series with valve VCR>>20 (Testr Step 58)
For'two series isolation valves tested separately use the. lower leakage- rate.
~
Use I ower of 8000. 0 or 0. 0 0.0 14.. Test Step 120,121 Val ve ECR-416,417 Valves ECR-416 and ECR-417 are in series. The penalty is computed by using. the lower- As found'minus the lower As left.. .!
Penalty=250.0-0.0 = 250 sccm 250.0 15'. Test Step 4. (type: 3) Zone 4 Penetrations Bellows s pe(
s rrA, The Zone 4 Penetrations Bellows are not,part ';W I ~ PSf'.
of the containment pressure boundary;therefore, this leakage is not included, in the penalty. 0.0 Total As found, - As, left Penalty (sccm) ~34 5%7 1
I'I
~
C. Total type B IIl C As found and As left leakages.. P This calculation applies AEPSC generated guidelines- to each Test Step to establish leak rates for both the As found and As left conditions.
As found. As left'
1. Test, Steps 1-6'o indicated leakage 0.0 0.0
2. Test Steps 7,8 Valves MCR-932,933,934,935 No Repairs;therefore, As found=As left
. Use guideline C.1 (Attachment 1)
Use smaller of 280.0 or 0.0 0.0 0.0
3. Test Steps 9>>12 No indicated leakage 0.0 0.0
4. Test Steps 13,14 Valves MCR-904,905,906,907 No 'repairs;therefore, As found=As left Use guideline C. 1 (Attachment 1)
Use smaller of 60.0 or 80.0 60.0 60.0
5. Test Steps 15,16 Valves MCR-908,909,910,911 No repairs;therefore, As found~As left Use guideline C. 1 (Attachment 1)
Use smaller of 40.0 or 100.0 4o.o 40.0
/
$ g d. ~ ~ g e 4I o-0't 9.'-~
APPENDXX E LEAKAGE TEST RESULTS OF TYPE A, B and C TESTS D. C. COOK'LANT UNXT 2 - l984
AAAAAAAAAA EEEEEEEEEEEE PPPPPPPPPPP 00000000 777777777777 JJJJJJJJJJ PPPPPPPPPPP AAAAAAAAAAAA EEEEEEEEEEEE PPPPPPPPPPPP 0000000000 77777777777 JJJJJJJJJJ PPPPPPPPPPPP AA AA EE PP PP 00 0000 77 77 JJ PP PP AA AA EE PP PP 00 00 00 77 JJ PP PP
. AA AA EE PP PP 00 00 00 77 .JJ PP PP AAAAAAAAAAAA EEEEEEEE PPPPPPPPPPPP 00 00 00 77 JJ PPPPPPPPPPPP AAAAAAAAAAAA EEEEEEEE PPPPPPPPPPP 00 00 00 77 JJ PPPPPPPPPPP AA AA EE PP 00 00 00 77 tJ PP AA AA EE PP 0000 00 77 JJ JJ PP AA AA EE PP 000 00 77 JJ JJ PP AA AA EEEEEEEEEEEE PP 0000000000 77 JJJJJJJJ PP AA AA EEEEEEEEEEEE ,PP 00000000 77 JJJJJJ PP IIIIZIIIII LL RRRRRRRRRRR SS SS 11 " 8888888888 00000000 3333333333 IZZZIIZIII LL SS SS III 888688888888 0000000000 333333333333 ZI II LL LL RRRRRRRRRRRR RR RR SSSSSSSSSSSS RR SSSSSSSSSSSS lll II I
88 88 88 00 88 00 0000 33 00 00 33 33 II ZI LL LL RR RR RR SS SS SS SS llll 88 88888868 88 00 00 00 00 00 00 3333 33 II II LL LL RRRRRRRRRRRR RRRRRRRRRRR SS SS SS llll -86888686 88 88 00 00 00 00 00 00 '333 33 II II LL RR RR RR RR SSSSSSSSSSSS ll ll 88 88 88 0000 -
88 000 00 33 IIIZIIIIIZ IIIIIIIZII LL, LLLLLLLLLLLL RR LLLLLLI.LLLLL RR RR RR RR RR SSSSSSSSSSSS SS SS SS SS llllllllll llllllllll 888888888888 8888888888 0000000000 00000000 00 33 333333333333 3333333333 33 JJJJJJJJJJ JJJJJJJJJJ ll lll sseesseees 888888888888 00000000 0000000000 3333333333 333333333333 AAAAAAAAAA JJ JJ llll ll 88 88 88 88 00 00 0000 00 00 33 33 33 AAAAAAAAAAAA AA AA JJ JJ ll ll 88 88888888 88 00 00 00 00 00 00 33 3333 AA AA AA AA JJ JJ ll ll es 86888888 ee 00 00 00 00 00 00 3333 33 AAAAAAAAAAAA AAAAAAAAAAAA AA AA JJ JJ 11 68 68 0000 00 33 JJ JJJJJJJJ JJ ll llllllllll 88 88 000 00 33 33 AA AA AA AA JJJJJJ llllllllll 888888888888 8888888888 0000000000 00000000 333333333333 3333333333 AA AA AA AA
~%~~ GENERAL INFORHATION ~w%wwwwwtHtww%w%wwwwwww~ww~4ww~ww~ww~wwwwwwwWN~WN~wwwwwwwwJOB THROUGtlPUT SUtNARY %wxKwEm%xm
%%%ttXXWE% %%%%%%3E%3f
.DELIVER CODE - AEP 07JP AHERZCAN ELECTRIC POHER www%www INPUT FROH CANTOth.CCCR.INTRDR JOB NAHE - ILRS'1803 SERVICE CORPORATION wow%% ON 01 OCT 84 AT 1.39.13 PH EST JOB NUttBER 1803 EXECUTION BEGAN ON CANTON.CCCR PROGRAtlHER PROBST COLUtKUS ~ %~ ON Ol OCT 84 AT 1.39 ~ 16 PH EST ZN CLASS C ROOtk NUttBER 07JP OPERATIONS >w> ><<<% PRINTED ON COLUttBUS.COCB.PRZNTR3 SYSOUT CLASS - A ~ %%%~%% ~ COttPLEX %% %%%%K%% ON Ol OCT 84 AT R.OR.13 PH EST
%X%%%%%%%K%%%%%X%%%%%%%%%%%K%%KKK%%KttK%%%%X%%%%%%%%%%X%%%%Wf%K%%%%K%%Ã%%%%%%%%%%%%%%%% %%%%%%%% 3&%%%%%%%3EX KWEK%%X X%%M%%%%X%%% % %%%% K%
gQ JES2 JOB LOG SYSTEH CCC2 NODE CANTON 13.39.15 JOB 1803 SHASP901 ILR¹1803 JOB 1803 CLASS=C CPU TIHE= 1 13.39.16 JOB 1803 SllASP373 ILR¹1803 STARTED - -
INIT 6 CLASS C - SYS CCC2 13.39.16 JOB 1803 IEF4031 ILR¹1803 - STARTED 13.39.18 JOB 1803 SRASP375 ILR¹1803 ESTIllATED LINES EXCEEDED 13.39.18 JOB 1803 CHASP375 ILR¹1803 ESTItlATEO LINES EXCEEDED BY 2000 13.39.19 JOB 1803 IEFOOOI ILR¹1803 - ENDED 13.39.19 JOB 1803 SlfASP395 ILR¹1803 ENDED JES2 JOB STATISTICS Ol OCT 8% JOB EXECUTION DATE 500 CARDS READ 3>670 SYSOUT PRINT RECORDS 0 SYSOUT PUtKH RECORDS 0.05 MINUTES EXECUTION TINE
0 //ILRII803
// JOB (4989y52707JPplpl pOp yly p ) p PROBST >HSGLEVEL t REGION=128K ')SGCLASS=H >CLASS=C lpl) p JOB 1803
%%CROUTE PRINT NODROOO S020R502
%%CROUTE PUNCH N08ROOO S020R502 wxwDELIVER SAEP07JP
%%CROUTE PRINT LOCAL I wwwJOBPARH COPIES=2
<>>DELIVER SAEP07JP-2 3
// EXEC.PILRpC='w'XPILR PROC PROG=ILRTEST,REG=128K,C=A 80169001 XXGO EXEC PGH=SPROGpREGION=&REG 80169002 5 XXSTEPLIB DD DSN-LIB PEP pDISP-SHR 80169003 6 XXFT05F001 DD DONA))E-"DATA 80169004 7 XXFT10F001 DD SYSOUT"-2C>DCB=t RECFH-"FBA>LRECL=133pBLKSIZE=931) 80169005 8 XXFT09F001 DD SYSOUT=RCpDCB=lRECFH=FBApLRECL=133pBLKSIZE=931) 80169006
9. XXFT06F001 DD SYSOUT=AC DCB=(RECFH=FBA LRECL=133 BLKSIZE=931) 80169007 10 //GO.DATA DD %
4.
S)MT NO. HESSAGE Cj IEF653I SUBSTITUTION JCL - PGM=ILRTEST>REGION"-128K 7 ZEF653Z SUBSTITUTIOtl JCL SYSOUT=>yDCB=(RECFH"-FBApLRECL=133yBLKSIZE=931) 8 IEF653I SUBSTITUTIOt) JCL SYSOUT <>DCB (RECFH FBA>LRECL-133pBLKSIZE 931) 9 IEF653I SUBSTITUTION JCL - SYSOUT-">pDCB=(RECFt)=FBApLRECL=133pBLKSIZE=931)
IEF236I ALLOC. FOR ILR))1803 GO ZEF237Z A60 ALLOCATED TO STEPLIB IEF237I 961 ALLOCATED TO SYS00697 ZEF237I JES2 ALLOCATED TO FT05F001 IEF237I JES2 ALLOCATED TO FT10F001 ZEF237I JES2 ALLOCATED TO FT09F001 ZEF237Z JES2 ALLOCATED TO FT06F001 IEF102I ILR))1803 GO - STEP WAS EXECUTED - COND CODE 0000 ZEF285I LIB.PEP KEPT IEF285I VOL SER NOS= CD0183.
IEF285I SYSCTLG. VCDB001. KEPT IEF285I VOL SER NOS= CDB001.
IEF285Z JES2. JOB01803. SI0101 SYSIN ZEF285Z JES2.JOB01803.S00102 SYSOUT ZEF285I JES2.JOB01803.S00103 SYSOUT IEF285I J ES2. JOB01803. S00100 SYSOUT ZEF373I STEP /GO IE F37%I STEP /GO
// START Bct275.1339 STOP 8%275.1339 CPU DMIN 01.23SEC SRB DMIN 00.03SEC VIRT 72K SYS 256K IEF375Z JOB /ILR))1803/ START 8%275.1339 IEF376I JOB /ILR))1803/ STOP 80275.1339 CPU Ot)lth 01.23SEC SRB OHIN 00.03SEC
IsPP~
<~ ILR ERROR AHD WARNING HESSAGES ~I>
CONVERTED DEW POINT -0.01 RUW HNIBER 1 IS OUT OF RANGE FOR VAPOR PRESSURE CAI.CULATION AHD HAS BEEN IGttORED xxKHAHONETER READING 0.0 NOT IN CALZBRATIOH RAHGE - RUN It ls ENTRY NUttBER 3 CONVERTED DEW POINT -0.01 RUW HNIBER 2 IS OUT OF RAIIGE FOR VAPOR PRESSURE CALCULATION AND IIAS BEEN IGttORED
%%KHAHOtIETER READING 0.0 NOT IN CALIBRATION RANGE RUH It 2p ENTRY WUtIBER 3 CONVERTED DEW POINT -0.01 RUN HNIBER 3 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATIOH AHD HAS BEEN IGttORED 3fwxHANOIIETER READING 0.0 HOT IN CALIBRATION RANGE - RUH It 3y ENTRY tINIBER 3 CONVERTED DEW POINT -0.01 RUW tIUttBER 4 IS OUT OF RAtIGE FOR VAPOR PRESSURE CALCULATIOW AND IIAS BEEN IGtIORED 38fKHAHOIIETER READING 0.0 HOT IN CALIBRATION RAtlGE - RUN I 4p ENTRY HNIBER 3 COIIVERTED DEW POINT -0.01 RUN HNtBER 5 XS OUT OF RAIIGE FOR VAPOR PRESSURE CALCULATION AHD llAS BEEN IGNORED
%%%HANOHETER READING 0.0 NOT IN CALIBRATION RANGE RUN It 5p ENTRY NNIBER 3 CONVERTED DEW POINT -0.01 RUW HN%ER 6 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED wwwtIAHOHETER READING 0.0 HOT IN CALIBRATION RANGE - RUW It 6p ENTRY NUttBER 3 CONVERTED DEW POINT -0.01 RUN HNIBER 7 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED
%%%HANOIIETER READZtIG 0.0 ttOT IN CALIBRATION RANGE - RUN It 7y ENTRY HNIBER 3 CONVERTED DEW POINT -0.01 RUN ttNIBER 8 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AHD IIAS BEEN IGNORED
<w>HAIIOHETER READING 0.0 HOT IN CALIBRATIOH RANGE RUN It Bp ENTRY NUl%3ER 3 CONVERTED DEW POINT -0.01 RUN HNIBER 9 IS OUT OF RAIIGE FOR VAPOR PRESSURE CALCULATIOH AIID HAS BEEN IGNORED
%%%IIAWOHETER READING 0.0 HOT IN CALIBRATION RANGE - RUH It 9p ENTRY HNIBER 3 CONVERTED DEW POINT 29.48 RUW HUtIBER 10 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED CONVERTED DEW POZttT -0.01 RUH HNIBER 10 ZS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AWD HAS BEEN IGNORED
~NHANOIIETER READING 0.0 NOT IN CALIDRATIOW RANGE RUN lt 10 p ENTRY tIUIIBER 3 CONVERTED DEW POINT CONVERTED DEH POINT 30.38
-0.01 RUH RUW NUttBER NUtIBER ll ll IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AHD IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEH IGNORED IIAS BEEN IGNORED
%xKHANOIIETER READIHG 0.0 WOT IH CALIBRATZOW RANGE - RUH It lip ENTRY NUMBER 3 CONVERTED DEW POINT 30.92 RUN HUIIBER 12 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN XGtIOPED CONVERTED DEW POINT -0.01 RUtk NUttBER 12 IS OUT OF RANGE FOR VAPOR PRESSURE CAI.CULATION AND HAS BEEN IGNORED KMNHANOIIETER READING 0.0 NOT Itt CALZBRATIOH RANGE RUW 4 12> ENTRY NUIIBER 3 COtlVERTED DElt POINT 31.64 RUN HNIBER - 13 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEtl IGNORED CONVERTED DEW POINT -0.01 RUN HUIIBER 13 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATIOW AND HAS BEEN IGNORED
><NHANOHETER READING 0.0 NOT ZN CALIBRATION RANGE -
RUN I 13> ENTRY HNIBER 3 wxxtIAHOIIETER READING 0.0 NOT It) CALIBRATION RANGE RUH It 14> ENTRY HNIBER 3
%%%MANOMETER READING 0.0 NOT IN CALIBRATIOtl RAttGE - RUN It 15> ENTRY HUtIBER 3
%%%ISLHOHETER READING 0.0 HOT IN CALIBRATION RANGE - RUH It 16> ENTRY HNIBER xxxHAHOHETER READING 0' HOT IN CALIBRATION RAttGE - RUH It 17> ENTRY HNIBER 3 wwwtIANOIIETER READING 0.0 NOT IN CALIBRATION RAtIGE - RUN 0 18m ENTRY HNSER 3
%%NHANOHETER READING 0.0 HOT IN CALIBRATION RANGE " RUN It 19> ENTRY HNIBER 3
%%%MANOMETER READING 0.0 NOT IH CALIBRATIOH RAIIGE - RUN It 20 ENTRY tIUIIBER 3
~NIIAttOHETER READING 0.0 HOT IN CALIBRATION RAtIGE - RUN S 2lp ENTRY HNIBER p><HAIIOtIETER READING 0~0 NOT IN CALIBRATION RAtlGE RUW It 22> ENTRY WUtIBER 3
~>MANOMETER READItIG 0.0 NOT IN CALIBRATIOH RANGE - RUW 4 23'NTRY NNIBER 3 wxxHAHOIIETER READING 0.0 HOT IN CALIBRATION RANGE - RUH It 24> ENTRY NUMBER 3 xxwHAHOt4ETER READIHG 0.0 HOT IH CALIBRATION RANGE - RUN It 25> ENTRY ttNQER 3 HAtIOtIETER READIttG 0.0 HOT Itt CALIBRATZOW RANGE - RUW It 26> ENTRY NNIBER 3
%%NHAHOHETER READING 0.0 HOT IN CALIBRATIOll RANGE - RUN It 27'NTRY HNIBER 3
%%NHAHOttETER READING 0.0 NOT IN CALIBRATION RANGE - RUN It 28'NTRY IIUIIBER
%%WIIANOHETER READING 0.0 HOT ZH CALIBRATION RAttGE RUN It 29> ENTRY NNIBER 3 xxxHANOIIETER READING 0.0 HOT IN CALIBRATION RANGE RUH It 30'NTRY HNIBER 3
%~HANOt!ETER READING 0.0 HOT XN CALIBRATION RAtlGE - RUH It 31 ENTRY HNIBER 3
%%KHANOtIETER READIttG 0.0 HOT IN CALIBRATION RANGE - RUN It 32> EtITRY NJtIBER 3 wwHAHOHETER READING 0.0 NOT IN CALIBRATION RANGE - RUN It 33> ENTRY NNtBER 3
~
~MANOMETER READIttG 0.0 HOT ZH CALIBRATIOH RANGE RUH It 34'NTRY NNIBER 3
%%%MANOMETER BEADING 0.0 HOT IN CALIBRATION RANGE RUH It 35> ENTRY HNIBER 3
%%IHAHOHETER BEADING 0.0 HOT IN CALIBRATIOt) RANGE RUN It 36> EtlTRY HNIBER 3 xxwHANOHETER READIHG 0.0 ttOT IN CALIBRATION RANGE - RUN It 37 ENTRY NNIBER 3 CONVERTED DEW POINT "0.01 RUW HNIBER 30 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AHD HAS BEEN IGNORED WOHETER READItlG 0.0 HOT XH CALIBRATION RANGE - RUN It 3 s ENTRY NNIBER 3 C TED DEW POINT -0 01 RUN
~ HNIBER 39 IS OUT OF RANGE FOR VA 'RESSURE CALCULATION AND HAS BEEN IGNORED gA
$ >>S
KKKISlNOMETER READING 0.0 tIOT IN CALIBRATION RANGE - RUW II 39> ENTRY thUISER CONVERTED DEW POINT -0.01 RUth NUISER 40 IS OVT OF RANGE FOR VAIOR PRESSURE CALCULATION AND HAS BEEN ZGIIORED NKKMANOIIETER READING 0.0 NOT IN CALIBRATIOth RANGE - RUN II 40> ENTRY NUtSER 3 COthVERTED DEW POINT 29.66 RUH NUISER 41 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AWD HAS BEEN IGtiORED CONVERTED DEW POINT -0.01 RUN NJISER 41 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEth IGNORED xmMANOMETER READING 0.0 ttOT IN CALIBRATION RANGE RUN It 41 p ENTRY NUISER 3 CONVERTED DEW POINT CONVERTED DEH POINT xxxHANOMETER READING
-0 'l 31.28 RUN NUISER 42 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATIOth AND O.a RVN thUISER 42 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND NOT IH CALIBRATION RANGE - RUH II 42'NTRY WUISER 3 HAS BEEN IGIIORED HAS BEEN IGthORED CONVERTED DEW POINT -0.01 RUN NVISER 43 IS OUT OF RAttGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED wwxMAHOMETER READIthG 0.0 WOT IN CAI.IBRATION RAthGE - RUN II 43> ENTRY thUISER CONVERTED DEW POINT -0.01 RUN NUISER 44 IS OUT OF RAHGE FOR VAPOR PRESSURE CALCVLATION AND HAS BEEth IGNORED
%%%I IAIIOMETER READING 0.0 NOT IN CALIBRATION RANGE " RUW It 44> ENTRY NUtSER 3 COthVERTED DEW POINT -0.01 RUN tmtSER 45 IS OUT OF RAHGE FOR VAPOR PRESSURE CALCVLATION AHD HAS BEEN IGNORED KJrwtIANOMETER READING 0.0 NOT ZN CALIBRATION RANGE - RUW II 45'NTRY NOSER' CONVERTED DEI'I POINT -0.01 RUH NUISER 46 IS OVT OF RANGE FOR VAPOR PRESSURE CALCULATIOH AND HAS BEEN IGthORED
~KMANOtlETER READING 0.0 NOT IN CALIBRATION RANGE RUN II 46'HTRY IIUISER 3 CONVERTED DEW POINT -0.01 RUN NUIIBER 47 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AIID HAS BEEN IGNORED
<><IIANOMETER READXthG 0.0 NOT IN CALIBRATION RAthGE RUN II 47'NTRY thMSER 3 3BfwMANOIIETER READING 0.0 NOT XN CALIBRATION RANGE - RUN II 48> ENTRY NUISER 3
%%KHANOMETER READING 0.0 HOT XN CALIBRATION RANGE RVII II 49> ENTRY NUtSER 3 CONVERTED DEW POINT -0.01 RUN NUMBER 50 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGthORED
%%xlIANOIIETER READIthG 0.0 NOT IN CALIBRATIOlh RANGE - RUN II 50'NTRY NUISER 3 CONVERTED DEW POINT -0.01 RUN NmSER 51 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATIOH AND HAS BEEN IGNORED
%%NMANOMETER READZHG 0.0 HOT IN CALIBRATION RAthGE RUN II 51> ENTRY NUtlBER 3 CONVERTED DEW POZthT 28.22 RUN NUtSER 52 IS OUT OF RAlhGE FOR VAPOR PRESSURE CAI.CULATION AND HAS BEEN IGttORED CONVERTED DEH POINT -0.01 RUN NUISER 52 IS OUT OF RAHGE FOR VAPOR PRESSURE CALCULATION AHD HAS BEEN IGNORED
%wwthANOtIETER READING 0.0 NOT ZN CALIBRATION RANGE - RUN II 52> ENTRY NUtSER 3 CONVERTED DEH POINT 28.40 RUW HUISER 53 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AthD HAS BEEN IGNORED COthVERTED DEW POINT -0.01 RUN NUISER 53 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AWD HAS BEEN XGNORED
%%xthAIIOIIETER READING 0.0 NOT IN CALIBRATION RAthGE - RUN II 53> EthTRY NUISER 3 COthVERTED DEI'I POZthT 29.12 RUN thUISER 55 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGthORED CONVERTED DEW POZNI -0.01 RUN NUISER 55 IS OVT OF RANGE FOR VAPOR PRESSURE CALCULATIOH AHD HAS BEEN IGNORED 3ENXMAHOMETER READING 0.0 HOT ZN CALIBRATIOH RAthGE - RUtl II 55'thTRY thUISER 3 CONVERTED DEW POINT 29.48 RVH NUISER 56,IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED CONVERTED DEW POINT -0.01 RUN thUISER 56 IS OUT OF RAHGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGWORFD wwwMAWOMETER READING 0.0 NOT ZN CALIBRATIOH RANGE - RUN It 56> ENTRY thUISER 3 CONVERTED DEll POINT 29.84 RUN NUISER 57 IS OUT OF RAthGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED COHVERTED DEW POINT -0.01 RUH NUISER 57 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED amwMANOMETER READIHG 0.0 HOT IN CALIBRATION RANGE - RUN II 57~ ENTRY NUISER 3 CONVERTED DEW POINT 30.20 RUN NUtSER 58 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGIIORED COthVERTED DEH POIthT -0.01 RUN NUtSER 58 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED wxxtIANOMETER READING 0~0 HOT IN CALIBRATION RANGE - RUN II 58> ENTRY HUISER 3 CONVERTED DEW POINT 30.02 RVN HUISER 59 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGttORED CONVERTED DEH POINT -0.01 RUN NmSER 59 IS OUT OF RAIIGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEt( IGthORED
<%>MANOMETER READING 0.0 NOT IN CALIBRATION RANGE - RUN It 59 ENTRY NUIIBER 3 CONVERTED DEW POINT 30.38 RUN NUISER 60 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGthORED CONVERTED DEW POINT -0.01 RUH NUISER 60 IS OUT OF RAIIGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED
%~MANOMETER READING 0.0 NOT IH CALIBRATION RANGE - RUN It 60> ENTRY NUMBER
lP w%% ILR PROGRAH RESULTS w>ii SlBNARY OF AVERAGES RUN O ELAPSED AVG TEHP AVG PRESS AVG V PRESS AVG TEHP AVG PRESS AVG V PRESS AVG TEHP AVG PRESS AVG V PRFSS TIHE UPPER UPPER UPPER LONER. LMER LOHER ICE ICE ICE 1 0.0 73.6350 26.8910 0.1063 72.9923 26.9007 0 F 1088 16.5234 26.9328 0.0378 2 0.50 73.6328 26.8908 0.1066 73.0032 26.8999 0.1090 16.5008 26.9331 0.0381 3 1.00 73.6021 26.8893 0.1059 72 '950 26.8990 0.1090 16.6170 26.9366 0.0403 1.50 73.6069 26.8907 0.1062 72.9993 26.8999 0.1090 16.5822 26.9323 0.0400 5 2.00 73.5646 26.8897 0.1069 73.0450 26.8987 0. 1091 16.5737 26.9325 0.04R4 6 2.50 73.5487 26.8860 0.1042 73.0282 26.8956 0. 1092 16. 7174 26.9290 0.0388 7 3.00 73.5097 26.884i5 0.1045 73.0557 26.8943 0.1092 16.5888 26.9282 0.0398 8 3.50 73.5279 26.8862 0.1050 73.0486 26.8954 0.1089 16.5525 26.9281 0.0421 9 4.00 73.5105 26.8859 0.1052 73.0481 26.8950 0.1090 16.4978 26.9289 0 '392 10 4.50 73.4839 26.8843 0. 1017 73.0703 26.8939 0.1092 16.5131 26.9248 0.0391 ll la 5.00 5.50 73.4658 73.4574 Zs.eeas 26.8838 0.1022 0.1026 73.0629 73.0982 26.8923 26.8932 0.1093 0.1092 16.5279 16.5164 26.9231 26.9248 0.0419 0.0345 13 6.00 73.4181 R6.8809 0.1025 73.0873 26.8898 0.1092 6447 26.9228 0.033R 14 6.50 73.4004 26.8809 0.1023 73.0979 26.8896 0. 1100 16.5743 26.9206 0.0340 15 7.00 73.3917 26.8801 0.1024 73. 1176 26.8894 0.1104 16.5798 26.920R 0.0368 16 7.50 73.3882 26.8810 0.10R1 73.0999 26.8904 0.1107 16.6251 26.9210 0.0352 17 18 8.00 8.50 73.3430 73.3737 as+8?98 26.8791 0.1017 0.1028
73. 1157
?3.1392 26.8890 26.8875 O. llll 0.1116 16.5111 16.5315 26.9197 26.9181 0.0338 0.0353 19 9.00 73.3160 26.8756 0.1026 73.1169 26.8847, 0.1118 16.5893 26.9156 0.0385 Ro 9.50 73.3240 26.8744 0.1025 73.1290 Zs.e842 0.1122 16.6241 26.9150 0.0344 21 10.00 73.2817 26. 8745 0.1024 73.1148 Zs.ee41 0. 1124 16.4346 26.9151 0.0360 22 10.50 73.2598 26.8745 0.1017 73.1151 26.8841 0.1126 1425 26.9152 0.0369 23 11.00 73.2144 26.8722 0.1022 73.1Z85 26.8812 0.1129 16.6325 26.9127 0.0395 24 11.50 73 '130 26.8759 0.1026 73.1661 R6.8844 0.11Rl 16.604O 26.9166 0.0357.
25 1'2. 00 73.2055 26. 8743 0. 1022 73. 14Z8 26.8834 0. 1126 16.6286 26. 9150 0.0397 26 12.50 73.1777 26.8714 0. 1024 73.1564 Rs.coos 0.1129 16 '941 26.9123 0.0375 27 13.00 73.1413 26.8693 0.1028 73.1766 26.8782 0.1133 16.8032 26.9109 0.0394 28 13.50 73.1214 26.87R4 0.1025 73.1848 26.8821 0.1136 16 '762 26.9165 0.0405 29 14.00 73.1088 26.8716 0.10RR 73.1861 26.8808 0.1140 16.7471 26.9110 0.0394 30 14.50 73.0655 26.8704 0.0980 73.2041 26.8797 0.1144 16.8159 26.9089 0.0390 31 15.00 73.0370 26.8672 0.0977 73.R839 26.8764 0. 1148 16.8130 26.9049 0.0410 32 15.50 73.0720 Zs.e?o4 0.0941 73.2359 R6.8797 0. 1147 16.7908 26.9087 0.0437 33 16+00 '3.0165 26.8664 0.0957 73.2042 26.8757 0.1152 16.9242 26.9047 0.0390 34 16o50 72.9861 26.8653 0.0957 73.2203 26.874ie 0.1157 16.8093 26.9035 0.0375 35 17.00 72.9818 R6.8631 0.0967 73.2525 26.8727 0.1163 16.8521 26.9016 0.0426 36 17.50 72.9545 26.8665 0.0960 73.2520 26.8759 0.1167 16.8890 26.9055 0.0377 37 18.00 72.9398 26 '650 0.0962 73.2606 R6.8742 0.1173 16.8739 26.9043 0.0380 38 18.50 72.9190 26.8631 0.0956 73.2271 26,8724 0.1073 16.8975 26.9025 0.0392 39 19.00 72.8819 26.8599 0.0967 73.253R 26.8690 0.1074 16.9193 26.8980 0.0419 40 "
19.50 72.8787 26 ~ 8601 0.0966 73.2619 26.8694 0. 1074 16. 9741 26.8967 0.0377 41 20 F 00 72.8323 26.8600 0.0984 73.2629 26.8688 0.1074 16.8934 26.8962 0.0392 42 20.50 72.8278 26.8604 0.0984 73.2242 26.8695 0.1075 16.934? 26.8970 0.0421 43 21.00 72.8049 26.8581 0.0937 73.2522 R6.8673 0.1076 17.1532 26.8945 0.0445 44 21.50 7R.?894 26.8622 0.0946 73.2594 26.8714 0.1076 17.1978 26.8991 0.0433 4i5 22. 00 72.7762 26.8609 0.0953 73.2436 26.8708 0.1077 17.289R 26.8982 0.0440 46 22.50 72.7554 26.8593 0.0957 73.2545 26.8686 0.1078 17.4i887 26.8961 0.0454 47 23. 00 72.7289 26.8581 0.0957 73.2705 26.86'72 0.1077 17.54i59 26.8944 0.0454 48 23.50 72.7151 26.8610 0.0958 73.2566 26.8701 0.1131 17.5147 26.8981 0 '422 49 24.00 72.7202 26.8605 0 '951 -73.2505 26.8699 0.1134 17.5125 26.8978 0.0425 24.50 72 '949 26 0600 0.0952 73.2834 26.8690 0.1078 17.5982 26.8966 0.0432 25.00 72.6849 26.8579 0.0986 73.2875 Oj" 0.1080 17.6243 26.8945 0.0429
52 25.50 72.6477 26.8581 0.0993 73.2760 26.8674 0.1080 17.4559 26.8949 0.0437 53 26.00 72.6652 26.8533 0.0989 73.2651 26.8623 0. 1078 17.4347 26.8900 0.0383 55 27. 00 72.6368 26.8494 0.0921 73.3084 26.8584 0.1079 17.1104 26.8868 0.0396 56 27.50 72.6281 26.8530 0. 0931 73.2612 26.8619 0.1067 17.1975 26.8904 0.0303 57 28. 00 72.6123 26.8563 0.0927 73.2602 26.8604 0.1068 17.1651 26.8890 0.0377 58 28.50 72.5976 26.8538 0.0931 73.2702 26.8595 0.1069 17.2051 26.8882 0.0404 59 29. 00 72.5783 26.8545 0.0928 73.2619 26.8598 0.1070 17.2416 26.8889 0.0451 60 29.50 72.5853 26.8520 0.0935 73.2703 26.8533 0.1072 17.3535 26.8865 0.0355
(pe:
RESULTS OF TtlE LINEAR REGRESSION ANAlYSIS H LEAKAGE RATE LEAKAGE H UPPER H LONER I$ ICE EXPERIHENTAL UPPER LIMIT RATE CONTAINt1ENT CONTAINtENT CONDEttSER 3 0.99996 -0.12190 -0.08438 1.00001 0.99992 0.99985 0.99998- -0.12136 -0.03094 1.00004 0.99995 0.99978 5 0.99994 -0.10272 -0.05191 1.00006 0.99981 0.99971 6 0.99988 -0.15827 -0.09610 1.00005 0.99973 0.99941 7 0.99988 -0.14356 -0.10153 1.00006 0.99963 0.99962 8 0.99990 -0.12050 -0.08513 1.00007 0.99969 0.99960 9 0.99993 -0.09872 -0.06168 1.00008 0.99967 0.99985 10 0.99996 -0.07724 -0.04015 1.00020 0.99958 0.99968 ll 12 0.99989 0 ~ 99995
-0.07180
-0.05718
-0.04190
-0.02924 1.00015 1.00020 0.99954 0.99951 0 ~ 99948 0.99984 13 0.99987 -0.05809 "0.03414 1.00017 0.99940 0.99955 14 0.99988 -0.05500 -0.03465 1.00021 0.99934 0.99958 15 0.99984 -0.05752 -0.03935 1.00019 0.99928 0.99945 16 0.99988 -0.05262 -0.03657 1.00025 0.99934 0.99945 17 0.99992 -0.04600 -0.03072 1.00030 0.99925 0 ~ 99969 18 0.99979 -0.05182 -0.03692 1.00017 0.99913 0.99953 19 0.99972 -0.06Z33 -0.04614 1.00016 0.99906 0.99920 20 0.99968 -0.07194 "0.05495 1.00010 0.99900 0.99925 Zl 0.99978 -0.07006 -0.05474 1.00019 0.99902 0.99960 22 0.99981 -0.06622 -0.05208 1.00026 0.99901 0.99955 23 0 ~ 99968 -0.06963 -0.05613 1.00024 0.99886 0.99896 24 0.99982 -0.06501 -0.05200 1.00036 0.99894 0.99930 25 0.99977 -0.06265 -0.05063 1.00033 0.99893 0.99905 26 0.99964 -0.06586 -0.05423 1.00027 0.99878 0.99868 27 0.99957 -0.07135 -0.05944 1.000Z4 0.99865 0.99854 28 0.99973 -0.06871 "0.05750 1.00041 0.99877 0.99876 29 0.99970 -0.06702 -0.05656 1.00041 0.99870 0.99866 30 0.99976 -0.06367 -0.05346 1.00061 0.99861 0.99845 31 0.99962 -0.06435 -0.05473 .1.00055 0.99832 0.99824 32 0.99980 -0.06041 -0.05049 1.00074 0.99854 0.9983Z 33 0.99968 -0.05917 -0.04984 1.00064 0.99843 0 ~ 99807 34 0.99970 -0. 05751 -0.04866 1.00065 0.99835 0.99832 35 0.99954 -0.05964 -0.05100 1.00054 0.99819 0.99797 36 0.99972 -0.05726 -0.04884 1.00074 0.99829 0.99822 37 0.99967 -0.05589 -0.04787 1.00071 0.99819 0.99820 38 0.99975 -0.05324 -0.04523 1.00070 0.99856 0.99803 39 0.99961 -0.05310 "0.04550 1.00061 0.99838 0.99772 40 0.99962 -0.05261 -0.04539 1.00062 0.99838 0.99772 41 0.99963 -0.05181 -0.04493 1.00064 0.99835 0.99781 42 0.99965 -0.05063 -0.04402 1.00066 0.99845 0.99765 43 0.99961 -0.05001 -0.04370 1.00080 0.99831 0. 99701 44 0 '9976 -0.04769 -0.04120 1.00095 0.99845 0.99713 45 0 '9970 -0.04607 -Oo03972 1.00090 0.99846 0.99688 46 0.99958 -0.04600 -0.03992 1.00086 0.99835 0.99633 47 0.99953 -0.04638 -0.04053 1.00086 0.99827 0.99615 48 0.99963 -0.04542 -0.03977 1.00100 0.99820 0 ~ 99647 49 0.99962 -0.04453 -0.03907 1.00099 0.99819 0.99646 50 0.99964 -0.04350 -0.03819 1.00102 0.99831 0.99620 51 0,99949 -0.04408 -0.03893 1.00083 0.99822 0.99608 52 .0.99957 "0.04361 -0.03865 1.00088 0.99826 0.99642 53 0 99942 -0.04481 -0.03990 1.00068 0.99809 0.99648 55 0.99951 -0.04469 -0.03996 1.00085 0.99786 0 '9699 56 0.99965 -0.04329 -0.03856 1.00096 0.99813 0.99699 P.ggg74 -0.04141 -0.03645 +113 0.99807 0.99763
~ M f~kr.q 0.99965 -0.04020 -0.03530 1.00105 0.99801 0.99682 59 0 '9967 -0.03888 -0.03401 1.00112 0.99804 0.99659 60 0.99952 -0.03874 -Oo03404 1.00099 0.99777 0.99663 FINAL LEAKAGE RATE (% PER DAY) = -0.03404 INTERCEPT"- 0.99994 UPPER CONFIDENCE LIMIT FOR THE RATE IS -0.03874 WX>TYPE A TEST COMPLETION CRITERIA MESSAGES>>K TYPE C LEAKAGE PENALTY = -867.00 (SCCM) = -0.0020 'tiMf/OAY)
THE LEAK RATE UPPER LIMIT HAS CONVERGED TO AN ACCEPTABLE LEVEL THE DIFFERENCE BETNEEN THE LEAK RATE UPPER LIMIT AND MEASURED LEAK RATE IS ACCEPTABLE FOR COMPLETION.
LEAK RATE UPPER LIMIT DOES NOT SHON NEGATIVE TREND OVER LAST 5 RUNS.
MEASURED LEAK RATE SHONS NEGATIVE TREND IN LAST 5 RUNS - CONTINUE TESTING
17
<>><<><<<>< FIXED INPUT DATA %%K%K%K%%xxx TEST START = RUN 0 ~0 TEST END = RUN C 0 RTD MILLI-VOLTTO FAHRENHEIT CONVERSION COEFFICIENTS UPPER LONER ICE 2.00 0.0 2.00 0.0 2.00 0.0 HYGROMETER MILLI"VOLTTO FAHRENHEIT CONVERSION COEFFICIENTS UPPER-1 LOWER-1 ICE-1 0.00053 1.97638 -0.05018 0.00061 1.96939 -0.01108 0 '0069 1.96622 -0.03787 UPPER"2 LOWER-2 ICE-2 0.0 18.00000 32.00000 0.00063 1.96888 "0.00069 0.0 18.00000 32.00000 MANOMETER PRESSURE CORRECTION COEFFICIENTS Wl Rl H2 R2 H3 R3 H4 R4 W5 R5 PU-1 34.9568 35.2180 29.9629 30.1800 24.9693 25.1380 19.9754 20.0950 14.9815 15.0680 PU-2 29.9632 29.9634 28.4652 28.4663 26.9671 26.9684 25.4689 25.4688 0.0 0.0 PL"1 0.0 0.0 "
0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 PL-2 29.9632 29.9648 28.4652 28.6466 26.9671 26.9688 25.4689 25.4694 0.0 0.0 PI-1 29.9632 29.9609 28.4652 28.4640 26.9671 26. 9681 25.4689 25.4688 0.0 0.0 PI-2 29.9632 29.9618 28.4652 28.4656 26. 9671 26.9685 25.4689 25.4689 0.0 0.0 P-ATM 14.7020 14.7100 13.5010 13.5010 llo5010 11.4960 9.5020 9.5020 7.5020 7.5000 RTD WEIGHTING FACTORS UPPER
.0628 .1161 .0831 .0831 .0960 .0960 .0960 .0960 .0296 .0296
.0296 .0296 .0740 .0105 .0167 .0513 LOWER
.0415 .0415 .0415 .0415 .0102 .0284 ~ 0586 .0086 .0266 ~ 0586 .1037
.1037 .1037 .1037 .0500 .0092 .0244 .0145 .0170 .0249 .0219 .0240 .0423 .0 ICE
0735 .0735 .0711 0711 .2231 ~ 2789 .2089 VOLUME HEIGHTING FACTORS UPPER LOl'lER ICE 2.0144 1.0000 0.3713 C LEAKAGE PENALTY= -867.00(SCCM)p
~
~
TYPE A MEASURED LEAK f+P -0.02065 {/HT/DAY)) IMPOSED LEAK RATE = -3.000 (SCFM
~%rr k r
(c-"",))
%%%%%%%)f%%% FIXED INPUT DATA %%K%K%xmwww%
TEST START = RUN ¹ 0 TEST END = RUN ¹ 0 RTD MILLI-VOLTTO FAHRENllEIT CONVERSION COEFFICIENTS UPPER LOWER ICE 2.00, 0.0 2.00 0.0 2.00 0.0 HYGROMETER MILLI-VOLTTO FAHRENHEIT CONVERSION COEFFICIENTS UPPER-1 LOWER-1 ICE"1
0. 00053 l. 97638 -0. 05018 0. 00061 l. 96939 . -0. 01108 0.00069 1.96622 -0.03787 UPPER-2 LOWER-2 ICE-2 0.0 18.00000 32.00000 0.00063 1.96888 -0.00869 0.0 18.00000 32.00000 MANOMETER PRESSURE CORRECTION COEFFICIENTS Hl Rl W2 R2 H3 R3 H4 R4 H5 R5 PU-1 34.9568 35.2180 29.9629 30.1800 24.9693 25.1380 19-9754 20.0950 14 9815 15.0680 PU-2 29.9632 29.9634 28.4652 28.4663 26.9671 26 '684 25.4689 25.4688 0.0 0.0 PL-1 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 PL"2 29.9632 29,9648 28.4652 28.6466 26.9671 26.9688 25.4689 25.4694 0.0 0.0 PI-1 29.9632 29.9609 28.4652 28.4640 26.9671 26.9681 25.4689 25.4688 0.0 0.0 PI-2 29.9632 29.9618 28.4652 28.4656 26.9671 26.9685 25.4689 25.4689 0.0 0.0 P-ATM 14.7020 14.7100 13.5010 13.5010 11.5010 11.4960 9.5020 9.5020 7.5020 7.5000 RTD WEIGHTING FACTORS UPPER
.0628 .1161 .0831 .0831 .0960 .0960 .0960 .0960 .0296 .0296
~ 0296 .0296 .0740 o0105 .0167 .0513 LOHER
~ 0415 .0415 .0415 .0415 .0102 .0284 .0586 .0086 .0266 .0586 .1037
~ 1037 ~ 1037 .1037 .0500 .0092 .0244 .0145 .0170 .0249 .0219 .0240 .0423 .0 ICE
.0735 .0735 .0711 .0711 .2231 .2789 .2089 VOLUME HEIGRTING FACTORS UPPER LOWER ICE 2.0144 1.0000 0.3713 C LEAKAGE PENALTY- 867 00tSCCM)) TYPE A
~ MEASURED LEAK R~ 0 ~ 02065 (/HT/DAY)) IMPOSED LEAK RATE -3.000 [SCFM) i
(4 RUN NUHBER 1 ELAPSED TINE 0.0 CONTAINHENT TEHPERATURES DATA CllECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTO ttILLI-VOLTS DEG. F.
ETR"101 40.88 81.76 ETR-122 35.70 71.40 ETR-115 9. 13 18.26 ETR-102 ETR-103 38.89 35.83 77 '8 71.66 ETR-123 ETR-124 36.54 37.11
73. 08
74. 22 ETR-116 9. 08 8.86 18.16 ETR-117 17.72 ETR-104 35. 75 71.50 ETR-125 35.83 71.66 ETR-118 10.49 20.98 ETR-105 36.82 73.64 ETR-126 35.94 71.88 ETR-119 7.93 15.86 ETR-106 36.96 73.92 ETR-127 33.99 67.98 ETR-120 7.57 15.14 ETR-107 36: 77 73.54 ETR-129 36.94 73.88 ETR-121 7. 98 15.96 ETR-108 36.74 73.48 ETR-130 35.62 71.24 ETR-109 35.55 71.10 ETR-131 34.07 68.14 ETR-110 35.38 70.76 ETR-132 37.54 75.08 ETR-111 35.59 71.18 ETR-134 36.53 73.06 ETR-112 35.60 71.20 ETR-135 36.39 72.78 ETR-114 34.73 69.46 ETR-136 36.50 73.00 ETR-128 36. 35 72.70 ETR-137 36.11 72.22 ETR-133 34.31 68.62 ETR-138 36.57 73.14 ETR-113 37.34 74.68 ETR-139 33.58 67. 16 ETR"140 36.40 72.80 ETR-141 37.02 74.04 ETR-142 36.00 72.00 ETR"143 37.52 75.04 ETR-144 36.80 73 '0 ETR-145 41.47 82.94 ETR-146 36.90 73.80 UPPER VOLUHE (DEG. F. )
UPPER VOLUttE (DEG. R. )
73.63 533.33 'CE SUHHARY OF HEIGHTED AVERAGE TEHPERATURES LONER VOLUHE (DEG. F. )
LONER VOLUttE (DEG. R. )
CONTAIttttENT VAPOR PRESSURE DATA CHECK HILLI- DEN POINT 72.99 532.69 ICE CONDENSER tDEG.
CONDENSER tDEG.
F.)
R.)
16.52 476.22 COtA'AINtfENT PRESSURES DATA CHECK VAPOR PRESSURE UNCORRECTED CORRECTED HYGROttETER VOLTS [DEG. F.) (PSIA) HANOHETER READING t PSIA) READIttG t PSIA)
UPPER: UPPER:
VPU-1 18.37 36.43 0.1058 PU-1 27.0510 26.8639 VPU-2 0.26 36.68 0.1068 PU-2 26.9194 26.9182 LOWER: LOWER:
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL"2 18.76 37.15 0. 1088 PL-2 26.9023 26.9007 ICE -'PI ICE:
1 7. 88 15.50 0.0406 PI-1 26 '231 26. 9221 VPI-2 -1.08 12.56 0.0351 PI-2 26.9449 26.9435 AtSIEtfT 14.5050 14.4984 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT t PSIA) 0.1063 LONER CONTAINHENT ( PSIA) 0.1088 AVERAGE UPPER PRESSURE (PSIA) 26.8910 ICE CONDENSER (PSIA) 0.0378 AVERAGE LOWER PRESSURE tPSIA) 26.9007 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9328 AVERAGE CONTAINHENT PRESSURE ( PSIA ) 26. 9082 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.4098
)
(jig RUN NUHBER 2 ELAPSED TIHE 0.50 CONTAINMENT TEMPERATURES DATA CHECK UPPER VOLUME LOWER VOLUME ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 CD.86 81. 72 ETR-122 35.65 71.30 ETR-115 . 9.30 18.60 ETR-102 38. 87 77. 74 . ETR-123 36.54 73.08 ETR-116 9.21 18.42 ETR-103 35.80 71.60 ETR-124 37.12 74.24 ETR-117 8.75 17.50 ETR-104 35.77 71.54 ETR-125 35.86 71.72 ETR"118 10.08 20. 16 ETR-105 36.85 73.70 ETR-126 35.96 71.92 ETR"119 7.94 15.88 ETR-106 36. 95 73.90 ETR-127 34.01 68.02 ETR-120 7.59 15.18 ETR-107 36. 79 73.58 ETR-129 36.97 73.94 ETR-121 7. 96 15. 92 ETR-108 36 74
~ 73.48 ETR"130 35.61 71.22 ETR-109 35.53 71.06 ETR-)31 34.01 68.02 ETR-110 35.34 70.68 ETR-132 37.54 75.08 ETR-ill 35.59 71.18 ETR-134 36.55 73 '0 ETR-112 35. 60 71. 20 ETR-135 36.39 72.78 ETR-114 34.74 69.48 ETR-136 36.49 72.98 ETR-128 36. 35 72.70 ETR-137 36.13 72.26 ETR-133 34.31 68.62 ETR-138 36.59 73.18 ETR-113 37. 35 74.70 ETR"139 33.58 67. 16 ETR-140 36.41 72.82 ETR-14) 37.02 74.04 ETR-142 36.01 72.02
~ ETR-143 37 '2 75.04 ETR-144 36.81 73.62 ETR-145 41.48 82.96 ETR-146 36.90 73.80
SUMMARY
OF WEIG((TED AVERAGE TEHPERATURES
'UPPER VOLUt(E (DEG. F.) 73.63 LOWER VOLUHE (DEG. F.) 73.00 ICE CONDENSER (DEG. F.) 16.50 UPPER VOLUHE (DEG. R.) 533'33 LOt(ER VOLUHE (DEG. R.) 532.70 ICE CONDENSER (DEG. R. ) 476.20 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK Hli.LI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER
VOLTS (DEG. Fo) (PSIA) HANOtfETER READING (PSIA) READING (PSIA)
UPPER:. UPPER:
VPU-1 18.41 36.51 0.1061 PU-1 27.0510 26.8639 VPU-2 0.26 36.73 0.1070 PU-2 26.9189 26.9177 LO((ER'PL-1 LOWER:
0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.78 37.19 0.1090 PL-2 26.9015 26.8999 ICE: ICE'I-1 VPI-1 7. 68 15.11 0.0398 26.9231 26.9221 VPI-2 -1.04 13.28 0.0364 PI-2, 26.9455 26.9441 AHBI5)(T 14. 5050 14.4984 AVERAGE VAPOR PRESSURES SUHMARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.1066 LOWER CONTAINHENT (PSIA) 0.1090 AVERAGE UPPER PRESSURE (PSIA) 26.8908 ICE CONDENSER (PSIA) 0.0381 AVERAGE LOWER PRESSURE (PSIA) 26.8999 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26 ~ 9331 AVERAGE COt(TAIt(t(ENT PRESSURE (PSIA) 26.9079 AVERAGE CONTAIN((ENT PRESSURE (PSIG) 12.4096
'~
RUN NJt )DER 3 ELAPSED TIHE 1.00 CONTAINttENl TEHPERATURES DATA CIIFCK UPPER VOLUME LONER VOLUMC ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F~ RT 0 MILLI "VOLTS DEG. F.
ETR-101 40.85 81.70 ETR-122 35.69 71.38 ETR-115 9.52 19.04 ETR-102 38.86 77.72 ETR-123 36.56 73.12 ETR-116 9. 25 18.50 ETR-103 35.80 71.60 ETR-124 37.11 74.22 ETR-117 8.98 17.96 ETR-104 35. 78 71.56 ETR"125 35.89 71.78 ETR-118 10 ~ 2 1 20.42 ETR-105 36.79 73.58 ETR-126 35.96 71.92 ETR-119 7.95 15.90 ETR-106 36. 94 73.88 ETR-127 34.02 68.04 ETR-120 7.60 15.20 ETR-107 36.76 73.52 ETR-129 36.97 73.94 ETR-121 8.00 16.00 ETR-108 3'6. 67 73.34 ETR-130 35.61 71.22 ETR-109 35.53 71.06 ETR-131 34.02 68.04 ETR-110 35.35 70.70 ETR-13Z 37.55 75.10 ETR-ill 35.58 71.16 ETR-134 36.46 72.92 ETR-112 35.61 71. 22 ETR-135 36.41 72.82 ETR-114 34. 74 69.48 ETR-136 36.48 72 '6 ETR-128 36. 36 72.72 ETR-137 36.11 72.22 ETR-133 34.31 68.62 ETR-138 36.58 73. 16 ETR-113 37.38 74.76 ETR-139 33.59 67. 18 ETR-140 36.41 72.82 ETR-141 37.04 74.08 ETR-142 36.02 72.04 ETR-143 37.53 75.06 ETR-144 36.82 73.64 ETR-145 41.50 83.00 ETR-146 36.92 73.84 SUHHARY OF HEIGllTED AVERAGE TEMPERATURES UPPER VOLUME tDEG. F.) 73.60 LONER VOLUHE tDEG. F.) 73.00 ICE CONDENSER tDEG. F.) 16.62 UPPER VOLUME tDEG. R.) 533.30 LONER VOLUME tDEG. R.) 532.69 ICE CONDENSER tDEG. R.) 476.32 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA Cl>ECK HILLI- DEN POINT VAPOR PRESSURE U)tCORRECTED CORRECTED HYGROMETER VOLTS t DEG. F. ), tPSIA) HANOMETER READING tPSIA) READING tPSIA)
UPPER: UPPER'U-1 VPU-1 18.33 36.35 0.1054 27.0490 26.8620 VPU-2 0.26 36.59 0.1064 PU-2 26.9179 26.9167 LONER: LOt tER:
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0~0 VPL-2 18.79 37.21 0.1090 PL-2 26.9006 26.8990 ICE: ICE:
VPI-1 8.15 16.02 0.0416 PI-1 26.9219 Z6.9209 VPI-2 "0.96 14.72 0.0390 PI-2 26.9536 26.9522 AMBIENT 14.5050 14.4984 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT t PSIA) 0.1059 LONER CONTAItWENT t PSIA) 0.1090 AVERAGE UPPER PRESSURE tPSIA) 26.8893 ICE CONDENSER tPSIA) 0.0403 LONER PRESSURE tPSIA) 26.8990 'VERAGE AVERAGE ICE CONDENSER PRESSURE tPSIA) 26.9366 AVERAGE CONTAINMENT PRESSURE t PSIA) 26. 9083 AVERAGE CONTAINMENT PRESSURE t PSIG) 12.4099
-sim igl 7 RUN NU)KER ELAPSED TIME 1.50 CO)lTAINMENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 40.83 81.66 ETR-122 35.71 71.42 ETR-115 9.42, 18.84 ETR-102 38. 85 77.70 ETR-123 36.57 73. 14 ETR-116 9.23 18.46 ETR-103 35.81 71.62 ETR-124 37.09 74.18 ETR-117 8.86 17.72 ETR-104 35. 77 71.54 ETR-125 35.88 71.76 ETR-118 10.17 20.34 ETR-105 36. 83 73.66 ETR-126 35.97 71.94 ETR-119 7.95 15. 9D ETR-106 36.93 73.86 ETR-127 34.01 68.02 ETR-120 7. 61 15.22 ETR-107 36. 76 73.52 ETR-129 36.95 73.90 ETR-121 8.00 16.00 ETR-108 36.66 73.32 ETR-130 35.63 71.26 ETR-109 35.59 71.18 ETR-131 34.03 68.06 ETR-110 35.45 70.90 ETR-132 37. 56 75.12 ETR-lll 35.58 71.16 ETR-134 36.55 73.10 ETR-112 35.63 71.26 ETR-135 36.35 72 '0 ETR-114 34. 73 69.46 ETR-136 36.48 72.96 ETR"128 36. 36 72.72 ETR-137 36 F 09 72.18 ETR-133 34. 30 68.60 ETR-138 36.59 73.18 ETR-113 37. 35 74.70 ETR-139 33.61 67.22 ETR-140 36.43 72.86 ETR-141 37. 05 74.10 ETR-142 36.04 72.08 ETR"143 37.53 75.06 ETR-144 36.82 73.64 ETR"145 41.49 82.98 ETR-146 36.92 73.84
SUMMARY
OF HEIGHTED AVERAGE TEMPERATURES UPPER VOLUME lDEG. F.) 73.61 LONER VOLUME tDEG. F.) 73.00 ICE CONDENSER tDEG. F.) 16.58 UPPER VOLUME (DEG. R. ) 533.31 LOHER VOLUME tDEG. R.) 532.70 ICE CONDENSER (DEG. R.) 476.28 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINi')ENT PRESSURES DATA CHECK MILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGRO))ETER VOLTS <DEG. F.) t PSIA) HANOHETER READING {PSIA) READING (PSIA)
UPPER: UPPER:
VPU-I 18.35 36.39 0.1056 PU-I 27.0510 26.8639 VPU"2 0.26 36.66 0.1067 PU"2 26.9187 26.9175 LOilER: LONER:
VPL-I 0.0 -0.01 0.0 PL-I 0.0 0.0 VPL-2 18.79 37.21 0.1090 PL-2 26.9015 26.8999 ICE: ICE:
VPI"I 8.05 15.84 0.0412 PI "I 26.9230 26.9220 VPI-2 -0 '7 14.54 0.0387 PI-2 26.9440 14.5069 26.9426 AMBIENT 14.5003 AVERAGE VAPOR PRESSURES SU)iMARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT t PSIA) 0.1062 LONER CONTAINHENT (PSIA) 0.1090 AVERAGE UPPER PRESSURE OPSIA) 26.8907 ICE CONDENSER t PSIA) 0.0400 AVERAGE LOi'iER PRESSURE (PSIA) 26.8999 AVERAGE ICE CONDENSER PRESSURE OPSIA) 26.9323 AVERAGE CONTAINMENT PRESSURE OPSIA) 26.9076 AVERAGE CONTAINMENT PRESSURE t PSIG) 12.4074
(
RUN NUMBER 5 ELAPSED TIME 2.00 CONTAINHENI TEHPERATlJRES DATA CHECK UPPER VOLUME LOWER VOLUHE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.~
ETR-101 40.80 81.60 ETR"122 35. 71 71.42 ETR"115 9.24 18.40 ETR-102 38. 83 77.66 ETR-123 36.56 73.12 ETR-116 9. 19 18.38 ETR-103 35.78 71.56 ETR-124 37.12 74.24 ETR-117 8.86 17. 72 ETR-104 35. 76 71.52 ETR-125 35.88 71.76 ETR-118 10.13 20.26 ETR-105 36.81 73.62 ETR-126 35.96 71.92 ETR-119 7. 96 15.92 ETR-106 36. 91 73.82 ETR"127 33.98 67.96 ETR "120 7. 67 15.34 ETR-107 36.73 73.46 ETR-129 36 '4 73.88 ETR-121 7. 98 15.96 ETR-108 36. 64 73.28 ETR-130 35.61 71.22 ETR"109 35.56 71.12 ETR-131 34.03 68.06 ETR-110 35. 37 70.74 ETR-132 37.56 75.12 ETR-111 35.58 71.16 ETR"134 36.59 73.18 ETR-112 35.60 71.20 ETR-135 36.45 72.90 ETR-114 34. 70 69.40 ETR-136 36.53 73.06 ETR-128 36. 38 72 ~ 76 ETR-137 36.13 72.26 ETR-133 34.31 68.62 ETR-138 36.58 73.16 ETR-113 37.37 74.74 ETR-139 33.61 67.22 ETR-140 36.44 72.88 ETR"141 37.07 74.14 ETR-142 36.04 72.08 ETR-143 37.54 75.08 ETR-144 36.83 73.66 ETR-145 41.50 83.00 ETR-146 36.90 73.80 SUMHARY OF HEIGI(TED AVERAGE TEHPERATURES UPPER VOLUME (DEG. F.) 73.56 LOWER VOLUME tDEG. F.) 73.04 ICE CONDENSER (DEG. F. ) 16.57 UPPER VOLUME (DEG. R. ) 533.26 LOWER VOLUJ(E tDEG. R. ) 532.74 ICE CONDENSER (DEG. R.) 476.27 CONTAINHENT VAPOR PRESSURE DATA Ct(ECK CONTAINJ(ENT PRESSURES DATA HILLI- DEI'I POINT VAPOR PRESSURE UNCORRECTED CORRECTED C(IECK'YGROMETER VOLTS (DEG, F.) (PSIA) HANOHE TER READING (PSIA) READI((G (PSIA)
UPPER: UPPER:
VPU-1 18.43 36.55 0.1063 PU-1 27.0500 26.8629 VPU-2 0.27 36.84 0. 1075 PU-2 26.9176 26.9164 LOWER:
VPL-1 VPL-2 .
0.0 18.80
'O.D1 37. 23 0.0 0.1091 LOWER:
PL-1 PL-2 0.0 26.9003 , 26.8987 0.0 ICE- ICE:
VPI-1 8.74 17. 21 0.0441 PI-1 26.9213 26.9203 VPI-2 -0. 91 15.62 0.0408 PI-2 26.9460 26.9446 AHDIENr 14.4992 14.4926 AVERAGE VAPOR PRESSURES
SUMMARY
OF CORRECTED AVERAGE PRESSURES 1JPPER CONTAINMENT (PSIA) 0.1069 LOWER CONTAINHENT t PSIA) 0.1091 AVERAGE UPPER PRESSURE (PSIA) 26.8897 ICE CONDENSER (PSIA) 0.0424 AVERAGE LO)IER PRESSURE (PSIA) 26.8987 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9325 AVERAGE CONTAIN((E)(T PRESSURE tPSIA) 26.9069 AVERAGE Cm(TAINHENT PRESSURE (PSIG) 12.4143
)
RUN NUHBER 6 ELAPSED TINE 2.50 CONTAINt(Et(T TEHPERATURES DATA CHECK UPPER VOLUIIE LOWER VOLUtIE ICE COtiDENSER RTD NILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40.81 81.62 ETR"122 35. 75 71.50 ETR-115 9. Zl 18.42 ETR-102 38.81 77.62 ETR"123 36.56 73.12 ETR-116 9.21 18.42 ETR-103 35.80 71.60 ETR-124 37. 14 74.28 ETR-117 8. 91 17.82 ETR-104 35. 74 71.48 ETR-1Z5 35.85 71.70 ETR-118 10.96 21.92 ETR"105 36.80 73.60 ETR-126 .35.97 71.94 ETR"119 7.98 15.96 ETR-106 36. 91 73.82 ETR-127 34.02 68.04 ETR-120 7.66 15.32 ETR-107 36. 71 73.42 ETR-129 36.96 35.63 73 '2 71.26 ETR-121 8. 02 16.04 ETR"108 36.62 73.24 ETR-130 ETR-109 35.55 71. 10 ETR-131 34.01 68.02 ETR-110 35.36 70.72 ETR"132 37.56 75. 12 ETR"ill 35.57 71. 14 ETR-134 36.50 73.00 ETR-112 35.59 71.18 ETR-135 36.41 72.82 ETR-114 34.71 69.42 ETR-136 36.52 73.04 ETR-128 36.38 72.76 ETR-137 36.13 72.26 ETR-133 34.31 68.62 ETR-138 36.60 73.20 ETR-113 37.35 74.70 ETR-139 33.61 67.22 ETR"140 36.46 72.92 ETR-141 37.07 74.14 ETR-142 36.04 72.08 ETR-143 37.55 75.10 ETR-144 36.84 73.68 ETR-145 41.50 83.00 ETR-146 36.92 73.84 SUIIHARY OF WEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEGo F ~ ) 73+55 LOI'IER VOLUIIE ( DEG F ~ ) 73 ~ 03 ICE CONDENSER '( DEGo F ~ ) 16.72 UPPER VOLUHE (DEG. R. ) 533.25 LOWER VOLUHE (DEG. R. ) 532.73 ICE CONDENSER .(DEG. R. ) 476.42 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINIIENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS '(DEG. F. ) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-) 17.83 35.36 0.1013 PU-1 27.0460 26.8590 VPU-2 0.26 36.75 0.1071 PU-2 26.9142 26.9130 LOWERi LOWER-'L-1 VPL-1 0.0 -0.01 0.0 0.0 0.0 VPL"2 18.81 37.25 0.1092 PL-2 26.8972 26.8956 ICE '- ICE:
VPI-1 7.90 15.54 0.0406 PI-1 26.9181 26.9171 VPI-2 -1.02 13.64 0.0370 PI-2 26.9422 26.9408 AHBIE 14.5050 14.4984 AVERAGE VAPOR PRESSURES tit'UIOIARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINtIENT (PSIA) 0.1042 LOWER CONTAINHENT (PSIA) 0.1092 AVERAGE UPPER PRESSURE (PSIA) 26.8860 ICE CONDENSER (PSIA) 0.0388 AVERAGE LOWER PRESSURE (PSIA) 26.8956 AVERAGE ICE COtiDENSER PRESSURE (PSIA) 26.9290 AVERAGE CONTAINIIENT PRESSURE ( PSIA) 26. 9035 AVERAGE CONTAINIENT PRESSURE (PSIG) 12.4052
(:~y RUN tlUtRER 7 ELAPSED TINE 3.00 CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUttE LOWER VOLUHE ICE CONDENSER RTD HILLI "VOLTS DEG ~ F. RTD NIL LI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40. 79 81.58 ETR".122 35.70 71.40 ETR-115 9. 04 18.08 ETR-102 38. 79 77.58 ETR-123 36.56 73.12 ETR-116 9.02 18.04 ETR" 103 35. 78 71.56 ETR-124 37.14 74.Z8 ETR-117 8.70 17.40 ETR-104 35. 76 71.52 ETR"125 35.88 71.76 ETR-118 10.50 21.00 ETR-105 36. 71 73.42 ETR-126 35.97 71.94 ETR-119 7.98 15.96 ETR-106 36. 91 73.82 ETR-127 34.03 68.06 ETR-120 7+ 68 15.36 ETR-107 36. 60 73.20 ETR-129 36.93 73.86 ETR-121 8. 04 16.08 ETR-108 36.61 73.22 ETR-130 35.63 71. 26 ETR-109 35.54 71.08 ETR-131 34.03 68.06 ETR-110 35.45 70.90 ETR-132 37.56 75.12 ETR-111 35.57 71.14 ETR"134 36.56 73.12 ETR-112 35.60 71.20 ETR-135 36.46 72.92 ETR-114 34.73 69.46 ETR-136 36.52 73.04 ETR-128 36.42 72.84 ETR-137 36.16 72 '2 ETR-133 34. 32 68.64 ETR-138 36.60 73.20 ETR-113 37.34 74.68 ETR-139 33.62 67.24 ETR-140 36.46 72.92 ETR-141 37.08 74.16 ETR-142 36.05 72.10 ETR-143 37.55 75.10 ETR-144 36.85 . 73.70
~ ETR-145 41.50 83.00 ETR-146 36.93 73.86 SUHttARY OF WEIGHTED AVERAGE TEHPERATllRES UPPER VOLUt1E (DEG. F. ) 73.51 LOWER VOLUHE 1DEG. F. ) 73.06 ICE CONDENSER tDEG. F ) 16.59 UPPER VOLUHE (DEG. R.) 533.21 LONER VOLUHE (DEG. R. ) 532.76 ICE CONDENSER (DEG. R. ) 476.29 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED tlYGROHETER VOLTS 1DEG. F. ) 1PSIA) HAN011ETER READING t PSIA) READING 1PSIA)
UPPER'-
UPPER-'PU-1 17.89 35.48 0.1018 PU-1 27 0440 26.8570 VPU-2 0.26 36.77 0.1072 PU-2 26.9132 26.9120 LO)IER'- LOI'tER:
VPL"1 0.0 -0.01 0' PL-1 0.0 0.0 VPL-2 18.81 37.25 0.1092 PL-2 26.8959 26.8943 ICE'PI-1 ICE:
8.21 16.15 0.0419 PI-1 26.9168 26.9158
'PI-2
-1.00 14. 00 0.0377 PI-2 26.9420 26.9406 AHBIENT 14.5050 14.4984 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONT AIttt1ENT 1PSIA) 0.1045 LOWER CONTAIttttENT (PSIA) 0.1092 AVERAGE UPPER PRESSURE 1PSIA) 26.8845 ICE CONDENSER (PSIA) 0.0398 AVERAGE LONER PRESSURE (PSIA) 26.8943 AVERAGE ICE CONDENSER PRESSURE 1PSIA) 26.9282 AVERAGE COttTAIttHENT PRESSURE (PSIA) 26.9023 AVERAGE CONTAINtiENT PRESSURE 1PSIG) 12.4040 g :>>
kA~,
RUN NU)SER 8 ELAPSED TINE 3.50 CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LOllER VOLUHE ICE CONDENSER RTD ) tILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40.78 81.56 ETR-122 35. 73 71.46 ETR-115 9. 07 18.14 ETR-102 38. 77 77.54 ETR-123 36.59 73.18 ETR-116 9.03 18.06 ETR-103 35. 80 71.60 ETR-124 37. 15 74.30 ETR-117 8. 73 17.46 ETR" 104 35. 78 71.56 ETR-125 35.88 71.76 ETR-118 10. 37 20.74 ETR-105 36.76 73.52 ETR-126 35.99 71. 98 ETR-119 7.98 15.96 ETR-106 36. 90 73.80 ETR-127 34.01 68.02 ETR"120 7. 63 15.26 ETR-107 36.68 73.36 ETR"129 36.98 73.96 ETR 121 8. 04 16.08 ETR-108 36. 60 73.20 ETR-130 35.62 71.24 ETR-109 35.56 71.12 ETR-131 34.01 68.02 ETR-110 35.41 70.82 ETR-132 37.57 75.14 ETR-ill 35.58 71.16 ETR-134 36.51 73.02 ETR"112 35.60 71. 20 ETR"135 36.46 72.92 ETR-114 34.68 69.36 ETR-136 36.52 73.04 ETR-128 36.43 72.86 ETR-137 36.11 72.22 ETR-133 34.32 68.64 ETR-138 36.61 73.22 ETR-113 37. 38 74.76 ETR-139 33.62 67.24 ETR")40 36.48 72.96 ETR-141 37. 11 74.22 ETR-142 36.06 '72.12 ETR"143 37.55 75.10 ETR-144 36.85 73.70 ETR-145 41.49 82.98 ETR-146 36.93 73.86 SUHHARY OF HEIGllTED AVERAGE TEHPERATURES UPPER VOLmtE tDEG. F.) 73.53 LONER VOLUHE tDEG. F.) 73.05 ICE CONDENSER tDEG. F.) 16.55 UPPER VOLUltE tDEG. R.) 533.23 LONER VOLUHE tDEG. R.) 532.75 ICE CONDENSER tDEG. R.) 476 '5 CONTAINHENT VAPOR PRESSURE DATA Cl)ECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETE R VOLTS tDEG. F.) t PSIA) HANOHETER READING tPSIA) READING tPSIA)
UPPER- UPPER:
VPU-1 17.94 35.58 0.1022 PU-1 27.0460 26.8590 VPU-2 0.27 36.90 0.1077 PU-2 26.9147 26.9135 LONER: LOt lER:
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.77 37.17 0.1089 PL-2 26.8970 26.8954 ICE- ICE:
VPI-1 8.83 17.38 0.0444 PI-1 26.9188 26.9178 VPI-2 -0; 94 15.08 0.0397 PI-2 26.9397 26.9383 AHBIENT 14.5050 14.4984 AVERAGE VAPOR PRESSURES SUGARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT t PSIA) 0.1050 LONER CONTAINttENT t PSIA) 0.1089 AVERAGE UPPER PRESSURE tPSIA) 26.8862 ZCE CONDENSER t PSIA) 0.0421 AVERAGE LONER PRESSURE tPSIA) 26.8954 AVERAGE ICE CONDENSER PRESSURE tPSZA) 26.9281 AVERAGE CO)tTAINHENT PRESSURE tPSIA) 26.9032 AVERAGE CONTAINHENT PRESSURE t PSIG) 12.4049
~
RUN NUIIDER 9 ELAPSED TIHE 4.00 CONTAINHENT TEHPERATURES DATA CIIECK UP PER VOLUHE LONER VOLUHE ICE COt(DENSER RTD HILLI-VOLTS DEG. F ~ RTD HILLI-VOLTS DEG. F~ RTD HILLI-VOLTS DEG. F.
ETR-101 40.77 81.54 ETR"122 35. 74 71.48 ETR-115 9. 24 18.48 ETR-102 38.76 77.52 ETR-123 36.55 73.10 ETR-116 8.99 17. 98 ETR"103 35.81 71.62 ETR-124 37.16 74.32 ETR-117 8.57 17. 14 ETR-104 35.75 71.50 ETR-125 35.90 71.80 ETR-118 9.85 19. 70 ETR-105 36.75 73.50 ETR-126 35.99 71.98 ETR-119 8. 00 16.00 ETR-106 36.89 73.78 ETR-127 33.98 67. 96 ETR-120 7. 64 15.28 ETR-107 36 '6 73.32 ETR-129 36.95 73. 90 ETR-121 8. 06 16.12 ETR-108 36.60 73.20 ETR-130 35.63 71. 26 ETR-109 35.55 71.10 ETR-131 34.04 68.08 ETR-110 35.33 70.66 ETR-132 37.57 75.14 ETR-ill 35.58 71.16 ETR-134 36.49 72.98 ETR-112 35.60 71.20 ETR-135 36.42 72.84 ETR-114 34.69 69.38 ETR-136 36.53 73.06 ETR-128 36.45 72.90 ETR-137 36. 15 72.30 ETR-133 34.31 68.62 ETR"138 36.61 73.22 ETR-113 37.39 74.78 ETR-139 33.64 67.28 ETR-140 36.49 72.98 ETR-141 37.10 74.20 ETR-142 36.06 72.12 ETR-143 37.56 75.12 ETR-144 36.87 73.74 ETR"145 41.52 83.04 ETR"146 36 '5 73.90 SUHHARY OF HEIGIITED AVERAGE TEMPERATURES UPPER VOLUtIE (DEG. F. ) 73.51 LOHER VOLUHE IDEG. F. ) 73.05 ICE CONDENSER (DEG. F.) 16.50 UPPER VOLUHE (DEG. R. ) 533.21 LOHER VOLUHE (DEG. R. ) 532.75 ICE CONDENSER (DEG. R.) 476.20 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHEt(T PRESSURES DATA CIIECK HILLI- DEH POINT VAPOR PRESSURE Ut(CORRECTED CORRECTED HYGROHETER VOLTS (DEG. F.) (PSIA) HANOt(ETER READING (PSIA) READIIIG (PSIA)
UPPER: UPPER:
VPU-1 17.96 35.61 0. 1024 PU-1 27.0460 26.8590 VPU-2 0.27 36.95 0.1079 PU-2 26. 9140 26.9128 LOIIER: "
LOHER:
VPL"1 0.0 "-0.01 0.0 PL-1 0.0 0.0 VPL"2 18 79 F 37. 21 0.1090 PL-2 26.8966 26.8950 ICE ICE:
VPI-1 8.19 16. 11 0.0418 PI-1 26.9164 VPI-2 -1.03 13.46 0.0367 PI-2 26.9413 AHBIENT 14.4984 AVERAGE VAPOR PRESSURES
(
SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINIIENT (PSIA) 0.1052 LONER CONTAINIIENT (PSIA) 0.1090 AVERAGE UPPER PRESSURE (PSIA) 26.8859 ICE CONDENSER (PSIA) 0.0392 AVERAGE LOHER PRESSURE (PSIA) 26.8950 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9289 AVERAGE CONTAINtIENT PRESSURE (PSIA) 26 '032 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.4049
RUN NU)KER 10 ELAPSED TINE 4.50 CONTAINHENT TEHPERATURES DATA CtlECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD NILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40. 76 81.52 ETR-122 35.73 71.46 ETR-115 9. 27 18.54 ETR-102 38. 74 77.48 ETR-123 36.56 73.12 ETR-116 8.93 17.86 ETR-103 35. 77 71.54 ETR-124 37.19 74.38 ETR-117 8.63 17. 26 ETR-104 35. 76 71.52 ETR-125 35.90 71.80 ETR-118 9. 94 19.88 ETR-105 36.78 73.56 ETR-126 35.99 71.98 ETR-119 7. 99 15.98 ETR-106 36.87 73.74 ETR-127 34.00 68.00 ETR-120 7. 66 15.32 ETR-107 36.58 73 F 16 ETR-129 37.01 74.02 ETR "121 8. 04 16.08 ETR-108 36.56 73.12 ETR-130 35.63 71.26 ETR-109 35.55 71.10 ETR"131 34.03 68.06 ETR-110 35.38 70.76 ETR-132 37.56 75.12 ETR-ill 35.58 71.16 ETR-134 36.57 73.14 ETR-112 35.61 71.22 ETR-135 36.43 72.86 ETR-114 34. 74 69.48 ETR-136 36.51 73.02 ETR"128 36.43 72.86 ETR-137 36.15 72.30 ETR-133 34. 31 68.62 ETR-138 36.59 73.18 ETR-113 37. 34 74.68 ETR-139 33.65 67.30 ETR-140 36.49 72.98 ETR-141 37.12 74.24 ETR-142 36.07 72.14 ETR-143 37.56 75.12 ETR-144 36.86 73.72 ETR-145 41.52 83.04 ETR-146 36.95 73.90 SUHHARY OF HEIGHTED AVERAGE TEttPERATURES UPPER VOLUHE tDEG. F ~ ) 73.4i8 LONER VOLUHE (DEG. F. ) 73.07 ICE CONDENSER tDEG. F. ) 16.51 UPPER VOLUHE tDEG. R.) 533.18 LOttER VOLUHE tDEG. R.) 532.77 ICE CONDENSER tDEG. R. ) 476.21 CONTAINHENT VAPOR PRESSURE DATA Cl)ECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROttETE R VOLTS (DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17.87 35.44 0.1017 PU-1 27.0440 26.8570 VPU-2 -0.14 29.4i8 0.0 PU-2 26. 9128 26. 9116 LONER: LOHERi VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.81 37'25 0 '092 PL-2 26.8955 26.8939 ICE: ICE:
VPI-1 8. 20 16.13 0.0418 PI-1 26.9160 26.9150 VPI-2 -1.04 13. 28 0 '364 PI"2 26.9360 26.9346 AttBIEtfT 14.5108 14.5041 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTEO AVERAGE PRESSURES UPPER CONTAINHENT tPSIA) 0.1017 LONER CONTAINHENT (PSIA) 0.1092 AVERAGE UPPER PRESSURE (PSIA) 26.8843 ICE CONDENSER t PSIA) 0.0391 AVERAGE LONER PRESSURE (PSIA) 26.8939 AVERAGE ICE CONDEttSER PRESSURE (PSIA) 26.9248 AVERAGE COttTAINttENT, PRESSURE ( PSIA ) 26. 9010 AVERAGE CONTAINHENT PRESSURE t PSIG) 12.3969
0 6
RUN ttUttDER ELAPSED TIHE ll 5.00 CONTAINHENT TEHPERATURES DATA CIIECK UPPER VOLUME LONER VOLUttE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD ttILLI"VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR"101 40.71 81.42 ETR-122 35.76 71.52 ETR-115 9. 11 18.22 ETR-102 38. 72 77.44 ETR-123 36.56 73.12 ETR-116 9.03 18.06 ETR" 103 35. 77 71.54 ETR-124 37.16 74.32 ETR-117 8. 61 17.22 ETR-104 35. 74 71.48 ETR-125 35.90 71.80 ETR-118 9.94 19.88 ETR-105 36. 73 73.46 ETR-126 35.99 71.98 ETR-119 7.99 15.98 ETR-106 36.85 73.70 ETR-127 33.99 67.98 ETR-120 7. 70 15.40 ETR-107 36. 64 73.28 ETR-129 37.00 74.00 ETR-121 8.05 16.10 ETR-108 36.55 73.10 ETR-130 35.62 71.24 ETR-109 35.55 71.10 ETR-131 34.02 68.04 ETR-110 35.38 70.76 ETR-132 37.57 75.14 ETR-111 35.58 71.16 ETR"134 36.54 73.08 ETR-112 35.60 71.20 ETR-135 36.40 72.80 ETR-114 34.73 69.46 ETR-136 36.51 73.02 ETR-128 36. 43 72.86 ETR-137 36.16 72.32 ETR-133 34.31 68.62 ETR-138 36.60 73.20 ETR-113 37.36 74.72 ETR-139 33.66 67.32 ETR-140 36.49 72.98 ETR-141 37.12 74.24 ETR-142 36.07 72.14 ETR-143 37.56 '75.12 ETR-144 36.87 73.74 ETR-145 41.54 83.08 ETR-146 36.97 73.94 SUNtARY OF HEIGI)TED AVERAGE TEMPERATURES UPPER VOLUME tDEG. F. ) 73.47 LONER VOLUttE (DEG. F. ) 73.06 ICE CONDENSER (DEG. F. ) 16.53 UPPER VOLUME tDEG. R.) 533.17 LOHER VOLUME (DEG. Ro) 532.76 ICE COttDENSER (DEG. R.) 476.23 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROt'tETER VOLTS (DEG. F. ) (PSIA) MANOMETER READING tPSIA) READING tPSIA)
UPPER- UPPER-'U"1 VPU"1 17. 94 35.58 0.1022 27.0420 26.8550 VPU-2 -0.09 30.38 0.0 PU"2 26.9112 26.9100 LO)tER t LOHER-VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.82 37.27 0.1093 PL-2 26.8939 26.8923 ICE- ICE:
VPI-1 8.99 17.69 0.0451 PI"1 26.9146 26.9136 VPI-2 -0.97 14.54 0.0387 PI-2 26.9340 26.9326 At)DIENT 14.5108 14.5041 AVERAGE VAPOR PRESSURES SWARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINt!ENT (PSIA) 0.1022 LOllER CONTAINMENT (PSIA) 0. 1093 AVERAGE UPPER PRESSURE [PSIA) 26.8825 ICE COttDENSER t PSIA) 0.0419 AVERAGE LONER PRESSURE (PSIA) 26.8923 AVERAGE ICE CONDENSER PRESSURE tPSIA) 26.9231 AVERAGE COttTAINMENT PRESSURE t PSIA) 26.8993 AVERAGE CONTAIttMENT PRESSURE (PSIG) 12.3952
)
Q>>;
RUN NUIISER 12 ELAPSED TIME 5.50 CONTAINHENT TEMPERATURES DATA CllECK UPPER VOLUME LOHER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTO HILL1-VOLTS DEG. F ~ RTD HILLI "VOLTS DEG. F.
ETR-101 40.71 81.42 ETR-122 35. 75 71.50 ETR-115 9. 05 18.10 ETR-102 - 38. 71 77.42 ETR-123 36.59 73.18 ETR-116 9. 03 18.06 ETR"103 35. 79 71.58 ETR"124 37. 15 74.30 ETR-117 8.59 17.18 ETR-104 35.77 71.54 ETR"125 35.89 71.78 ETR-118 9.90 19.80 ETR-105 36. 71 73.42 ETR-126 35.99 71.98 ETR-119 8.00 16.00 ETR-106 36.85 73.70 ETR-127 33.95 67. 90 ETR-120 7. 71 15.42 ETR-107 36. 63 73.26 ETR-129 37.01 74. 02 ETR-121 8. 04 16.08 ETR-108 36. 50 73-00 ETR"130 35.62 71.24 ETR-109 35.55 71.10 ETR-131 34.00 68.00 ETR-110 35.38 70.76 ETR-132 37.57 75.14 ETR-ill ETR"112 35:56 35.59 71 '2 71.18 ETR-134 ETR-135 36.59 36.46 73.18 72.92 ETR-114 34.76 69.52 ETR-136 36.57 73. 14 ETR-128 36. 46 72.92 ETR-137 36.17 72.34 ETR-133 34.30 68.60 ETR-138 36.60 73.20 ETR-113 37.34 74.68 ETR-139 33.67 67.34 ETR-140 36.50 73.00 ETR-141 37.13 74.26 ETR-142 36.08 72.16 ETR-143 37.57 75.14 ETR-144 36.87 73.74 ETR-145 41.54 83.08 ETR-146 36. 95 73.90 SUHMARY OF HEIGIITED AVERAGE TEHPERATURES UPPER VOLUME IDEG. F.) 73.46 LOHER VOLUME IDEG. F.) 73.10 ICE CONDENSER (DEG. F.) 16.52 UPPER VOLUME IDEG. R.) 533.16 LOHER VOLUME IDEG. R.) 532.80 ICE CONDENSER IDEG. R.) 476.22 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CIIECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS IOEG. F. ) IPSIA) HANOMETER READBIG IPSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17.99 35. 67 0. 1026 PU-1 27.0440 26.8570 VPU-2 -0.06 30.92 0.0 PU-2 26. 9119 26.9107 LOHER- LWER'L-1 VPL-1 0.0 "0.01 0.0 0.0 0.0 VPL-2 18.81 37.25 0.1092 PL-2 26.8948 26.8932 ICE: ICE:
VPI-1 7.73 15. 21 0.0400 PI-1 26.9156 26.9146 VPI-2 -l. 29 8.78 0.0290 PI-2 26.9364 26.9350 AMBIENT 14.5185 14.5118 AVERAGE VAPOR PRESSURES
SUMMARY
OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT IPSIA) 0.1026 LOHER CONTAINMENT IPSIA) 0.1092 AVERAGE UPPER PRESSURE IPSIA) 26.8838 ICE CONDENSER IPSIA) 0.0345 LONER PRESSURE IPSIA) 26.8932 'VERAGE AVERAGE ICE CONDENSER PRESSURE IPSIA) 26.9248 AVERAGE CONTAINMENT PRESSURE IPSIA) 26.9006 AVERAGE CONTAINIIENT PRESSURE t PSIG) 12.3888
")%per Mp+~
RUN ((U(%ER 13 ELAPSED TIME F 00 CONTAIN((ENT TEHPERATURES DATA CHECK UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLI"VOLTS DEG. F.
ETR-101 40. 68 81.36 ETR-122 35. 78 71.56 ETR "115 9. 00 18.00 ETR-102 38. 70 77.40 ETR-123 36.57 73.14 ETR-116 9. 01 18.02 ETR-103 35. 77 71.54 ETR-124 37.16 74.32 ETR-117 8.70 17.40 ETR-104 35. 75 71.50 ETR-125 35.90 71.80 ETR-118 10.90 21.80 ETR-105 36. 65 73.30 ETR-126 35.99 71.98 ETR-119 8. 01 16.02 ETR-106 36.84 73.68 ETR-127 33.97 67. 94 ETR-120 7. 66 15.32 ETR"107 36.56 73. 12 ETR-129 36.99 73.98 ETR-121 8.05 16. 10 ETR-108 36 55 73.10 ETR-130 35.63 71.26 ETR-109
~
35.57 71.14 ETR-131 34 '2 68.04 ETR-110 35. 32 70.64 ETR-132 37.58 75.16 ETR-111 35.56 71.12 ETR-134 36.50 73.00 ETR-112 35. 58 71.16 ETR-135 36.50 73.00 ETR"114 34.73 69.46 ETR-136 36.54 73.08 ETR-128 36. 47 72.94 ETR-137 36.17 72.34 ETR-133 34. 30 68.60 ETR-138 36.59 73.18 ETR-113 37.32 74.64 ETR-139 33.67 67.34 ETR-140 36.51 73.02 ETR-141 37.13 74.26 ETR-142 36.09 72. 18 ETR-143 37.57 75.14 ETR-144 36.87 73.74 ETR"145 41.55 83.10 ETR-146 36.97 73.94 SU((MARY OF HEIG((TED AVERAGE TEMPERATURES UPPER VOLU)(E (DEG. F. ) 73.42 LONER VOLUME (DEG. F. ) 73.09 ICE CONDENSER (DEG. F. ) 16.64 UPPER VOLUHE (DEG. R.) 533.12 LONER VOLUHE (DEG. R.) 532.79 ICE CONDENSER (DEG. R. ) 476.34 CONTAINMENT VAPOR PRESSURE DATA CHECK CO)(TAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F. ) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17. 97 35.63 0 '025 PU-1 27.0410 26.8540 VPU-2 LONER:
-0 '2 31.64 0.0 PU-2 LONER:
26.9089 26.9077 VPL-1 0.0 -0.01 0.0 PL-1 0~0 0.0 VPL-2 18.81 37.25 0.1092 PL-2 26.8914 26.8898 ICE: ICE'I-1 VPI-1 6.88 13.51 0.0368 26.9125 26.9116 VPI-2 -1.27 9.14 0.0296 PI-2 26.9355 26.9341 AHBIENT 14.5205 14.5137 AVERAGE VAPOR PRESSURES SUH((ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.1025 LONER CONTAINMENT (PSIA) 0.1092 AVERAGE UPPER PRESSURE (PSIA) 26+8809 ICE CONDENSER (PSIA) 0.0332 AVERAGE LONER PRESSURE (PSIA) 26.8898 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9228 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8978 AVERAGE CONTAINHENT PRE SURE (PSIG) 12.3841 p
RUH NUHBER 14 Et.APSED TitlE 6.50 CONTAiNHEtfT TEHPERATURES DATA CHECK Q
~ ETR-101 RTD UPPER VOLIJHE HILLI-VOLTS DEG.
40. 67 81.34 F., RTD ETR-122 LOHER VOLUHE HILLI-VOLTS DEG. F; 35'1 71.42 RTD ETR-115 ICE COtQENSER ttILLI-VOLTS So 97 DEG. F.I 17.94 ETR-102 38.68 . 77.36 ETR"123 36.59 73.18 ETR-116 8. 93 17.86 ETR-103 35.78 71.56 ETR-124 37.17 74.34 ETR-117 8.68 17.36 ETR-104 35. 73 71.46 ETR-125 35. 92 71.84 ETR-118 lb.37 20.74
'TR-i05 36.59 73'iS ETR-126 36.00 72.00 ETR-119 8.02 16.04 ETR-106 ETR"107 36.84 36.57 73 '8 73 14 ETR"127 ETR-129 33.99 37.02
. 67.9S 74.04 ETR-120 ETR"121 7.68 8.07 15.36 16.14 hTR-10t) 36.50 73.00 ETR-130 35.63 71.26 ETR"'109
'5
'5.54 71.08 ETR"131 34.02 68.04 I 'TR-111
=
~
hTR 110 ETR-112 ETR-114 ETR-128 35.57 35.61 34.72 36+50 42
'1.22 70 '84 71.14 69.44 73.00 ETR 132 ETR-134 ETR-135 ETR-136 ETR-137 37o58 36o54 36.47 .
36.55 36+17 75 16 73.08 72.94 73.10 72.34, ETIAM-133 34:3i 48.62 ETR"138 36.61 73.22 hTR-iiS . 37.35 74;70 ETR-139 33.68 67.36 ETR-140 36.52 73.04
, ETR-141
'6.09 37. 14 74. 28 ETR-142 72.18
-='-'-4.-' - " ~ hTR-'143 37.57 75:14 ETR"144 36.88 73. 76 ETR-145 . 41.53 83.06 ETR-146 36 c 98 73 a 96 '
0 SAHARA t)F kaiGttTED AY+EDGE TEHPhRATt)RES
..-g'= OPINER VOLUHE tbEd'o) --
6.40 -'ONER llOL6IE )DEG. Fs f "
73~10 iCE CONDENSER tDEG. F.i 16+57 t)t)PER VOLUtlE tDEG. tt' 533'id 'ONER 'VOLUttE tbEO. lt.) 432s80 ICE L'ONDEHSER tDEGo R.) 476;27
.","'"'.;,",<<,-;.c,, ', bt)ftTAIHHENT VAPOR PRESSVRE DATA CHECK COHTAIf&EHT PRESSURES DATA CHECK
.'- '.= =-'=-."'tILLI"-~..'-. DEN PbINT ',. 'QPbk PRESSURE , 4HCORRECTED CORRECTED
4,';,,'--.",., ffYGRbttETER., P VOLTS -:. 'bEt)c Ftf,, . tPSIA) READING tPSIA) READIHG tPSIA) e '.=.-:-'",. j:.'-i'.;P-;.'.. VPU-'i '-- ..=.. '. if.t)S;-",,;
- -="."
=
-.55.hd;;;,';. '.. OiiO2$ ': ';
UPPER>
Pt)-1 27.O4id 26.8540
-,-~:~-'.'.<<'Vpu-k"..-"'-'--"- O;0 "3k;OO- - -. - D.O PV-2 26.9090 26.9078
'7'5 k
LdiEkt
'5<9) ' PL-i 6 ,'i~"'"~";.j~,,VPL-"i;,>.';,'.
VPl k
'. i8o81
57+4( = '
w='"
Oili08 Oil092 i L-2 0.0 26i8912 0.0 26i8896 7o36'4ik6 ',
"~g.,'f I;F~~."'-'PI-~"
<<" g, "
VPI i ~
-.= '
"i.27..., 9.14,,;, t)ob385 Oi0296,'" -',;-..
ICE'I-1 PI-2 26.9124 26'9312 26.9115 26.9298 Q s%,4, I
~
AHBIEttT 14.5224 14.5157
~, ~&~~"~+~:C' ..-g" ., "
AVENIAG6 'N'FOR PRESSERS
,,=.-.'.*."'"":
'CC UPPER COHTAINHkNT OPSIA)'.-";,i 0 1623 LbHER COHTAINHEkT tP5IA)
COHDENSEtt '..
'. t OPSIA). =." '- Oob340 Oaii00,'-',"-",,;a~:;-.,~~>z,'.
SQlSLRY OF CORRECTED AVERAGE PRE SSURE AVERAGE UPPER PRESSURE
'.AVERAGE LONER PRESSURE tPSIA) tPSIA) 26.
26. 8896 AVERAGE ICE CDNDENSER PRESSURE tPSIA) 12'800
26. 9206 Q-.:;-;.:, ';...=;-,.;-.'-' .*'. AVERAGE COHTAINttEftT PRESSURE AVERAGE CONTAINMENT PRESSURE t PSIA) t PSIG)
26. 8970 tm) l y
0 Thy>>
RUN ttUHBER 15 ELAPSED TIME 7.00 CONTAINMENT TEMPERATURES DATA CHECK UPPER VOLUME LOWER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLI<<VOLTS DEG. F.
ETR-101 40. 64 81.28 ETR"122 35.75 71.50 ETR-115 9.05 18.10 ETR-102 38.66 77.32 ETR-123 36.58 73.16 ETR-116 9. 11 18.22 ETR-103 35. 75 71.50 ETR-124 37. 18 74.36 ETR-117 8.60 17.20 ETR-104 35.71 71.42 ETR-125 35. 91 71.82 ETR-118 10.12 20 24 ETR-105 ETR-106
36. 64 36.83 73 '8 73.66 ETR-126 ETR-127 36.01 33.98 72.02 67.96 ETR-119 ETR-120 8.03
7. 69 16.06 15.38 ETR-107 36.51 73.02 ETR-129 3'7. 04 74.08 ETR-121 8.08 16.16 ETR "108 36.50 73.00 ETR-130 35.63 71.26 ETR-109 35.55 71. 10 ETR-131 34.03 68.06 ETR-110 35.37 70.74 ETR-132 37.58 75.16 ETR-111 35.57 71.14 ETR-134 36.59 73.18 ETR-112 35.61 71.22 ETR-135 '6.50 73.00 ETR-114 34.80 69.60 ETR-136 36.54 73.08 ETR-128 36.50 73.00 ETR-137 36.17 72.34 ETR-133 34. 32 68.64 ETR-138 36.61 73.22 ETR-113 37.37 74.74 ETR-139 33.68 67.36 ETR-140 36.52 73.04 ETR-141 37.16 74.32 ETR-142 36.09 72.18 ETR-143 37.57 75.14 ETR-144 36.87 73.74 ETR-145 41.53 83.06 ETR-146 36.98 73.96 SUHHARY OF WEIGHTED AVERAGE TEMPERATURES UPPER VOLUHE (DEG. F. ) 73.39 LOWER VOLUHE tDEG. F.) 73.12 ICE CONDENSER tDEG. F.) 16.58 UPPER VOLUME (DEG. R.) 533.09 LOWER VOLUME tDEG. R.) 532.82 ICE CONDENSER (DEG. R. ) 476.28 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINttEttT PRESSURES DATA CHECK HILLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F ) tPSIA) MANOMETER READIttG (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 lf.96 35.61 0.1024 PU-1 27.0400 26.8530 VPU-2 0.0 32.00 0.0 PU-2 26.9083 26.9071 LOWER-'PL-1 LOWER:
19 08 F 37. 79 0.1116 PL-1 0.0 0.0 VPL-2 18.81 37. 25 0.1092 PL"2 26.8910 26.8894 ICE>> ICE:
VPI-1 8.26 16.25 0.0421 PI-1 26.9122 26.9113 VPI-2 -1.20 10.40 0.0315 PI-2 26.9305 26.9291 AMBIENT 14.5243 14.5176 AVERAGE VAPOR PRESSURES SUGARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT t PSIA) 0.1024 LOllER COttTAINHENT t PSIA) 0.1104 AVERAGE UPPER PRESSURE (PSIA) 26.8801 ICE CONDENSER (PSIA) 0.0368 -AVERAGE LOWER PRESSURE tPSIA) 26.8894 AVERAGE ICE COttDEttSER PRESSURE tPSIA) 26.9202 AVERAGE CONTAIttttEttT PRESSURE [PSIA) 26.8965 AVERAGE CONTAIN)1ENT PRESSURE t PSIG) 12.3790
RUN NUHBER 16 ELAPSED TIHE 7.50 CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUIIE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD NILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40.62 81. 24 ETR-122 35.75 71.50 ETR-115 9.40 18.80 ETR-102 38.65 77.30 ETR-123 36.56 73. 12 ETR-116 9. 07 18.14 ETR-103 35. 76 71'52 ETR-124 37.19 74.38 ETR-117 8.72 17.44 ETR-104 35. 69 71.38 ETR-125 35.91 71.82 ETR-118 9. 91 19.82 ETR-105 36. 69 73.38 ETR-126 36.00 72.00 ETR-119 8.03 16.06 ETR-106 36.82 73. 64 ETR-127 34.01 68.02 ETR-120 7.69 15.38 ETR-107 36.50 73. 00 ETR-129 37.01 74.02 ETR-121 8.11 16.22 ETR-108 36.51 73.02 ETR-130 35.63 71.26 ETR-109 35.56 71. 12 ETR-131 33.97 67.94 ETR-110 35. 36 70.72 ETR-132 37.58 75.16 ETR-ill 35.56 71.12 ETR-134 36.53 73.06 ETR-112 35.58 71.16 ETR-135 36.49 72.98 ETR-114 34.80 69.60 ETR-136 36.56 73.12 ETR-128 36.52 73.04 ETR-137 36.17 72.34 ETR-133 34. 30 68.60 ETR-138 36.60 73.20 ETR-113 37 '5 74.70 ETR-139 ETR"140 33.68 36.53 67.36 73.06 ETR-141 37.16 74.32 ETR"142 36.09 72.18 ETR-143 37.57 75.14 ETR-144 36.88 73.76 ETR-145 41.54 83.08 ETR-146 36.96 73.92 SUHHARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 73.39 LOHER VOLUHE IDEG. F. ) 73.10 ICE CONDENSER IDEG. F.) 16.63 UPPER VOLUHE (DEG. R. ) 533.09 LONER VOLUHE (DEG. R. ) 532.80 ICE CONDENSER IDEG. R. ) 476.33 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEII POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS I DEG. F. ) IPSIA) HAN011ETER READING IPSIA) READING IPSIA)
UPPER'- UPPER:
VPU-1 17. 92 35.54 0. 1021 PU-1 27.0410 26.8540 VPU-2 0.0 32.00 0.0 PU-2 26.9092 26.9080 LOITER: LOI'IER:
VPL-1 19.15 37. 93 0.1122 PL-1 0.0 0.0 VPL-2 18.82 37. 27 0.1093 PL"2 26.8920 26.8904 ICE ICE:
VPI-1 7.88 15.50 0.0406 PI-1 26.9121 VPI-2 -1.26 9.32 0.0298 Pl-2 26.9300 AHBIENT 14.5232 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.1021 LONER CONTAINHENT 1 PSIA) 0.1107 AVERAGE UPPER PRESSURE IPSIA) 26.8810 ICE CONDENSER (PSIA) 0.0352 AVERAGE LONER PRESSURE (PSIA) 26.8904 AVERAGE ICE CONDENSER PRESSURE IPSIA) 26.9210 AVERAGE CONTAINHENT PPESSURE IPSIA) 26.8975 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.3743 g
p RUN NUMBER 17 ELAPSED TIME 8.00 CONTAINHENT TEMPERATURES DATA CltECK UPPER VOLUt'IE LOHER VOLUttE ICE COttDENSER RTD t tlLLI "VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD tlILl.I-VOLTS DEG. F.
ETR-101 40.58 81. 16 ETR-122 35. 73 71.46 ETR-115 9. 15 18.30 ETR-102 38. 63 77. 26 ETR-123 36.59 73.18 ETR-116 8.90 17.80 ETR-103 35.77 71.54 ETR-124 37.17 74.34 ETR-117 8,57 17.14 ETR-104 35.72 71.44 ETR-125 35.91 71.82 ETR-118 9.81 19.62 ETR-105 36.56 73. 12 ETR-126 36.01 72.02 ETR-119 8. 03 16.06 ETR-106 36.81 73. 62 ETR-127 33.98 67.96 ETR-120 7. 69 15.38 ETR-107 36.50 73. 00 ETR-129 37.02 74.04 ETR-121 8. 07 16.14 ETR-108 36.50 73.00 ETR-130 35.63 71. 26 ETR-109 35.54 71.08 ETR-131 33.99 67. 98 ETR-110 35.35 70.70 ETR-132 37.59 75.18 ETR"ill 35.56 71.12 ETR-134 36.60 73.20 ETR-112 35.59 71.18 ETR-135 36.47 72.94 ETR-114 34.73 69.46 ETR-136 36.54 73.08 ETR-128 36.53 73. 06 ETR-137 36.18 72.36 ETR-133 34.30 68. 60 ETR-138 36.59 73.18 ETR"113 37.33 74.66 ETR-139 33.70 67.40 ETR-140 36.55 73.10 ETR-141 37.16 74.32 ETR-142 36.10 72.20 ETR-143 37.58 75.16 ETR-144 36.89 73.78 ETR"145 41.57 83.14 ETR-146 37.00 74.00 SUHttARY OF NEIGtlTED AVERAGE TEMPERATURES UPPER VOLUHE (DEG. F.) 73.34 LO)tER VOLUtfE tDEG. F.) 73.12 ICE CONDENSER t DEG. F. ) 16.51 UPPER VOLUME tDEG. R.) 533.04 LONER VOLUME 'tDEG. R.) 532.82 ICE CONDENSER tDEG. R. ) 476.21 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK MILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED ttYGROHETER VOLTS (DEG. F. ) tPSIA) MANOMETER READING t PSIA) READIttG t PSIA)
UPPER- UPPER:
VPU"1 17.87 35.44 0.1017 PU-1 27.0400 26.8530 VPU"2 0.0 32.00 0.0 PU-2 26.9078 26.9066 LONER: LOtlER:
VPL-1 19.23 38.09 0.1129 PL-1 0.0 0.0 VPL-2 18.82 37. 27 0.1093 PL-2 26.8906 26.8890 ICE: ICED VPI-1 7.49 14. 72 0.0390 PI-1 26.9115 26.9106 VPI"2 -1.31 8.42 Oo0285 PI-2 26.9302 26.9288 AMBIENT 14.5300 14.5232 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT t PSIA) 0.1017 LOHER CONTAINHEtlT (PSIA) 0.1111 AVERAGE UPPER PRESSURE (PSIA) 26.8798 ICE CONDENSER (PSIA) 0.0338 AVERAGE LOt'IER PRESSURE tPSIA) 26.8890 AVERAGE ICE CONDENSER PRESSURE tPSIA) 26.9197 AVERAGE CONTAIttHENT PRESSURE 'tPSIA) 26.8962 AVERAGE CONTAItNEttT PRESSURE t PSIG) 12.3730
Q@
RUN NU))DER 18 ELAPSED TIHE 8.50 CONTAINHENT TEHPERATURES DATA CHECK NIL UPPER VOLUHE LOWER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD "VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40.57 81.14 ETR-122 35.80 71.60 ETR"115 9.02 18.04 ETR-102 38. 60 77.20 ETR"123 36.58 73.16 ETR-116 8.94 17.88 ETR-103 35. 75 71.50 ETR-124 37. 18 74.36 ETR-117 8.53 17.06 ETR-104 35. 71 71.42 ETR-125 35.94 71.88 ETR-118 9.82 19. 64 ETR-105 36. 64 73.28 ETR-126 36.02 72.04 ETR-119 8.04 16.08 ETR-106 36.80 73 '0 ETR-127 34.03 68.06 ETR-120 7. 75 15.50 ETR-107 36. 56 73.12 ETR-129 37.04 74.08 ETR-121 8.07 16. 14 ETR-108 36.50 73.00 ETR-130 35.65 71.30 ETR-109 35.57 71.14 ETR"131 34.00 68.00 ETR-110 35.42 70.84 ETR-132 37.59 75.18 ETR-111 35. 56 71. 12 ETR-134 36.61 73-22 ETR-112 35. 60 71.20 ETR-135 36.50 73.00 ETR"114 34. 77 69.54 ETR-136 36.54 73.08 ETR-128 36. 53 73.06 ETR-137 36.19 72.38 ETR-133 34.31 68.62 ETR-138 36.61 73.22 ETR-ll'3 37.39 74.78 ETR-139 33.70 67.40 ETR-140 36.54 73.08 ETR-141 37.17 74.34 ETR-142 36.11 72.22 ETR"143 37.58 75.16 ETR"144 36.89 73. 78 ETR-145 41.53 83.06 ETR-146 36.98 73.96 SUHHARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 73.37 LOWER VOLUHE (DEG. F.). 73.14 ICE CONDENSER (DEG. F. ) 16.53 UPPER VOLUHE (DEG. R.) 533.07 LOWER VOLUHE [DEG. R.) 532.84 ICE CONDENSER (DEG. R. ) 476.23 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS t DEG. F. ) (PSIA) HANOHETER READING (PSIA) READING t PSIA)
UPPER: UPPER:
VPU-1 18. 01 35.71 0.1028 PU"1 27.0400 26.8530 VPU"2 0.0 32.00 0.0 PU-2 26.9063 26.9051 LOHER'- LOHER-'L-1 VPL-1 19.34 .38.31 0.1139 0.0 0.0 VPL-2 18.82 37.27 0.1093 PL-2 26.8891 26.8875 ICE: ICE'-
VPI-1 8. 08 15.89 0.0413 PI-1 26.9099 26.9090 VPI-2 -1.28 8.96 0.0293 PI-2 26.9287 26.9273 AHBIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUt1)ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0 '028 LOWER CONTAINHENT (PSIA) 0.1116 AVERAGE UPPER PRESSURE (PSIA) 26.8791 ICE CONDENSER . (PSIA) 0.0353 AVERAGE LOHER PRESSURE (PSIA) 26.8875 AVERAGE ICE CONDENSER PRESSURE OPSIA) 26 ~ 9181 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8949 AVERAGE CONTAINHENT PRESSURE ( PSIG) 12.3618 g ~
O RUN NUMBER 19 ELAPSED TIHE 9.00 CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUME LOWER VOLUME ICE CONDENSER RTD - HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40.55 81.10 ETR-122 35.79 ?1.58 ETR-115 9. 01 18.02 ETR-102 38.57 77.14 ETR-123 36.57 73 '4 ETR-116 9. 08 18.16 ETR-103 35.76 71.52 ETR-124 37.18 74.36 ETR-117 8.57 17. 14 ETR-104 35. 69 71.38 ETR-125 35.94 71.88 ETR-118 10. 15 20.30 ETR-105 36.59 73.18 ETR-126 36.02 72.04 ETR-119 8. 04 16.08 ETR-106 36. 77 73.54 ETR-127 34.00 68.00 ETR-120 7. 71 15.42 ETR-107 36.47 72 )4 ETR-129 37.05 74.10 ETR-121 8. 09 16.18 ETR" 108 36.48 72. 96 ETR-130 35.63 71.26 ETR-109 35.56 71.12 ETR-131 34.00 68.00 ETR-110 35.36 70.72 ETR-132 37.59 75.18 ETR-ill 35.56 71. 12 ETR"134 36.55 73.10 ETR-112 35.59 71. 18 ETR-135 36.46 72.92 ETR-114 34.75 69.50 ETR-136 36.56 73.12 ETR-128 36.53 73.06 ETR-137 36.17 72.34 ETR-133 34.33 68.66 ETR-138 36.60 73.20 ETR-113 37.36 74.72 ETR-139 33.71 6?.42 ETR-140 36.55 73.10 ETR-141 37.17 74.34 ETR-142 36.11 72.22 ETR-143 37.58 75.16 ETR-144 36.89 73.78 ETR-145 41.54 83.08 ETR-146 36.99 73.98 SUHMARY OF WEIGHTED AVERAGE TEHPERATURES UPPER VOLUME (DEG. F.) 73.32 LOl'(ER VOLUME (DEG. F.) 73.12 ICE CONDEt(SER (DEG. F. ) 16.59 UPPER VOLUHE (DEG. R. ) 533.02 LOWER VOLUME (DEG. R. ) 532.82 ICE CONDENSER (DEG. R.) 476.29 CONTAINMENT VAPOR PRESSURE DATA CllECK CONTAINMENT PRESSURES DATA CIIECK HILLI- DEW POINT VAPOR PRESSURE Ut(CORRECTED CORRECTED HYGROt(ETER VOLTS (DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER-VPU-1 17.99 35.67 0.1026 PU-1 2?.0360 26.8491 VPU-2 0.0 32.00 0.0 PU-2 26.9033 26. 9021 LOWER'PL-1 LOWER'L-1 19.40 38.43 0.1144 0.0 0.0 VPL-2 18.82 37.27 0.1093 PL-2 26.8863 26.8847 ICE: ICE:
VPI-1 9.06 17.83 0.0454 PI-1 26.9074 26.9065 VPI-2 -1.20 10.40 0.0315 PI-2 26.9261 26.9247 AHBIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUMHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIN(%NT (PSIA) 0.1026 LOWER CONTAINMENT (PSIA) 0.1118 AVERAGE UPPER PRESSURE (PSIA ) 26.8756 ICE CONDENSER (PSIA) 0.0385 AVERAGE LOWER PRESSURE (PSIA) 26.8847 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9156 AVERAGE CONTAINtlENT PRESSURE (PSIA) 26.8920 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3588 g
RUN NUMBER 20 ELAPSED TIME 9.50 CONTAINHENT TEHPERATllRES DATA C(IECK UP PER VOLUME LOWER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI"VOLTS DEG. F ~ RTD HILLI-VOLTS DEG. F.
ETR-101 40.52 81. 04 ETR-122 35.75 71.50 ETR-115 8. 94 17.88 ETR-102 38.56 77. 12 ETR-123 36.60 73.20 ETR-116 8.92 17.84 ETR-103 35. 76 71.52 ETR-124 37.17 74.34 ETR-117 8.56 17.12 ETR-104 35.72 71.44 ETR-125 35.94 71.88 ETR-lie 10.77 21.54 ETR-105 36.65 73.30 ETR-126 36.02 72.04 ETR-119 8.04 16.08 ETR-106 36.77 73.54 ETR-127 33.97 67.94 ETR-120 7. 70 15. 40 ETR-107 36.49 72.98 ETR-129 37. 05 74.10 ETR-121 8. 06 16.12 ETR-108 36.45 72.90 ETR-130 35. 63 71.26 ETR-109 35.54 71.08 ETR-131 34.01 68.02 ETR-110 35.39 70.78 ETR-1'32 37.60 75.ZO ETR-ill 35.56 71.12 ETR-134 36.53 73.06 ETR-112 35.59 71. 18 ETR-135 36.51 73.02 ETR-114 34.76 69.52 ETR-136 36.58 73.16 ETR"128 36.54 73.08 ETR"137 36.18 72.36 ETR-133 '4.31 68.62 ETR-138 36.60 ,
73.20 ETR-113 37.34 74.68 ETR-139 33.72 67.44 ETR-140 36.55 73.10 ETR-141 37.18 74.36 ETR-142 36.11 72.22 ETR-143 37.58 75.16 ETR-144 36.89 73.78 ETR-145 41.54 83.08 ETR-146 37.00 74.00
SUMMARY
OF NEIGHTED AVERAGE TEt(PERATURES UPPER VOLUME (DEG. F.) 73.32 LONER VOLUHE (DEG. F.) 73.13 ICE CONDENSER (DEG. F.) 16.62 UPPER VOLUME (DEG. R. ) 533.02 LOHER VOLUME (DEG. R.) 532.83 ICE CONDENSER (DEG. R. ) 476.32 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK t(IL.I- DEII POINT VAPOR PRESSURE UNCORRECTED CORRECTED t(YGROMETER VOLTS (DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER'PU-1 UPPER:
17.97 35.63 0. 1025 PU-1 27.0340 26.8471 VPU-2 0.0 32.00 0.0 PU-2 26.9029 26.9017 LO)IER: LOtlER:
VPL-1 19.46 38.55 0. 1149 PL-1 0.0 0.0 VPL-2 18.83 37.29 0.1094 PL-2 26.8858 26.8842 ICE: ICE'I VPI-1 7.88 15.50 0.0406 "1 26.9066 26.9057 VPI-2 -1.32 8.24 0.0283 PI-2 26.9257 26.9243 AH8IENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUHt(ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIN((Et(T (PSIA) 0.1025 LOHER CONTAItWENT (PSIA) 0.1122 AVERAGE UPPER PRESSURE (PSIA) 26.8744 ICE CONDENSER (PSIA) 0.0344 AVERAGE LOWER PRESSURE (PSIA) 26.8842 AVERAGE ICE CONDEttSER PRESSURE (PSIA) 26.9150 AVERAGE CONTAINt(ENT PRESSURE (PSIA) 26.8912 AVERAGE CONTAINHEt(T PRESSURE ( PSIG) 12.3581

::-3
RUN t(UMBER 21 ELAPSED TIME 10.00 CONTAINMENT TEHPERATURES DATA CHECK UPPER VOLUt(E LOWER VOLUME ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD llILLI-VOLTS DEG. F.
ETR-101 40.50 81.00 ETR"122 35.81 71.62 ETR-115 8.77 17.54 ETR-102 . 38.53 77.06 ETR-123 36.60 73.20 ETR-116 8. 72 17.44 ETR-103 35. 76 71.52 ETR"124 . 37.19 74.38 ETR-117 8.40 16.80 ETR-104 35. 72 71.44 ETR-125 35.91 71.82 ETR-118 10. 07 20.14 ETR-105 36.56 73.12 ETR-126 36.01 72.02 ETR-119 8.03 16.06 ETR-106 36. 75 73.50 ETR-127 33.98 67. 96 ETR-120 7.70 15.40 ETR-107 36.44 72.88 ETR-129 37.06 74.12 ETR"121 8.04 16. 08 ETR-108 36.45 72.90 ETR-130 35.63 71. 26 ETR-109 35.53 71.06 ETR-131 33.98 67. 96 ETR-110 3'5. 33 70.66 ETR-132 37.60 75.20 ETR-111 35.56 71.12 ETR-134 36.57 73. 14 ETR"112 35.60 71.20 ETR-135 36.43 72.86 34.76 'TR-114 69.52 ETR-136 36.53 73.06 ETR-128 36.56 73.12 ETR-137 . 36.18 72.36 ETR-133 34. 31 '8.62 ETR-138 36.61 73.22 ETR"113 37.35 74.70 ETR-139 33.74 67.48 ETR-140 36.56 73. 12 ETR-141 37.20 74.40 ETR-142 36.11 72.22 ETR-143 37e59 75.18 ETR-144 36.89 73.78 ETR-145 41.54 83.08 ETR-146 36.97 73.94 SUHHARY OF WEIGHTED AVERAGE TEMPERATURES UPPER VOLUME (DEG. Fo ) 73.28 LOWER VOLUt(E (DEG. F. ) 73.11 ICE COtmENSER (DEG. F.) 16.43 UPPER VOLUME (DEG. R. ) 532.98 LONER VOLUME (DEG. R. ) 532.81 ICE CONDENSER (DEG. R.) 476.13 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F.) ( PSIA ) HANOt(ETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU"1 17. 96 35.61 0.1024 PU-1 27.0340 26.8471 VPU-2 0.0 32.00 0.0 PU-2 26.9031 26.9019 LOWER: LOWER:
VPL-1 19.52 38.66 0. 1155 PL-1 0.0 0.0 VPL-2 18.82 37. 27 0.1093 PL-2 26.8857 26.8841 ICE: ICE:
VPI-1 8 46 16.65 0.0429 PI-1 26.9068 26.9059 VPI"2 -1. 29 8.78 0.0290 PI-2 26.9257 26.9243 AMBIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SU(CSLRY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.1024 LOI(ER CONTAINHENT (PSIA) 0. 1124 AVERAGE UPPER PRESSURE (PSIA) 26.8745 ICE CONDENSER (PSIA) 0.0360 AVERAGE LOWER PRESSURE (PSIA) 26.8841 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9151 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8912 AVERAGE CONTAINMENT PRESSURE (PSIG) 12,3581
)
Q RUN NUHBER 22 ELAPSED TIHE 10.50 CONTAINMENT TEHPERATURES DATA CllECK UPPER VOLUHE LOttER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 40.45 80.90 ETR-122 35.83 71.66 ETR-115 9. 00 18.00 ETR-102 . 38.51 77.02 ETR-123 36.61 73.22 ETR-116 8. 90 17. 80 ETR"103 35.78 71.56 ETR-124 3?. 19 74.38 ETR-117 8.40 16.80 ETR-104 35. 67 71.34 ETR-125 35.94 71.88 ETR-118 9.77 19.54 ETR-105 36.54 73.08 ETR-126 36.01 72.02 ETR-119 8.03 16.06 ETR-106 36. 74 73.48 ETR-127 33.99 67.98 ETR-120 7. 69 15.38 ETR-107 36.43 72.86 ETR-129 37.02 74.04 ETR-121 8.03 16.06 ETR-108 36.44 72.88 ETR-13D 35.63 71.26 ETR-109 35.54 71.08 ETR-131 33.97 67.94 ETR"110 35.41 70.82 ETR-132 37.61 75.22 ETR-111 35.56 71.12 ETR-134 36.55 73. 10 ETR-112 35.59 71 ~ 18 ETR-135 36.43 72.86 ETR-114 34.78 69.56 ETR-136 36.53 73.06 ETR-128 36.56 73. 12 ETR-137 36.17 72.34 ETR "133 34.31 68.62 ETR-138 36.60 73.20 ETR-113 37.31 74.62 ETR-139 33.73 67.46 ETR-140 36.57 73.14 ETR-141 37.19 74.38 ETR-142 36.12 72.24 ETR"143 37.60 75.20 ETR-144 36.90 73.80 ETR-145 41.55 83.10 ETR-146 37. 02 74.04 SUNRY OF NEIGHTED AVERAGE TEtlPERATURES UPPER VOLUME lDEG. F. ) ,
73+26 LOi'IER VOLUME lDEG. F. ) 73.12 ICE CONDENSER lDEG. F.) 16.44 UPPER VOLUME lDEG. R. ) 532.96 LOl'IER VOLUME lDEG. R. ) 532.82 ICE CONDENSER lDEG. R. ) 476.14 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CllECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS lDEG. F.) lPSIA) HANOttETER READING lPSIA) READING lPSIA)
UPPER- UPPER:
VPU-I 17.87 35 44 0.1017 PU-I 27.0340 26.8471 VPU-2 0.0 32.00 0.0 PU-2 26.9032 26.9020 LONER: LONER:
VPL-I 19.58 38.78 0.1160 PL"I 0.0 0.0 VPL-2 18.81 37.25 0.1092 PL-2 26.8857 26.8841 ICE: ICE-VPI-I 8+ 79 17.30 0.0443 PI-I 26.9067 26.9058 VPI-2 -1.27 9.14 0.0296 PI-2 26.9260 26.9246 AtteIEttT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUtlHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT l PSIA) 0.1017 LONER CONTAINttENT lPSIA) 0.1126 AVERAGE UPPER PRESSURE lPSIA) 26.8745 ICE CONDENSER lPSIA) 0.0369 AVERAGE LONER PRESSURE lPSIA) 26.8841 AVERAGE ICE CONDENSER PRESSURE lPSIA) 26.9152 AVERAGE COttTAItlHENl PRESSURE l PSIA) 26.8913 AVERAGE CONTAINMENT PRESSURE lPSIG) 12.3581
,::I
A~
RUN NUMBER 23 ELAPSED TIME 11,00 CONTAIN((ENT TEMPERATURES DATA CHECK MILLI UPPER VOLUME LOl'lER VOLUHE ICE COt)DEt(SER RTD "VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.I ETR-101 40.44 80.88 ETR"122 35.83 71.66 ETR-115 9. 29 18.58 ETR-102 38.48 76.96 ETR-123 36.61 73.22 ETR-116 9.11 18.22 ETR-103 "104
35. 77
35. 69 71 '4 71.38 ETR-124 37. 19
35. 91 74.38 71.82 ETR-117 8.86 17.72 ETR ETR-125 ETR-118 9. 99 19.98 ETR-105 36. 46 72.92 ETR-126 36.02 72.04 ETR-119 8.04 16.08 ETR-106 36. 72 73.44 ETR-127 33.95 67.90 ETR<<120 7. 71 15.42 ETR-107 36.37 72.74 ETR-129 37.06 74.12 ETR-121 8.04 16.08 ETR-108 36.36 72.72 ETR-130 35.63 71.26 ETR-109 35.54 71.08 ETR-131 33.98 67.96 ETR-110 35.44 70.88 ETR-132 37. 61 75.22 ETR-ill 35.55 71.10 ETR-134 36.51 73.02 ETR-112 35.60 71.20 ETR-135 36.50 73.00 ETR-114 34.80 69.60 ETR"136 36.54 73.08 ETR-128 36. 58 73.16 ETR-137 36.19 72.38 ETR-133 34.31 68.62 ETR-138 36.63 73.26 ETR"113 37.33 74.66 ETR-139 33.73 67.46 ETR-140 36.57 73 '4 74.38 ETR-141 37.19 ETR"142 36.13 72.26 ETR-143 37.59 75.18 ETR-144 36.89 73.78 ETR-145 41.56 83.12 ETR"146 36.99 73.98-
SUMMARY
OF HEIGHTED AVERAGE TEMPERATURES UPPER VOLUME tDEG. F.) 73.21 LOt(ER VOLUME (DEG. F.) 73.13 ICE CONDENSER (DEG. F.) 16.63 UPPER VOLUME (DEG. R. ) 532.91 LONER VOLUHE (DEG. R. ) 532.83 ZCE CONDENSER (DEG. R.) 476.33 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HYGROHETER UPPER:
VPU-1
'ILLI- VOLTS 17.94 OEN POINT (DEG. F. )
35.58 VAPOR PRESSURE (PSIA) 0.1022 MANOHETER UPPER:
PU-1 UNCORRECTED READING tPSIA)
27. 0320 CORRECTEO READIt(G (PSZA) 26.8451 VPU-2 0.0 32.00 0.0 PU"2 26.9005 26.8993 LONER: LQ'lER:
VPL"1 19.65 38.92 0.1166 PL-1 0.0 0.0 VPL-2 18.81 37.25 0.1092 PL-2 26.0820 . 26.8812 ZCE! ICE:
VPI-1 9.50 18. 71 0.0474 PI-1 26.9040 26.9031 VPZ-2 -1.20 10.40 0. 0315 PI-2 26.9236 26 '223 At(SIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.1022 LOt(ER CONTAINMENT (PSIA) 0.1129 AVERAGE UPPER PRESSURE (PSIA) 26.8722 ICE CONDENSER (PSIA) 0.0395 AVERAGE LONERPRESSURE (PSIA) 26.8812 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9127 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8887 AVERAGE COt(TAINHENT PRESSURE (PSIG) 12.3556
p RUN NUMBER ELAPSED TIME 24 11.50 CONTAINHENT TEHPERAllJRES DATA CHECK UPPER VOLUME LO('lER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTO HILLI-VOLTS DEG. F.
ETR-101 40.42 80.84 ETR-122 35.80 71.60 ETR"115 9.28 18.56 ETR-102 38. 46 76.92 ETR"123 36.61 73.22 ETR-116 9.10 18.20 ETR-103 35. 77 71.54 ETR-124 37.19 74.38 ETR-117 8. 66 17.32 ETR-104 35. 70 71.40 ETR"125 35.95 71. 90 ETR-118 9.94 19.88 ETR-i05 36.46 72.92 ETR-126 36.03 72.06 ETR-119 8.05 16.10 ETR"106 36.72 73.44 ETR-127 33.96 67. 92 ETR"120 7.72 15.4i4 ETR-107 36. 38 72.76 ETR-129 37.06 74. 12 ETR-121 8. 04 16.08 ETR-108 36.41 '2.82 ETR"130 35.63 71.26 ETR" 109 35.52 71.04 ETR-131 34.00 68.00 ETR-110 35.37 70. 74 ETR-132 37. 62 75.24 ETR-ill 35.56 71.12 ETR-134 36.64 73.28 ETR"112 35.60 71.20 ETR-135 36.50 73.00 ETR-114 34.76 69.52 ETR"136 36.55 73.10 ETR-128 36.59 73.18 ETR-137 36.20 72.40 ETR-133 34.31 68.62 ETR-138 36.63 '3.26 ETR-113 37.36 74.72 ETR"139 33.74 67.48 ETR-14iO 36.57 73.14 ETR-141 37.20 74.40 ETR-142 36.13 72 '6 ETR-143 37.60 75.20 ETR-144 36.90 73.80 ETR-145 41.55 83.10 ETR-146 37.01 74.02
SUMMARY
OF HEIGHTEO AVERAGE TEHPERATURES r
UPPER VOLUHE (DEG. F.) 73.21 LONER VOLUHE tDEG. F.) 73.17 ICE CONDENSER tDEG. F.) 16.60 UPPER VOLUME tDEG. R.) 532.91 LONER VOLUME (DEG. R.) 532.87 ICE CONDENSER tDEG. R.) 476.30 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK MILLZ- DEH POINT VAPOR PRESSURE U((CORRECTEO CORRECTED HYGROHETER VOLTS t DEG. F. ) tPSZA) MANOMETER READING t PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17. 99 35. 67 0.1026 PU-1 27.0360 26.8491 VPU-2 0.0 32.00 0.0 PU-2 26.9040 26.9028 LONER: LOHER'-
yPL-'1 19. 72 39.06 0. 1173 PL-1 0' 0.0 VPL-2 18.54 36. 71 0.1069 PL-2 26.8860 26.8844 ICE: ICE:
VPI-1 7.34 14.43 0. 0385 ~ PI-1 26.9078 26.9069 VPI"2 -l. 15 11.30 0.0329 PZ-2 26.9276 26.9262 AHBIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUH((ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.1026 LONER CONTAINMENT t PSIA) 0.1121 AVERAGE UPPER PRESSURE (PSIA) 26. 8759 ZCE CONDENSER (PSIA) 0.0357 .AVERAGE LONER PRESSURE (PSIA) 26.8844 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9166 AVERAGE CONTAIN((ENT PRESSURE (PSIA) 26.8923 AVERAGE CONTAIN(ENT PRESSURE (PSIG) 12.3592
~
RUN NUHDER 25 ELAPSED TIME 12.00 CONTAINHENT TEHPERATlJRES DATA CllECK UPPER VOLUME LOWER VOLUt!E ICE CONDEt(SER RTD MILLI"VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40.40 80.80 ETR-122 35.81 36.57 71 '2 73.14 ETR-115 9.13 18.26 18.24 ETR-102'.. 38.45 76.90 ETR-123 ETR-116 9. 12 ETR=103 35. 77 71.54 ETR-124 37. 20 74.40 ETR-117 8.72 17.44 ETR"104 35.72 71.44 ETR-125 35.94 71.88 ETR-118 9.96 19.92 ETR-105 36.44 72.88 ETR-126 36.02 72. 04 ETR-119 8.06 16.12 ETR-106 36.72 73.44 ETR-127 33.98 67. 96 ETR-120 7. 77 15.54 ETR-107 36. 35 72 F 70 ETR-129 37.08 74.16 ETR-121 8. 04 16.08 ETR"108 36.41 72.82 ETR-130 35.63 71.26 ETR-109 35.54 71 08 F ETR-131 33.99 67.98 ETR-110 35.43 70.86 ETR-132 37.62 75.24 ETR-111 35.56 71.12 ETR-134 36.52 73.04 ETR-112 35. 61 71. 22 ETR-135 36.48 72.96 ETR-114 34. 76 69.52 ETR-136 36.56 73.12 ETR-128 36.59 73.18 ETR-137 36.21 72.42 ETR-133 34. 32 68.64 ETR-138 36.64 73.28 ETR"113 37. 34 74.68 ETR"139 33 '5 36.57 67.50 ETR-140 73.14 ETR-141 37. 22 74.44 ETR-142 36. 13 72.26 ETR-143 37.60 75.20 ETR-144 36.90 73.80 ETR-145 41.54 83.08 ETR-146 37.01 74.02 SUt(MARY OF WEIGllTED AVERAGE TEMPERATURES UPPER VOLUHE (DEG. F.) 73.21 LOWER VOLUME (DEG. F. ) 73.14 ICE CONDENSER (DEG. F.) 16.63 UPPER VOLUME (DEG. R. ) 532.91 LOWER VOLUME (DEG. R.) 532.84 ICE CONDENSER (DEG. R.) 476.33 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CMECK HILLI- OEM POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F.) (PSIA) MANOt(ETER READING (PSIA) READING (PSIA)
UPPER- UPPER:
VPU-1 17. 94 35.58 0.1022 PU-1 27.0340 26.8471 VPU-2 0.0 32.00 0.0 PU-2 26.9028 26.9016 LOWER: LOI JER:
VPL-1 19.78 39.18 0.1178 PL"1 0.0 0.0 VPL-2 18.59 36.81 0.1073 PL-2 26.8850 26.8834 ICE: ICE:
VPI-1 8.48 16.68 0.0430 PI-1 26.9057 26.9048 VPI-2 -1.04 13.28 0.0364 PI-2 26.9265 26.9251 At(DIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.1022 LOt(ER CONTAINHEt(T (PSIA) 0 '126 AVERAGE UPPER PRESSURE (PSIA) 26.8743 ICE CONDENSER (PSIA) 0.0397 AVERAGE LOWER PRESSURE (PSIA) 26.8834 AVERAGE ICE CONDEttSER PRESSURE (PSIA) 26.9150 AVERAGE COt(TAINt(Et(T PRESSURE (PSIA) 26.8909 AVERAGE COt(TAINHEt(T PRESSURE (PSIG) 12.3578
A.
RUN t(Ut%ER 26 ELAPSED TII(E 12.50 CONTAINHENT TEt(PERATlJRES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR"101 40.36 80.72 ETR-122 35.83 71.66 ETR-115 9.15 18.30 ETR-102 38.41 76.82 ETR-123 36.60 73.20 ETR"116 9.19 18.38 ETR-103 35. 75 71.50 ETR-124 37.20 74.40 ETR-117 8.87 17.74 ETR-104 35. 68 71.36 ETR-125 35.94 71.88 ETR-118 10.81 21 '2 ETR-105 36.41 72.82 ETR-126 36.03 72.06 ETR-119 8.07 16.14 ETR "106 36. 70 73.40 ETR-127 33.99 67.98 ETR-120 7. 78 15.56 ETR-107 36. 43 72.86 ETR-129 37.08 74.16 ETR-121 8.04 16.08 ETR-108 36.38 72.76 ETR"130 35.63 71.26 ETR-109 35. 50 71.00 ETR-131 33.95 67.90 ETR"110 35.39 70.78 ETR"132 37.63 75.26 ETR-111 35.56 71.12 ETR-134 36.59 73.18 ETR-112 35. 60 71.20 ETR-135 36.45 72.90 ETR"114 34.74 69.48 ETR-136 36.53 73.06 ETR-128 36.59 73.18 ETR-137 36.23 72.46 ETR-133 34. 34 68.68 ETR-138 36.63 73.26 ETR-113 37. 38 74.76 ETR-139 33.75 67.50 ETR-140 36.59 73.18 ETR"141 37.22 74.44 ETR-142 36.14 72.28 ETR-143 37.61 75.22 ETR-144 36.92 73.84 ETR-145 41.56 83.12 ETR-146 37.02 74.04 SUHHARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 73.18 . LONER VOLUHE (DEG. F.) 73.16 ICE CONDENSER (DEG. F. ) 16.79 UPPER VOLUHE (DEG. R. ) 532.88 LONER VOLUHE (DEG. R. ) 532.86 ICE CONDENSER (DEG. R. ) 476.49 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE U(KORRECTED COttRECTED I(YGROHETER VOLTS (DEG. F.) (PSIA) HANOt(ETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17. 96 35.61 0.1024 PU-1 27.0310 26.8441 VPU-2 0,0 32.00 0.0 PU-2 26.8999 26.8987 LONER: LO)IER:
VPL-1 19.85 39.32 0.1185 PL"1 0.0 0.0 VPL-2 18.59 36.81 0.1073 PL-2 26.8821 26.8805 ICE'PI-1 ICE:
7.98 15. 70 0.0409 PI-1 26.9026 26.9017 VPI-2 -1.11 12.02 0.0341 PI-2 26.9242 26.9229 At(BIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUN(ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.1024 LO)(ER CONTAIt(t(ENT (PSIA) 0. 1129 AVERAGE UPPER PRESSURE (PSIA) 26.8714 ICE CONDENSER (PSIA) 0.0375 AVERAGE LOllER PRESSURE (PSIA) 26.8805 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9123 AVERAGE COt(TAIt((tENT PRESSURE (PSIA) 26.8880 AVERAGE COt(TAItD(ENT PRESSURE (PSIG) 12.3549
A@
RUN NUHDER 27 ELAPSED TIHE 13.00 CONTAINMENT TEMPERATURES DATA CHECK UPPER VOLUHE LONER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 40.32 80.64 ETR-122 35. 79 71.58 ETR-115 9. 27 18.54 ETR-102 38. 38 76.76 ETR-123 36.59 73.18 ETR-116 9.15 18.30 ETR-103 '5.74 71.48 ETR-124 37 '2 74 44 ETR-117 8.86 17.72 ETR 104 35.71 71.42 ETR-125 35.96 71.92 ETR-118 10.77 21.54 ETR-105 36. 44 72.88 ETR-126 36.03 72.06 ETR-119 8.08 16.16 ETR-106 36. 69 73.38 ETR-127 33.99 67.98 ETR-120 7. 78 15.56 ETR-107 36.31 72.62 ETR-129 37.12 74.24 ETR-121 8. 04 16.08 ETR-108 36. 33 72.66 ETR-130 35.63 71.26 ETR-109 35. 49 70.98 ETR"131 33.95 67.90 ETR-110 35.40 70.80 ETR-132 37.63 75.26 ETR-ill 35.56 71.12 ETR-134 36.64 73.28 ETR-112 35.60 71.20 ETR-135 36 44 72.88 ETR-114 34. 75 69.50 ETR-136 36.58 73.16 ETR-128 36. 60 73.20 ETR-137 36.20 72.40 ETR-133 34. 35 68.70 ETR-138 36.66 73.32 ETR-113 37. 37 74.74 ETR-139 33.77 67.54 ETR-140 36.59 73.18 ETR-141 37.23 74.46 ETR-142 36.15 72.30 ETR-143 37.61 75.22 ETR-144 36.90 73.80 ETR-145 41.54 83.08 ETR-146 37.04 74.08 SLRNARY OF ttEIGHTED AVERAGE TEHPERATURES UPPER VOLUME tDEG. F.) 73.14 LONER VOLUME tDEG. F.) 73.18 ICE CONDENSER (DEG. F. ) 16.80 UPPER VOLUHE tDEG. R.) 532.84 LONER VOLUME tDEG. R.) 532.88 ICE CONDENSER tDEG. R.) 476.50 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE U)CORRECTED CORRECTED MYGROHETER VOLTS (DEG. F ~ ) [PSIA) HANOltETER READING tPSIA) READlt)G tPSIA)
UPPER: UPPER:
VPU-1 18.01 35.71 0.1028 PU-1 27.0290 26.8422 VPU-2 0.0 32.00 0.0 PU-2 26.8976 26.8964 LONER- LO) E'ER:
VPL-1 19. 92 ~ 39.46 0. 1191 PL-1 0.0 0.0 VPL-2 18.60 36.83 0 '074 PL-2 26.8798 26.8782 ICE- ICE:
VPI-1 8.53 16.78 0.0432 PI-1 26.9008 26.8999 VPI-2 -1.06 12.92 0.0357 PI"2 26.9232 26.9219 AHBIENT 14.5400 l4.5331 AVERAGE VAPOR PRESSURES SUt)MARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT t PSIA) 0.1028 LONER CONTAIN)ENT t PSIA) 0. 1133 AVERAGE UPPER PRESSURE (PSIA) 26.8693 ICE CONDENSER (PSIA) 0.0394 AVERAGE LONER PRESSURE OPSIA) 26.8782 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9109 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8861 AVERAGE CO)A'AltlHEtA PRESSURE ( PSIG ) 12.3530
RUN NUHBER 28 ELAPSED TIME 13.50 CONTAINMENT TEMPERATURES DATA CHECK UPPER VOLUME LOWER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR "101 40. 28 80.56 ETR-122 35.83 71.66 ETR-115 9. 22 18.44 ETR-102 . 38.35 76.70 ETR-123 36.63 73.26 ETR-116 9.14 18.28 ETR-103 35. 78 71.56 ETR-124 37.21 74.42 ETR"117 8.90 17.80 ETR-104 35. 73 71.46 ETR-125 35.95 71.90 ETR-118 10.50 21.00 ETR-105 36.36 72.72 ETR-126 36.04 72.08 ETR-119 8.10 16.20 ETR-106 36.68 73.36 ETR-127 34.02 68.04 ETR-120 7. 79 15.58 ETR-107 36. 26 72.52 ETR-129 37.11 74.22 ETR-121 - 8. 04 16.08 ETR-108 36. 35 72.70 ETR-130 35.63 71.26 ETR-109 35.54 71.08 ETR-131 33.99 67.98 ETR-110 35.43 70.06 ETR-132 37.63 75.26 ETR-ill 35.57 71.14 ETR-134 36.59 73.18 ETR-112 35.60 71.20 ETR-135 36.45 72.90 ETR-114 34. 75 69.50 ETR-136 36.57 73.14 ETR-128 36.61 73.22 ETR-137 36.25 72.50 ETR-133 34. 34 68.68 ETR-138 36.65 73.30 ETR-113 37.37 74.74 ETR-139 33.78 67.56 ETR-140 36.60 73.20 ETR"141 37.25 74.50 ETR-142 36.16 72.32 ETR-143 37.61 75.22 ETR-144 36.90 73.80 ETR-145 41.57 83.14 ETR-146 37. 02 74.04 SUWRY OF WEIGI(TED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 73.12 532.82 LOWER VOLUME (DEG. F.)
R.)
73.18 ICE CONDENSER (DEG. F ~ ) 16 '8 UPPER VOLUHE (DEG. R. ) LOWER VOLUHE (DEG. 532.88 ICE CONDENSER (DEG. R.) 476.48 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK HILLI- DEW POINT VAPOR PRESSURE Ut(CORRECTED CORRECTED I(YGROHETER VOLTS (DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER-VPU-1 17. 98 35.65 0.1025 PU-1 27.0320 26.8451 VPU-2 0.0 32.00 0.0 PU-2 26.9010 26.8998 LOHER: LOWER-'L-1 VPL-1 19. 99 39.60 0.1198 0.0 0.0 VPL-2 18.59 36.81 0.1073 PL"2 26.8837 26.8821 ICE: ICE:
VPI-1 8.86 17.45 0.0446 PI-1 26 '048 26.9039 VPI-2 -1.04 13.28 0.0364 PI-2 26.9305 26.9291 A(SIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUGARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIN((ENT (PSIA) 0. 1025 LOWER CONTAIN(ENT (PSIA) 0. 1136 AVERAGE UPPER PRESSURE (PSIA) 26.8724 ICE CONDENSER ( PSIA) 0.0405 AVERAGE LOWER PRESSURE (PSIA) 26.8821 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9165 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8903 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3572
p RUN NUMBER ELAPSED TIME 29 14.00 CONTAINMENT TEHPERATlJRES DATA CHECK UPPER VOLUME LONER VOLUME ICE CO)(DENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 40.25 80.50 ETR"122 35.84 71.68 ETR"115, 9.40 18.80 ETR-102 38.32 76.64 ETR-123 36.61 73.22 ETR" 116 9. 20 18.40 ETR-103 35.75 71.50 ETR-124 37.22 74.44 ETR-117 8. 79 17.58 ETR-104 35. 68 71.36 ETR-125 35.97 71+94 ETR-118 10.04 20.08 ETR"105 36.44 72.88 ETR-126 36.04 72.08 ETR-119 8.10 16.20 ETR-106 36. 65 73.30 ETR-127 33.99 67.98 ETR" 120 7. 79 15.58 ETR-107 36.31 72.62 ETR"129 37.08 74.16 ETR-121 8. 08 16.16 ETR-108 36.32 72.64 ETR-130 35.63 71.26 ETR-109 35. 53 71.06 ETR-131 33.98 67.96 ETR-110 35. 40 70.80 ETR-132 37.64 75.28 ETR"ill 35.56 71.12 ETR-134 36.62 73.24 ETR-112 35.59 71.18 ETR-135 36.45 72.90 ETR-114 34.76 69.52 ETR-136 36.57 73.14 ETR-128 36. 63 73.26 ETR-137 36.23 72.46 ETR "133 -
34.33 68.66 ETR-138 36.65 73.30 ETR-113 37.37 74.74 ETR-139 33.78 67.56 ETR-140 36.60 73.20 ETR-141 37.24 74.48 ETR-142 36.17 72.34 ETR-143 37.62 75.24 ETR-144 36.91 73.82 ETR-145 41.56 83.12 ETR-146 37.04 74.08
SUMMARY
OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLt)HE (DEG. F. ) 73.11 LO)'(ER VOLUME (DEG. F. ) 73.19 ICE CONDENSER tDEG. F. ) 16.75 UPPER VOLUME (DEG. R.) 532.81 LONER VOLUME (DEG. R.) 532.89 ICE CONDENSER (DEG. R.) 476.45 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED IlYGROHETER VOLTS (DEG. F. ) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17.94 35.58 0.1022 PU-1 27.0310 26.8441 VPU-2 0.0 32.00 0.0 PU-2 26.9002 26.8990 LONER: LONER:
VPL"1 20.07 39. 76 0.1205 PL-1 0.0 0.0 VPL-2 18. 60 36.83 0.1074 PL-.2 26.8824 26.8808 ICE- ICE'I-1 VPI-1 8.67 17.06 0.0438 26.9036 26.9027 VPI-2 -1.08 12.56 0.0351 PI-2 26.9207 26.9194
%(DIENT 14.5400 14.5331 AVERAGE VAPOR PRESSURES Slk(MARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT tPSIA) 0.1022 LONER CO)(TAINMENT (PSIA) 0. 1140 AVERAGE UPPER PRESSURE (PSXA) 26.8716 ICE CONDENSER t PSIA) 0.0394 AVERAGE LONER PRESSURE tPSIA) 26.8808 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9110 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8878 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3547
C'UN NUHDER 30 ELAPSED TIME 14.50 CONTAINMENT TEMPERATURES DATA CI[ECK UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTO MILLI"VOLTS DEG. F. RTD 1!ILLI-VOLTS DEG. F.
ETR-101 40. 21 80.42 ETR-122 35.85 71.70 ETR-115 9.51 19. 02 ETR-102 38.30 76.60 ETR-123 36.64 73.28 ETR-116 9. Zl 18. 42 ETR-103 35.76 71.52 ETR-124 37 '4 74.48 ETR-117 8. 92 17.84 ETR-104 35.71 71.42 ETR-125 35.97 71.94 ETR-118 10.23 20.46 ETR-105 36.33 72.66 ETR"126 36.04 72.08 ETR" 119 8. 10 16.20 ETR-106 36.64 73.28 ETR-127 33.99 67.98 ETR-120 7.80 15.60 ETR-107 36. 21 72.42 ETR-129 37. 11 74.22 ETR-121 8. 08 16.16 ETR-108 36. 28 72.56 ETR"130 35.65 71.30 ETR-109 35.54 71.08 ETR-131 33.97 67.94 ETR-110 35.45 70.90 ETR"132 37.64 75.28 ETR-ill 35.57 71.14 ETR-134 36.62 73. 2,4 ETR-112 35.61 71.22 ETR-135 36.47 72.94 34.79 'TR-114 69.58 ETR-136 36.57 73.14 ETR-1Z8 36 ~ 64 73.28 ETR-137 36.25 72.50 ETR-133 34.35 68.70 ETR-138 36.65 73.30 ETR-113 37. 36 74.72 ETR-139 33.80 67.60 ETR-140 36.60 73.20 ETR-141 37.26 74.52 ETR"142 36. 17 72.34 ETR-143 37. 62 75.24 ETR-144 36. 92 73.84 ETR-145 41.56 83.12 ETR-146 37.04 74.08
SUMMARY
OF WEIGHTED AVERAGE TEMPERATURES UPPER VOLUME \DEG. F.) 73.07 LO)(ER VOLUME (DEG. F.) 73.20 ICE CONDENSER (DEG. F.) 16.82 UPPER VOLUME (DEG. R. ) 532.77 'ONER VOLUME tDEG. R. ) 532.90 ICE CONDENSER (DEG. R.) 476.52 CONTAINMENT VAPOR PRESSURE DATA CHECK CO((TAIWHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F. ) (PSIA) HAWOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER-VPU-1 17.41 34.52 0.0980 PU-1 27.0300 26.8431 VPU-2 0.0 3Z.OO 0.0 PU-2 26.8989 26.8977 LONER: LONER:
VPL-1 20.16 39. 94 0.1214 PL-1 0.0 0.0 VPL-2 18.60 36.83 0.1074 PL-2 26.8813 26.8797 ICE'PI-1 ICE:
8.60 16.93 0.0435 PI-1 26.9022 26.9013 VPI-2 -1. 10 12 '0 0.0345 PI-2 26.9179 26.9166 AHBIE)(T 14.5400 14.5331 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIN((ENT tPSIA) 0 '980 LONER CONTAIN((ENT (PSIA) 0.1144 AVERAGE UPPER PRESSURE tPSIA) 26.8704 ICE CONDENSER (PSIA) 0.0390 AVERAGE LOMER PRESSURE (PSIA) 26.8797 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9089 AVERAGE COWTAI(()(ENT PRESSURE (PSIA) 26.8863 AVERAGE COt(TAIN)(ENT PRESSURE (PSIG)
0 6
RUN HO/(DER 31 ELAPSED TINE 15.00 CONTAIt(MENT TEHPERATURES DATA Ct(ECK UPPER VOLUME LONER VOLUHE ICE CONDEt(SER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40. 18 80.36 ETR-122 35.83 71.66 ETR-115 9.44 18.88 ETR-102 . 38.27 76.54 ETR-123 36.63 73.26 ETR-116 9. 29 18.58 ETR-103 35. 76 71.52 ETR-124 37.21 74.42 ETR-117 8.89 17.78 ETR-104 ETR"105
35. 69 36.30 71 '8 72.60 ETR-125 ETR-126 35.94 36.04 71.88 72.08 ETR-118 ETR-119 10.21 8.10 20.42 16 F 20 ETR-106 36. 64 73.28 ETR-127 34.03 68. 06 ETR-120 7.82 15.64 ETR-107 36 20
~ 72.40 ETR-129 37.14 74.28 ETR-121 8.06 16. 12 ETR-108 36 27 F 72.54 ETR-130 35.63 71.26 ETR"109 35.56 71.12 ETR-131 33.98 67.96 ETR-110 ETR-Ill 35.46 70 '2 71.12 ETR-132 37.64 36.63 75.28 73.26 35.56 ETR-134 ETR-112 35. 61 71.22 ETR-135 36.46 72.92 ETR-114 34. 73 69.46 ETR-136 36.60 73.20 ETR-128 36. 63 73.26 ETR-137 36.26 72.52 ETR-133 34. 35 68.70 ETR-138 36.66 73.32 ETR-113 37.39 74.78 ETR-139 37.78 75.56 ETR-140 36.61 73.22 ETR-141 37.25 74.50 ETR-142 36.18 72.36 ETR-143 37.62 75.Z4 ETR-144 36.92 73.84 ETR-145 41.54 83.08 ETR-146 37.03 74.06
SUMMARY
OF HEIGI(TED AVERAGE TEHPERATURES UPPER VOLUt(E (DEG. F.) 73.04 LOHER VOLUME (DEG. F.) 73.28 ICE CONDEt(SER (DEG. F. ) 16.81 UPPER VOLUHE (DEG. R.) 532.74 LONER VOLUME (DEG. R.) 532 '8 ICE CONDEt(SER (DEG. R.) 476.51 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CKECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F ~ ) (PSIA) HANOMETER READING (PSIA) READING (PSIA)
UPPER'-, UPPER:
VPU-1 17.37 34.44 0.0977 PU-1 ,27.0270 26.8402 VPU-2 0.0 32.00 0.0 PU-2 26.8955 26.8943 LONER: LONER:
VPL-1 20. 25 40.12 0.1222 PL-1 0.0 0.0 VPL-2 18.60 36.83 0.1074 PL-2 26.8780 26.8764 ICE'PI-1 ICE:
9. 19 18.09 0.0460 PI "1 26.8985 Z6.8976 VPI-2 -1.05 13.10 0.0360 PI "2 26.9136 26.9123 AHBIENT 14.5300 14.5232 AVERAGE VAPOR PRESSURES SUt(MARY OF CORRECTED AVERAGE PRESSURES UPPER COt(TAIt(t(ENT (PSIA) 0.0977 LOt(ER CONTAItNEW ( PSIA ) 0.1148 AVERAGE UPPER PRESSURE (PSIA) 26.8672 ICE CONDENSER (PSIA) 0.0410 AVERAGE LOt(ER PRESSURE (PSIA) 26.8764 AVERAGE ICE CONDEt(SER PRESSURE (PSIA) 26.9049 AVERAGE COt(TAIt(t(ENT PRESSURE (PSIA) 26.8828 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3596
O."-.;
RUN NUtIDER 32 ELAPSED TIIIE 15.50 CONTAINMENT TEMPERATURES DATA CHECK UPPER VOLUtIE LOItER VOLUIIE ICE CONDEttSER RTD MILLI-VOLTS DEG. F. RTD HILLI"VOLTS DEG. F. RTD tIILLI-VOLTS DEG. F.,
ETR-101 40. 16 80.32 ETR-122 35.84 71.68 ETR-115 9.28 18.56 ETR-102 38. 24 76.48 ETR-123 36.63 73.26 ETR-116 9. 27 18.54 ETR-103 35.76 71.52 ETR-124 37.22 74.44 ETR-117 8.84 17.68 ETR-104 35. 68 71.36 ETR-125 35.95 71.90 ETR-118 10. 08 20.16 ETR-105 36.37 72.74 ETR"126 36.04 72.08 ETR-119 8. 12 16.24 ETR" 106 36. 63 73.26 ETR" 127 34.02 68.04 ETR-120 7.85 15.70 ETR-107 36. 31 72.62 ETR-129 37.12 74.24 ETR-121 8. 07 16.14 ETR-108 36. 26 72.52 ETR-130 35.65 71.30 ETR-109 35.51 71 02 F ETR-131 34.01 68.02 ETR-110 35.49 70.98 ETR-132 37. 65 75.30 ETR-ill 35.57 71.14 ETR-134 36.69 73.38 ETR-112 35. 60 71. 20 ETR-135 36.52 73.04 ETR-114 34.81 69.62 ETR-136 36.58 73.16 ETR-128 36. 66 73.32 ETR-137 36.25 7R.50 ETR-133 34.35 68.70 ETR"138 36.67 73.34 ETR-113 37.43 74.86 ETR-139 33.80 67.60 ETR-140 36.61 73.RR ETR-141 37. 26 74.52 ETR-142 36. 18 72.36 ETR-143 37. 63 75.26 ETR-144 36.93 73.86 ETR-145 41.54 83.08 ETR-146 37.05 74.10 SUHHARY OF HEIGHTED AVERAGE TEMPERATURES UPPER VOLUME tDEG. F.) 73.07 LONER VOLUHE tDEG. F.) 73.24 ICE CONDENSER tDEG. F.) 16.79 UPPER VOLUME tDEG. R.) 532.77 LOttER VOLUHE tDEG. R.) 532.94 ICE CONDENSER tDEG. R.) 476.49 CONTAINMENT VAPOR PRESSURE DATA CHECK COttlAINHENT PRESSURES DATA CHECK HILLI- DEN POZNI VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS tDEG. F.) tPSIA) HANOHETER READING tPSIA) READING tPSIA)
UPPER: UPPER:
VPU-1 17.46 34. 62 0.0984 PU"1 27.0300 26.8431 VPU-2 0.02 32.34 0.0898 PU-2 26.8988 26.8976 LOI'IER'- LONER:
VPL-1 20.33 40.28 0.1230 PL-1 0.0 0.0 VPL-2 18.49 36.61 0.1065 PL-2 26.8813 26.8797 ICE: ICE:
VPI-1 9.85 19o40 0.0490 PI-1 26.9023 26.9014 VPZ-2 -0+98 14.36 0.0383 PI-2 26.9173 26.9160 AMBIEttT 14.5300 14.5232 AVERAGE VAPOR PRESSURES SUtIMARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT tPSZA) 0.0941 LOtIER CONTAINHENT t PSIA) 0.1147 AVERAGE UPPER PRESSURE tPSIA) .26.8704 ICE CONDENSER t PSIA) 0.0437 AVERAGE LONER PRESSURE tPSIA) 26.8797 AVERAGE ICE CONDENSER PRESSURE tPSIA) 26.9087 AVERAGE CONTAINIIEWT PRESSURE t PSIA) '6.8862 AVERAGE COIITAINtIENT PRESSURE t PSIG) 12.3630 Og
'UN NU)DER 33 ELAPSED TIHE 16.00 CONTAINHENT TEHPERATURES DATA Cl(ECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40. 13 80.26 ETR-122 35. 84 71.68 ETR-115 9. 22 18.44 ETR-102 . 38. 20 76.40 ETR-123 36. 64 73.28 ETR-116 9.24 18.48 ETR" 103 35. 75 71.50 ETR-124 37. 24 74.48 ETR-117 8.87 17.74 ETR-104 35. 69 71.38 ETR-125 35. 95 71.90 ETR-118 11.03 22.06 ETR-105 36. 36 72.72 ETR-126 36. 04 72.08 ETR"119 8.13 16.26 ETR-106 36 ~ 60 73.20 ETR-127 33.99 67.98 ETR-120 7. 84 15.68 ETR-107 36.22 72.44 ETR-129 37. 10 74.20 ETR-121 8.09 16.18 ETR-108 36. 24 72.48 ETR-130 35. 64 71.28 ETR-109 35.51 71.02 ETR" 131 33. 97 67.94 ETR-110 35.46 70.92 ETR-132 37. 65 75.30 ETR-ill 35.56 71. 12 ETR-134 36. 61 73.22 ETR "112 35. 61 71.22 ETR-135 36.47 72.94
. ETR-114 34. 76 69.52 ETR-136 36.60 73.20 ETR-128 36. 66 73 '2 68.68 ETR-137 36.22 36.66 72.44 73.32 ETR-133 34.34 ETR-138 ETR"113 37.39 74.78 ETR-139 33.79 67.58 ETR-140 36. 62 73.24 ETR-141 37. 26 74.52 ETR "142 36. 18 72.36 ETR-143 37.63 75.26 ETR-144 36. 92 73.84 ETR-145 41.57 83.14 ETR-146 37. 06 74.12 SUHHARY OF HEIGRTED AVERAGE TEt(PERATURES UPPER VOLUHE (DEG. F. ) 73 ~ 02 LOt(ER VOLUHE (DEG. F. ) ?3.20 ICE COttDENSER (DEG. F. ) 16.92 UPPER VOLUHE (DEG. R. ) 532.72 LOl(ER VOLUHE (DEG. R.) 532.90 ICE CONDENSER (DEG. R.) 476.62 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETE R VOLTS (DEG. F. ) l PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER- UPPER:
VPU-1 17.46 34. 62 0.0984 PU-1 27. 0260 26.8392 VPU-2 0. 07 33.19 0.0929 PU-2 26.8948 26.8936 LO)(ER: LOI'lER:
VPL-1 20.40 40.42 0.1236 PL-1 0.0 0.0 VPL"2 18.52 36.67 0.1067 PL-2 26.8773 26.8757 ICE-'PI-1 ICE:
8.75 17.23 0.0441 PI-1 26.8982 26.8973 VPI"2 -1.12 11.84 0.0338 PI-2 26. 913ip 26.9121 AHBIENT 14.5200 14.5133 AVERAGE VAPOR PRESSURES SUt(HARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0957 LONER CONTAINHENT (PSIA) 0.1152 AVERAGE UPPER PRESSURE (PSIA) 26.8664 ICE CONDENSER (PSIA) 0.0390 AVERAGE LO((ER PRESSURE (PSIA) 26.8757 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9047 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8822 AVERAGE CO((TAINt(Et(T PRESSURE (PSIG) 12.3690 p
RUN NUMBER 34 ELAPSED TIME 16.50 CONTAINHENT TEHPERATURES DATA Cl)ECK UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR"101 40.12 80.24 ETR-122 35.89 71.78 ETR-115 9. 12 18.24 ETR-102 38. 18 76.36 ETR-123 36.59 73.18 ETR-116 9. 12 18. 24 ET R-103 35. 74 71.48- ETR-124 37. 28 74.56 ETR-117 8.79 17.58 ETR-104 35. 66 71.32 ETR-125 ~
35.98 71,96 ETR-118 10. 50 21.00 ETR-105 36.27 72.54 ETR-126 36.05 72.10 ETR-119 8. 13 16.26 ETR-106 36.59 73.18 ETR-127 33.98 67.96 ETR-120 7.84 15.68 ETR" 107 36. 23 72.46 ETR-129 37.13 74.26 ETR-121 8.10 16.20 ETR-108 36. 22 72.44 ETR-130 35.65 71.30 ETR-109 35.52 71.04 ETR-131 33.96 67. 92 ETR-110 35.39 70.78 ETR-132 37.66 75.32 ETR-ill 35.57 71.14 ETR-134 36.56 73.12 ETR"112 35.60 71.20 ETR-135 36.50 73.00 ETR-114 34.80 69.60 ETR"136 36.59 73.18 ETR"128 36. 67 73.34 ETR-137 36.27 72.54 ETR-133 34. 36 68.72 ETR-138 36.67 73.34 ETR-113 37. 39 74.78 ETR-139 33.82 67.64 ETR-140 36.62 73.24 ETR-141 37.27 = 74.54 ETR-142 36. 19 72.38 ETR-143 37. 63 75.26 ETR"144 36.94 73.88 ETR-145 41.57 83.14 ETR-146 37.05 74.10 SUHHARY OF NEIGHTED AVERAGE TEMPERATURES UPPER VOLUME fDEG. F.) 72.99 LONER VOLUME fDEG. F.) 73.22 ICE COtfDENSER fDEG. F. ) 16.81 UPPER VOLUME fDEG. R.) 532.69 LONER VOLUffE tDEG. R.) 532.92 ICE CONDENSER tDEG. R. ) 476.51 CONTAINMENT VAPOR PRESSURE DATA CMECK CONTAINMENT PRESSURES DATA CllECK HILLI- DEN POI)fT. VAPOR PRESSURE UffCORRECTED CORRECTED flYGROHETER VOLTS fDEG. F. ) t PSIA) MANOMETER READING fPSIA) READING fPSIA)
UPPER: UPPER:
VPU-1 17.41,. 34.52 0.0980 PU-1 27.0250 26.8382 VPU-2 0.07 33.31 0.0934 PU-2 26.8937 26.8925 LOHERf LONER:
VPL"1 20.49 40.60 0. 1245 PL-1 0.0 0.0 VPL-2 18.54 36. 71 0.1069 PL-2 26.8764 26.8748 ICE-'PI-1 ICE -'I-1 9.05 17.81 0.0454 26.8967 26.8958 VPI-2 "1.27 9.14 0.0296 PI-2 26.9125 26.9112 AHDIENT 14.5200 14.5133 AVERAGE VAPOR PRESSURES SUMffARY OF CORRECTED AVERAGE PRESSURES'PPER CONTAINHEWT f PSIA) 0.0957 LONER CONTAINMENT f PSIA) 0.1157 AVERAGE UPPER PRESSURE tPSIA) 26.8653 ICE CONDENSER fPSIA) 0.0375 AVERAGE LONER PRESSURE fPSIA) 26.8748 AVERAGE ICE CONDENSER PRESSURE fPSIA) 26.9035 AVERAGE CONTAINlfEffT PRESSURE f PSIA) 26.8812 AVERAGE CONTAINffENT PRESSURE 't PSIG) 12.3679
RUt( tnt(BER 35 ELAPSED TIHE 17.00 COt(TAINHENT TEHPERATURES DATA C)IECK UPPER VOLUHE LO) (ER VOLUHE ICE CONDENSER RTD HILLI "VOLTS DEG. Fo RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 40. 13 80.26 ETR-122 35.84 71. 68 ETR-115 9. 26 18.52 ETR-102 38. 15 76.30 ETR-123 36.62 73. 24 ETR"116 9.28 18.56 ETR-103 35. 75 71.50 ETR-124 37.25 74.50 ETR-117 8.85 17. 70 ETR-104 35. 69 71.38 ETR-125 35.97 . 71.94 ETR-118 10.49 20.98 .
ETR-105 36.25 72.50 ETR-126 36.05 72.10 ETR" 119 8. 13 16.26 ETR-106 36.58 73.16 ETR-127 33.98 67.96 ETR-120 7.84 15.68 ETR-107 36. 18 72.36 ETR-129 37.13 74.26 ETR-121 8.08 16.16 ETR-108 36.21 72.42 ETR-130 35.64 71.28 ETR"109 35.59 71.18 ETR-131 33.98 67.96 ETR-110 35.49 70.98 ETR-132 37.66 75.32 ETR-ill 35.55 71 F 10 ETR-134 36.74 73.48 ETR"112 35.60 71.20 ETR-135 36.48 72.96 ETR-114 34.81 69. 62 ETR-136 36.60 73.20 ETR-128 36. 67 73.34 ETR-137 36.27 72.54 ETR" 133 34. 35 68.70 ETR"138 36.66 73.32 ETR-113 . 37.41 74.82 ETR"139 33.82 67.64 ETR-140 36.63 73.26 ETR-141 37. 29 74.58 ETR-142 36. 18 72.36 ETR-143 37. 63 75.26 ETR-144 36.94 73.88 ETR-145 41.58 83.16 ETR-146 37. 06 74. 12
SUMMARY
OF HEIGI(TED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F.) 72.98 LONER VOLUHE (DEG. F.) 73.25 ICE CONDENSER (DEG. F. ) 16.85 UPPER VOLUME (DEG. R.) 532.68 LOHER VOLUME (DEG. R.) 532.95 ICE CONDENSER (DEG. R. ) 476.55 CONTAINMENT VAPOR PRESSURE DATA Ct!ECK CON)AINHENT PRESSURES DATA CHECK HILLI- DEH POINT VAPOR PRESSURE Ut(CORRECTED CORRECTED HYGROMETER VOLTS. (DEG. F. ) (PSIA) HAt(OHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17.51 34.72 0.0988 PU-1 '7.0230 26.8362 VPU-2 0.09 33.66 0.0947 PU-2 26.8913 26.8901 LONER: LONER:
VPL-1 20 '0 40.82 0.1256
0. 1071 PL-1 PL-2 0.0 0.0 VPL-2 18.56 36.75 26.8743 26.8727 ICE:
ICE'PI-1 0.0498 PI-1 26. 8948 10.02 19. 73 26.8939 VPI-2 -1.07 12. 74 0.0354 PI-2 26.9106 26.9093 At(BIENT 14.5200 14.5133 AVERAGE VAPOR PRESSURES SUttHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0967 LONER CONTAINMENT (PSIA) 0.1163 AVERAGE UPPER PRESSURE (PSIA) 26,8631 ICE COWDEWSER (PSIA) 0.0426 AVERAGE LOHER PRESSURE (PSIA) 26.8727 AVERAGE ICE COttDEf(SER PRESSURE (PSIA) 26.9016 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8791 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3659
A~
RUN NUt(DER 36 ELAPSED TItfE 17.50 CONTAINHENT TEHPERATURES DATA C(IECK UPPER VOLUHE LOl'(ER VOLUHE ICE CONDENSER RTD HILLI"VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40.10 80.20 ETR-122 35.85 71. 70 ETR-115 9.58 19.16 ETR"102 38. 12 76.24 ETR-123 36.67 73.34 ETR-116 9.27 18.54 ETR-103 '5.75 71.50 ETR-124 37.25 74.50 ETR-117 8.92 17.84 ETR-104 35. 67 71.34 ETR-125 36.01 72.02 ETR-118 10. 10 20.20 ETR-105 36. 27 72.54 ETR-126 36.06 72.12 ETR-119 8.15 16.30 ETR-106 36. 56 73.12 ETR-127 34.00 68.00 ETR-120 7.86 15. 72 ETR-107 36. 16 72.32 ETR-129 37. 15 74.30 ETR-121 8. 12 16. 24 ETR-108 36. 21 72.42 ETR-130 35.65 71.30 ETR-109 35.51 71.02 ETR-131 33.98 67.96 ETR-110 35.48 70.96 ETR-132 37.66 75.32 ETR"ill 35.57 71.14 ETR-134 36.60 73.20 ETR-112 35.60 71. 20 ETR-135 36.54 73.08 ETR-114 34.78 69.56 ETR-136 36.63 73.26 ETR-128 36. 68 73.36 ETR-137 36.26 72.52 ETR-133 34.35 68.70 ETR-138 36.66 73.32 ETR-113 37.40 74.80 ETR-139 33.81 67.62 ETR-140 36.64 73.28 ETR-141 37.29 74.58 ETR"142 36.18 72.36 ETR-143 37.64 75.28 ETR-144 36.93 73.86 ETR-145 41.55 83.10 ETR-146 37.07 74.14 SUHHARY OF WEIGtlTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.95 LOWER VOLUHE (DEG. F. ) 73.25 ICE CO(4)ENSER (DEG. F.) 16.89 UPPER VOLUHE (DEG. R. ) 532 '5 LOWER VOLUHE (DEG. R. ) 532.95 ICE CONDENSER (DEG. R.) 476.59 CONTAINtfENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRE~~ES DATA CHECK HILLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED I(YGROtfETER VOLTS (DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPERt VPU-1 17.44 34.58 0.0982 PU-1 27.0260 26.8392 VPU-2 0.08 33.42 0.0938 PU-2 26.8950 26.8938 LOI'lER: LOWER'-
VPL-1 20.69 41.00 0.1265 PL-1 0.0 0.0 VPL-2 18.55 36.73 0 F 1070 PL"2 26.8775 26.8759 ICE: ICE-'I-1 VPI-1 7. 72 15. 18 0.0399 26.8986 26.8977 VPI-2 -1.07 12.74 0.0354 PI-2 26.9147 26.9134 AHDIENT 14.5100 14.5033 AVERAGE VAPOR PRESSURES SUtftfARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0960 LOWER CONTAINHENT (PSIA) 0.1167 AVERAGE UPPER PRESSURE (PSIA) 26.8665 ICE CONDENSER (PSIA) 0.0377 AVERAGE LOt(ER PRESSURE (PSIA) 26.8759 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9055 AVERAGE CONTAIN(Et(T PRESSURE (PSIA) 26.8826 AVERAGE CONTAIttHENT PRESSURE (PSIG) 12.3793
~
RUN tKIIBER 37 ELAPSED TIIIE 18.00 CONTAINMENT TEHPERATURES DATA CIIECK UPPER VOLUHE LO)IER VOLUHE ICE CONDEtISER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 40. 05 80.10 ETR-122 35.87 71.74 ETR-115 ' ~ 49 18.98 ETR-102 38.09 76.18 ETR-123 36.65 73.30 ETR-116 9. 24 18.48 ETR-103 35. 76 71.52 ETR-124 37.24 74.48 ETR-117 8. 88 17. 76 ETR-104 35. 71 71.42 ETR-125 35.99 71.98 ETR-118 10. 17 20.34 ETR-105 36. 24 72.48 ETR-126 36.05 72.10 ETR-119 8.14 16.28 ETR-106 36. 56 73.12 ETR-127 33.98 67.96 ETR-120 7.85 15.70 FTR-107 36. 11 72.22 ETR-129 37.16 74.32 ETR-121. 8.14 16.28 ETR-108 36. ZO 72.40 ETR-130 35.65 71.30 ETR-109 35.59 71.18 ETR"131 33.96 67.92 ETR-110 35.38 70.76 ETR-132 37.66 75.32 ETR-111 35.57 71.14 ETR-134 36.65 73.30 ETR"112 . 35. 60 71.20 ETR-135 36.51 73.02 ETR-114 34.84 69.68 ETR-136 36.62 73.24 ETR-128 36. 70 73.40 ETR-137 36.31 72.62 ETR-133 34. 36 68.72 ETR-138 36.64 73.28 ETR-113 37. 39 74.78 ETR-139 33 '3 67.66 ETR-140 36.64 73.28 ETR-141 37.28 74.56 ETR-142 36.18 72.36 ETR-143 37.64 75.28 ETR-144 36.93 73.86 ETR-145 41.57 83.14 ETR-146 37.08 74.16 UPPER VOLUME IDEG. F. )
UPPER VOLUME IDEG. R. )
72.94 532.64 CONTAINMENT VAPOR PRESSURE HILLI-
'CE
SUMMARY
OF HEIGHTED AVERAGE TEHPERATlJRES LONER VOLUME IDEG. F. )
LONER VOLUME IDEG. R. )
DATA CIIECK DEN POINT VAPOR PRESSURE 73.26 532.96 CONDENSER (DEG.
ICE CONDENSER IDEG.
F.)
R.)
CONTAINMENT PRESSURES 16.87 476.57 UNCORRECTED DATA CIIECK CORRECTED
)IYGROHETER VOLTS (DEG. F.) IPSIA) MACHETE R READING IPSIA) READItIG (PSIA)
UPPER: UPPER:
VPU-1 17.46 34.62 0.0984 PU-1 27.0250 . 26.8382 VPU-2 0.08 33.48 0.0940 PU-2 26.8930 26.8918 LOITER'PL-1 LO)IER:
20 ~ 78 41. 18 0.1273 PL-1 0.0 0.0 VPL-2 18.57 36.77 0.1072 PL-2 26.8758 26.8742 ICE: ICE'I-1 VPI-1 8.03 15.80 0.0411 26.8967 26. 8958 VPI-2 -1.09 12.38 0.0348 PI-2 26.9141 26.9128 AMBIENT 14.5100 14.5033 AVERAGE VAPOR PRESSURES SUNRY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINtIENT I PSIA) 0.0962 LOITER CONTAINMENT I PSIA) 0.1173 AVERAGE UPPER PRESSURE {PSIA) 26.8650 ICE CONDENSER I PSIA) 0.0380 AVERAGE LOI'IER PRESSURE IPSIA) 26.8742 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.9043 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8811 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.3778
1
C!
RUN NUMBER 38 ELAPSED TIME 18.50 CONTAINMENT TEMPERATURES DATA CHECK s UPPER VOLUME LOWER VOLUME ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD t 1ILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 '0.04 80.08 ETR-122 35.85 71.70 ETR-115 9.37 18.74 ETR-102 38. 06 76.12 ETR-123 36.65 73.30 ETR-116 9.30 18.60 ETR-103 35. 75 71.50 71.34 ETR-124 37 '5 74.50 ETR-117 8. 89 17.78 ETR-104 35. 67 ETR-125 35.97 71. 94 ETR"118 10.17 20.34 ETR-105 36. 20 72.40 ETR-126 36.05 72.10 ETR-119 8.15 16.30 ETR 106 36.54 73.08 ETR-127 33.96 67.92 ETR-120 7. 92 15.84 ETR-107 36. 17 72.34 . ETR"129 37.18 74.36 ETR "121 8. 11 16.22 ETR-108 36.19 72.38 ETR-130 35.65 71.30 ETR-109 35.56 71. 12 ETR-131 33.97 67.94 ETR-110 35.43 70.86 ETR-132 37.66 75.32 ETR-ill 35.57 71. 14 ETR-134 36.56 73.12 ETR-112 35.61 71.22 ETR"135 36.46 72.92 ETR-114 34.79 69.58 ETR-136 36.64 73.28 ETR" 128 36. 71 73.42 ETR-137 36.26 72.52 ETR-133 34.36 68.72 ETR-138 36.65 73.30 ETR-113 37.42 74.84 ETR-139 33.84 67.68 ETR-140 36.66 73.32 ETR-141 37.29 74.58 ETR-142 36.18 72.36 ETR-143 37.64 75.28 ETR-144 36.94 73.88 ETR-145 41.58 83.16 ETR-146 37.07 74.14
SUMMARY
OF WEIGHTED AVERAGE TEt!PERATURES UPPER VOLUME (DEG. F. ) 72.92 LOWER VOLUHE tDEG. F. ) 73.23 ICE CONDENSER (DEG. F. ) 16.90 UPPER VOLUHE (DEG. R. ) 532.62 LOWER VOLUtlE 1DEG. R. ) 532.93 ICE CONDENSER 1DEG. R.) 476.60 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CtlECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED ttYGROMETER VOLTS 1DEG. F.f (PSIA) HANOHETER READING tPSIA) READING (PSIA)
UPPER: UPPER-VPU-1 17A2 34.54 0.0981 PU"1 27.0230 26.8362 VPU-2 0.07 33.22 0.0931 PU-2 26.8913 26.8901 LOl'1ER-LOWER'PL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.58 36.79 0.1073 PL-2 26.8740 26.8724 ICE: ICE:
VPI-1 8.42 16.57 0.0427 PI-1 26.8948 26.8939 VPI-2 -1.06 12.92 0.0357 PI-2 26.9124 26.9111 AMBIENT 14.5100 14.5033 AVERAGE VAPOR PRESSURES SUt01ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0956 LOWER CONTAINMENT (PSIA) 0.1073 AVERAGE UPPER PRESSURE (PSIA) 26.8631 ICE CONDENSER t PSIA) 0.0392 AVERAGE LOttER PRESSURE (PSIA) 26.8724 AVERAGE ICE CONDENSER PRESSURE tPSIA) 26.9025 AVERAGE CONTAINt1ENT PRESSURE 1 PSIA) 26.8793 AVERAGE CONTAIN)tENT PRESSURE 1 PSIG) 12.3760 Ob
gQ RUN NR(BER 39
~ ELAPSED TIHE 19.00 CONTAINMENT TEMPERATURES DATA CHECK UPP ER VOLUME LONER VOLUME ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 39. 99 79.98 ETR-122 35.87 71.74 ETR-115 9.31 18.62 ETR-102 38.03 76.06 ETR-123 36.63 73.26 ETR-116 9.42 18.84 ETR-103 35.72 71.44 ETR-124 37.25 74.50 ETR"117 8.85 17. 70 ETR-104 35.67 71.34 ETR-125 35.94 71.88 ETR-118 10. 28 20.56 ETR-105 36.24 72.48 ETR-126 36.06 72.12 ETR-119 8.16 16.32 ETR-106 36.53 73.06 ETR-127 33.96 67.92 ETR" 120 7. 91 15.82 ETR-107 36.10 72.20 ETR-129 37.14 74.28 ETR-121 8. 12 16.24 ETR-108 36.16 72.32 ETR-130 35.67 71.34 ETR-109 35.50 71.00 ETR-131 33.96 67. 92 ETR-110 35 45 70.90 ETR-132 37.66 75.32 ETR-ill 35.57 71.14 ETR-134 36.69 73. 38 ETR-112 35.61 71.22 ETR-135 36.55 73.10 ETR-114 '4.79 69.58 ETR-136 36.59 73.18 ETR-128 36.71 73.42 " ETR"137 36.26 72.52 ETR-133 34.36 68.72 ETR-138 36.64 73.28 ETR-113 37. 39 74.78 ETR-139 33.84 67.68 ETR-140 36.65 73.30 ETR-141 37.29 74.58 ETR-142 36.18 72.36 ETR-143 37.64 75.28 ETR-144 36.94 73.88 ETR-145 41.55 83.10 ETR-146 37. 08 74.16 SUN(ARY OF NEIGI(TED AVERAGE TEMPERATURES
. UPPER VOLUME (DEG. F.) 72.88 LONER VOLUME (DEG. F.) 73.25 ICE CONDENSER (DEG. F.) 16.92 UPPER VOLUME (DEG. R.) 532.58 'ONER VOLUME (DEG. R.) 532.95 ICE CONDENSER (DEG. R.) 476.62 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAI((MENT PRESSURES DATA CllECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS (DEG. F. ) (PSIA) l(ANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17.57 34.84 0.0993 PU-1 27.0200 26.8332 VPU-2 O.D9 33.53 0.0942 PU"2 26.8878 26.8866 LONER: LONER:
VPL-1 0.0 "0.01 0.0 PL-1 0.0 0.0 VPL-2 18.60 36.83 0.1074 PL"2 26.8706 26.8690 ICE: ICE:
VPI-1 9.13 17. 97 0 '457 PI"1 26.8913 26.8904 VPI-2 "0.99 14.18 0.0380 PI-2 26.9069 26.9056 AMBIENT 14.4953 14.4888 AVERAGE VAPOR PRESSURES SUMHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0967 LONER CONTAINMENT (PSIA) 0.1074 AVERAGE UPPER PRESSURE (PSIA) 26.8599 ICE CONDENSER (PSIA) 0.0419 AVERAGE LONER PRESSURE (PSIA) 26.8690 AVERAGE ICE CONDENSER PRESSURE '(PSIA) 26.8980 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8756 AVERAGE COt(TAINMENT PRESSURE (PSIG) 12.3869
(gQ RUM NUt(DER 40 ELAPSED TIHE 19.50 CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDEt)SER RTO HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD t(ILLI-.VOLTS DEG. F.
ETR-101 40.00 80.00 ETR-122 35.89 71.78 ETR-115 9. 26 18.52 ETR-102 38. 00 76 F 00 ETR-123 36.64 73.28 ETR-116 9. 22 18.44 ETR-103 35. 74 71.48 ETR"124 37. 27 74.54 ETR-117 8. 93 17.86 ETR-104 35. 67 71.34 ETR-125 35. 96 71.92 ETR-118 10.94 21.88 ETR-105 36. 22 72.44 ETR-126 36.06 72.12 ETR-119 8. 17 16.34 ETR-106 36.52 73.04 ETR-127 33.99 67.98 ETR-120 7.87 15. 74 ETR-107 36.08 72.16 ETR-129 37.15 74.30 ETR-121 8.13 16.26 ETR-108 36. 15 72.30 ETR-130 35.65 71 '0 ETR-109 35.54 71.08 ETR-131 33 '6 37.66 67.92 ETR-110 35.45 70.90 ETR-132 75.32 ETR-ill 35.57 71. 14 ETR-134 36.68'6.55 73.36 ETR-112 35.61 71. 22 ETR-135 73.10 ETR-114 34.87 69.74 ETR-136 36.58 73.16 ETR-128 36. 71 73.42 ETR-137 36.26 72.52 ETR-133 34.35 68.70 ETR-138 36.65 73.30 ETR-113 37.36 74.72 ETR-139 33.85 67.70 ETR-140 . 36.66 73.32 ETR"141 37.30 74.60.
ETR-142 36.19 72.38 ETR-143 37.64 75.28 ETR-144 36.95 73.90 ETR-145 41.57 83.14 ETR-146 37.09 74.18 SUHHARY OF HEIG)ITED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 72.88 LONER VOLUt(E (DEG. F.) 73.26 ICE CONDENSER (DEG. F.) 16.97 UPPER VOLUHE (DEG. R.) 532.58 LONER VOLUHE (DEG. R.) 532.96 ICE CONDENSER (DEG. R.) 476.67 COt(TAINHENT VAPOR PRESSURE DATA CllECK CONTAINHENT PRESSURES DATA CtlECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED 'ORRECTED HYGROHETER VOLTS ( DEG. F ~ ) ( PSIA ) HAt(OHETER READING (PSIA) READIt(G (PSIA)
UPPER- UPPER:
VPU-1 17.51 34.72 0.0988 PU-1 27.0200 26.8332 VPU-2 0.09 33.58 0.094i4 PU-2 26.8882 26.8870 LO((ER: LONER:
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.60 36.83 0.1074 PL-2 26.8710 26.8694 ICE: ICE:
VPI-1 8. 12 15.97 0.0415 PI-1 26.8916 26.8907 VPI"2 -1.12 11.84 0.0338 PI "2 26. 9041 26.9028 AHBIENT 14.4953 14.4888 AVERAGE VAPOR PRESSURES SUttHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0966 LONER CONTAIN((ENT (PSIA) 0.1074 AVERAGE UPPER PRESSURE (PSIA) 26.8601 ICE CONDENSER (PSIA) 0.0377 AVERAGE LONER PRESSURE (PSIA) 26.8694 AVERAGE ICE COt(DENSER PRESSURE (PSIA) 26.8967 AVERAGE COt(TAIt(t'IENT PRESSURE (PSIA) 26.8754 .
AVERAGE CONTAINHENT PRESSURE (PSIG) 12.3867
~
Qq~ q RUN NUt(DER 41 ELAPSED TIHE 20.00 COt(TAINHENT TEMPERATURES DATA CtlECK UPPER VOLUME LOWER VOLUHE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS 'EG. F.,
ETR-101 39.95 79.90 ETR-122 35.87 71.74 ETR-115 9.15 18.30 ETR-102 37. 98 75.96 ETR-123 36.64 73.28 ETR-116 9. 12 18. 24 ETR-103 35.73 71.46 fTR-124 37.25 74.50 ETR-117 8.84 17. 68 ETR-104 35. 67 71.34 ETR-125 35.99 36.06 71 '8 72.12 ETR" 118 10. 53
8. 18
21. 06 ETR-105 36. 16 72. 32 ETR-126 ETR-119 16. 36 ETR-106 36.50 73.00 ETR-127 33.96 67. 92. ETR-120 7.90 15.80 ETR"107 36.06 72.12 ETR-129 37.15 74.30 ETR-121 8.13 16.26 ETR-108 36.11 72.22 ETR-130 35.65 71.30 ETR-109 35.54 71.08 ETR-131 33.95 67.90 ETR-110 35.39 70.78 ETR-132 37.66 , 75.32 ETR-ill 35.56 71.12 ETR-134 36.67 73.34 ETR-112 35. 61 71.22 ETR-135 36.56 73.12 ETR-114 34.85 69.70 ETR-136 36.60 73.20 ETR-128 36. 73 73.46 ETR-137 36.28 72.56 ETR"133 34.34 68.68 ETR"138 36.62 73.24 ETR-113 37.36 74.72 ETR-139 33.84 67.68 ETR-140 36.66 73.32 ETR-141 37.30 74.60 ETR-142 36.19 72.38 ETR-143 37.63 75.26 ETR-144 36.94 73.88 ETR-145 41.55 83.10 ETR-146 37.10 74.20
SUMMARY
OF WEIGHTED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F.) ,72.83 LOWER VOLUHE (DEG. F.) 73.26 ICE CONDENSER (DEG. F.) 16.89 UPPER VOLUHE (DEG. R.) 532.53 LOWER VOLUME (DEG. R.) 532.96 ICE CONDENSER (DEG. R.) 476.59 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK MYGROt(ETER
'UPPER:
VPU"1
'ILLI- VOLTS 17.46 DEW POINT (DEG. F. )
34.62 VAPOR PRESSURE (PSIA) 0.0984 MANOMETER UPPER:
PU"1 UNCORRECTED READING (PSIA) 27.0200 CORRECTED READING (PSIA) 26.8332 VPU"2 -0. 13 29.66 0.0 PU-2 26.8879 26.8867 LOWER ~ LOWER:
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.60 36.83 0.1074 PL-2 26.8704 26.8688 ICE'PI-1 ICE'I-1 8.57 16.86 0.0433 26.8912 26.8903 VPI-2 -1.08 12.56 0.0351 PI-2 26.9035 26.9022 AMBIENT 14.4953 14.4888 AVERAGE VAPOR PRESSURES SUttHARY OF CORRECTED AVERAGE PRESSURES
()PPER CONTAINt(ENT (PSIA) 0.0984 LOWER CONTAIN)(ENT (PSIA) 0.1074 AVERAGE UPPER PRESSURE (PSIA) 26.8600 ICE CONDENSER (PSIA) 0.0392 AVERAGE LOtlER PRESSURE (PSIA) 26.8688 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8962 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8750 AVERAGE CONTAINt(ENT PRESSURE (PSIG) 12.3862
0
$8 RUN ttUtQER 42 ELAPSED TIHE 20.50 COtfTAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F ~
ETR-101 39.96 79. 92 ETR-122 35.87 71.74 ETR-115 9.32 18.64 ETR-102 37. 95 75. 90 ETR-123 36.65 73.30 ETR"116 9.37 18.74 ETR-103 35. 73 71.46 ETR-124 37.21 74.42 ETR-117 8.86 17.72 ETR-104 35.66 71. 32 ETR-125 35.99 71.98 ETR-118 10 '9= 20.38 ETR-105 36. 20 72.40 ETR-126 36.07 72.14 ETR-119 8.18 16.36 ETR-106 36.50 73.00 ETR-127 33 '5 37;ll 67.90 ETR" 120 7. 90 15.80 ETR"107 36.05 72.10 ETR-129 74.22 ETR-121 8. 19 16.38 ETR-108 36.11 72 F 22 ETR-130 35.64 71.28 ETR-109 35.56 71.XZ ETR-131 33.96 67.92 ETR-110 35.42 70.04 ETR"132 37. 64 75.28 ETR-111 35.57 71.14 ETR-134 36.64 73.28 ETR-112 35. 61 71.22 ETR-135 36.49 72.98 ETR-114 34.77 69.54 ETR-136 36.56 73.12 ETR"128 36. 73 73.46 ETR-137 36.28 72.56 ETR-133 34.38 68.76 ETR-138 36.63 73.26 ETR-113 37.40 74.00 ETR-139 33.85 67.70 ETR-140 36.65 73.30 ETR-141 37.31 74.62 ETR-142 36. 19 72.38 ETR"143 37.64 75.28 ETR-144 36.95 73.90 ETR-145 41.56 83.12 ETR-146 37. 07 74.14 SUHHARY OF NEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE tDEG. F. ) 72.83 LONER VOLU)K (DEG. F.) 73 .22 ICE CONDENSER tDEG. F.) X6.93 UPPER VOLUHE tDEG. R.) 532.53 LONER VOLUHE tDEG: R.) 532 .92 ICE CONDENSER 'lDEG. R.) 476.63 CONTAINHENT VAPOR PRESSURE DATA CllECK CONTAINtKNT PRESSURES DATA CHECK DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGRO! IETER VOLTS (DEG. F. ) <PSIA) HANOHETER READING OPSIA) READING [PSIA)
UPPER: UPPER:
, VPU"1 17.46 34.62 0.0984 PU-1 27.0200 26.8332 VPU"2 -0.04 31'28 0.0 PU-2 "
26.8888 26.8876 VPI"2'ILLI-LONERS VPL-1 0.0 "0.01 0.0 LOHER-'L-1 0.0 0.0 VPL-2 18.61 36.85 0.1075 PL-2 26.8711 26.8695 ICE: ICE:
VPI-1 9.37 18.45 0. 0468. PI-1 26.8917 26.8908
-1 01
~ X3.82 0,0373 PI-2 26.9045 26.9032 Att81ENT 14.4915 X4.4849 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTEO AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0984 LS'tER CONTAINHENT t PSIA) 0.1075 AVERAGE UPPER PRESSURE tPSIA) 26.8604 ICE CONDENSER t PSIA) 0.0421 .AVERAGE LOHER PRESSURE (PSIA) 26.8695 AVERAGE ICE COttDENSER PRESSURE (PSIA) 26.8970 AVERAGE COtA'AINttENT PRESSURE (PSIA) 26.8756 AVERAGE CONTAINHENT PRESSURE t PSIG) 12.3907 p p
Jl'pss RUN NUt(DER 43 ELAPSED TIHE 21.00 COt(TAINMEt(T TEMPERATURES DATA CllECK UPPER VOLUME LOttER VOLUME ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD MIL LI "VOLTS DEG. F. RTD ttILLI-VOLTS DEG. F.
ETR-101 39. 96 79. 92 ETR-122 35.88 71.76 ETR-115 9.83 19.66 ETR-102 37. 92 75.84 ETR-123 36.66 73.32 ETR-116 9.60 19.20 ETR-103 35.'?2 71.44 ETR-124 37. 24 74.48 ETR-117 9.33 18.66 ETR-104 35. 66 71.32 ETR"125 35.99 71.98 ETR-118 10.45 20.90 ETR-105 36.16 72.32 ETR-126 36.05 72.10 ETR-119 8.19 16.38 ETR-106 36.49 72. 98 ETR-127 33.98 67.96 ETR "120 7. 91 15.82 ETR-107 36. 06 72 '2 ETR-129 37. 17 35.65 74.34 71.30 ETR-121 8. 18 16.36 ETR-108 36. 10 72.20 ETR-130 ETR-109 35.56 71. 12 ETR-131 33.96 67.92 ETR-110 35.46 70.92 ETR-132 37.65 75.30 ETR"ill 35.56 71.12 ETR-134 36.69 73.38 ETR-112 35.60 71.20 ETR-135 36.51 73.02 ETR-114 34.76 69.52 ETR-136 36.56 73.12 ETR-128 36. 75 73.50 ETR-137 36.25 72.50 ETR-133 34.36 68.72 ETR-138 36.67 73.34 ETR-113 37.36 74.72 ETR-139 33.85 67.70 ETR-140 36.65 73.30 ETR-141 37.32 74.64 ETR-142 36.20 72.40 ETR-143 37.64 ?5.28 ETR-14i4 36.94 73.88 ETR-145 ETR-146 41.56 37.09 83 '2 74.18 SUHHARY OF HEIGHTED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F.) 72.80 LOl<ER VOLUME (DEG. F.) 73.25 ICE CONDENSER (DEG. F.) 17.15 UPPER VOLUME (DEG. R.) ~ 532.50 LOHER VOLUME (DEG. R. ) 532.95 ICE CONDENSER (DEG. R.) 476.85 CONTAINMENT VAPOR PRESSURE DATA C(IECK CONTAINHENT PRESSURES DATA Cl(ECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETE R VOLTS (DEG. F. ) (PSIA) HANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17.48- 34.66 0.0986 PU-1 27.0180 26.8313 VPU-2 0.01 32.09 0.0889 PU-2 26.8862 26.8850 LOI(ER-'PL-1 (.ONER:
0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.62 36.87 0.1076 PL-2 26.8689 26.86?3 ICE: ICE:
VPI-1 9. 97 19 62 0.0495 PI-1 26.8892 26.8883 VPI-2 -0.95 14.90 0.0394 PI-2 26.9021 26.9008 AHBIEt(T 14.4915 14.4849 AVERAGE VAPOR PRESSURES SUt(MARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENl (PSIA) 0.0937, LONER CONTAINHEt(T (PSIA) 0.1076 AVERAGE UPPER PRESSURE (PSIA) 26.8581 ICE CONDENSER (PSIA) 0.0445 AVERAGE LOHER PRESSURE (PSIA) 26.8673 AVERAGE ICE COt(DENSER PRESSURE (PSIA) 26.8945 AVERAGE CONTAINt(ENT PRESSURE (PSIA) 26.8733 AVERAGE CONTAINt(Et(T PRESSURE (PSIG) 12.3884 p :~
e RUN HUt(DER ELAPSED TIME 21.50 CONTAINHENT TEMPERATURES DATA CIIECK UPPER VOLUHE LONER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLIVOLTS DEG. F.
ETR-101 39.93 79.86 ETR"122 35.90 71.80 ETR-115 9.78 19.56 ETR-102 37 ~ 91 75.82 ETR-123 36.66 73.32 ETR" 116 9. 64 19.28 ETR-103 35. 71 71.42 ETR-124 37.23 74.46 ETR"117 9.27 18.54 ETR-104 35.66 71.32 ETR-125 35.97 71.94 ETR-118 10 '6 20.92 ETR-105 36. 16 72.32 ETR-126 36.06 72.12 ETR-119 8. 20 16.40 ETR-106 36.47 72.94 ETR-127 34.00 68.00 ETR-120 7. 96 15. 92 ETR-107 36. 03 72.06 ETR-129 37.15 74.30 ETR-121 8. 23 16.46 ETR-108 36.07 72.14 ETR-130 35.65 71.30 ETR-109 35.54 71.08 ETR-131 33.95 67.90 ETR-110 35.46 70 '2 71.14 ETR-132 37.66 36.67 75.32 73.34 ETR"111 35.57 ETR-134 35.59 'TR-112 71.18 ETR-135 36.54 73.08 ETR-114 34.84 69. 68 ETR-136 36.56 73.12 ETR-128 36. 75 73.50 ETR-137 36.28 72.56 ETR-133 34.36 68.72 ETR-138 36.65 73.30 ETR-113 37.33 74.66 ETR-139 33.85 67.70 ETR-140 36.66 73.32 ETR-141 37.33 74.66 ETR-142 36.19 72.38 ETR-143 37.63 75.26 ETR-144 36.94 73.88 ETR-145 41.57 83.14 ETR-146 37. 11 74.22 SUHHARY OF NEIGl(TED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F.) 72.79, LONER VOLUME (DEG. F.) 73.26 ICE COt(DENSER (DEG. F.) 17.20 UPPER VOLUME (DEG. R.) 532.49 LOHER VOLUME (DEG. R.) 532.96 ICE CONDENSER (DEG. R.) 476.90 CONTAINHENT VAPOR PRESSURE DATA CKECK CONTAINMENT PRESSURES DATA CIIECK HILLI- DEN POIt(T VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROHETER VOLTS (DEG. F, ) (PSIA) MANOMETER READING ( PSIA ) READING ( PSIA)
UPPER: ~ UPPER(
VPU-1 17.49 34. 68 0.0986 PU-1 27.0220 26.8352
, VPU-2 0.03 32.54 0.0905 PU"2 26.8905 26.8893 LOHERt'PL-1 LONER-'L-1 0.0 -0.01 0.0 0.0 0.0 VPL-2 18.62 36.87 0.1076 PL"2 26.8730 26.8714 ICE: ICE:
VPI"1 9.78 19.26 0.0487 PI-1 26.8938 26.8929 VPI-2 -0.99 14.18 0.0380 PI-2 26.9066 26.9053 Al(DIENT 14.4895 14.4830 AVERAGE VAPOR PRESSURES SUt(MARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0 '946 LONER CONTAIN((Et(T (PSIA) 0. 1076 AVERAGE UPPER PRESSURE (PSIA) 26.8622 ICE CONDENSER (PSIA) 0.0433 AVERAGE LOt(ER PRESSURE (PSIA) 26.8714 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8991 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8776 AVERAGE COt(TAIt(HEt(r PRESSURE (PSIG) 12.3946
~
RUN NUHSER 45 ELAPSED TIHE 22.00 CONIAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDEt(SER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD NILLI-VOLTS DEG. F.
ETR-101 39.93 79.86 ETR"122 35.88 71.76 ETR-115 9. 78 19.56 ETR-102 37.88 75.76 ETR-123 36.63 73.26 ETR-116 9.78 19.56 ETR-103 35. 74 71,4IS ETR-124 37.27 74.54 ETR-117 9.39 18.78 ETR-104 35. 66 71.32 ETR-125 35.97 71. 94 ETR-118 10. 63 21.26 ETR-105 36.15 72.30 ETR"126 36 '6 72.12 ETR-119 8.21 16.42 ETR-106 36.46 72.92 ETR-127 33.96 67.92 ETR-120 8.05 16.10 ETR-107 36. 02 72.04 ETR-129 37.14 74.28 ETR-121 8.17 16.34 ETR-108 36. 06 72.12 ETR-130 35.64 71.28 ETR-109 35.49 70.98 ETR-131 33.96 67.92 ETR-110 35. 46 70.92 ETR-132 37.65 75.30 ETR-ill 35.57 71.14 ETR-134 36.62 73.24 ETR-112 35.59 71.18 ETR-135 36.50 73.00 ETR-114 34.83 69.66 ETR-136 36.60 73.20 ETR-128 36. 76 73.52 ETR-137 36.27 72.54 ETR-133 34.38 6e.76 ETR-138 36.65 73.30 ETR"113 37.33 74.66 ETR-139 33.87 67.74 ETR-140 36.66 73.32 ETR-141 37.32 74.64 ETR-142 36.20 72.40 ETR-143 37.64 75.28 ETR-144 36.95 73.90 ETR-145 41.56 83.12 ETR-146 37. 12 74.24 SUt(NARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 72.78 LOHER VOLUHE (DEG. ) 73.24 ICE CONDENSER (DEG. F.) 17.29
'9 F ~
UPPER VOLUHE (DEG. R.) 532.48 LONER VOLUHE (DEG. R.) 532.94 ICE CONDENSER (DEG. R.) 476 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAIN((Et(i PRESSURES DATA Cl(ECK HILLI- DEI( POINT VAPOR PRESSURE UNCORRECTED CORRECTEO HYGROt(ETER VOLTS (DEG. F. ) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER-VPU"1 17.52 34.74 0.0989 PU-1 27.0210 26.8342 VPU-2 0.05 32.85 0.0917 PU-2 26.8888 26.ee76 LONER: LONER'L-1 VPL-1 0.0 -0.01 0.0 0.0 0.0 VPL-2 18.63 36.89 0.1077 PL-2 26.8724 26.8708 ICE '- ICE:
VPI-1 10.64 20. 96 0.0528 PI-1 26.8928 26.8919 VPI-2 -i+08 12.56 0.0351 PI"2 26.9059 26.9046 AHBIEt(T 14.4953 14.4887 AVERAGE VAPOR PRESSURES SUtm(ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIN((ENT (PSIA) 0.0953 LONER CONTAIttt(ENT (PSIA) 0.1077 AVERAGE UPPER PRESSURE (PSIA) 26.8609 ICE CONDENSER (PSIA) 0.0440 AVERAGE LOl'(ER PRESSURE (PSIA) 26.8708 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8982 AVERAGE COt(TAIttttENT PRESSURE (PSIA) 26.8766 AVERAGE COt(TAINHENT PRESSURE (PSIG) 12.3879 j
"tt RUN NUMDER 46 ELAPSED TltkE 22.50 CONTAINMENT TEHPERATURES DATA CHECK UPPER VOLUME LONER VOLUttE ICE COttDEttSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR"101 39.86 79.72 ETR-122 35.91 71.82 ETR-115 9.85 19 '0 ETR-102 37. 86 75.72 ETR-123 36.61 73.22 ETR-116 9. 88 19.76 ETR-103 35. 69 71.38 ETR-124 37.25 74.50 ETR-117 9. 63 19.26 ETR-104 35. 65 71.30 ETR-125 36.01 72.02 ETR-118 11. 39 22.78 ETR-105 36. 14 72.28 ETR-126 36.07 72.14 ETR-119 8.22 16.44 ETR-106 36.44 72.88 ETR-127 33.97 67,94 ETR-120 8.04 16.08 ETR-107 36. 02 72.04 ETR-129 37.15 74.30 ETR-121 8.25 16.50 ETR-108 36. 08 72.16 ETR-130 35.65 71.30 ETR-109 35.54 71.08 ETR-131 33.94 67.88 ETR-110 35.44 70.88 ETR-132 37.65 75. 30 ETR-ill 35.56 71.12 ETR-134 36.64 73.28 ETR-112 35. 60 71.20 ETR-135 36.54 73.08 ETR-114 34.85 69. 70 ETR-136 36.59 73.18 ETR-128 36. 77 73. 54 ETR-137 36.26 72.52 ETR-133 34. 37 68. 74 ETR-138 36.64 73.28 ETR-113 37.33 74.66 ETR-139 33.88 67.76 ETR-140 36.67 73.34 ETR-141 37.34 74.68 ETR-142 36 '0 72.40 ETR>>143 37.64 75.28 ETR-144 36.95 73.90 ETR"145 41.57 83.14 ETR-146 37.10 74.20 SUHHARY OF NEIGHTED AVERAGE TEttPERATlJRES UPPER VOLUME (DEG. F.) 72. 76 LONER VOLUttE tDEG. F. ) 73.25 ICE CONDENSER (DEG. F.) 17.49 UPPER VOLUME (DEG. R.) 532.46 LONER VOLUHE tDEG. R.) 532.95 ICE CONDENSER (DEG. R.) 477.19 CONTAINHENT VAPOR PRESSURE DATA CHECK . CONTAINMENT PRESSURES DATA CHECK MI!.LI" DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS t DEG. F. ) t PSIA) HANOltETER READING (PSIA) READING {PSXA)
UPPER: UPPER:
VPU-1 17.60 34. 90 0.0995 PU-1 27.0190 26.8322 VPU-2 0.05 32. 94 0.0920 PU"2 26.8875 26.8863 LOHERt LONER:
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.64 36.91 0.1078 PL-2 26.8702 26.8686 ICE: ICE:
VPI-1 10.58 20.84 0.0525 PI-1 26.8908 26.8899 VPI"2 -0.98 14.36 0.0383 PI-2 26.9037 26 '024 AHBIENT 14.5050 14.4984 AVERAGE VAPOR PRESSURES OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT t PSIA)
LOttER CONTAINHENT t PSIA)
ICE CONDENSER t PSIA) 0.0957
'0+1078 0.0454 0'UHHARY AVERAGE AVERAGE UPPER PRESSURE (PSIA)
LO)tER PRESSURE (PSIA) 26.8593 26.8686 AVERAGE ICE COttDEttSER PRESSURE t PSIA) 26.8961 AVERAGE CONTAIN)lENT PRESSURE l PSIA ) 26 8747 AVERAGE CONTAINMENT PRESSURE t PSIG) 12.3763
C RUN NV)(DER 47 ELAPSED TIME 23.00 CONTAINMENT TEMPERATURES DATA CHFCK UPPER VOLUME LONER VOLUME " ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI"VOLTS DEG. F.
ETR-101 -
39.90 79.80 ETR"122 35. 92 71.84 ETR-115 9.92 19.84 ETR-102 37.84 75.68 ETR-123 36.66 73.32 ETR-116 9.94 19.88 ETR-103 35. 70 71.40 ETR"124 37.26 74.52 ETR-117 9.61 19. 22 ETR-104 35. 62 71.24 ETR-125 36.00 72.00 ETR-lie 11 47 22.94 ETR-105 36. 09 72.18 ETR-126 36.07 72.14 ETR-119 8.23 16.46 ETR-106 36. 44 72.88 ETR-127 33.96 67.92 ETR-120 8. 07 16.14 ETR-107 36.00 72.00 ETR-129 37.17 74.34 ETR-121 8. 27 16.54 ETR-108 36. 05 72.10 ETR-130 35.67 71.34 ETR-109 35.51 71.02 ETR-131 33.95 67.90 ETR-110 35. 41 70.82 ETR-132 37.65 75.30 ETR-ill 35.57 71. 14 ETR-134 36.72 73.44 ETR-112 35. 60 71.20 ETR-135 36.50 73.00 ETR-114 34.81 69.62 ETR-136 36.56 73.12 ETR-128 36. 79 73.58 ETR"137 36.28 72.56 ETR-133 - 34.37 68.74 ETR-138 36.65 73.30 ETR-113 37.37 74.74 ETR-139 33.87 67.74 ETR-140 36.66 73.32 ETR-141 37.33 74.66 ETR-142 36.20 72.40 ETR-143 37. 64 75.28 ETR-144 36. 94 73.88 ETR-145 41.57 83.14 ETR-146 37. 13 74.26 SUGARY OF NEIGIITED AVERAGE TEHPERATVRES UPPER VOLUHE (DEG. F.) '2.73 LONER VOLUHE (DEG. F.) 73.27 ICE CONDENSER (DEG. F ~ ) 17.55 UPPER VOLUHE (DEG. Rs) 532.43 LOITER VOLUME tDEG. R. ) 532.97 ICE CONDENSER (DEG. R.) 477. 25 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINIIENT PRESSURES DATA CtlECK HILLI- DER POINT VAPOR PRESSVRE UNCORRECTED CORRECTED tlYGROMETER VOLTS (DEG. F. ) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER'- UPPER:
VPU-1 17.60 34.90 0.0995 PU-1 27.0180 26.8313 VPU"2 0.05 32.94 0.0920 PU-2 26.8861 26.8849 LOIIER'- LONER:
VPL"1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.63 36.89 0 '077 PL-2 26.e68e 26.8672 ICE- ICE:
VPI-1 10.50 20.68 0. 0521 PI-1 26.8890 26.8881 VPI"2 -0.97 14.54 0.0387 PI-2 26.9021 26.9008 AMBIENT 14.5108 14.5041 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIN)IENT (PSIA) 0.0957-LONER CONTAINMENT t PSIA) 0.1077 AVERAGE UPPER PRESSVRE (PSIA) 26.8581 ICE CONDENSER (PSIA) 0.0454 AVERAGE LONER PRESSURE (PSIA) 26.8672 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8944 AVERAGE CONTAINMENT PRESSURE t PSIA) 26.8732 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.3691 p g
RUN NUHBER 48 ELAPSED TIHE 23.50 CONTAIttHENT TEHPERATURES DATA CHECK UPPER VOLUME LOWER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F ~
ETR-101 39.87 79.74 ETR-122 35.90 71.80 ETR-115 9.88 19.76 ETR-102 37.83 75.66 ETR-123 36.64 73.28 ETR-116 9. 97 19.94 ETR"103 35.70 71.40 ETR-124 37.27 74.54 ETR-117 9.69 19.38 ETR-104 35. 60 71.20 ETR"125 35.98 71.96 ETR-118 11.15 22.30 ETR"105 36.11 72.22 ETR-126 36.07 72.14 ETR-119 8.24 16.48 ETR-106 36.43 72.86 ETR-127 33.99 67.98 ETR-120 8. 07 16.14 ETR-107 35. 98 71.96 ETR-129 37.20 74.40 ETR-121 8. 27 16.54 ETR-108 36. 02 72.04 ETR-130 35.65 71.30 ETR-109 35.54 71.08 ETR-131 33.95 67.90 ETR-110 35.35 70.70 ETR-132 37.66 75.32 ETR ill ETR-112 35.54 35.59 .
71.08 71.18 ETR-134 ETR-135 36.63'6.49 73 '6 72.98 ETR-114 34.86 69.72 ETR-136 36.58 73.16 ETR-128 36. 79 73.58 ETR-137 36.29 72.58 ETR-133 34. 40 68.80 ETR-138 36.65 73.30 ETR-113 37 36
~ 74.72 ETR"139 33.89 67.78 ETR-140 36.68 73.36 ETR"141 37.34 74.68 ETR-142 36.20 72.40 ETR-143 37.64 75.28 ETR-144 36.94 73.88 ETR-145 41.58 83.16 ETR-146 37.09 74.18 SUHHARY OF WEIGHTED AVERAGE TEMPERATURES UPPER VOLUtlE (DEG. F.) 72.72 LOWER VOLUttE tDEG. F.) 73.26 ICE CONDENSER tDEG. F.) 17.51 UPPER VOLUHE tDEG. R.) 532.42 LOWER VOLUHE tDEG. R.) 532.96 ICE CONDENSER tDEG. R. ) 477.21 CONTAINMENT VAPOR PRESSURE DATA C)IECK CONTAINHENT PRESSURES DATA CHECK HZLLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS (DEG. F. ) tPSZA) HANOHETER READING tPSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17.60 34.90 0.0995 PU-1 27.0210 26.8342 VPU-2 0 F 05 32.95 0.0921 PU-2 26.8890 26.8878 LONER: LOWER:
VPL-1 19.84 39.30 0.1184 PL-1 0.0 0.0 VPL"2 18.65 36.93 0.1078 PL-2 26.8717 26.8701 ICE-'PI-1 ZCE:
8.74 17. 19 0.0440 PZ "1 26.8926 26.8917 VPI-2 -0.92 15.44 0.0404 PZ-2 26.9058 26.9045 AHBIEN) 14.5147 14.5080 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0. 0958 LONER CONTAINttENT (PSIA) 0.1131 AVERAGE UPPER PRESSURE tPSIA) 26.8610 .
ICE CONDENSER (PSZA) 0.0422 AVERAGE LOtlER PRESSURE (PSIA) 26.8701 AVERAGE ICE COttDENSER PRESSURE tPSIA) 26.8981 AVERAGE CONTAINMENT PRESSURE t PSIA) 26.8764 AVERAGE CONTAINHEttT PRESSURE (PSIG) 12.3684
.:0
RUN NUMBER 49 ELAPSED TIME 24.00 CONTAINMENT TEHPERATURES DATA CHECK UPPER VOLUME lOWER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 39. 86 79.72 ETR"122 35. 93 71.86 ETR-115 10. 05 20. 10 ETR-102 37.81 75.62 ETR-123 36.62 73.24 ETR"116 10.00 20.00 ETR-103 35.70 71 '0 ETR-124 37.26 '4.52 ETR-117 9.59 19.18 ETR-104 35.62 71.24 ETR"125 36.01 72. 02 ETR-118 10.81 21.62 ETR-105 36.10 72.20 ETR-126 36. 08 72.16 ETR"119 8.25 16.50 ETR-106 36.43 72.86 ETR-127 33 '6 67. 92 ETR-120 8. 08 16. 16 ETR-107 35.98 71.96 ETR-129 37.18 74.36 ETR-121 8.32 16. 64 ETR-108 36.03 72.06 ETR-130 35.65 71.30 ETR-109 35.60 71.20 ETR"131 33.94 67.88 ETR-110 35.43 70.86 ETR-132 37.66 75.32 ETR-ill 35.56 71.12 ETR-134 36.60 73.20 ETR-112 35.60 71.20 ETR-135 36.56 73.12 ETR-114 ETR-128 34.84 69. 68 73.60 ETR-136 ETR-137 36 '5 36.26 73.10 72.52
- 36 80 F
ETR-133 34.38 68.76 ETR-138 36.64 73.28 ETR-113 37 37 74.74 ETR-139 33.87 67.74 ETR-140 36.68 73.36 ETR-141 37.33 74.66 ETR-142 36.20 72.40 ETR-143 37.64 75.28 ETR"144 36.94 73.88 ETR-145 41.56 83.12 ETR-146 37.12 74.24 SU(MARY OF WEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 72.72 LOWER VOLUME (DEG. F.) 73.25 ICE CONDENSER (DEG. Fo) 17.51 UPPER VOLUME (DEG. R.) 532.42 LOWER VOLUME (DEG. R.) 532.95 ICE CONDENSER (DEG. R. ) 47>.2l CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAIt(MENT PRESSURES DATA CHECK HILLI- DEN POIt(T VAPOR PRESSURE Ut(CORRECTED CORRECTED IIYGROMETER VOLTS (DEG. F.) (PSIA) t(ANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 17.50 34.70 0.0987 PU-1 27.0200 26.8332 VPU-2 0 F 05 32.81 0.0915 PU-2 26.8890 26.8878 LOWER'- LOWER:
VPL-1 19. 91 39.44 0.1190 PL"1 0.0 0.0 VPL-2 18.65 36. 93 0.1078 PL-2 26.8715 26.8699 ICE: ICE:
VPI-1 9.09 17.89 0.0456 PI-1 26.8922 26.8913 VPI-2 -0.95 14.90 0.0394 PI-2 26.9057 26.9044 At(DIENT 14.5089 14.5022 AVERAGE VAPOR PRESSURES SUt%(ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0951 LOWER CONTAINMENT (PSIA) 0.1134 AVERAGE UPPER PRESSURE (PSIA) 26.8605 ICE COt(DENSER (PSIA) 0.0425 AVERAGE LOWER PRESSURE (PSIA) 26.8699 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8978 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8761 AVERAGE CONTAINtIENT PRESSURE (PSIG) 12.3738 Oy ,~
RUN NU((BER 50 ELAPSED TIHE 24.50 CONIAINHENT 'TEMPERATURES DATA CIIECK UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD t tILLI-VOLTS DEG. F.
ETR-101 39.85 79.70 ETR-122 35. 93 71.86 ETR-115 10.22 20 44 ETR-102 37. 79 75.58 ETR-123 36.63 73.26 ETR-116 9.98 19.96 ETR-103 35. 70 71.40 ETR-124 37.28 74.56 ETR-117 9. 72 19.44 ETR-104 ETR-105
35. 61
36. 08 71.22 72.16 ETR-125 ETR-126 36.02 36.08 72.04 72.16.
ETR-118 10 '0 8.26 21.80 ETR-119 16.52 ETR-106 36.40 72.80 ETR-127 33.96 67.92 ETR"120 8.10 '16. 20 ETR-107 35.99 71.98 ETR-129 '7. 17 74 '4 ETR-121 8.36 16.72 ETR-108 36. 02 72.04 ETR-130 35.65 71.30 ETR "109 35.54 71.08 ETR-131 33.96 67.92 ETR-110 35.45 70. 90 ETR-132 37.65 75.30 ETR"ill 35.57 71.14 ETR-134 36.66 73.32 ETR-112 35. 60 71.20 ETR"135 36,59 73.18 ETR"114 34.81 69.62 ETR-136 36.59 73.10 ETR-128 36. 79 73.58 ETR-137 36.27 72.54 ETR-133 34. 39 68.78 ETR-138 36.64 73.28 ETR-113 37.35 74.70 ETR-139 33.87 67.74 ETR-140 36.67 73.34 ETR"141 37.35 74.70 ETR-142 36.21 72.42 ETR-143 37.64 75.28 ETR-144 36.95 73.90 ETR-145 41.58 83.16 ETR"146 37.12 74.24, SUHMARY OF MEIGHTED AVERAGE TEHPERATURES UPPER VOLUME (DEG. F.) 72.69 LONER VOLUME tDEG. F.) 73.28 ICE CONDENSER (DEG. F.) 17. 60 UPPER VOLUME tDEG. R.) 532.39 LOHER VOLUHE (DEG. R.) 532.98 ICE CONDENSER (DEG. R.) 477.30 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK HILLZ- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F.) (PSIA) HANOMETER READING ( PSIA ) READIt(G ( PSIA)
UPPER: UPPER:
VPU"1 17e54 34.78 0.0990 PU-1 27.0200 26.8332 VPU"2 0.04 32o79 0.0915 PU-2 26.8879 26.8867 LO( (ER-'PL"1 LO)(ER:
0.0 -0.01 0.0 PL"1 0.0 0.0 VPL-2 18.65 36.93 0.1078 PL-2 26.8706 26.8690 ICE: ICE:
VPZ-1 9.34 18.40 0.0467 PI-1 26.8907 26.8898 VPZ-2 . -0.94 15.08 0.0397 PI-2 26.9047 26.9034 A)(BIENT 14.5045 14.4978 AVERAGE VAPOR PRESSURES
SUMMARY
OF CORRECTED AVERAGE PRESSURES UPPER CONl'AINHENT (PSIA) 0.0952 LONER CONTAINHENT t PSIA) 0. 1078 AVERAGE UPPER PRESSURE tPSIA) 26.8600 ICE CONDENSER (PSIA) 0.0432 AVERAGE LOt'(ER PRESSURE (PSIA) 26.8690 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8966 AVERAGE COklTAI((MENT PRESSURE (PSIA) 26.8752, AVERAGE CONTAIN((ENT PRESSURE (PSIG) 12.3774
/
/~pe)
RUN ttUHBER 51 ELAPSED TIHE 25.00 CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUME ICE CONDENSER RTD HI LLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F~ RTD HILLI-VOLTS DEG. F.
ETR-101 39. 86 79.72 ETR-122 35.91 71.82 ETR-115 10.16 20.32 ETR-102 37.77 75.54 ETR-123 36.64 73.28 ETR-116 9. 98 19.96 ETR-103 35.71 71.42 ETR-124 37.26 74.52 ETR-117 9. 62 19.24 ETR-104 35. 64 71.28 ETR-125 35.97 71.94 ETR-118 10. 93 21.86 ETR-105 36. 08 7Z.16 ETR"126 36.08 72.16 ETR-i19 8.27 16.54 ETR-106 36.40 72.80 ETR-127 33.95 67.90 ETR-120 8. 12 16.24 ETR-107 35. 98 71. 96 ETR-129 37.18 74.36 ETR-121 8.43 16.86 ETR-108 35. 98 71. 96 ETR-130 35.66 71.32 ETR-109 35.56 71. 12 ETR-131 33.96 67.92 ETR-110 35.43 70. 86 ETR-132 37 '6 75.32 ETR"ill 35.56 71.12 ETR-134 36.65 73.30 ETR-112 35.58 71.16 ETR-135 36.59 73.18 ETR-114 34.81 69 '2 ETR-136 36.62 73.24 ETR" 128 36. 80 73.60 ETR-137 36.28 72.56 ETR-133 34. 39 68.78 ETR-138 36.63 73.26 ETR-113 37.33 74.66 ETR-139 33.89 67.78 ETR-14io 36.67 73.34 ETR 141 37.36 74.72 ETR"142 36.22 72.44 ETR-143 37.64 75.28 ETR"144 36.96 73.92 ETR-145 41.59 83.18 ETR-146 37. 14 74.28 SUHHARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 72.68 LONER VOLUHE tDEG. F.) 73.29 ICE CONDENSER tDEG. F.) 17.62 UPPER VOLUHE (DEG. R.) 532.38 LONER VOLUHE tDEG. R.) 532.99 ICE CONDENSER tDEG. R.) 477.32 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- OEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED IlYGROHETER VOLTS (DEG. F.) [PSIA) HANOHETER READING t PSIA) READING <PSIA)
UPPER: UPPER:
VPU-1 17.49 34. 68 0.0986 PU-1 27. 0180 26.8313 VPU-2 0.0 32.00 0.0 PU"2 ~
26.8858 26.884i6 LONERi LOtlER:
VPL-1 0.0 "0.01 0.0 PL-1 0.0 0.0 VPL-2 18.67 36.97 0.1080 PL-2 26.8686 26.8670 ICE ICE i
'PI-1 9.29 18. 29 0.0465 PI-1 26.8887 26.8878 VPI-2 -0.95 14.90 0.0394 PI-2 26.9026 26.9013 AHBIENT 14.5050 14 4984 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIttHENT (PSIA) 0.0986 LONER CONTAINHENT (PSIA) 0.1080 AVERAGE UPPER PRESSURE (PSIA) 26.8579 ICE CONDENSER (PSIA) 0.0429 AVERAGE LOl'tER PRESSURE tPSIA) 26.8670 AVERAGE ICE CONDENSER PRESSURE tPSIA) 26.894i5 AVERAGE COtffAINHENT PRESSURE t PSIA) Z6.8731 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.3748 i
il((<<('Utt RUBBER 52 ELAPSED TIME 25.50 CONTAIt04ENT TEMPERATURES DATA CIIECK UPPER VOLUME LOWER VOLUME ICE COttDENSER RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F ~ RTD HILLI-VOLTS DEG. F.
ETR-101 39.84 79.68 ETR-122 35.91 71.82 ETR-115 9.86 19. 72 ETR-102 37.76 75.52 ETR-123 36.67 73.34 ETR-116 9.80 19.60 ETR-103 35. 67 71.34 ETR-1Z4 37. 21 74.42 ETR-117 9.31 18.62 ETR-104 35. 61 71. 22 ETR-125 36. 03 72.06 ETR-118 10. 67 21.34 ETR-105 36.06 72. 12 ETR-126 36.08 72.16 ETR-119 8.27 16.54 ETR-106 36. 38 72.76 ETR-127 33.95 67.90 ETR-120 8.15 16.30 ETR-107 35. 93 71.86 ETR-129 37.14 74.28 ETR-121 8. 35 16.70 ETR"108 35 98
~ 71.96 ETR"130 35.66 71.32 ETR-109 35. 60 71. 20 ETR-131 33.96 67.92 ETR"110 35.41 70.82 ETR-132 37. 66 75.32 ETR-ill 35.56 71.12 ETR-134 36.65 73.30 ETR-112 35.56 71. 12 ETR-135 36.58 73.16 ETR-114 34.79 69.58 ETR-136 36.60 73.20 ETR-128 36. 79 73.58 ETR-137 36.27 72.54 ETR" 133 34.38 68. 76 ETR-138 36.64 73.28 ETR-113 37.33 74. 66 ETR"139 33.87 67.74 ETR-140 36.68 73.36 ETR"141 37.36 74.72 ETR-142 36.22 72.44 ETR"143 3'7. 64 75.28 ETR-144 36.95 73.90 ETR-145 41.59 83.18 ETR "146 37. 11 74.22 SWARY OF WEIGI)TED AVERAGE TEHPERATURES UPPER VOLUME tDEG. F.) 72.65 LOtlER VOLUttE tDEG. F.) 73.28 ICE CONDENSER tDEG. F.) 17.46 UPPER VOLUME tDEG. R.) 532.35 LOWER VOLUME tDEG. R.) 532.98 ICE CONDENSER tDEG. R.) 477.16 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINtlENT PRESSURES DATlt CHECK HILLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS tDEG. F.) tPSIA) HAttOHETER READING tPSIA) READING tPSIA)
UPPER- UPPER:
VPU-1 17.58 34.86 0.0993 PU-1 27.0180 26.8313 VPU-2 -0. 21 28. 22 0.0 PU-2 26.8862 26.8850 LOWERt LONER:
VPL-1 0.0 "0.01 0.0 PL-1 0.0 0.0 VPL-2 18.67 36.97 0.1080 PL-2 26.8690 26.8674 ICE'PI"1 ICE:
9.58 18.86 0.0477 PI-1 26.8891 26.8882'6.
VPI-2 -0. 94 15.08 0.0397 PI-2 26.9030 9017 AHBIEtfT 14.4967 14.4901 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT t PSIA) 0.0993 LOWER CONTAIt0)ENT t PSIA) 0.1080 AVERAGE UPPER PRESSURE tPSIA) 26.8581 ICE CONDEttSER t PSIA) 0.0437 AVERAGE LOttER PRESSURE tPSIA) 26.8674 AVERAGE ICE CONDENSER PRESSURE OPSIA) 26.8949 AVERAGE CONTAINtlEtff PRESSURE t PSIA) 26.8735 AVERAGE CONTAINttENT PRESSURE (PSIG) 12.3833
(
p v'jg r
RUN NUt%ER 53 ELAPSED TIHE 26.00 CONTAIttMENT TEMPERATURES DATA CHECK UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD HILLI "VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 39.83 79.66 ETR-122 35.92 71.84 ETR-115 9.54 19. 08 ETR-102 37.74 75.48 ETR-123 36.69 73.38 ETR-116 9.54 19. 08 ETR-103 35.67 71.34 ETR-124 37.24 74.48 ETR-117 9.19 18.38 ETR-104 35. 62 71.24 ETR-125 36.00 72.00 ETR-118 11.15 22.30 ETR-105 36.07 72. 14 ETR-126 36.09 72.18 ETR-119 8.28 16.56 ETR-106 36. 38 72.76 ETR-127 33 '5 37.16 67.90 74.32 ETR-120 ETR-121 8.12 8.41 16.24 16.82 ETR-107 35. 98 71.96 E.TR-129 ETR-108 35. 95 71.90 ETR-130 35.65 71.30 ETR-109 35. 60 71.20 ETR-131 33.94 67.88 ETR-110 35.45 70.90 ETR-132 37.67 75.34 ETR-ill 35.55 71. 10 ETR-134 36.61 73.22 ETR"112 35.58 71. 16 ETR-135 36.54 73.08 ETR-114 34.87 69.74 ETR-136 36.59 73.18 ETR-128 36.83 73.66 ETR"137 36.27 72.54 ETR-133 34.39 68.78 ETR-138 36.64 73.20 ETR-113 37.33 74.66 ETR-139 33.90 67.80 ETR-140 36.69 73.38 ETR-141 3?.35 74.70 ETR-142 36.22 72.44 ETR-143 37.64 75.28 ETR"144 36.95 73.90 ETR-145 41.58 83.16 ETR-146 37. 14 74.28
SUMMARY
OF NEIGtlTED AVERAGE TEMPERATURES UPPER VOLUHE tDEG. F. ) 72.67 LONER VOLUME (DEG. F. ) 73.27 ICE CONDENSER tDEG. F.) 17.43 UPPER VOLUME (DEG. R.) 532.37 LO)IER VOLUHE tDEG. R.) 532.97 ICE CONDEt)SER tDEG. R.) 477.13 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK r
HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS [DEG. F.) {PSIA) HANOHETER READING (PSIA) READIttG (PSIA)
UPPER'- UPPER:
VPU"1 17.53 34.76 0.0989 PU-1 27 . 0130 26.8263 VPU-2 -0+20 28.40 0.0 PU-2 Z6.8815 26.8803 LOttER: LONER:
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.65 36.93 0. 1078 PL-2 26.8639 26.8623 ICE- ICE:
VPI-1 8.27 16.27 0.0421 PI-1 26.8830 VPI-2 -1.10 12.20 0.0345 PI-2 26.8971 AHDIENT 14.4901 AVERAGE VAPOR PRESSURES SUMttARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAItNENT (PSIA) 0.0989 LONER CONTAINMENT (PSIA) 0.1078 AVERAGE UPPER PRESSURE tPSIA) 26.8533 ICE CONDENSER (PSIA) 0.0383 AVERAGE LOtlER PRESSURE (PSIA) 26.8623 AVERAGE ICE COWDEttSER PRESSURE OPSIA) 26.8900 AVERAGE CONTAIttMEWT PRESSURE t PSIA) 26.8685 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3784
RUN NU)(DER 55 ELAPSED TINE 27.00 CONTAINMENT TEHPERATllRES DATA CIIECK UPPER VOLUHE LOWER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F~ RTD HILLI-VOLTS DEG. F.
ETR-101 39.82 79.64 ETR-122 35.88 71.76 ETR-115 9. 20 18.40 ETR" 102 37. 72 75.44 ETR-123 36.66 73.32 ETR-116 9. 08 18.16 ETR-103 35.67 71.34 ETR-124 37.23 74.46 ETR-117 8.67 17.34 ETR-104 ETR"105
35. 61 36.07
71. 22 72.14 ETR-125 ETR-126 35.99 36.08 71.98 72.16 ETR-118 10.33 20 '6 ETR-119 8. 30 16.60 ETR-106 36.36 72.72 ETR"127 33.97 67.94 ETR-120 8. 09 16.18 ETR-107 35. 96 71. 92 ETR-129 37.17 74.34 ETR-121 8. 39 16.78 ETR-108 35. 95 71.90 ETR-130 35.65 71.30 ETR-109 35.57 71.14 ETR-131 33.96 67.92 ETR"110 35.37 70.74 ETR-132 37.65 75.30 ETR-ill 35. 54 71.08 ETR"134 36.75 73.50 ETR-112 35.55 71.10 ETR-135 36.61 73.22 ETR"114 34.86 69.72 ETR-136 36.59 73.18 ETR-128 36.86 73.72 ETR-137 36.30 72.60 ETR-133 34. 38 68.76 ETR-138 36.63 73.26 ETR-113 37.30 74.60 ETR-139 33.92 67.84 ETR-140 36.70 73.40 ETR-141 37.36 74.72 ETR-142 36.22 72.44 ETR-143 37.64 75.28 ETR-144 36.95 73.90 ETR-145 41.58 83.16 ETR-146 37.14 74.28 SUHMARY OF WEIGHTED AVERAGE TEt(PERATURES UPPER VOLUME (DEG. F.) 72.64 LOWER VOLUHE (DEG. F ~ ) 73.31 ICE CONDENSER (DEG. F.) 17.11 UPPER VOLUME (DEG. R. ) 532.34 LOWER VOLUME (DEG. R. ) 533.01 ICE CONDEttSER (DEG. R. ) 4?6.81 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK HILLI- DEW POIt(T VAPOR PRESSURE UNCORRECTED CORRFCTED HYGROMETER VOLTS (DEG. F.) (PSIA) HANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER VPU-1 16.63 32.96 0-0921 PU-1 27.0090 26.8223 VPU-2 -0.16 29.12 0.0 PU-2 26.8777 26.8765 LOWER: LOWER:
VPL-1 0.0 .-0.01 0.0 PL-1 0.0 0.0 VPL-2 ICE-
18. 66 36 '5 0.1079 PL-2 ICE:
26.8600 26.8584 VPI-1 8.68 17. 09 0.0438 PI-1 26.8799 26.8790 VPI-2 -1.07 12. 74 0.0354 PI-2 26.8960 26.8947 AtteIENT 14.4890 14.4825 AVERAGE VAPOR PRESSURES
SUMMARY
OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0921 l.OWER CONTAINMENT t PSIA) 0.1079 AVERAGE UPPER PRESSURE (PSIA) 26.8494 ICE CONDENSER t PSIA) 0.0396 AVERAGE LOIIER PRESSURE (PSIA) 26.8584 AYERAGE IGE coNDENsER pREssURE tpsIA) 26.8868 AVERAGE CONTAINMENT PRESSURE I PSIA) 26.8649 AVERAGE CONTAINMENT PRESSURE I PSIG) 12.3824
)
/(Ag Vg RUN NUt(BER 56 ELAPSED TIttE 27.50 CONTAINHENT TEMPERATURES DATA C(IECK UPPER VOLWE LO('IER VOLWE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR"101 39.82 79. 64 ETR-122 " 35.90 71.80 ETR-115 9.54 19.08 ETR-102 37. 71 75.42 ETR-123 36.69 73.38 ETR" 116 9. 23 18.46 ETR-103 35. 67 71.34 ETR-124 37.25 74.50 ETR-117 8.80 17.60 ETR-104 35. 62 71. 24 ETR-125 36.00 72.00 ETR-118 10. 01 20.02 ETR-105 36. 07 72. 14 ETR-126 36.08 72.16 ETR-119 8.31 16.62 ETR-106 36. 36 72. 72 ETR-127 33.93 67.86 ETR-120 8. 12 16.24 ETR-107 35. 94 71.88 ETR-129 37. 19 74.38 ETR-121 8.44 16 88 F
ETR-108 35.91 71.82 ETR-130 35. 65 71.30 ETR-109 35. 60 71 '0 ETR-131 33 '4 67.88 ETR-110 35.35 70.70 ETR-132 . 37.66 75.32 ETR-ill 35.55 71. 10 ETR"134 36.60 73.20 ETR-112 35.57 71. 14 ETR-135 36.59 73.18 ETR-114 34.86 69.72 ETR-136 36.54 73.08 ETR-128 36.85 73.70 ETR-137 36.26 72.52 ETR-133 34. 39 68.78 ETR-138 36.65 73.30 ETR-113 37.31 74.62 ETR-139 33.90 67.80 ETR-140 36.71 73.42 ETR-141 37.36 74.72 ETR"142 36. 23 72.46 ETR-143 37. 64 75.28 ETR-144 36. 95 73.90 ETR-145 41.58 83.16 ETR-146 37. 11 74.22 SUMHARY OF WEIGHTED AVERAGE TEHPERATlJRES UPPER VOLVO)E (DEG. F.) 72.63 LONER VOLUHE (DEG. F.) 73.26 ICE COttDENSER (DEG. F.) 17.20 UPPER VOLUHE (DEG. R.) 532.33 LOI(ER VOLWE (DEG. R.) 532.96 )ICE CONDENSER (DEG. R.) 476.90 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CtlECK P
HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED I(YGROMETER VOLTS (DEG. F. ) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER0 VPU"1 16.'77 33.24 0.0931 PU-1 27.0130 26.8263 VPU-2 "0.14 29.48 0.0 PU-2 26.8810 26.8798 LONER: LO)(ER(
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL"2 18.52 36.67 0 '067 PL-2 26.8635 26.8619 ICE: ICE:
VPI-1 9.16 18.04 0.0459 PI-1 26.8835 26.8826 VPI"2 -1.23 9.86 0.0307 PI-2 26.8995 26.8982 AMBIENT 14,4832 14.4767 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINt(ENT (PSIA) 0.0931 LONER CONTAINHENT (PSIA) 0.1067 AVERAGE UPPER PRESSURE (PSIA) 26.8530 ICE CONDENSER (PSIA) 0.0383 AVERAGE LONER PRESSURE (PSIA) 26.8619 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8904 AVERAGE COt(TAIttt(ENT PRESSURE (PSIA) 26.8684 AVERAGE COt(TAINl(ENT PRESSURE (PSIG) 12.3917
,>> :~
(Q RUN NUMBER 57 ELAPSED TIHE 28.00 COt(TAINHENT TEHPERATURES DATA Cl(ECK UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI "VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 39. 79 79.58 ETR-122 35.91 71.82 ETR-115 9.47 18.94 ETR-102 37. 70 75.40 ETR-123 36.65 73.30 ETR"116 '.21 18.42 ETR-103 35. 68 71.36 ETR-124 37.27 74.54 ETR-117 8.87 17.74 ETR-104 35. 62 71 ~ 24 ETR-125 36.01 72.02 ETR-118 10.09 20.18 ETR-105 36.04 72.08 ETR-126 36.07 72.14 ETR-119 8.31 16.6Z ETR "106 36.35 72. 70 ETR"127 33.95 67.90 ETR-120 8. 07 16.14 ET(t-107 35. 94. 71.88 ETR-129 37.17 74.34 ETR"121 8.41 16.82 ETR-108 35.95 71.90 ETR-130 35.65 71.30 ETR-109 35.53 71.06 ETR-131 33.94 67.88 ETR-110 35. 37 70.74 ETR"132 37.65 75.30 ETR-Ill 35.56 71.12 ETR-134 36.61 73.22 ETR-112 35.60 71.20 ETR-135 36.56 73.12 ETR-114 34.83 69.66 ETR-136 36.56 73.12 ETR-128 36. 84 73.68 ETR-137 36.27 72.54 ETR-133, 34.39 68.78 ETR-138 36.64 73.28 ETR"113 37.25 74.50 ETR-139 33.89 67.78 ETR-140 36.69 73.38 ETR-141 37. 36 74.72 ETR-142 36.23 72.46 ETR-143 37. 63 75.26 ETR-144 36. 96 73.92 ETR-145 41.58 83.16 ETR-146 37. 13 74.26 SUHMARY OF t(EIGHTED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F.) '72.61 LOHER VOLUt(E (DEG. F. ) 73.26 ICE COt(DENSER (DEG. F. ) 17. 17 UPPER VOLUME (DEG. R. ) 532.31 LONER VOLUt(E (DEG. R. ) 532.96 ICE CONDENSER (DEG. R. ) 476.87 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CllECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F. ) (PSIA) t(ANOHETER READING (PSIA) READING (PSIA)
UPPER'- I UPPER:
VPU-1 16;71 33.12 0.0927 PU-1 27. 0210 26.8342 VPU"2 "0.12 29.84 0.0 PU"2 26.8795 26.8783 LOt(ER: LONER:
VPL-1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.53 36.69 0.1068 PL-2 26 '620 26.8604 ICE: ICE:
VPI-1 8.70 17.11 0.0439 PI-1 26.8820 26.8811 VPI-2 -1.20 '10.40 0.0315 PI-2 26.8982 26.8969 At(DIENT 14.4851 14.4786 AVERAGE VAPOR PRESSURES SUt(MARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMEt(T (PSIA) 0.0927 LONER CONTAINMEtff (PSIA) 0.1068 AVERAGE UPPER PRESSURE (PSIA) 26.8563 ICE CONDENSER (PSIA) 0.0377 AVERAGE LONER PRESSURE (PSIA) 26.8604 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8890 AVERAGE COt(TAINHENT PRESSURE (PSIA) 26.8685 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3899
RUN NUtIDER 58 ELAPSED TIME 20.50 COtlTAINtIENT TEMPERATURES DATA CHECK UPPER VOLUtIE LONER VOLUME ICE COtIDENSER RTO tIILLI "VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 39.81 79.62 ETR-122 35.92 71.84 ETR-115 9.34 18.60 ETR-102 37.68 75.36 ETR-123 36.66 73.32 ETR-116 9.28 10.56 ETR-103 35. 64 71.28 ETR-124 37.27 74.54 ETR-117 8.87 17.74 ETR-104 35.59 71. 10 ETR-125 36.03 72.06 ETR-110 10. 09 20.18 ETR" 105 36. 01 72.02 ETR-126 36.00 72. 16 ETR-119 0.31 16.62 ETR-106 36. 35 72.70 ETR-127 33.96 67.92 ETR-120 8.12 16. 24 ETR-107 35. 90 71.80 ETR-129 37.17 74.34 ETR-121 8.46 16.92 ETR-108 35.92 71.84 ETR-130 35.65 71.30 ETR-109 35. 63 71.26 ETR"131 33.95 67.90 ETR-110 35.4Z 70.84 ETR-132 37. 64 75.20 ETR-ill 35.54 71.08 ETR-134 36. 63 73.26 ETR-112 35.56 ?1.12 ETR-135 36.56 73.12 ETR-114 34.86 69. 72 ETR-136 36.56 73.12 ETR-128 36.87 73.74 ETR-137 36 '6 72.52 ETR-133 34. 38 68.76 ETR-138 36.66 73.32 ETR-113 37.33 74.66 ETR-139 33.89 67. 78 ETR-140 36.70 73.40 ETR-141 37. 37 74.74 ETR-142 36.23 72.46 ETR-143 37.63 75.26 ETR-144 36. 96 73.92 ETR-145 41.50 83.16 ETR-146 37. 15 74.30 SUHHARY OF WEIGHTED AVERAGE TEMPERATURES UPPER VOLUME IDEG. F.) 72.60 LOWER VOLUHE (DEG. F.) '3.27 ICE CONDENSER (DEG. F.) 17. 21 UPPER VOLUME (DEG. R.) 532.30 LOWER VOLUME (DEG. R.) 532.97 ICE CONDEttSER (DEG. R. ) 476. 91 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CIIECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROHETER ~ VOLTS (DEG. F.) IPSIA) MANOMETER READING I PSIA) READING I PSIA)
UPPERS UPPER:
VPU-1 16:77 33.24 0.0931 PU-1 27.0170 26.0303 VPU-2 -0.10 30.20 0.0 PU-2 26.0786 26.8774 LOWER:
LOWER'PL"1 0.0 -0.01 0.0 PL-1 0.0 0.0 VPL-2 18.54 36.71 0.1069 PL-2 26.8611 26.0595 ICE'PI-1 ICE:
9. 27 18.26 0.0464 PI-1 26.8011 26.8802 VPI-2 -1.10 12.20 0.0345 PI-2 26.0976 26.096'3 AMBIENT 14.4851 14.4786 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT I PSIA) 0.0931 LOWER CONTAIQIENT I PSIA) 0.1069 AVERAGE UPPER PRESSURE (PSIA) 26.8538, ICE CONDENSER (PSIA) 0.0404 AVERAGE LOWER PRESSURE I PSIA) 26.8595 AVERAGE ICE COIIDENSER PRESSURE IPSIA) 26.8882 AVERAGE CONTAIMIENT PRESSURE IPSIA) 26.8672 AVERAGE COWTAINMEtIT PRESSURE IPSIG) 12.3886
Qi";
RUN ttUtRER 59 ELAPSED TINE 29.00 CONTAINHEt)T TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD t 1ILLI "VOLTS DEG. F. RTD HILLI-VOLTS DEG'. RTD WILLI-VOLTS DEG. F.
ETR-101 39. 77 79.54 ETR"122 35.96 71.92 ETR"115 9.36 18.72 ETR-102 37.68 75.36 ETR"123 36.66 73.32 ETR"116 9.39 18.78 ETR-103 35. 64 71. 28 ETR-124 37.26 74.52 ETR-117 8.08 17.76 ETR-104 35.58 71.16 ETR-125 35.99 71. 98 ETR-118 10. 22 20.44 ETR-105 36. 02 72.04 ETR-126 36.09 72.18 ETR-119 8.32 16 64 ETR-106 36.34 72.68 ETR-127 33.92 67.84 ETR-120 8. 10 16.20 ETR-107 35.90 71.80 ETR-129 37.17 74.34 ETR-121 8.47 16.94 ETR-108 35. 93 71.86 ETR-130 35.65 71.30 ETR-109 35.57 71.14 ETR"131 33.95 67.90 ETR"110 35.46 70.92 ETR"132 37.66 75.32 ETR-111 35.54 71.08 ETR-134 36.63 73.26 ETR-112 35.58 71.16 ETR-135 36.53 73.06 ETR-114 34.82 69. 64 ETR-136 36.59 73.18 ETR-128 36.85 73.70 ETR-137 36.23 72.46 ETR-133 34.38 68.76 ETR-138 36.66 73 '2 ETR-113 37.25 74.50 ETR-139 33.91 67.82 ETR-140 36.70 73.40 ETR-141 37.36 74.72 ETR-142 36.24 72.48 ETR-143 37.63 75.26 ETR-144 36.96 73.92 ETR-145 .41.61 83.22 ETR-146 37.11 74.22 SUHHARY OF WEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.58 LOUR VOLUtlE [DEG. F. ) 73.26 ICE COttDENSER (DEG. F. ) I7.24 UPPER VOLUHE tDEG. R.f 532.28 LOWER VOLUttE (DEG. R.) 532.96 ICE CONDENSER (DEG. R.) 476.94 CONTAINHENT VAPOR PRESSURE DATA CHECK COttTAINHENT PRESSURES DATA CI)ECK HILLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGRO)1ETER VOLTS [DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.73 33.16 0.0928 PU-1 27.0180 26.8313 VPU-2 -0.11 30.02 0.0 PU-2 26.8790 26.8778 LONER: LONER)
VPL-1 0.0 -0.01 0.0 PL"1 0.0 0.0 VPL-2 18.55 36. 73 0.1070 PL-2 26.8614 26.8598 ICE- ICE:
VPI-1 10.39 20.47 0.0516 PI-1 26.8820 26.8811 VPI-2 -0.97 14.54 0.0387 PI-2 26.8980 26.8967 AHBIEttT 14.4832 14.4767 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0928 LOWER CONTAINttENT (PSIA) 0.1070 AVERAGE UPPER PRESSURE (PSIA) 26.8545 ICE CONDENSER (PSIA) 0 '451 AVERAGE LOWER PRESSURE (PSIA) 26.8598 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8889 AVERAGE CONTAIttt4ENT PRESSURE (PSIA) 26.8677 AVERAGE CONTAIN)Et)T PRESSURE (PSIG) 12.3910 0)
tQ RUN NUt&ER 6D ELAPSED TIHE 29.50 CONTAIt(MENT TEMPERATURES DATA CIIECK UPPER VOLUtfE LOWER VOLUME ICE CONDENSER RTD MILLI "VOLTS DEG. F. RTD MI(.LI"VOLTS DEG. F. RTD, HILLI "VOLTS DEG. F.
ETR" 101 39.?5 79.50 ETR-122 35.93 71.86 ETR-115 9. 27 18.54 ETR-102 37. 67 75.34 ETR-123 36.64 73.28 ETR-116 9.26 18.52 ETR-103 35. 67 71.34 ETR"124 3?.28 74.56 ETR-117 8.99 17.98 ETR-104 35.59 71.18 ETR-125 36.01 72.02 ETR-118 11.24 22.48 ETR-105 36.06 72.12 ETR-126 36.08 72.16 ETR-119 8.33 16.66 ETR-106 36.33 72.66 ETR-127 33 '3 67.86 ETR-120 8. 07 16.14 ETR-107 35. 92 71.84 ETR-129 37.17 74.34 ETR-121 8.46 16.92 ETR-108 35.88 71.76 ETR"130 35.66 71.32 ETR-109 35.57 71.14 ETR-131 33.94 67.88 ETR-110 35.40 70.80 ETR-132 37.65 75.30 ETR-111 35.55 71.10 ETR"134 36.64 73.28
'ETR-112 35.56 71. 12 ETR-135 36.54 73.08 ETR-114 34.83 69. 66 ETR-136 36.59 73.18 ETR-128 36.85 73. 70 ETR-137 36.25 72.50 ETR-133 ~ 34.37 68. 74 ETR-138 36.63 73.26 ETR-113 37.33 74.66 ETR-139 33.92 67.84 ETR-140 36.73 73.46 ETR-141 37.38 74.76 ETR-142 36. 24 72.48 ETR-143 37.63 75.26 ETR-144 36. 96 73.92 ETR-145 41.60 83.20 ETR"146 37. 15 74.30 SUHMARY OF WEIGflTED AVERAGE TEtfPERATURES UPPER VOLUME (DEG. F.) 72.59 LOWER VOLUtfE (DEG. F.) 73.27 ICE CONDENSER (DEG. F.) 17.35 UPPER VOLUHE (DEG. R.) 532.29 LOWER VOLUME (DEG. R.) 532.97 ICE COt(DENSER (DEG. R.) 477.05 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED f(YGROHETER VOLTS (DEG. F. ) (PSIA) HANOt(ETER READING (PSIA) READING (PSIA)
UPPER-, UPPER-VPU-1 16.82 33.34 0.0935 PU"1 27. 0150 26.8283 VPU-2 -0.09 30.38 0.0 PU-2 26.8769 26.8757 LOWER: LOtfER-'L-1 VPL-1 0.0 -0.01 0~0 0.0 0.0 VPL-2 18.57 36.77 0.1072 PL-2 26.8549 26.8533 ICE: ICE:
VPI-1 7.00 13.77 0.0372 PI-1 26.8791 26.8782 VPI-2 "1.12 11.84 0 '338 PI-2 26.8962 26.8949 AMBIENT 14.4032 14.4767 AVERAGE VAPOR PRESSURES SUHf(ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0935 LOWER CONTAINtfENT (PSIA) 0. 1072 AVERAGE UPPER PRESSURE (PSIA) 26.8520 ICE CONDENSER (PSIA) 0.0355 AVERAGE LOl'IER PRESSURE (PSIA) 26.8533 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8865 AVERAGE COt(TAINMENT PRESSURE (PSIA) 26.8639 AVERAGE CONTAIt(t(Et(T PRESSURE (PSIG) 12.3872
)
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A.E.F.S.C. - M.EJL 1NSTRUMENTAT10N AND CONTROLS SECTiON ADMINlSTRATIVE 1NSTRUCTlON AND OES1GN PROCEDURE
'NG1NEER!NG'ONTROL PROCEDURE'ONTROLLED DISTRIBUTION FOR F C.P. PACKAGE I'; =. INITIALISSUE
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In order to ccmplete the ILZP two leakage penalty values must be canputed in addition to the As found and As left leakage values. This calculation is divided into three sections:
A Type C penalty for systems which axe not vented during the Type A test B. The As found minus As left penalty for repaired type B & C canponents.
C The overall B and C leaka both As f and As Left.,
C penalty for unvented, systems is generated by applying AEPSC generated guidelines to the "Type C Penalty Form" fran Plant Pxcxmhlxe 12 THP 4030 STP.202. This penalty is based on the As left condition, of the valves listed on the above form.
The As found minus As generated ~lines Left Type to Type B & C ~ty is ~~ated B & C Ccmponents which by applying AEPSC were repaixed during pexfoznance of Plant Raceduxe 2 THP 4030 STP.203.
'lee total type B & C As found. and As left leakages are generated by applying AEPSC generated guidelines to all type B & C ccmponent leakages naasuxed during performance of Plant Pxocedure 12 THP 4030 STP.203.
II. Results:
A. Calculated Values (uncorrected)
Type C Penalty for unvezrted systems 850.0 scan Type B & C As found-As left penalty 34256.7 sccm Mtal type B & C Leakage (As found) 37130.1 sccm Total type B & C Leakage (As left) 3676.8 sccm B. Corrected, Values The glow natexs used for performing the type B & C test are small ball float meters calibrated at 12 psig and 70'F. Due to vm~tions.in izmtnment sizes and nonlinear viscous coma~on factors, a unifozm correction factor is not available.
Calculations (ECP 12-N~7) were performed to show that at 60'F (lowest recorded test tenperatuxe) and 12;5 psig (highest recorded test pxessure) the ccu~ct~on factor 'is less than 2% of the indicated reading;. thexefore, consezvative.corrected values are 102% of the calculated values:
Type C Penalty for unvented systems 867.0 sccm
~
Type B & C Total type type As found-As left penalty B and C Leakage B and C Leakage (As found)
(As left) 34941.8 sccm 37872.7'sccm 3750.3 sccm
Penalt sccm)
g. Test Step 117 Valve R-157 Hote: For this calculation this valve is taken to be in series with valve VCR-20 (Test Step 58)
For two series isolation valves tested separately use the lower leakage rate.
Use lower of 8000.0 or 0.0 0.0
14. Test Step 120,121 Valve ECR-416,417 Valves ECR-416 and ECR-417 are in series. The penalty is computed by using the lower As found minus the lower As left.
Penalty=250.0-0'.0 = 250 sccm 250.0
15. Test Step 4 (type 3) Zone 4 Penetrations Sellows The Zone 4 Penetrations Hellows are not part of the containment pressure boundary;therefore, this leakage is not included in the penalty. 0.0 Total As found - As left Penalty (sccm) 3342 36.
C. Total type 8 Im C As found and As left leaka es.
This calculation applies AEPSC generated guidelines to each Test Step to establish leak rates for both the As found and As left conditions.
As found As left
1. Test Steps 1-6'o indicated leakage 0.0 0.0
2. Test Steps 7,8 Valves MCR-932,933,934,935 No Repairs;therefore, As found=As left Use guideline C.l (Attachment 1)
Use smaller of 280.0 or 0.0 0.0 0;0
3. Test'Steps 9-12 No indicated leakage 0.0 0.0
4. Test Steps 13,14 Valves MCR-904,905,906,907 No repairs;therefore, As found=As left Use guideline C.l (Attachment 1)
Use smaller of 60.0 or 80.0 60.0 60.0
5. Test Steps 15,16 Valves MCR-908,909,910,911 Ho repairs;therefore, As found=As left Use guideline C. 1 (Attachment 1)
Use smaller of 40.0 or 100.0 40.0 40.0
6 Test'teps'7'8 Valves RK 924 / 925 g 926'27 No repairs;therefore, As found=,As left Use guideUz~ C. 1 (Attachment 1)
. Use sInaller of 0.0 or-300.0 0.0 0.0 70 Test Steps 19-28 No indicated leakage 0.0 0.0
8. Test Step 29 Valve VCR-101,201 No repairs;therefore, As found=As left Use gui6~~~m B (Attachment 1)
Leakage =1/3 As. found ~1/3 (225.0) =75 scan 75.0 75.0 I
9. Vest Step 30 Valves VCR-102,202 No repairs;therefore, As found=As left Use guideliIM. B (Attachaant 1)
Leakage ~1/3 As found = 1/3 (360.0)=120.0sccm 120.0 120.0
10. Test Step 31 Valves. VCR-103,203 No repairs;therefore, As found=As left Use guideline B (Attachment 1)
Leakage=l/3 as found =1/3 (1300) = 433.3 sccm 433.3 433.3 Test Step 32'o indicated leakage 0.0 0.0
12. Vest Step 33 Valves VCR-105,205 Valves Repaired Use guise line B As found=l/3 (20000) =6666. 7'can As left=1/3 (80) = 26.7 sccm 6666..7 26. 7
13. Test Step 34 No indicated leakage. 0.0 0.0
14. Vest Step 35 Valves VCR-107',207 No repairs;therefore, As found=As left Use guideline B (Attachment 1)
Use 1/3 As found ~ 1/3 (60) ~ 20 scan 20.0 20.0
15. Test Steps 36-49 No indicated leakage 0.0 0.0
16. Test Step 50 Valve SZ-189 No repair;therefore, As found=As left Single Valve measuzed leakage =30.0 sccm 30.0 30.. 0
17. Vest Step 51 and 124 Valves K&1,ZCR-36 Valves SN-1 and ECR-36 are in series and tested individually. Use guideline E
{Attachment 1) ECR-36 had no indicated leakage. 0.0 0.0 8
'Ql As found As Ieft 18; Test Step 52,86' No indicated leakage for either test step, 0.0 0.0 19; Test Step 53,85 Valves N-159,GCR-301 Valves N-159 and GCR-301 are in series and tested. individually. Use guideline E (Attachment I) GCR-301. had no indicated leakage. 0.0 0.0
20. Test Step 54,88 Valves PM-275, NCR-252 Valves. PM-275 and NRC-252 are in series and tested individually. Use guideline E
.(Attachment I).. NCR-252 had, no indicated leakage. 0.0 0.0
21. Test Step 55 Valve CS-321 *s This is a single isolation valve which ,s required repair. As found = 24000.0 sccm ~ 'I As left = 750.0 sccm 24000.0 750.0
22. Test Steps 56-58 No indicated, leakage 0.0 0,0
23. Test'tep 59,60 Valves OCR-201,203,207,N-160 This configuration represents two sets of two series valves on the same. penetration. Valves OCR-207 and N-160 are in series and, were both repaired. Assume OCR-201 and OCR-203 were tight;therefore, all leakage was through valves OCR-207 and N-160. Use guideline E (Attachment I)
As found is the smaller of 300,0 or 1650.
As left is the smaller of 20.0 or 260.0 300.0 20. 0 F
24. Test Step 61 Valves OCR-610,611 No repair;therefore, As found=As left Use guideline B (Attachment I)
Leakage I/3 As found=l/3 (140.0) ~46.7 scan 46.7 46. 7
25. Test Steps 63,64 hler No indicated leakage 0.0 0.0
26. Test'teps 65,66 Valves qCR-300,301 Valves qCR-300 and gCR-301 are in series and tested individually. Use guideline E
{Attachment I) Valve qCR-300 had no indicated leakage. 0.0 0.0
27. Test Steps 67 No indicated leakage 0.0 0.0 els t
~ 't ~
s S' c,c ~ //~8/i'
As found As 'left
28. Test. Steps 68 Valve ICM-305 This valve was repaired Use guideline 0 (Attachment 1)
As found 1/3 (6000.0) sccm As left. = 1/3 0) sccm 2000.0 0.0
29. Test Step 69 Valve ICM-306 No repairs;therefore, As found=As left Use guideline 0 (Attachment 1)
Leakage=l/3(750.0)=250eQ sccm 250.0 250.0
30. Test Steps 70-78 No indicated leakage 0.0 0.0
31. Test Step 79 Valves ECR-33,35 These valves were repaired Use guideline 8 (Attachment 1)
As found 1/3 (2500.0)
As left=1/3 (1900.0) 833.3 633.3
32. Test Steps 80,81 No indicated leakage 0.0 0.0 33.. Test Step 82 Valves ECR-31,32 These valves were repaired Use guideline 8 (Attachment 1)
As found=l/3 (1300.0) 433.3 416.7 As. left~1/3 (1250.0)
34. Test Step 0.0 83'o indicated leakage 0.0
35. Test Step 84 XCR-102,103 No repairs;therefore, As found As left Use guideline 8 (Attachment 1)
Leakage 1/3 (540.0) = 180.0 sccm 180.0 180.0
36. Test Steps 85,86 Refer to items 18 and 19 ahove
37. Test Steps 87-91 No indicated leakage 0.0 0.0
38. Test Steps 92,93 Valves CCR-455,456,457,CCM-135 The piping associated with these valves forms a safety related closed loop inside containment.
Use guideline C.2 (Attachment 1)
Leakage 0.0 0.0 0.0
39. Test Steps94-100 No indicated leakage 0.0 0.0 10
As found As left
40. Test Step 101 Valve- ICM-251 This valve was repaired Use guideline D (Attachment 1)
As found~I/3 (700.0) = 233.3 sccm 13.3 As left=1/3 (40.0) = 13.3 sccm 233.3'16.
41. Test Step 102 Valve- ICM-250 This valve was repaired Use guideline- D (Attachment 1)
As found. = 1/3 (1850.0) = 616.7 sccm As left =1/3 (50.0) = 16.7 sccm 7 16.7 Test: Step 103-105 No indicated leakage 0.0. 0.0
43. Test Step 106-115 The: valves and piping associated test steps form a safety related with'hese closed loop inside- containment.
Use guideline C.l (Attachment 1) 0.0 0.0
44. Test Step 116 No indic~ted leakage 0.0 '.0,
45. Test Step llT Valve R-15T For this calculation R-157 is considered to be= in series with VCR-20. From Test Step 58, VCR-20 showed no indic~ted leakage. Use guideline E .(Attachment 1)
Leakage ~. 0.0 0.0 0.0 Test Steps 118,119 No indic~ted. Ie~k~ge 0.0 0.0 47; Test Steps 120,121 Valves ECR-416,417'oth of these valves were repaired.
They are in series and tested separately; therefore, use guideline E (Attachment 1)
Use the lower leak rate.
As found = 250.0 sccm As left = 0.0 sccm 250.0 0.0 Test Steps 122,123 Valves ECR-535,536 No repairs;therefore, As found=As left These two valves are in series and tested separately. Use guideline E (Attachment 1).
8oth Valves indicated 20 sccm leakage. 20.0 20.0 11
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I As found As left 49 50.
Test Step 124 Refer to item 17 ~
Test Steps 125,126'alves PCR-40,PA-342 No repairs;therefore, As found=As left
'Ihese valves are in series and tested separately. Use guideline E (Attachment 1) .
Use lower leak. rate. (0.0 scan) 0.0 0.0 51 Test Steps 1 Personnel Airlock No repairs;therefor'e, As found=As left Use guideline F (Attachment 1)
Use 35.0 sccm 35. 0 35.0 52.. Test Steps 2,3 No indicated leakage 0.0 0.0 53., Test Step 4 Zone 4 Penetrations The initial Zone 4 leakage was attrr'laxly&
to Bellows leakage on outside of containaent.
This leakage was not. associated with the contairutent boundary. After isolation of the identified leakage, the measured leakage was 800 scan.. Using. guideline B (Attachment 1) .
The rreasrnmd leakage ~ 1/3 (800) = 266.7 scan left
']Ms is to be used for both As found and leakage.
As 266. 7'66. 7
54. Test Step 5 Fue1 Transfer Tube Flanges No indicated leakage 0.0 0.0
55. Test Step 6 Plant Air Penetration As found and As left 0.0 show no indicated leakage 0.0
56. Test Step 7 Ice Loading Penetration CPN-57 Use guideline B (Attachnant 1)
As found = 1/3 (50.0) ~16.7 scan As left = 1/3 (80.0) = 26.7 scan 16. 7 26.7
57. Test Step 8 Ice Loading Penetration CPN-80 Use guideline B (Attachnent 1)
As found = 1/3 (50) = 16.7 sccm As left = 1/3 (30) = 10.0 scan 16.7 10.0
58. Test Step 9 Flux Thimble Penetration CPM-76 No repair;therefore, As found=As le&
Use guideline B (Attachment 1 )
Leakage = 1/3 (200)=66.7 scan 66. 7 66.7 12
As fmzxl As left
59. Test Steps. 10,11 No indicated leakage 0.0 0.0
60. Test Step 12 Personnel Lock Cover Flange Use indicated leakage As, found=120 scan As left=120 sccm 120.0 120.0 Tota3. As found Type B a C. Leakage 37130.1.
Rrta3. As left. Type B. & C'eakage 3676.8
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OATm~ tune', 1984 susgscTi NRC pppendix J ~Liance Aud t PROilt K,, Far3.cM TOR 1.
2 . S. H.. Steinhart/R F'ering
3. J. G. Feinstein/M. P. Alexich 4., H. G'mith p Jz'.,
This aena is in zesponse to the May 31, 1984 W. G. Smith,Jr. mrna to M P. Alexich. The following constitutes the AEPSC response to the tea items mised by Mr. Steve Hair of the. NRC during his May 31, 1984 Appendix J..
Ccmpliance Audit Exit Intezview.
1) AEPSC'eels, that incozpozation of, the "As Found" minus "As-fran the type
~
B and C leak zate test constitutes an extension of Left"'eakage the zequizarants of 10 50 Appendix J and the licensing basis of the plant. Fu~ narc since the inclusion of this leakage is strictly an arithmetic. exercise that will do no more than create the potential for failing otherwise acceptable type A tests; to the health and safety of the pubLic.
tt~ is no possible benefit, AEPSC'oes concur. with the Plant assessaent. that tte NRC. is Likely to require incozpozation of the "As Found" minus. "As Left" type B and C leakage into the test results.Attachment 1 has been developed to offer guidance as to how the leak rata penalty is to be calculated.
2) AEPSC. concurs that it is possible- foz a change in the level of the Contairumnt mmps could affect the neasuzed leak rata of a type A test.
'Ibis will occur only if the water accmnulated in the sumps is introduced to the Contairmant fran an outside source during the conduct of the type,.
A test. The potential exists to mask nearly 75% of the allowable leakage (0.75 La) if the sutras went fran empty to full over the test
'l duration. Although aceuaulation of this large quantity of water is Test Pzoceduze be revised to require aaasuzeaent of all containment sump levels before and after the test. It is further zecamnded that all sumps be..peeped down prior to the initial neasunment of 1evel.
tHTRA SYSTEM
~ 1~~ ~ priorrate fez; the Type A Test shoUld continue to be calculated as
~
done tests
~
~cept far any changes which are attributable to re~ed, a separate leakage rate including the level changes..
~
<As Found< minus >As Le~" cont~mnt isolation valve penalty can be calculated based on the S. K. Farlav Instztzmntation 6 Control Section emu,cal Engineering Division cc. W. G. Smith S. H. Stairs~ ai "'
R. L. Shoberg Z. A. Kobyra
K. S. Chapman
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File: 3ZRC
APPENDIX F SUPPLEMENTAL TEST PLOW CORRECTION UNIT 2 - 1984
A.E.P,S.C. - M.EJL 3a INSTRUMENTATION AND CONTROLS'ECTION ADMINISTRATIVE INSTRUCTION, AND DESIGN PROCEDURE.
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APPENDIX G SUKRJJARY'F TYPE B AND C'ESTS PERFORMED SINCE LAST TYPE A TEST D. C. COOK PLANT - UNIT TWO OUTAGE OF 1982-1983 OUTAGE OF 1984
APPENDIX F SUPPLEMENTAI TEST
SUMMARY
UNIT 2 1984
('AAAAAAAAA EEEEEEEEEEEE PPPPPPPPPPP 6 777777777777 JJJJJJJJJJ PPPPPPPPPPP AAAAAAAAAAAA EEEEEEEEEEEE PPPPPPPPPPPP 0000000000 77777777777 JJJJJJJJJJ PPPPPPPPPPPP AA AA EE PP PP 00 0000 77 77 JJ PP =PP AA AA EE PP PP 00 00 00 77 JJ PP PP AA AA EE PP PP 00 00 00 77 JJ PP PP AAAAAAAAAAAA EEEEEEEE PPPPPPPPPPPP 00 00 00 77 JJ PPPPPPPPPPPP AAAAAAAAAAAA EEEEEEEE PPPPPPPPPPP 00 00 00 77 JJ PPPPPPPPPPP AA AA Ef PP 00 00 00 77 JJ PP AA AA EE PP 0000 00 77 JJ JJ PP AA AA EE PP 000 00 77 JJ JJ PP AA AA EEEEEEEEEEEE PP 0000000000 77 JJJJJJJJ PP AA AA EEEEEEEEEEEE PP 00000000 77 JJJJJJ PP IIIIIIIIII LL ZIIIZZIZZZ LL RRRRRRRRRRR RRRRRRRRRRRR II II II 1 1 ll 888888888888 8888888888 2222222222 222222222222 ll ill II II LL LL RR RR IQQIQIQIIQQI QQ ll 1
ll'11 88 88 88 88 22 22 22 llll ll ZI II LL LL RR RR RR IQQQQQQQQQQQ RR II II II IQ ll ll 88 88888888 88 22 22 ll ll llll ll RRRRRRRRRRRR ZI LL II II 88888888 22 II II LL LL RR RRRRRRRRRRR RR II QI IQQQQQQQQQQI ll 88 88 88 88 22 22 ll ll II LL IIIIIIIIII LLLLLLLLLLLL RR RR RR RR RR RR IQQQQQQIQQQI II II ll llllll1ill 88 888888888888 88 22 222222222222 ll llllllllll IIIIIZIIII LLLLLLLLLLLL RR RR II II illll illll 8888888888 222222222222 1111111111 JJJJJJJJJJ JJJJJJJJJJ ll 888888888888 ill 8888888888 2222222222 222222222222 ll ill AAAAAAAAAA JJ JJ llll ll 88 88 88 88 22 22 22 llll ll AAAAAAAAAAAA AA AA JJ JJ ll ll 88 88888888 88 22 22 ll ll AA AA AA AA JJ JJ ll ll 88 88888888 88 22 22 ll ll AAAAAAAAAAAA AAAAAAAAAAAA JJ JJ JJ JJ ll ll 88 88 88 88 22 ll ll AA AA AA AA JJJJJJJJ JJJJJJ llllllllll 888888888888 1llllillll 8888888888 22 222222222222 222222222222 llllllllll llllllllll AA AA AA AA AA AA
><>~<><>< GENERAL INFORMATION >><<>>><<<~><<><<<><>x<>>%<%%%<NK>%%%%%MMKKwxwxKKxhwxxm~~%%JO ~ Tll., O'=CPUT SUHMARY wx~mKx
%%XXKXX%%
DELIVER CODE - AEP 07JP AMERICAN ELECTRIC POWER wwwwwww INPUT FROM CANTON.CCC2.INTRDR JOB NAME - ILRI1821 SERVICE CORPORATION <>><> ON Ol OCT 84 AT 1.61.14 PH EST JOB NUMBER - 1821 %XX %K% EXECUTION BEGAN ON CANTON.CCC2 PROGRAHHER " PROBST %%X COLUMBUS ON Ol OCT 84 AT 1.01.17 PH EST IN CLASS C ROON NNSER - 07JP OPERATIONS PRINTED ON COLEUS.COCB.PRINTS SYSOUT CLASS - A %XXX%%% COMPLEX ON Ol OCT 84 AT 2.01.55 PH EST
%%KKXKWE%
XXXK% %%%%XX X KK 3f % K%%% KX%%%% %%%% %%%%%%%%%%Wf%%%% X%XK% X%% K%% XMKKK%XK%%% K%KXX%~%%%k%% K%%%% K% KK% %%%Ã%%%%%%%%% K%%%%% %%%%%%%%%%%%%%%%%%% W
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JES2 JOB LOG SYSTEN CCC - NODE CANTON 13.41.15 JOB 1821 SHASP901 ILR¹1821 JOB 1821 CLASS=C CPU TINE= 1 13.41 '7 JOB 13.41.17 1821 SHASP373 ILR¹1821 STARTED INIT 7 - CLASS C - SYS CCC2 JOB 1821 ZEF403I ZLR¹1821 STARTED 13.41.19 JOB 1821 SHASP375 ILR¹1821 ESTINATED LINES EXCEEDED 13.41.20 JOB 1821 ZEF404I ZLR¹1821 - ENDED 13.41.20 JOB 1821 SHASP395 ZLR¹1821 ENDED JES2 JOB STATISTICS Ol OCT 84 JOB EXECUTION DATE 260 CARDS READ 1>860 SYSOUT PRINT RECORDS 0 SYSOUT PUNCH RECORDS 0.06 NIWUTES EXECUTION TZHE
6 //ILRI1821
//
JOB (4989 52 07JP 1 1 0 1 REGION=128K p NSGCLASS=H p CLASS=C
) 'PROBST'SGLE 1 1) JOB 1821
<<<<<<ROUTE PRINT NOBROOO S020R502
<<<<<<ROUTE PRKH N08ROOO S020R502
<<<<<<DELIVER SAEP07JP
<<<<<<ROUTE PRINT LOCAL
<<<<<<JOBPARH COPIES"-2
<<<<<<DELIVER SAEP07JP 2
3
// EXEC PILR,C"-'<<'XPILR PROC PROG=ILRTESTpREG=128KpC=A 80169001 4 XXGO EXEC PGH=&PROGpREGION=&REG 80169002 5 XXSTEPLIB DD DSN=LIB. PEP pDISP=SHR 80169003 6 XXFT05F001 DD DDNAHE-"DATA 80169004 7 XXFTlOF001 DD SYSOUT=&C>DCB=(RECFN=FBA>LRECL=133sBLKSIZE=931) 80169005 8 XXFT09F001 DD SYSOUT=&C)DCB=(RECFN=FBA)LRECL=133)BLKSIZE=931) 80169006 9 XXFT06F001 DD SYSOUT=&C pDCB"-(RECFH=FBA)LRECL=133)BLKSIZE=931) 80169007 10 //GO.DATA DD <<
STHT NO ~ HESSAGE IEF653I SUBSTITUTIOth JCL - PGH=ILRTEST,REGION=128K 7 IEF653I SUBSTITUTION JCL SYSOUT=> tDCB=l RECFH=FBA > LRECL 133 >BLKSIZE 931 )
8 IEF653I SUBSTITUTIOtt JCL - SYSOUT-"> DCB=(RECFH=FBA,LRECL=133~BLKSIZE-"931) 9 IEF653I SUBSTITUTIOt) JCL - SYSOUT=>zDCB=tRECFH=FBArLRECL=133>BLKSIZE=931)
IEF236I ALLOC. FOR ILR))1821 GO IEF237I A60 ALLOCATED TO STEPLIB ZEF237I 961 ALLOCATED TO SYS00116 IEF237I JES2 ALLOCATED TO FT05F001 ZEF237I JES2 ALLOCATED TO FT10F001 IEF237I JES2 ALLOCATED TO FT09F001 IEF237I JES2 ALLOCATED TO FT06F001 IEF142I ILR))1821 GO - STEP HAS EXECUTED COND CODE 0000 IEF285I LIB.PEP KEPT IEF285I VOL SER NOS= CD0183 ~
IEF285I SYSCTLG.VCDB001 KEPT IEF285I VOL SER NOS= CDB001.
IEF285I JES2. JOB01821. SI0101 SYSIN IEF285I JES2.JOB01821.S00102 SYSOUT IEF285I JES2, JOB01821. S00103 SYSOUT ZEF285I JES2. JOB01821. S00104 SYSOUT IEF373I IEF374I STEP /GO STEP /GO
// START STOP 84275.1341 84275.1341 CPU OHIN 00.65SEC SRB OHIN 00.02SEC VIRT 72K SYS 252K IEF375I JOB /ILRtt1821/ START 84275.1341 IEF376I JOB /ILRI1821/ STOP 84275.1341 CPU OHIN 00.65SEC SRB OHIN 00.02SEC
p)"
w~ ILR ERROR AND tlARNI SSAGES <<<
xxmMANOMETER READING 0.0 NOT IN CALIBRATION RANGE - RUN tt lp ENTRY NUMBER 3 NKKMANOttETER READING 0.0 NOT IN CALIBRATION RANGE - RUN lt 2i ENTRY HUttDER 3 KwwttANOHETER READING 0.0 NOT IN CALIBRATIOH RANGE - RUN 0 3 ENTRY NUlSER 3
%%%ttAttQtETER READING 0.0 NOT IN CALIBRATIOH RANGE - RW 4 4w ENTRY NUMBER 3 wwwMAtRHETER READZNG 0.0 NOT IN CALIBRATION RAHGE - RUH 0 5p ENTRY NUMBER 3
%%%MAttOMETER READING 0.0 tlOT IN CALIBRATIOtt RANGE - RW tt 6p ENTRY NUttBER xhxttAHQlETER READING 0.0 tiOT IN CALIBRATION RANGE - RUH tt 7t ENTRY NUMBER
%%)tMAttOMETER READZttG 0.0 NOT IN CALIBRATION RANGE - RUN tt 8> ENTRY NUMBER 3
<>>MANOMETER READING 0.0 NOT IN CALIBRATION RANGE - RUN tt 9p EttTRY NUMBER 3
<<<MANOMETER READIttG 0.0 NOT IN CALIBRATION RAttGE - RUH 4 10'NTRY NUtlBER
%%xHANOttETER READING 0.0 HOT IN CALIBRATIOH RANGE - RW tt ll> ENTRY NUMBER 3
%%%HAHOMETER READING 0.0 NOT IN CALIBRATIOH RAtlGE - RW 0 12> ENTRY NUMBER 3 wwwMAttOtlETER READING 0.0 NOT ZN CALIBRATIOtl RANGE " RW tt 13> ENTRY HUt%ER
%%%MANOMETER READING 0.0 NOT IN CALIBRATION RANGE " RUN tt 14> ENTRY NUMBER 3 w<<tfAttOMETER READING 0.0 HOT IN CALIBRATION RANGE - RUN 4 15 ENTRY tlWBER 3 M~HAttOMETER READING 0.0 NOT ZN CALIBRATION RANGE RUN tt 16'NTRY NUMBER 3
~xMAttOMETER READING 0.0 HOT ZN CALIBRATIOti RAttGE - RUN tt 17 ENTRY HUttBER 3 wx>MAttOttETER READING 0.0 NOT IN CALIBRATION RAttGE - RUN tt 18'NTRY NUMBER 3 xxxMANQ1ETER READING 0.0 HOT Ztk CALZBRATIOtt RANGE - RUN tt 19 ENTRY HUttBER 3 wx>MANOtfETER READIttG 0.0 NOT ZN CALIBRATION RANGE RUN tt 20> ENTRY NUMBER 3 wwwttANOttETER Rf ADItlG 0.0 HOT IN CALIBRATION RAtlGE - RUH tt 21 ENTRY NUttBER 3 wxwtiAttOMETER READING 0.0 NOT IN CALIBRATION RANGE - RUN tt 22> ENTRY HmtBER 3 COttVERTED DEH POINT 28.04 RUN NUMBER 23 ZS OUT OF RAHGE FOR VAPOR PRESSURE CALCULATION AHD HAS BEEN IGNORED CONVERTED DEH POINT -0 00 RW HUt tBER 23 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND MAS BEEN ZGtiORED
<<>MANQtETER READING
~
0.0 ttOT IN CALIBRATION RANGE - RUN lt 23 ENTRY HUttBER '
COtiVERTED DEH POINT 28.40 RUth ttUt tBER 24 IS OUT OF RAttGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED COtiVERTED DEH POINT 0.02 RUN NUt tBE R 24 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED wxwMANQ1ETER READING 0.0 NOT ZN CALIBRATION RANGE - RUN tt 24'NTRY NUttBER 3 CONVERTED DEH POINT 28.40 RUN NUttBER 25 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND MAS BEEN IGNORED
<>>MANOMETER READING 0.0 HOT Itt CALIBRATION RANGE - RUN tt 25 ENTRY HUttBER 3 CONVERTED DEH POINT 28.04 RUN NUMBER 26 ZS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND MAS BEEN IGNORED xxxMAttOttETER READING 0.0 ttOT IN CALIBRATION RANGE - RUN e 26'NTRY NC%ER 3 CQtVERTED DEli POINT 28.22 RUH NUMBER 27 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED
%MKMANOtlETER READING 0.0 NOT IN CALIBRATION RANGE - RUN tt 27> ENTRY NUMBER 3 CONVERTED DEH POINT 28.40 RUN HUttBER 28 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGNORED
>>>t tANQiETER READING 0.0 HOT IN CALIBRATION RANGE - RUN tt 28> ENTRY NUMBER 3 COttVERTED DEH POINT 28.94 RUN HUttBER 29 IS OUT OF RANGE FOR VAPOR PRESSURE CALCULATION AND HAS BEEN IGHORED zxxMANOMETER READING 0.0 NOT IN CALIBRATION RANGE - RUH 4 29> EttTRY HUMBER 3
44 3=; 444444 ILR PROGRAH RESULTS SUHHARY OF AVERAGES ELAPSED AVG TEHP AVG PRESS AVG V PRESS AVG TEHP AVG PRESS AVG V PRESS AVG TEHP AVG PRESS AVG V PRESS TZHE UPPER UPPER UPPER LONER LQKR LOHER ICE ZCE ICE 1 0.0 72.5562 26.850ij 0. 0934 73 '920 26.8565 0.1102 17.2338 26o8857 0.0401 2 0.50 72.5655 26.8481 0. 0934 73.3156 26.8545 0.1106 17.1156 26.8834 0.0368 3 1.00 72.5362 26.8476 0.0935 73.2979 26.8529 0.1110 17.1285 26.8806 0.04403 4 1.50 72.5377 26.8458 0.0933 73.3473 26.8513 0.1114 17.2876 26.8792 0.0415 5 2.00 72.5116 26.8438 0.0939 73.3336 26.8494 0.1117 17.2258 R6.8772 0.0352 6 2.50 72.5125 26.8430 0.0934 73.3669 26.8487 0.1120 17. 1175 26.8767 0.0383
? 3.00 72.5179 26.8418 0.0937 73.4222 26.8474 0. 1124 17. 0781 26.8754 0.0388 8 3.50 72.5250 26.8385 0.0937 73.3532 R6.81445'6.8428 0.1128 17. 1814 26.8728 0.0406 9 4.00 72.5308 26.8369 0.0942 73.3942 0. 1131 17.0658 26.8708 0.0381 10 4.50 72.5374 26.8360 0.0936 73.38R9 26.8420 0.1135 1?e0197 *26.8699 0.0384 ll 12 5.00 5.50 72.52440 72.5343 26.8332 26.8R98 0,09440 0.0941 73.3882 73.4099 26.83S9 26.8358 0.1139 0.1141 17.2124 17.0518 26.8667 26.8637 0.0365 0.0365 13 6.00 72.4963 26.8284 0.0939 73.3997 26.8343 0.1145 17 '036 26.86R7 0.0376 14 6.50 72.4759 26.8273 0.0943 73.4022 26.8332 0. 1149 16.9422 26.8619 0.0370 15 7.00 72.4839 26.8248 0.0942 73.4053 26.8305 0.1152 16.9664 26.8584 0.0368 16 8.00 72.4543 26.8220 0.0899 73.4409 26.827'? 0.1160 17.0081 26.8554 0.0386 17 8.50 72.4478 26.8189 0.0906 73.4265 26.8246 0.1158 17. 1162 26.8524 0.0349 18 9.00 72.4320 26.8161 0.0903 73.4106 26.8401 0.1162 16.9393 R6.8509 0.0356 19 9.50 72.3954 26.8133 0.0906 73.4252 26.8193 0.1166 16.8170 26.8474 0.0370 20 ~
10.00 72.3799 26.8128 0.0902 73.4332 26,8179 0. 11?1 16.8789 26.8472 0.0369 21 10.50 72.4088 26.8102 0.0904 73.4139 26.8163 0.1178 16.8021 26.8443 0.0318 22 11.00 ?2.4039 26.8072 0.0908 ?3.4308 '26.8137 0.1180 16.7648 26.8413 0.0345 23 11.50 72.347R 26.8024 0.0908 73.4274 26.8094 0.1067 16.8224 26.8374 0.0363 24 12.00 72.3651 26.8018 0.0910 73.4541 26.8083 0. 1065 16.9424 26.8363 0.0341 25 12.50 72.3449 26.8003 0.0910 73.4318 26.8074 0.1072 16.7956 26.8354 0.0355 26 13.00 72.3481 26.7983 0.0915 73.4388 26.8059 0.1079 16.7118 26.8334 0,0358 27 13.50 72.3339 R6.7945 0.0914 73.4314 26.8025 0.1085 16.8125 26.8300 0.0348 28 14.00 72.3256 26.7950 0.0908 73.4231 26.8027 0.1089 '16.7143 26.8203 0.0337 R9 14.50 72.3153 26.7933 0.0913 ?3.4357 26.8013 0.1092 16.7260 26.8295 0.0373
/
(-'y RESULTS OF THE LINEAR REGRESSION ~SIS N LEAKAGE RATE LEAKAGE N UPPER H LONER N ICE EXPERIllENTAL UPPER LIHIT RATE CONTAINHENT CONTAINtlENT CONDENSER 0.99991 -0.57764 -0.21530 0.99993 0.99982 1.00002 0.99977 -0.55713 -0.33766 0.99987 0.99966 0.99959 5 0.99976 -0.41656 -0.30551 0.99982 0.99960 0.99988 6 0,999?4 -0.34858 -0.26846 0.99981 0.99950 0.99998 7 0.99965 -0.32499 -0.27134 0.99974 0.99933'.99934 0.99999 8 0.99953 -0.34903 -0.29932 0.99960 0.99961 9 0.99946 -0.35394 -0.31336 0.99951 0.99919 0.99987 10 0.99945 -0.33964 -0.30719 0.99949 0.99917 0.99993 ll 12 0.99930 0.99919
-0.35387
-0.37085 "0.32291
-0.33983 0.99939 0.99924 0.99903 0.99886 0.99947 0 '9970 13 0.99919 -0.36438 -0.33835 0.99927 0.99881 0.99972 14 0.99918 -0.35342 "0.32951 0.99925 0.99875 0.99984 15 0.99906 0 '4983 -0.32925 0.99915 0.99863 0.99967 16 0.99903 -0.33755 -0.31672 0.99926 0.99843 0.99940 17 0.99891 -0.33247 -0.31430 0.99913 0.99835 0.99920 18 0.99908 -0.31874 -0.29276 0.99907 0.99894 0.99949 19 0.99882 -0.31566 -0.29263 0.99902 0.99812 0.99956 20 0.99880 -0.31092 "0. 29021 0.99905 0.99804 0.99943 21 0.99872 -0.30824 -0.28958 0.99889 0.99799 0.99967 22 0.99860 -0.30969 -0.29253 0.998?7 0.99785 0.99954 23 0.99859 "0.30781 -0.29218 0.99869 0.99812 0.99920 24 0.99850 -0.30735 -0.29302 0.99863 0.99804 0.99899 25 0.99851 -0.30399 -0.29060 0.99862 0.99802 0.99922 26 0.99844 -0.30171 "0.28929 0.99852 0.99792 0.99930 27 0.99830 -0 '0282 -0. 29117 0 '9840 0.99?79 0.99901 28 0.99832 -0.30085 -0.28997 0.99846 0.99779 0.99889 29 0.99828 -0.29861 -0.28835 0.99840 0. 99771 0.99907 FINAL LEAKAGE RATE (% PER DAY) = -0.28835 INTERCEPT~ 0.99997 I
UPPER CONFIDENCE LIHIT FOR TtlE RATE IS -0 .29861
<<>SUPPLEHENTAL TEST COHPLETION CRITERIA HESSAGES<<>
TYPE A LEAK RATE = -0.03404 (%liT/DAY) It(POSED LEAK RATE =, %.0700 (SCFH) = -0.2614 (%t(T/DAY)
TEST DURATIOtt HAS EXCEEDED TIIE 6 !lOUR HINIt%lt(
Tllf HEASURED COHPOSITE LEAKAGE HEETS RANGE REQUIREHENTS SUPPLEHENTARY TESTING COHPLETED(
(~ %%%%%%38E%%% FIKED INP A TEST START = RUN I 0 HILLI-VOLTTO FAttREtQEIT TEST END = RUN 4 0 RTD CONVERSION COEFFICIENTS UPPER LONER ICE 2.00 0.0 2.00 0.0 2.00 0.0 llYGRONETER HILLI-VOLTTO FAllRENIIEIT CONVERSION COEFFICIENTS UPPER"1 LONER-1 ICE-1 0.00053 1.97638 -0.05018 0.00061 1 '6939 -0.01108 0.00069 1.96622 "0.03787 UPPER"2 LOHER-2 ICE-2 0.0 18.00000 32.00000 0.00063 1.96888 -0.00869 0.0 18.00000 32.00000 HANOttETER PRESSURE CORRECTION COEFFICIENTS Hl Rl H2 R2 H3 H4 R4 PU-1 34.9568 35.2180 29.9629 30.1800 24.9693 25.1380 19.975$ 20.0950 14.9815 15.0680 PU-2 29.9632 29.9634 28.4652 28.4663 26.9671 26. 9684 25.4689 25.4688 0.0 0.0 PL-1 0.0 0.0 0.0 0.0 0~0 0.0 0.0 0.0 0.0 0.0 PL-2 29.9632 29.9648 28.4652 28.6466 26.9671 26.9688 25.4689 25.4694 0.0 0.0 PI-1 29.9632 29.9609 28.4652 28.4640 26.9671 26.9681 25.4689 25.4688 0.0 0.0 PI"2 29.9632 29.9618 28.4652 28 '656 26.9671 26.9685 25.4689 25.4689 0.0 0.0 P-AT)t 14.7020 14.7100 13.5010 13.5010 11.5010 11.4960 9.5020 9.5020 7.5020 7.5000 RTO HEIGllTItlG FACTORS UPPER
.0628 .1161 .0831 ~ 0831 0960 .0960 e0960 .0960 .0296 .0296
.0296 .0296 .0740 .0105 .0167 .0513 LONER
~ 0415 .0415 .0415 .0415 .0102 .0284 .0586 .0086 .0266 ~ 0586 .1037
~ 1037 .1037 .1037 .0500 .0092 .0244 .0145 .0170 .0249 .0219 .0240 .0423 .0 ICE
.0735 .0735 .0711 .0711 ~ 2231 .2789 .2089 VOLUtlE HEIGllTING FACTORS UPPER LOHER ICE 2.0144 1.0000 0.3713 TYPE C LEAKAGE PENALTY= -867.00lSCCH)) TYPE A ttEASURED LEAK RATE = -0 ~ 03404 (/Hl/DAY)) IHPOSED LEAK RATE -4.070 tSCFtt)
F
RUN R ELAPSED TIHE 30.50 CONTAIt(HENT TEHPERATURES DATA CIIECK UPPER VOLUHE LOWER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG, F. RTD NIL LI-VOLTS DEG. F.
ETR-101 39. 74 79.48 ETR-122 35.93 71.86 ETR-115 9. 62 19.24 ETR-102 37. 64 75.28 ETR-123 36.65 73.30 9. 20 'TR-116 18.40 ETR-103 35. 66 71.32 ETR-124 37.27 74.54 ETR-117 8.93 17.86 ETR-104 35. 61 71.22 ETR-125 36.01 72.02 ETR"118 10.00 20.00 ETR" 105 35. 99 71.98 ETR-126 36.08 72.16 ET/-119 8.34 16.68 ETR-106 36. 31 72.62 ETR-127 33.90 67.80 ETR-120 8.05 16.10 ETR-107 35.87 71.74 ETR-129 37.19 74.38 ETR-121 8.53 17.06 ETR-108 35.89 71.78 ETR-130 35.65 71.30 ETR-109 35.56 71.12 ETR-131 33.93 67.86 ETR-110 35.42 70.84 ETR-132 37.65 ?5.30 ETR-ill 35.54 71.08 ETR-134 36.67 73.34 ETR"112 35.59 71.18 ETR-135 36.60 73.20 ETR-114 34.83 69.66 ETR-136 36.57 73.14 ETR-128 36. 88 73.76 ETR-137 36.28 72.56 ETR-133 34.37 6e.?4 ETR-138 36.63 73.26 ETR-113 37.33 74.66 ETR-139 33.93 67.86 ETR-140 36.74 73.48 ETR"141 37.38 74.76 ETR-142 36.25 72.50 ETR-143 37.63 75.26 ETR-144 36.96 73.92 ETR-145 41.60 83.20 ETR-146 3?.15 74.30 SUHHARY OF WEIGI(TED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.56 LOWER VOLUHE (DEG. F.) 73.29 ICE CONDENSER (DEG. F.) 17. 23 UPPER VOLUt(E (DEG. R.) 532.26 LOWER VOLUHE (DEG. R.) 532.99 ICE CONDENSER (DEG. R.) '76. 93 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED I IYGROHETER VOLTS (DEG. F. ) ( PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.81 33 '2 0.0934 PU"1 27.0130 26.8263 VPU-2 0.0 32.00 0.0 PU-2 26.8757 26.8745 LOWER: LOWER:
VPL-1 19.28 38.19 0.1133 PL-1 0.0 0.0 VPL-2 18.57 36,77 0.1072 PL-2 26.8581 26.8565 ICE: ICE:
VPI-1 8.61 16.95 0.0435 PI-1 26.8?re 26.8769 VPI-2 -1.03 13.46 0.0367 PI-2 26.8958 26.8945 AHBIENT 14.4900 14.4835 AVERAGE VAPOR PRESSURES SUHt(ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIttHENT (PSIA) 0.0934 LOI(ER COt(TAIt(HENT (PSIA) 0.1102 AVERAGE UPPER PRESSURE (PSIA) 26.8504 ICE CONDENSER (PSIA) 0.0401 AVERAGE LOWER PRESSURE (PSIA) 26.8565 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8857 AVERAGE COt(TAINHENT PRESSURE (PSIA) 26.8642 AVERAGE CONTAIt(HENT PRESSURE ( PSIG) 12.3807 g>y
ELAPSED TINE 31.00
(
CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LOWER VOLUHE ICE CONDENSER RTD WILLI-VOLTS DEG. F. RTD HIL(.I-VOLTS DEG. F. RTD WILLI-VOLTS DEG. F.
ETR"101 39.73 79.46 ETR-122 35. 94 71.88 ETR-115 9.34 18. 68 ETR-102 37. 63 75.26 ETR-123 36.66 73.32 ETR-116 9.02 18. 04 ETR-103 35. 66 71.32 ETR-124 37.25 74.50 ETR-11? 8.70 17.40 ETR"104 35.60 71. 20 ETR-125 35. 99 71. 98 ETR-118 9.97 19. 94 ETR-105 36. 02 72.04 ETR-126 36.08 72.16 ETR-119 8.35 16.?0 ETR-106 36. 30 72.60 ETR-127 33.94 67.88 ETR-120 8. 07 16.14 ETR-107 35.90 71.80 ETR-129 37.17 74.34 ETR-121 .8.46 16.92 ETR-108 35.89 71.78 ETR-130 35.65 71.30 ETR-109 35. 61 71.22 ETR-131 33.93 67.86 ETR-110 35.39 70.78 ETR-132 37.66 75.32 ETR-ill 35.54 71.08 ETR-134 36.76 73.52 ETR-112 35.55 71. 10 ETR-135 36.59 "
73.18 ETR-114 34.86 69.?2 ETR-136 36.59 73.18 ETR-128 36. 88 73.76 ETR-137 36.28 72.56 ETR-133 34.36 68.72 ETR-138 36.67 ?3.34 ETR-113 37.35 74.70 ETR-139 33.93 67.86 ETR-140 36.75 73.50 ETR-141 37.38 74.76 ETR-142 36.25 72.50 ETR-143 37.63 75.26 ETR-144 36.97 73.94 ETR-145 41.57 83.14 ETR-146 37.15 74.30 SUHHARY OF WEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 72.57 LOt(ER VOLUtlE (DEG. F.) 73.32 ICE CONDENSER (DEG. F. ) 17. 12 UPPER VOLUHE (DEG. R. ) 532.27 LOWER VOLUHE (DEG. R. ) 53'3.02 ICE COt(DENSER (DEG. R. ) 476.82 COt(TAINHEt(T VAPOR PRESSURE DATA C(IECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEW POINT VAPOR PRESSURE UNCORRECTF 0 CORRECTED tlYGROHETER VOLTS (DEG. F.) (PSIA) NANO!(ETER READING ( PSIA ) READING ( PSIA)
UPPER: UPPER:
VPU-1 16.81 33.32 0 ~ 0934 PU-1 27.0101 26.8234 VPU-2 0.0 32.00 0.0 PU-2 26.8739 26.8727 LOWER: LOWER:
VPL-1 19.35 38.33 0. 1139 PL-1 0.0 0.0 VPL-2 18.59 36.81 0.1073 PL-2 26.8561 26.8545 ICE- ICE:
VPI-1 7.81 15.36 0.0403 PI-1 26.8759 26.8750 VPI-2 -1.14 11.48 0.0332 PI "2 26.8932 26.8919 At(DIENT 14.4800 14.4735 AVERAGE VAPOR PRESSURES I SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER COt(TAIt(HENT (PSIA) 0.0934 LOWER CO((TAINHENT (PSIA) 0.1106 AVERAGE UPPER PRESSURE (PSIA) 26.8481 ICE CONDENSER (PSIA) 0.0368 AVERAGE LOWER PRESSURE (PSIA) 26.8545 AVERAGE ICE COt(DENSER PRESSURE (PSIA) 26.8834 CONTAIt(t(ENT PRESSURE (PSIA) 26.8620 'VERAGE AVERAGE CONTAINt(ENT PRESSURE (PSIG) 12.3885
ELAPSED TIME 31.50 CONTAINMENT TEHPERATURES DATA CIIECK UPPER VOLUME LO) IER VOLUME ICE CONDENSER RTD HILLI-VOLTS DEG. F. ~
RTD MILLI-VOLTS DEG. F. RTD MILLI"VOLTS DEG. F.
ETR-101 39. 72 79.44 ETR-122 35.91 71.82, ETR-115 9. 16 18.32 ETR-102 37. 62 75.24 ETR-123 36.67 73.34 ETR-116 9.04 18.08 ETR-103 35. 64 71.28 ETR"124 37.25 74.50 ETR-117 8.68 17.36 ETR-104 35.57 71.14 ETR~ 125 36.04 72.08 ETR-118 9. 95 19.90 ETR-105 36. 00 72.00 ETR-126 36.10 72.20 ETR"119 8.36 16.72 ETR-106 36. 29 72.58 ETR-127 33.97 67.94 ETR-120 8. 10 16.20 ETR "107 35. 87 71.74 ETR-129 37.16 ?4.32 ETR-121 8.51 17.02 ETR-108 35.87 71.74 ETR-130 35.65 71.30 ETR-109 35.61 71.22 ETR-131 33.94 67.88 ETR-110 35.43 70.86 ETR-132 37.66 75.32 ETR-ill 35.55 71.10 ETR-134 36.65 73.30 ETR"112 35.58 71.16 ETR-135 36.55 73.10 ETR-114 34.84 69.68 ETR-136 36.63 73.26 ETR-128 36. 89 73.78 ETR-137 36.27 72.54 ETR-133 34.36 68.72 ETR"138 36.68 73.36 ETR"113 37.31 74.62 ETR-139 33.95 67.90 ETR"140 36.75 73.50 ETR-141 37.38 74.76 ETR-142 36.26 72.52 ETR-143 37.64 75.28 ETR-144 36.97 73.94 fTR"145 41.59 83.18 ETR-146 37.15 74.30
SUMMARY
OF HEIGHTED AVERAGE TEMPERATURES UPPER VOLUl(E (DEG. F.) 72.54 LOHER VOLUt(E (DEG: F ~ ) 73.30 ICE CONDENSER (DEG. F.) 17.13 UPPER VOLUME (DEG. R.) 532.24 LONER VOLUME (DEG. R. ) 533.00 ICE CONDENSER (DEG. R.) 476.83 CONTAINMENT VAPOR PRESSURE DATA CHECK COt(TAINHENT PRESSURES DATA CtlECK MILLI" DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROHETER VOLTS (DEG. F. ) (PSIA) MANOMETER READING (PSZA) READING (PSZA)
UPPER: UPPER:
VPU-1 16.82 33.34 0. 0935 PU-1 .
27.0090 26.8223 VPU-2 0.0 32. 00 0.0 PU-2 26.8740 26.8728 LOHER: LONER:
VPL-1 19.42 38.47 0.1146 PL-1 0.0 0.0 VPL-2 18.61 36.85 0.1075 PL-2 26.8545 26.8529 ICE: ICE:
VPI-1 8.80 17.31 0.0443 PI-1 26.8741 26.8732 VPI<<2 -1.04 13.28 0.0364 PI-2 26.8894 26.8881 AMBIENT 14.4900 14.4835 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIN!(ENT (PSIA) 0. 0935 LOHER COt(TAINt(ENT (PSIA) 0.1110 AVERAGE UPPER PRESSURE (PSIA) 26.8476 ZCE COt(DENSER (PSIA) 0. 01403 AVERAGE LOt(ER PRESSURE (PSIA) 26.8529 AVERAGE ICE CONDENSER PRESSURE (PSZA) 26.8806 AVERAGE CONTAIt(MENT PRESSURE (PSIA) 26.8604 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3769 g~P>)
~IV (M
RUN ~R 4 ELAPSED TIHE 32.00 COt(TAINHENT TEMPERATURES DATA CHECK UPPER VOLUHE LONER VOLUME ICE CONDENSER RTD IIILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD t(ILLI-VOLTS. DEG. F.
ETR-101 39.70 79.40 ETR-122 35.95 71.90 ETR" 115 9. 23 18.46 ETR-102 37.61 75.22 ETR-123 36.66 '?3.32 ETR-116 9. 20 18 40 ETR-103 35. 65 71.30 ETR-124 37.31 74.62 ETR-117 8.92 17.84 ETR" 104 35. 60 71.20 ETR-125 36.01 72.02 ETR-118 10.65 21.30 ETR-105 35.99 71.98 ETR-126 36.10 72.20 ETR-119 8.36 16 '2 ETR-106 36.29 ?2.58 ETR-127 33.91 67.82 ETR-120 8.10 16.20 ETR<<107 35.88 71. 76 ETR-129 37.17 74.34 ETR-121 8.49 16. 98 ETR-108 35. 83 .
71.66 ETR-130 35.66 71.32 ETR-109 35.56 71. 12 ETR-131 33.94 67.88 ETR-110 35.48 70.96 ETR-132 37.68 75.36 ETR-ill 35.56 71. 12 ETR-134 36.76 73.52 ETR-112 35.60 71.20 , ETR-135 36.59 73.18 ETR-114 34.85 69.70 ETR-136 36.66 73.32 ETR-12e 36.91 73.82 ETR"13? 36.28 72.56 ETR-133 34. 38 68.76 ETR-138 36.72 73.44 ETR-113 37.34 74.68 ETR-139 33.94 67.88 ETR-140 36.75 73.50 ETR-141 37.39 74.?e ETR-142 36.28 ?2.56 ETR"143 37.66 75.32 ETR-144 36.98 73.96 ETR-145 41.56 83.12 ETR-146 37 15 74.30 SUHHARY OF NEIGHTED AVERAGE:TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.54 LOI'IER VOLUME (DEG. F. ) 73.35 ICE CONDENSER (DEG. F. ) 17. 29 UPPER VOLUME (DEG. R. ) 532.24 LOIIER VOLUHE (DEG. R.) 533.05 ICE CONDENSER (DEG. R. ) 476.99 CONTAINNEt(T VAPOR PRESSURE DATA CHECK CONTAIt(MENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS '(DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16. 79 33.28 0.0933 PU-1 2?.ooea 26.8214 VPU-2 0.0 32. 00 0.0 PU"2 26.8714 26.8702 LOIIER: LONER:
VPL-1 19.50 38.63 0. 1153 PL-1 0.0 0.0 VPL-2 18.61 36.85 0.1075 PL-2 26.8529 26.8513 ICE: ICE:
VPI-1 9. 18 18.07 0.0460 PI "1 26.8726 26.8717 VPI-2 -1.02 13. 64 0.0370 PI-2 26.8880 26.8867 AMBIENT 14.4900 14.4835 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAItl(ENT (PSIA) 0.0933 LOIIER CONTAItIHEI(T (PSIA) 0. 1114 AVERAGE UPPER PRESSURE (PSIA) 26.8458 ICE CONDENSER (PSIA) 0.0415 AVERAGE LONER PRESSURE (PSIA) 26.8513 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8792 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.85SS AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3753
RUNNER 5 ELAPSED TINE 32.50 CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD NILLI-VOLTS DEG. Fo RTD HILLI-VOLTS DEG. Fo ETR-101 39. 69 79.38 ETR-122 35.92 71.84 ETR-115 9.15 18.30 ETR-102 37. 60 75.20 ETR-123 36.66 73.32 ETR"116 9.07 18.14 ETR-103 35. 62 s 71.24 ETR-124 37.29 74.58 ETR-117 8. 75 17.50 ETR-104 35.58 71.16 ETR-125 36.04 72.08 ETR-118 10.84 21.68 ETR-105 35.96 71.92 ETR-126 36.12 72.24 ETR"119 8.35 16.70 ETR-106 36. 28 ?2.56 ETR-127 33.93 6?.e& ETR-120 8. 07 16.14 ETR-107 35.86 71.72 ETR-129 37. 17 74.34 ETR-121 8.46 16.92 ETR-108 35. 84 71.68 ETR-130 35.64 71.28 ETR-109 35. 64 71.28 ETR-131 33.91 67.82 ETR-110 35.46 70.92 ETR"132 37.&9 ?5.38 ETR-ill 35.57 71.14 ETR-134 36.67 73.34 ETR-112 35.56 71.12 ETR-135 36.57 73.14 ETR-114 34.85 69. 70 ETR"136 36.69 73.38 ETR-128 36.88 73. 76 ETR-137 36.27 72.54 ETR-133 34. 36 68. 72 ETR-138 36.73 73.46 ETR-113 37.29 74.58 ETR-139 33.95 67.90 ETR-140 36.76 73.52 ETR-141 37.41 74.82 ETR"142 36. 29 72.58 ETR-143 37. 66 75.32 ETR-144 36.99 73.98 ETR-145 41.60 83.20 ETR-146 37.16 74.32 SUtlHARY OF HEIGtlTED AVERAGE TEHPERATURES UPPER VOLUHE <DEG. F.) 72.51 LONER VQLUttE (DEG. F.) 73.33 ICE CONDENSER (DEG. F. ) 17.23 UPPER VOLUHE (DEG. R.) 532.21 LONER VOLUHE (DEG. R. ) 533.03 ICE CONDENSER (DEG. R.) 476.93 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES CATA CHECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROttETER VOLTS [DEG. F. ) (PSIA) HANOHETER READING (PSIA) READINGS(PSIA)
UPPER: UPPER:
VPU-1 16.88 33.46 0.0939 PU-1 27.0060 26.8194 VPU-2 0.0 32.00 0.0 PU-2 26.8694 26.8682 Lot tER: LONER:
VPL-1 19.58 38.?8 0.1160 PL-1 0.0 0.0 VPL-2 18.60 36.83 0.1074 PL"2 26.8510 26.8494 ICE: ICE:
VPI-1 8.30 16.32 0.0422 PI-1 2&.e?06 26.8697 VPI-2 -1.32 8.24 0.0283 PI-2 26.8860 26.8847 AHBIEtfT 14.4900 14.4835 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIttHENT t PSIA) 0.0939 LONER CONTAIt4fENT (PSIA) 0. 1117 AVERAGE UPPER PRESSURE (PSIA) 26.8438 ICE CONDENSER (PSIA) 0.0352 AVERAGE LONER PRESSURE (PSIA) 26.8494 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8772 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8568 AVERAGE CONTAINHEtff PRESSURE (PSIG) 12.3733
RUN ~ER ELAPSED TINE 6
33.00
(
COt(TAINMENT TEHPERATURES DATA CHECK UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DfG. F.
ETR-101 39. 71 79.42 ETR-122 35.94 71.88 ETR-115 9.02 18.04 ETR"102 37.59 75.18 ETR-123 36.68 73.36 ETR-116 9.07 18.14 ETR-103 35.63 71.26 ETR-124 37.32 74.64 ETR-117 8.73 17.46 ETR-104 35.57 71.14 ETR-125 36.02 72.04 ETR-118 10. 24 20.48 ETR-105 35.98 71.96 ETR-126 36.12 72.24 ETR-119 8.36 16.72 ETR-106 36.27 72.54 ETR-127 33.90 67.80 ETR-120 8. 09 16.18 ETR-107 35. 84 71.68 ETR-129 37. 21 74.42 ETR-121 8.42 16.84 ETR-108 35.84 71.68 ETR-130 35.65 71.30 ETR-109 35.54 71.08 ETR-131 33.91 67.82 ETR-110 35.51 71.02 ETR-132 37.70 75.40 ETR"ill 35.56 71.12 ETR"134 36.73 73.46 ETR-112 35.59 71.18 ETR-135 36.62 73.24 ETR-114 34.87 69.74 ETR-136 36.67 73.34 ETR-128 36.90 73.80 ETR-137 36.29 72.58 ETR-133 34.36 68.72 ETR-138 36.74 73 '8 67,90 ETR-113 37.30 74.60 ETR-139 '3.95 ETR-140 ETR-141 36 '7 37.41 73.54 74.82 ETR-142 36.28 72.56 ETR-143 3$ .67 75.34 ETR"144 36.98 73.96 ETR-145 41.60 83.20 ETR-146 37.17 74.34 SUHMARY OF NEIGHTED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F.) 72.51 LOHfR VOLUME (DEG. F.) 73.37 ICE CONDENSER (DEG. F.) 17.12 UPPER VOLUME (OEG. R.) 532.21 LONER VOLUME (DEG. R.) 533.07 ICE CONDENSER (DEG. R.) 476.82 COIITAINHENT VAPOR PRESSURE DATA CHECK COI(TAINHEHT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F. ) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.81 33.32 0.0934 PU-1 27.0050 26.8184 VPU-2 0.0 32.00 0.0 PU-2 26.8689 26.8677 LONER: LONER(
VPL-1 19. 65 38.92 0.1166 PL-1 0.0 0.0 VPL-2 18.59 36.81 0.1073 PL"2 26.8503 26.8487 ICE: ICE VPI-1 8.99 17. 69 0.0451 PI-1 26.8700 26.8691 VPI-2 "1.20 10.40 0.0315 PI"2 26.8857 26.8844 AHBIEt(T 14.5000 14.4934 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAltRlft(T (PSIA) 0.0934 LONER CONTAIIR(ENT (PSIA) 0.1120 AVERAGE UPPER PRESSURE (PSIA) 26.8430 ICE CONDENSER (PSIA) 0.0383 AVERAGE LONER PRESSURE (PSIA) 26.8487 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8767 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8562 AVERAGE COt(TAINMENT PRESSURE (PSIG) 12.3628
RUN I~R ELAPSED TIHE 7
33.50 CONTAINHENT TEHPERATURES DATA CIIECK UPPER VOLUHE LONER VOLUHE ICE CONDEttSER RTD HILLI-VOLTS DEG. F. RTD HILLI "VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 39. 67 79.34 ETR"12R 35.93 71.86 ETR-115 9. 23 18.46 ETR-102 37.58 75.16 . ETR-123 36.73 73.46 ETR-116 9.01 18. 02 ETR-103 35. 63 71.26 ETR-124 37.31 74.62 ETR"117 8.62 1'7. 24 ETR-104 35. 57 71.14 ETR-125 36.05 72.10 ETR-118 9. 92 19.84 ETR-105 35. 99 71.98 ETR-126 36.13 ?2.26 ETR-119 8.35 16.70 ETR-106 36.26 72.52 ETR"127 33.89 67.78 ETR-120 8. 06 16.12 ETR-107 35.84 71.68 ETR"129 37.21 74.42 ETR-121 8.47 16.94 ETR-108 35.83 71.66 ETR-130 35.66 71.32 ETR-109 35.56 71.12 ETR-131 33.92 67,84 ETR-110 35.53 71.06 ETR"132 37.71 75.42 ETR-ill 35.56 71.12 ETR-134 36.82 73.64 ETR-112 35.55 71.10 ETR-135 36.67 73.34 ETR-114 34.83 69.66 ETR"136 36.68 73.36 ETR-128 36.92 73.84 ETR-137 36.37 72.74 ETR-133 ETR-113
34. 38 37.49 68.76 74.98 ETR-138 ETR-139 36 '4 33.96 73.48 67.92 ETR-140 36.7? 73.54 ETR-141 37.41 74.82 ETR-142 36.29 7R.58 ETR"143 37.68 75.36 ETR-144 37.00 74.00 ETR"145 41 '0 83.20 ETR-146 37.16 74.32 SUHHARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 7R.52 LONER VOLUHE IDEG. F. ) 73.42 ICE CONDENSER (DEG. F.) 17.08 UPPER VOLUIIE IDEG. R. ) 532.22 LOHER VOLUtIE IDEG. R.) 533.12 ICE CONDENSER (DEG. R.) 476.78 CONTAINHENT VAPOR PRESSURE DATA CIIECK CONTAINHENT PRESSURES DATA CMECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROHETER VOLTS IDEG. F. ) IPSIA) HANOHETER READING (PSIA) READING IPSIA)
UPPER: UPPER:
VPU-1 16.85 33.40 0 '937 PU-1 27.0040 26.8174 VPU-2 0.0 3R.OO 0.0 PU-2 26.8674 26.8662 LOHER: LONER:
VPL-1 19.73 39. 08 0.1174 PL-1 0.0 0.0 VPL"2 18.61 36.85 0.1075 PL-2 26.8490 R6.8474 ICE ICE:
VPI "1 8.94 17.59 0.0449 PI-1 26.8683 26.8674 VPI-2 -1 16
~ 11.12 0 '326 PI-2 26.8847 26.8834 AHBIENT 14.4900 14.4835 AVERAGE VAPOR PRESSURES SWARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINIIENT (PSIA) 0. 0937 LONER CONTAINHENT IPSIA) 0.1124 AVERAGE UPPER PRESSURE IPSIA) R6.8418 ICE CONDEIISER I PSIA) 0.0388 AVERAGE LOHER PRESSURE (PSIA) 26.8474 AVERAGE ICE CONDEttSER PRESSURE (PSIA) 26.8754 AVERAGE CONTAINHENT PRESSURE I PSIA) 26.8549 AVERAGE CONTAINHENT PRESSURE I PSIG) 1R.3714 (O
(4,
!~R
'UN ELAPSED TIVE 8
34.00 CONTAINtlENT TEttPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD NILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 39.64 79.28 ETR-122 35.95 71.90 ETR-115 9.47 18.94 ETR-102 37. 56 75.12 ETR-123 36.69 73.38 ETR-116 9.07 18. 14 ETR-103 35.66 71.32 ETR-124 3?.33 74.66 ETR"117 8.89 17.78 ETR-104 35.57 71. 14 ETR-125 36.03 72.06 ETR-118 10 F 00 20.00 ETR-105 36. 00 72.00 ETR-126 36.13 ,72.26 ETR-119 8.34 16.68 ETR-106 36. 26 ?2.5'2 ETR"127 33.87 67.74 ETR-120 8.07 16.14 ETR-107 35. 84 71 '8 ETR-129 37.22 74.44 ETR-121 8.49 16 '8 ETR-108 35.85 71.70 ETR-130 35.65 71.30 ETR-109 35. 62 71.24 ETR-1'3l 33.92 67.84 ETR-110 35.39 70.78 ETR-132 37.71 75.42 ETR"111 35.56 71.12 ETR-134 36.68 73.36 ETR-112 35.60 71.20 ETR-135 36.65 73.30 ETR-114 34.87 69.74 ETR"136 36.70 73.40 ETR-128 . 36.90 73.80 ETR-137 36.38 72.76 ETR-133 34. 38 68.76 ETR-138 36.75 73.50 ETR-113 37.50 75.00 ETR-139 33.97 67.94 ETR-140 36.77 73.54 ETR-141 37.43 74.86 ETR-142 36.29 72.58 ETR-143 37.69 75.38 ETR-144 36.00 72.00 ETR-145 41.61 83.22 ETR"146 37.17 74.34 SUttHARY OF I'lEIGHTED AVERAGE TEMPERATURES UPPER VOLUttE (DEG. F.) 72.52 LONER VOLUME (DEG. F.) 73.35 ICE CONDENSER (DEGAS Fe) 1?.lt)
UPPER VOLUME (DEG. R.) 532.22 LONER VOLUttE (DEG. R.) 533-05 ICE CONDENSER (DEG. R.) 476.08 CONTAINMENT VAPOR PRESSURE DATA Cl)ECK CONTAINMENT PRESSURES DATA CtlECK HZLLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F.) (PSIA) HANOHETER READING <PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.85 33.40 0.0937 PU-1 27.0000 26.8134 VPU-2 0.0 32.00 0.0 PU-2 26.8648 26.8636 LOltER: LONER:
VPL-1 19.80 39.22 0.1180 PL-1 0.0 0.0 VPL-2 18.61 36.e5 0.1075 PL"2 26.8461 26.8445 ICE- ICE:
VPI-1 9.36 18.42 0.0467 PI-1 26.e660 26;8651 VPZ"2 -1.10 12.20 0.0345 PI-2 26 '818 26.8805 AHBIEttT 14.4800 14.4735 AVERAGE VAPOR PRESSURES
SUMMARY
OF CORRECTED AVERAGE PRESSURES UPPER CONTAIttMENl'PSIA) 0.0937 LONER CONTAZNttENT (PSIA) 0.1128 AVERAGE UPPER PRESSURE tPSIA) 26.8385 ICE CONDENSER ( PSIA) 0.0406 AVERAGE LONER PRESSURE (PSIA) 26.8445 AVERAGE ICE CONDENSER PRESSURE [PSIA) 26.8728 AVERAGE CONTAZNHEtA PRESSURE (PSIA) 26.8519 AVERAGE CONTAZNHENT PRESSURE (PSIG) 12.3784
RUN R 9 ELAPSED TINE 34.50 CONTAZNHEttT TEHPERATURES DATA CHECK UPPER VOLUHE LOWER VOLUHE ICE CONDENSER RTD HZLLI "VOLTS DEG. F. RTD HILLI-VOLTS DEG. F~ RTD NILLI-VOLTS DEG. F.
ETR-101 39. 60 79.20 ETR-122 35.94 ?1.88 ETR-115 9. 23 18.46 ETR-102 37.55 75.10 ETR-123 36.71 73.42 ETR-116 8.92 17.84 ETR-103 35. 67 71.34 ETR"124 37.31 74.62 ETR-117 8.54 17.08 ETR-104 35. 65 71.30 ETR"125 36.04 72.08 ETR-118 9.86 19.72 ETR-105 36. 00 72.00 ETR-126 36.12 ?2.24 ETR-119 8.35 16.70 ETR-106 36. 27 72.54 ETR-127 33.88 67.76 ETR-120 8. 09 16.18 ETR-107 35.86 71.?2 ETR-129 37. 21 74.42 ETR-121 8.48 16.96 ETR-108 35.85 71.70 ETR-130 35.65 71.30 ETR-109 35.55 71.10 ETR-131 33.92 67.84 ETR-110 35.47 70.94 ETR-132 37. 71 75.42 ETR-111 35.58 71.16 ETR-134 36.72 73.44 ETR-112 35.58 71.16 ETR-135 36.62 73.24 ETR-114 34.83 69.66 ~ ETR-136 36.6? 73.34 ETR-128 36. 91 73.82 ETR-137 36.39 72.78 ETR-133 34.37 68.74 ETR-138 36.75 73.50 ETR"113 37.48 74.96 ETR-139 33.98 67.96 ETR"140 36.79 73.58 ETR-141 37.43 74.86 ETR-142 36 30
~ 72.60 ETR-143 37 68
~ 75.36 ETR"144 37.01 74.02 ETR-145 41. 60 83.20 ETR-146 37. 16 74.32 SUHHARY OF WEIGtlTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.53 LOWER VOLUHE (DEG. F. ) , 73.39 ZCE CONDENSER (DEG. Fo) 1?o 07 UPPER VOLUHE (DEG. R.) 532.23 LOWER VOLUHE (DEG. R.) 533.09 ZCE CONDENSER (DEG. R.) 476.77 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK ttILLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS [DEG. (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: F.)'3.54 UPPER:
VPU-1 16.92 0.0942 PU-1 26.9990 26.8124 VPU-2 0.0 32.00 0.0 PU-2 26.8626 26.8614 LOWER: LOWER'-
VPL-1 19.87 39.36 0. 1187 PL-1 0.0 0.0 VPL-2 18. 61 36.85 0.10?5 PL-2 26.8444 26.8428 ICE: ICE:
VPI-1 8.68 17.07 0.0438 PZ<<1 26.8640 26.8631 VPI-2 -1.17 10.94 0.0324 PI-2 26.8?99 26.8786 AHBIENT 14.4800 14 4735 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHEt)T (PSIA) 0.0942 LOWER CONTAZtNENT (PSIA) 0.1131 AVERAGE UPPER PRESSURE (PSZA) 26.8369 ICE CONDENSER (PSIA) 0.0381 AVERAGE LOWER PRESSURE (PSIA) 26.8428 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8708 AVERAGE CMTAINttEt)T PRESSURE (PSIA) 26.8502 AVERAGE CONTAINttENT PRESSURE (PSIG) 12.3767
RUN ~R ELAPSED TINE 10 35.00 CONTAINIENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. RTD HILLI-JOLTS DEG. F.
ETR-101 39. 59 79.18 ETR-122 35.92 71.84 ETR-115 9.03 18.06 ETR-102 37.54 ?5.08 ETR-123 36.72 73.44 ETR-116 8.92 17.84 ETR"103 35. 67 71.34 ~ ETR-124 37.31 74.62 ETR-117 8.55 17. 10 ETR-104 35. 61 71.22 ETR-125 36.04 72.08 ETR-118 9.85 19,70 ETR-105 35.99 ?1.98 ETR-126 36.13 72.26 ETR-119 8.35 16.70 ETR-106 36. 27 72.54 ETR-127 33.89 6?.78 ETR-120 8.09 16.18 ETR" 107 35. 88 71.76 ETR-129 37. 20 74.40 ETR-121 8.44 16.88 ETR"108 35.85 71.70 ETR-130 35.65 71.30 ETR"109 35.67 71.34 ETR-131 33.92 67.84 ETR-110 35.49 70.98 ETR-132 37.71 ?5.42 ETR-ill 35.58 71.16 ETR-134 36.75 73.50 ETR-112 35.57 71.14 ETR-135 36.60 73.20 ETR"114 34.87 69.74 ETR-136 36.65 73.30 ETR-128 36. 92 73.84 ETR-137 36.35 72.70 ETR-133 34. 37 68.74 ETR-138 36.75 73.50 ETR"113 3?.49 74.98 ETR-139 33.96 67.92 ETR-140 36.79 73.58 ETR-141 37.42 74.84 ETR-142 36.30 72.60 ETR-143 37.68 75.36 ETR-144 37.00 74.00 ETR-145 41.61 83.22 ETR-146 ~ 37.17 74.34 SUHHARY OF NEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 72.54 LONER VOLUHE (DEG. F. ) 73.38 ICE CONDENSER (DEG. F<<) 17.02 UPPER VOLUHE (DEG. R. ) 532.24 LO)KR VOLUHE (DEG. R. ) 533.08 ICE CONDENSER (DEG. R.) 476.72 CONTAINHENT VAPOR PRESSURE DATA CltECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROHETER VOLTS [DEG. F. ) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER-'U-1 VPU-1 16.84 33.38 0.0936 26.9980 26.8114 VPU-2 0.0 32.00 0.0 PU-2 26.8618 26.8606 LONER: LONER:
VPL-1 19. 94 39.50 0.1193 PL"1 0.0 0.0 VPL-2 18.63 36.89 0.1077 PL"2 26.8436 26.8420 ICE: ICE:
VPI-1 7. 77 15.28 0.0401 PI-1 26.8632 26.8623 VPI-2 -1.03 13.46 0.0367 PI-2 26.8789 26.8776 At)DIENT 14.4800 14.4735 AVERAGE VAPOR PRESSURES OF CORRECTED AVERAGE PRESSURES UPPER CONTAINttENT (PSIA) 0.0936 LONER COtA'AINttEtA'PSIA) 0.1135 AVERAGE UPPER PRESSURE (PSIA) 26.8360 ICE CONDENSER (PSIA) 0.0384 Q)-'UHHARY AVERAGE AVERAGE LONER PRESSURE (PSIA)
ICE CONDENSER PRESSURE (PSIA) 26.8420 26.8699 AVERAGE COttTAINtlENT PRESSURE OPSIA) 26.8493 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.3758
<<'g
ELAPSED TltlE 35.50 CONTAINNEtfT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F ~ RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 39.59 79.18 ETR-122 35.97 71.94 ETR-115 9.11 18.22 ETR-102 37.54 75.08 ETR-123 36.73 73.46 ETR-116 9.04 18.08 ETR-103 35. 69 71.38 ETR-124 37.27 74.54 ETR-117 8.80 17.60 ETR-104 35. 60 71. 20 ETR-125 36.04 72.08 ETR-118 10.84 21. 68 ETR-105 36. 00 72. 00 ETR-126 36.12 72.24 ETR-119 8.38 16. 76 ETR-106 36. 26 72.52 ETR-127 33.8S 67.76 ETR-120 8. 08 16. 16 ETR-107 35.86 71. 72 ETR-129 37.20 74,40 ETR-121 8.39 16.78 ETR-108 35.82 71.64 ETR-130 35.65 71.30 ETR" 109 35.55 71.10 ETR-131 33.91 , 67.82 ETR-110 35.60 71.20 ETR-132 37.71 75.42 ETR-ill 35.58 71. 16 ETR-134 36.77 73.54 ETR-112 35.57 71.14 ETR-135 36.62 73.24 ETR-114 34.86 69.72 ETR-136 36.'63 73.26 ETR-128 36. 94 73.88 ETR-137 36.34 72.68 ETR-133 34,38 68.76 ETR"138 36.76 73.52 ETR-113 37.45 74.90 ETR-139 33.96 67.92 ETR-140 36.79 73.58 ETR-141 37.44 74.88 ETR-142 36.30 72.60 ETR-143 37.68 75.36 ETR-144 37.01 74.02 ETR-145 41.61 83.22 ETR-146 37.18 74.36 SUttHARY OF HEIGHTED QVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.52 LONER VOLUHE lDEG. ) 73.39 CONDENSER (DEG. F. ) 17.21 UPPER VOLUHE lDEG. R. ) 532.22 LONER VOLUHE lDEG.
F ~
R. ) 533.09'CE ICE CONDENSER (DEG. R. ) 476.91 CONTAINHEN) VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- OEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS <DEG. F.) 4PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.89 33.48 0. 0940 PU-1 26.9950 26.8085 VPU-2 0.0 32.00 0.0 PU-2 26.8591 26.8579 LONER: LONER:
VPL-1 20 ~ 02 39.66 0.1201 PL-1 0.0 0.0 VPL"2 18.63 36.89 0.10?7 PL" 2 26.8405 26.8389 ICE: ICE:
VPI-1 7.52 14.79 0.0392 PI-1 26.8600 26.8591 VPI-2 -1.12 11.84 0.0338 PI-2 26.8756 26.8743 AttSIEttT 14.4800 14.4735 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTEO AVERAGE PRESSURES UPPER CONTAINHEttT (PSIA) 0.0940 LONER CONTAIM1ENT (PSIA) 0.1139 AVERAGE UPPER PRESSURE (PSIA) 26.8332 ICE CONDEttSER lPSIA) 0.0365 AVERAGE LONER PRESSURE (PSIA) 26.8389 AVERAGE ICE COttDENSER PRESSURE (PSIA) 26.866?
AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8463 AVERAGE CONTAIt4HENT PRESSURE (PSIG) 12.3727
( ~R RUN ELAPSED TIHE 12 36.00 Fy CONTAINHENT TEHPERATURES DATA CtlECK UPPER VOLUHE LONE R VOLUHE ICE CONDENSER RTD NIL LI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLZ-VOLTS DEG. F.
ETR-101 39.59 ?9.18 ETR-122 35. 98 71.96 ETR-115 8.97 17. 94 ETR-102 37. 52 75.04 ETR-123 36.69 ?3.38 ETR"116 8. 92 17.84 ETR-103 35. 68 71.36 ETR-124 37.31 74.62 ETR-11? 8.57 17. 14 ETR 104 35.60 71.20 ETR-125 36.02 72.04 ETR-118 10. 18 20.36 ETR-105, 35.99 71.98 ETR-126 36.12 72.24 ETR"119 - 8.38 16 '6 ETR-106 36.26 72.52 ETR-127 33.91= 6?.82 ETR-120 8. 08 16.16 ETR-107 35. 87 71.74 ETR-129 37.23 74.46 ETR-121 8.40 16.80 ETR-108 35.82 71.64 ETR"130 35.67 71.34 ETR-109 35. 63 71.26 ETR-131 33.91 67.82 ETR-110 35.60 71.20 ETR"132 37.71 75.42 ETR-111 35.57 71.14 ETR-134 36 '3 73.46 ETR-112 35.62 71. 24 ETR-135 36.67 73.34 ETR-114 34.90 69.80 ETR-136 36.67 73.34 ETR-128 36. 93 73.86 ETR-137 36.37 72.74 ETR-133 34. 37 68.74 ETR-138 36.76 73.52 ETR-113 37.49 74.98 ETR-139 33.98 6?. 96 ETR-140 36.79 73.58 ETR-141 37.43 74.86 ETR-142 36.31 72 '2 ETR-143 37. 68 75.36 ETR-144 37. Ol 74.02 ETR-145 41.61 83 '2 ETR"146 37.. 18 74.36 SUHHARY OF NEZGIITED AVERAGE TEHPERATURES UPPER VOLWE (DEG. F.) 72.53 LONER VOLUHE (DEG. F.) 73.41 " ICE CONDENSER (DEG. F.) 17.05 UPPER VOLWE (DEG. R.) 532.23 LONER VOLWE (DEG. R.) 533.11 ICE CONDENSER (DEG. R.) 476.75 COI(TAINHEI(T VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLZ- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROHETER VOLTS (DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.90 33.50 0.0941 PU-1 ~ 26.9910 26.8045 VPU-2 0.0 32.00 0.0 PU-2 26.8562 26.8550 Lot'IER: LONER:
VPL-1 20. 09 39.80 0.1207 PL-1 0.0 0.0 VPL-2 18.62 36.87 0.1076 PL-2 26.8374 26.8358 ICE: ICE:
VPI-1 7.61 14.96 0.0395 PI-1 26.8573 26.8564 VPI-2 -1.13 11.66 0.0335 PI"2 26.8723 26.8710 AHBIENT 14.4800 14.4735 AVERAGE VAPOR PRESSURES SWARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAZNHENT (PSIA) 0.0941 LONER CONTAINHENT (PSIA) 0. 1141 AVERAGE UPPER PRESSURE (PSIA) 26.8298 ICE CONDENSER (PSIA) 0.0365 AVERAGE LONER PRESSURE (PSIA) 26.8358 AVERAGE ZCE CONDENSER PRESSURE (PSIA) 26.8637 AVERAGE COI(TAINHENT PRESSURE (PSIA) 26.8431 AVERAGE CONI'AINHENT PRESSURE (PSIG) 12.3696 Qg
RUN ~RTItlE 13
('
ELAPSED 36.50 =
CONTAIt(MENT TEMPERATURES DATA Cl(ECK UPPER VOLUHE LO((ER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 39.54 79.08 ETR-122 35.94 71.88 ETR-115 8.89 17.78 ETR-102 37.50 75.00 ETR-123 36.71 '73 42 ETR-116 8.85 17.70 ETR-103 35.67 71.34 ETR-124 37.31 74. 62 ETR-117 8.48 16.96 ETR-104 35. 59 71.18 ETR-125 36.05 72. 10 ETR-118 10.09 20.18 ETR"105 35. 98 71 '6 ETR-126 36.12 72.24 ETR-119 8.36 16.72 ETR-106 36. 25 72.50 ETR-127 33.92 67.84 ETR-120 8. 08 16.16 ETR-107 35. 84 71.68 ETR-129 37.20 74.40 ETR-121 8.42 16.84 ETR-108 71.66 ETR-130 35.66 71.32
35. 60 71.20 ETR-131 33.92 67.84 35.83'TR"109 ETR-llo 35.48 70.96 ETR-132 37.71 75.42 ETR-111 35.57 71.14 ETR-134 36.69 73.38 ETR-112 35. 60 ?1.20 ETR-135 36.66 73.32 ETR-114 34.88 69.76 ETR-136 36.67 73.34 ETR-128 36. 95 73.90 ETR-137 36.39 72.78 ETR-133 34.36 68.72 ETR-138 36.75 73.50 ETR-113 37.46 74.92 ETR"139 33.98 67.96 ETR"140 36.79 73.58 ETR-141 37.43 74.86 ETR"142 36.31 72.62 ETR"143 37.68 75.36 ETR-144 36.99 73.98 ETR-145 41.62 83.24 ETR-146 37.17 74.34 SUHt(ARY OF t(EIGI(TED AVERAGE TEHPERATURES UPPER VOLUME (DEG. F.) 72.50 LONER VOLUME (DEG. F. ) 73.40 ICE CONDENSER (DEG. F.) 17.00 UPPER VOLUME (DEG. R.) 532.20 LONER VOLUt(E (DEG. R.) 533.10 ICE CONDEttSER (DEG. R. ) 476.70 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINMENT PRESSURES DATA CHECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F.) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16. 88 33.46 0.0939 PU-1 26.9900 26.8035 VPU-2 0.0 32. 00 0.0 PU-2 26.8544 26.8532 LONER: LONER:
VPL-1 20.17 39.96 0.1215 PL-1 0.0 0.0 VPL-2 18.61 36.85 0.1075 PL"2 26;8359 26.8343 ICE: ICE:
VPI-1 7. 94 15.62 0.0408 PI-1 26.8559 26.8550 VPI-2 -1.10 12.20 0.0345 PI-2 26.8718 26.8705 A)SIENT 14.4800 14.4735 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIN((ENT (PSIA) 0.0939 LONER CONTAINMENT (PSIA) 0.1145 AVERAGE UPPER PRESSURE (PSIA) 26.8284 ICE CONDENSER (PSIA) 0.0376 AVERAGE LONER PRESSURE (PSIA) 26.8343 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8627 AVERAGE CONTAIt(MENT PRESSURE (PSIA) 26.8418 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3683
.Se.
ELAPSED TIHE 37.00 Py COt(TAINHENT TEt(PERATURES DATA CHECK UPPER VOLUHE LONE R VOLUME ICE COt(DENSER RTD I(ILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG.
ETR-101 39.55 79.10 ETR-122 35.94 71.88 ETR-115 9.16 18.32 ETR-102 37.49 74.98 ETR-123 36.70 73.40 ETR-116 8. 75 17.50 ETR-103 35. 65 71.30 ETR-124 37.32 74.64 ETR-117 8. 39 16. 78 ETR-104 35.60 71.20 ETR-125 36.03 72.06 ETR-118 9.61 19.22 ETR-105 35. 96 71.92 ETR-126 36.12 72.24 ETR-119 8.37 16.74 ETR-106 36. 24 72.48 ETR-127 33.91 67.82 ETR-120 8. 07 16. 14 ETR-107 35.83 71.66 ETR-129 37.22 74.44 ETR"121 8.41 16.82 ETR-108 35.83 71.66 ETR-130 35.67 71.34 ETR-109 35.56 ?1.12 ETR-131 33.91 67.82 ETR-110 35.47 70.94 ETR-132 37.71 75.42 ETR-111 35.56 71.12 ETR-134 36.75 73.50 ETR-112 35.60 71.20 ETR-135 36.59 73.18 ETR-114 34.84 69. 68 ETR"136 36.68 73.36 ETR-128 36.97 73.94 ETR-137 36.39 72.78 ETR-1'33 34.36 68.72 ETR"138 36.75 73.50 ETR-113 37.45 74.90 ETR-139 33.99 67.98 ETR-140 36.80 73.60 ETR-141 37.44 74.88 ETR"142 36.31 72.62 ETR-143 37.69 75.38 ETR-144 37.00 74.00 ETR-145 41.62 83.24 ETR-146 37.18 74.36
SUMMARY
OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUt(E (DEG. F.) 72.48 LOt(ER VOLUME (DEG. F. ) 73.40 ICE CONDENSER (DEG. F ~ ) 16 ~ 94 UPPER VOLUt(E (DEG. R.) 532.18 LOt(ER VOLUHE (DEG. R. ) 533.10 ICE CONDENSER (DEG. R.) 476.64 CONTAINMENT VAPOR PRESSURE DATA Cl(ECK CONTAINMENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED t(YGROHETER VOLTS (DEG. F ~ ) (PSIA) t(ANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16. 93 33.56 0.0943 PU-1 26.9890 26.8025 VPU-2 0.0 32.00 0.0 PU-2 26.8532 26.8520 LO((ER: LONER:
VPL-1 20.23 40.08 0.1220 PL-1 0.0 0.0 VPL-2 18.64 36.91 0.1078 PL-2 26.8348 26.8332 ICE: ICE:
VPI-1 7.85 15.43 0.0404 PI-1 26.8546 26.8537 VPI-2 -1.13 11.66 0.0335 PI-2 26.8714 26.8701 AHBIENT 14.4800 14.4735 AVERAGE VAPOR PRESSURES SUMHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIt(MENT (PSIA) 0.0943 LONER CON)AINHENT (PSIA) 0.1149 AVERAGE UPPER PRESSURE (PSIA) 26.8273 ICE CONDENSER (PSIA) 0.0370 AVERAGE LONER PRESSURE (PSIA) 26.8332 I AVERAGE ICE CONDEt(SER PRESSURE (PSIA) 26.8619 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8408 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3673 e
RUNNER 15
'i ELAPSED TIHE 37.50 CONTAZNHEt(T TEMPERATURES DATA CtlECK UPPER VOLUME LONER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 39.50 79.00 ETR-122 35.98 ?1.96 ETR-115 9. 16 18.32 ETR-102 37.48 74.96 ETR-123 36.72 73.44 ETR-116 8.77 17.54 ETR-103 35.67 71.34 ETR-124 37.31 74.62 ETR"117 8.50 17.00 ETR-104 35. 59 71.18 ETR=125 36.07 72.14 ETR "118 9. 71 19.42 ETR-105 35.98 71.96 ETR"126 36.13 72.26 ETR-119 8.36 16.72 ETR-106 36.24 72.48 ETR"12? 33.87 67.74 ETR-120 8.0? 16.14 ETR-107 35.86 71.72 ETR-129 3?.24 74.48 ETR"121 8 40
~ 16.80 ETR-108 35.83 71. 66 ETR-130 35.66 71.32 ETR-109 35.58 71.16 ETR-131 33.90 67.80 ETR"110 35.49 70.98 ETR-132 37.71 75.42 ETR-ill 35.57 71.14 ETR-134 36.69 73.38 ETR-112 35.59 71.18 ETR-135 36.63 73.26 ETR-114 34.84 69.68 ETR-136 36.69 73.38 ETR "128 36. 95 73.90 ETR-137 36.38 72.76 ETR-133 34.37 68.74 ETR"138 36.74 73.48 ETR-113 37.48 74.96 ETR-139 33.98 67.96 ETR-140 36.81 73.62 ETR-141 37.44 74.88 ETR-142 36.31 72.62 ETR-143 37.69 75.38 ETR-144 37. Ol 74.02 ETR-145 41.63 83.26 ETR"146 37.18 74.36 SUHHARY OF I'IEIGIITED AVERAGE TEHPERATURES UPPER VOLUME (DEG. F. ) 72.48 LOHER VOLUME (DEG. F.) 73.41 ICE CONDENSER (DEG. ) 16.97 UPPER VOLUtlE (DEG. R.) 532.18 LOHER VOLUME (DEG. R.) 533.11 ICE CONDENSER (DEG.
F ~
R.) 476 '7 CONTAINHENt VAPOR PRESSURE DATA CIIECK COt(TAZNHENT PRESSURES DATA CIIECK HZLLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROtIETER VOLTS (DEG. F. ) (PSIA) HANOHETER READING (PSZA) READING (PSZA)
UPPER: UPPER:
VPU-1 16. 91 33.52 0. 0942 PU-1 26.9870 26.8006 VPU-2 0.0 32.00 0.0 PU-2 26.8503 26.8491 LOHER: LONER:.
VPL-1 20.31 40.24 0.1228 PL-1 0~0 0.0 VPL-2 18.62 36.87 0.1076 PL-2 26.8321 26.8305 ICE: ICE'I-1 VPZ-1 7.83 15.41 0.0404 26.8522 26.8513 VPI-2 -1.14 11.48 0.0332 PI-2 26.8669 26.8656 AHDIENT 14.4700 14.4636 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAIn(Et(T (PSIA) 0.0942 LOt(ER CONTAZNIIENT (PSIA) 0.1152 AVERAGE UPPER PRESSURE (PSIA) 26.8248 ZCE CONDEt(SER (PSIA) 0.0368 AVERAGE LOHER PRESSURE (PSIA) 26.8305 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8584 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8379 AVERAGE CONTAINtIENT PRESSURE (PSIG) 12.3743
.r?
(~~V RUN ~R ELAPSED TIHE 16 38.50 CONTAINHENT TEl(PERATURES DATA Ct(ECK UPPER VOLUHE LOHER VOLUHE ICE CONDENSER RTD HILLZ-VOLTS DEG. F. RTD HILLZ-VOLTS DEG. F. RTD HILLI-VOLTS DEG. P.
ETR-101 39.52 79.04 ETR-122 35.97 71.94 ETR"115 9. 04 18.08 ETR-102 37.45 74.90 ETR-123 36.71 73.42 ETR-116 8. 96 17.92 ETR-103 35. 67 71.34 ETR-124 37.31 74.62 ETR-117 8.45 16.90 ETR-104 35. 60 71.20 ETR-125 36.07 72.14 ETR"118 9.83 19.66 ETR-105 35. 96 71.92 ETR-126 36.12 72.24 ETR"119 8.38 16.?6 ETR-106 36. 22 72.44 ETR"127 33.87 67.74 ETR-120 8. 10 16.20 ETR-107 35.85 71.70 ETR-129 37.23 74.46 ETR-121 8. 39 16.?8 ETR-108 35.79 71.58 ETR-130 35.65 71.30 ETR-109 35. 57 71.14 ETR-131 33.92 67.84 ETR-110 35.50 71.00 ETR-132 37.72 75.44 ETR-ill 35.57 71.14 ETR-134 36.86 73.72 ETR-112 35. 61 71.22 ETR-135 36.65 73.30 ETR-114 34.81 69.62 ETR-136 36.66 73.32 ETR-128 36. 98 73.96 ETR-137 36.38 72.76 ETR-133 34. 38 68.76 ETR-138 36.75 73.50 ETR-113 37.41 74.82 ETR-139 34.01 68.02 ETR-140 36.81 73.62 ETR-141 37.45 7f. 90 ETR"142 36.32 72.64 ETR-143 37.69 75.38 ETR-144 37.00 . 74.00 ETR-145 41.63 83.26 ETR-146 37.20 74.40 SUHHARY OF NEIGt(TED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.45 LONER VOLUHE (DEG. F.) 73.44 ICE CONDENSER (DEG. F.) 17.01 UPPER VOLUHE (DEG. R.) 532.15 LOHER VOLUI(E (DEG. R.) 533.14 ICE CONDENSER (DEG, R.) 476.71 CONTAIt(HEt(T VAPOR PRESSURE DATA CIIECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS (DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.33 32.36 0.0899 PU-1 26.9840 26.7976 VPU-2 0.0 32.00 0.0 PU-2 26.8475 26.8463 LONER- LOHER-VPL-1 20 47 40.56 0.1243 PL-1 0.0 0.0 VPL-2 18.64 36. 91 0.1078 PL-2 26.8293 26.827?
ICE: ICE:
VPZ-1 9.25 18.21 0.0463 PZ-1 26.8493 26.8484 VPI-2 -1.22 10.04 - 0.0309 PI-2 26.8636 26.8623 AHBIENT 14.4600 14.4537 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINt(ENT (PSIA) 0.0899 LONER CONTAIN((ENT (PSZA) 0.1160 AVERAGE UPPER PRESSURE (PSIA) 26.8220 ZCE CONDEt(SER (PSIA) 0.0386 AVERAGE LONER PRESSURE (PSIA) 26.8277 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8554 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8350 AVERAGE CONTAINHEt(T PRESSURE (PSIG) 12.381<1
Fm RUN ~R 17 ELAPSED TIHE 39.00 CONTAIttHENT TEHPERATURES DATA CHECK UPPER VOLUHE LOHER VOLUHE ICE CONDENSER RTD ETR-101 ETR-102 HILLI-VOLTS DEG. F.
39.46 37.44 78.92 74.88 RTD ETR-122 ETR-123 t (I LLI-VOLTS DEG. F.
35.96 36.70 71.92 73,4io RTD ETR" 115 ETR<<116 HILLI-VOLTS DEG. Fi 98 8.91
17. 96 17.82 ETR-103 35. 66 71.32 ETR-124 37.34 74.68 ETR-117 8.62 17.24 ETR-104 35.59 71.18 ETR-125 36.09 72.18 ETR-118 10.73 21.46 ETR-105 35.96 71.92 ETR-126 36.13 72.26 ETR"119 8.38 . 16.76 ETR-106 36. 23 72.46 ETR-127 33.90 67.80 ETR-120 8. 08 16. 16 ETR-107 35.85 71.70 ETR-129 37.25 74.50 ETR-121 8.35 16.70 ETR-108 35.81 71.62 ETR-130 35.66 71.32 ETR-109 35.56 71.12 ETR-131 33.91 67.82 ETR-110 35.42 70.84 ETR-132 37.72 75.44 ETR-111 35.56 71.12 ETR-134 36.71 73 <42 ETR-112 35.54 71.08 ETR-135 36.65 73. 30 ETR-114 34.87 69.74 ETR-136 36.?0 73.40 ETR-128 36.95 73.90 ETR-137 36.40 72.80 ETR"133 34 ~ 37 68.74 ETR-138 36.74 73.48 ETR-113 37.44 74.88 ETR-139 34.00 68.00 ETR-140 36.80 73.60 ETR-141 37.46 74.92 ETR-142 36.32 72.64 ETR-143 37.69 75.38 ETR-144 37.01 74.02 ETR-14i5 41.64 83.28 ETR-146 37.18 74.36 STANNARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 72.45 LONER VOLUt(E (DEG. F.) 73.43 ICE CONDENSER (DEG. F.) 17.12 UPPER VOLUHE (DEG. R.) 532.15 LONER VOLUHE (DEG. R.) 533.13 ICE CONDENSER (DEG. R. ) 476.82 CONTAINHENT VAPOR PRESSURE DATA Ct(ECK CONTAIt(HENT PRESSURES DATA CHECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS (DEG. F. ) (PSIA) HANOHETER READIt(G (PSIA) READING (PSIA)
UPPER< UPPER(
VPU-1 16.43 32.56 0.0906 PU-1 26.9810 26 '946 VPU-2 0.0 32.00 0.0 PU-2 26.8444 26.8432 LOHERi LONER(
VPL-1 20.59 40.80 0.1255 PL-1 0.0 0.0 VPL"2 18.44 36.51 0.1061 PL-2 26.8262 26.8246 ICEi ICE VPI-1 8.18 16.08 0. 0417 PI-1 26.8460 26.8451 VPI-2 -1.33 8.06 0.0280 PI-2 26.8610 26.8597 AHBIENT 14.4700 14.4636 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0906 LONER CONTAINHENT (PSIA) 0.1158 AVERAGE UPPER PRESSURE (PSIA) 26.8189 ICE CONDENSER (PSIA) 0.0349 AVERAGE LONER PRESSURE (PSIA) 26.8246 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8524 AVERAGE CONTAIN(TNT PRESSURE (PSIA) 26.8320 AVERAGE COt(TAINHENT PRESSURE (PSIG) 12.3684 d'g>
/<i'-'))
RUN ~R ELAPSED TIHE 18 39.50 CONTAIt(HEt(T TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOI.TS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 39.45 78.90 ETR-122 35.97 71.94 ETR"115 8.86 17. 7R ETR-102 37.4R 74.84 ETR"123 36.?4 73.48 ETR-116 8.83 17. 66 ETR-103 35.6R 71.24 ETR-124 37.R9 74.58 ETR-117 8".43 16.86 ETR-104 35. 59 71.18 ETR-125 36.09 72.18 ETR" 118 10. 00 20.00 ETR-105 35. 93 71.06 ETR-126 36.13 72.26 ETR-119 8.38 16.76 ETR"106 36.21 72.42 ETR-127 33.91 67.82 ETR" 120 8. 05 16.10 ETR-107 35. 82 71.64 ETR-129 37.26 74.52 ETR-121 8.35 16.70 ETR-108 35.81 71.62 ETR"130 35.65 71.30 ETR-109 35. 62 71. 24 ETR"131 33.89 67.78 ETR-110 35.49 70.98 ETR-132 37.73 75.46 ETR-ill 35.56 71.12 ETR-134 36.69 ?3.38 ETR"llR 35.59 71.18 ETR-135 36.65 73.30 ETR"114 34.88 69.76 . ETR-136 36.66 73.3R ETR-128 36. 98 73.96 ETR-137 .36.38 72.76 ETR-133 34. 38 68.76 ETR-138 36.74 73 ~ 48 ETR-113 37.43 74.86 ETR-139 33.99 67.98 ETR-140 36.81 73.62 ETR"141 37.45 ?4.90 ETR-142 36.3R 72.64 ETR"143 37. 69 ?5.38 ETR-144 37.01 74.02 ETR-145 41. 62 83.24 ETR-146 37. 18 74.36 SUHHARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.43 LONER VOLUIIE (DEG. F. ) 73.41 ICE CONDENSER (DEG. F. ) 16. 94 UPPER VOLUHE (DEG. R.) 532.13 LONER VOLUHE (DEG. R.) 533.11 ICE CONDENSER (DEG. R.) 4?6.64 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS (DEG. F. ) (PSIA) HAI(OHETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.38 32.46 0.0903 PU-1 26.9780 26.7916 VPU-2 0.0 32.00 0.0 PU-2 26.8418 26.8406 LONER: LONER:
VPL-1 20.64 40.90 0.1260 PL-1 0.0 0.0 VPL-2 18.49 36. 61 0.1065 PL-2 26.8417 26.8401 ICE: ICE '-
VPI "1 8.40 16.53 0.0427 PI-1 26.8438 R6.8429 VPI-2 -1.31 8.42 0.0285 PI"2 26.8601 R6.8588 AHBIENT 14.4700 14.4636 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0903 LOt(ER COt(TAINHENT ( PSIA) 0. 1162 AVERAGE UPPER PRESSURE (PSIA) 26.8161 ICE CONDENSER (PSIA) 0.0356 AVERAGE LONER PRESSURE (PSIA) 26.8401 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8509 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8357 AVERAGE CONTAIWHENT PRESSURE (PSIG) 12.3721 O
RUN ~R El.APSED TINE 19 40.00 COt(TAINHENT TEHPERATURES DATA CIIECK UPPER VOLUHE LOWER VOLUHE ICE CONDENSER RTO NILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTO HILLI-VOLTS DEG.
ETR-101 39.41 78.82 ETR-122 35.98 71.96 ETR-115 8.84 17. 68 ETR-102 37.40 74.80 ETR-123 36.72 73.44 ETR"116 8.60 17.20 ETR-103 35. 61 71.22 ETR-124 37.35 74.70 ETR"117 8.22 16.44 ETR-104 35.58 71.16 ETR-125 36 F 07 72.14 ETR-118 9.54 19.08 ETR-105 35.91 71.82 ETR-126 36.15 72.30 ETR-119 8.38 16.76 ETR-106 36.20 72.40 ETR-12? 33.89 67.78 ETR-120 8. 06 16.12 ETR-107 35.80 71.60 ETR-129 37.26 74.52 ETR-121 8,36 16.72 ETR-108 35. 77 71.54 ETR"130 35.66 71.32 ETR-109 35.56 71.12 ETR-131 33.90 67.80 ETR-110 35.44 70.88 ETR-132 37. 72 75.44 ETR-ill 35.56 71.12 ETR-134 36.77 73.54 ETR-112 35.54 71.08 ETR-135 36.60 73.20 ETR-114 34.87 69.74 ETR-136 36.68 73.36 ETR-128 36. 97 73;94 ETR-137 36 '6 72.72 ETR-133 34. 37 68.74 ETR"138 36.77 73.54 ETR-113 37.48 74.96 ETR-139 34.01 68.02 ETR-140 36.81 73.62 ETR-141 37.45 ?4.90 ETR-142 36.32 72.64 ETR"143 37.70 75.40 ETR-144 37.00 74.00 ETR-145 41.66 83.32 ETR-146 ~ 37.20 74.40 SUHHARY OF WEIG11TED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) ?2.40 LOWER VOLUHE (DEG. F.) 73.43 ICE CONDENSER (DEG. F.) 16.82 UPPER VOLUHE (DEG. R. ) 532.10 LOWER VOLUt(E (DEG. R.) 533.13 ICE CONDENSER (DEG. R. ) 476.52 CONTAIt(t(ENT VAPOR PRESSURE DATA CtlECK CONTAIt(HENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS (DEG. F. ) (PSIA) HA)NHETE R READING (PSIA) READING (PSIA)
UPPER: UPPER(
VPU-1 16.43 32.56 0.0906 PU-1 26.9750 26.7887 VPU-2 0.0 32.00 0.0 PU-2 26.8391 26.8379 LO1'IER: LO)IER:
VPL-1 20.70 41.02 0.1265 PL"1 0.0 0.0 VPL-2 18.51 36.65 0.1067 PL-2 26.8209 26.8193 ICE- ICE:
VPI-1 8.83 17.38 0. 0445 PI-1 26.8409 26.8400 VPI-2 "1.27 9.14 0.0296 PI-2 26.8561 26.8548 AHBIENT 14.4500 14.4437 AVERAGE VAPOR PRESSURES SN(NARY OF CORRECTED AVERAGE PRESSURES UPPER COt(TAIt(t(ENT (PSIA) 0.0906 LOWER CONTAINHENT (PSIA) 0 '166 AVERAGE UPPER PRESSURE (PSIA) 26.8133 ICE CONDENSER (PSIA) 0.0370 AVERAGE LOWER PRESSURE (PSIA) 26.8193 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8474 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8267 AVERAGE CONTAIN(1Et(T PRESSURE (PSIG) 12.3830 ei
RUN R 20 ELAPSED TIHE 40.50 CONTAIt(MENT TEHPERATURES DATA CHECK UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG.
ETR-101 39.39 78.78 ETR-122 35.98 71.96 ETR-115 9.19 18.38 ETR-102 37.39 74.78 ETR-123 36.72 73.44 ETR-116 8.67 17.34 ETR-103 35.61 71.22 ETR-124 37.33 74.66 ETR-117 8.32 16.64 ETR"104 35.56 71.12 ETR-125 36.09 72 '8 ETR-118 9. 51 19.02 ETR-105 35.88 71.76 ETR-126 36.15 72.30 ETR"119 8.38 16. 76 ETR-106 36. 20 72.40 ETR-127 33.89 67.78 ETR-120 8.05 16. 10 ETR-107 35. 79 71.58 ETR-129 37.24 74.48 ETR-121 8.35 16. 70 ETR-108 35. 78 71.56 ETR-130 35.64 71.28 ETR-109 35. 65 71.30 ETR-131 33.90 6?.80 ETR-110 35.47 70.94 ETR-132 37.73 75.46 ETR-ill 35.59 71.18 ETR-134 36.79 73.58 ETR'-112 35.52 71. 04 ETR"135 36.61 73.22 ETR"114 34.83 69.66 ETR-136 36.68 73.36 ETR-128 36.99 73.98 ETR"137 36.37 72.?4 ETR-133 34.38 68.76 ETR-138 36.77 73.54 ETR-113 37.44 74.88 ETR-139 34.02 68.04 ETR-140 36.81 ?3.62 ETR-141 -37.46 74.92 ETR-142 36.33 ?2.66 ETR-143 37. 70 75.40 ETR-144 37. Ol 74.02 ETR-145 41.66 83.32 ETR"146 37. 20 74.40
SUMMARY
OF HEIGHTED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F. ) 72.38 LONER VOLUME (DEG. F. ) 73.43 ICE CONDENSER (DEG. F.) 16.88 UPPER VOLUHE (DEG. R. ) 532.08 LONER VOLUME (DEG. R. ) 533.13 ICE CONDEt(SER (DEG. R.) 476.58 CONTAINNEtA'APOR PRESSURE DATA CllECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROMETER VOLTS (DEG. F.) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.37 32.44 0.0902 PU-1 26.9750 26.7887 VPU-2 0' 32.00 0.0 PU-2 26.8381 26.8369 LONER: LONER:
VPL"1 20.?9 41.20 0. 1274 PL-1 0.0 0.0 VPL-2 18.52 36.67 0.1067 PL-2 26.8195 26.8179 ICE: ICE:
VPI-1 8.79 17.30 0. 0443 PI-1 26.8403 26.8394 VPI-2 -1 ~ 27 9.14 0.0296 PI-2 26.8562 26.8549 AMBIENT 14.4431 14.4369 AVERAGE VAPOR PRESSURES SUHMARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0902 LONER CONTAINMENT ( PSIA ) 0.1171 AVERAGE UPPER PRESSURE (PSIA) 26.8128 ICE CONDEt(SER (PSIA) 0.0369 AVERAGE LONER PRESSURE (PSIA) 26.81?9 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8472 AVERAGE CONTAINMEt(T PRESSURE (PSIA) 26.8260 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3891
i" RUN ~R ELAPSED TIHE 21 41.00 CONTAIttHENT TEMPERATURES DATA CllECK UPPER VOLUME LOWER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS OEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 39.39 78.78 ETR"122 35.97 71.94 ETR-115 8.96 17.92 ETR-102 37. 37 ?4.74 ETR-123 36.68 73.36 ETR-116 8. 60 17.20 ETR-103 35.66 71.32 ETR-124 37.36 74.72
?lan ETR-117 8.23 16.46 ETR-104 35.59 71.18 ETR-125 36.09 72.18 ETR-118 9. 47 18.94 ETR-105 35.94 71.88 ETR-126 36.14 72.28 ETR-119 8.37 16.74 ETR-106 36. 20 72.40 ETR-127 33.92 67.84 ETR-120 8.04 16.08 ETR"107 35.82 71.64 ETR-129 37.26 74.52 ETR-121 8.34 16.68 ETR-108 35.?9 71.58 ETR-130 35.65 30 ETR-109 35.58 ?1.16 ETR-131 33.90 67.80 ETR"110 35.42 70.84 ETR-132 37.73 75.46 ETR-ill 35.56 71.12 ETR-134 36.68 73.36 ETR-112 35.54 71.08 ETR-135 36.67 73.34 ETR-114 34.87 '69.74 ETR-136 36.67 73.34 ETR-128 36. 98 73.96 ETR-137 36.34 72.68 ETR"133 34.38 68.76 ETR-138 36.74 73.48 ETR-113 37.4? 74.94 ETR-139 34.02 68.04 ETR-140 36.81 73.62 ETR-141 37.46 74.92 ETR-142 36.33 72.66 ETR-143 37.70 75.40 ETR-144 37.01 74.02 ETR-145 41.66 83.32 ETR-146 37.20 74.40 SUHHARY OF WEIGHTED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F.) 72.41 LOWER VOLUME (DEG. F.) 73.41 ICE CONDENSER tDEG. F.) 16.80 UPPER VOLUME tDEG. R.) 532.11 LOWER VOLUME (DEG. R.) 533.11 ICE CONDENSER (DEG. R.) 476.50 CONTAINMENT VAPOR PRESSURE DATA CHECK CONTAINtlENT PRESSURES DATA CHECK HILLI- DE)'I POINT VAPOR PRESSURE UNCORRECTED CORRECTED ltYGROHETER VOLTS (DEG. F. ) (PSIA) HAttOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.40 32 50
~ 0.0904 PU-1 ~ 26 '720 26 '857 VPU-2 0.0 32.00 0.0 PU-2 26.8358 26.8346 LOWER: LOWER:
VPL-1 20.94 41.50 0. 1289 PL-1 0.0 0.0 VPL"2 18.51 36.65 0.1067 PL-2 26.8179 26.8163 ICE: ICE:
VPI-1 6.32 12.42 0.0348 PI-1 26.8380 26.8371 VPI-2 -1 30
~ 8.60 0.0288 PI-2 26.8527 26.8514 AHBIENT 14.4296 14.4235 AVERAGE VAPOR PRESSURES
SUMMARY
OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0904 LOWER CONTAINMEttT t PSIA) 0.1178 AVERAGE UPPER PRESSURE (PSIA) 26.8102 ICE COttDENSER (PSIA) 0.0318 AVERAGE LOWER PRESSURE (PSIA) 26.8163 AVERAGE ICE CONDEttSER PRESSURE (PSIA) 26.8443 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8236 AVERAGE CONTAINMENT PRESSURE t PSIG) 12.4001
RUN R 22 Cy ELAPSED TIHE 41.50 CONTAINMENT TEMPERATURES DATA CllECK UPPER VOLUHE LOWER VOLUME ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F ETR-101 39.38 78.76 ETR-122 35.9? 71.94 ETR"115 8.74 17.48 ETR-102 37. 35 74.70 ETR"123 36.75 73.50 ETR-116 8.63 17.26 ETR-103 35.65 71.30 ETR-124 37.25 74.50 ETR-ll'? 8.11 16.22 ETR-104 35.59 71.18 ETR-125 36.10 72.20 ETR-118 9.43 18.86 ETR-105 35. 90 71.80 ETR-126 36.16 72.32 ETR-119 8.40 16.80 ETR-106 36.19 72.38 ETR"127 33.89 67. 78 ETR-120 8. 04 16.08 ETR"107 35.84 71.68 ETR-129 37.27 74.54 ETR-121 8. 34 16.68 ETR-108 35.80 71.60 ETR-130 35.65 71.30 ETR"109 35. 60 71.20 ETR-131 33.90 67.80 ETR-110 35.47 70.94 ETR-132 37. 74 75.48 ETR-111 35.56 71.12 ETR-134 36. 72 73.44 ETR-112 35.55 71.10 ETR-135 36.64 73.28 ETR-114 34. 90 69.80 ETR-136 36.72 73.44 ETR-128 36. 98 73.96 ETR-137 36.37 72.74 ETR-133 34.36 68.72 ETR-138 36.73 73.46 ETR-113 37.45 74.90 ETR-139 34.03 68.06 ETR-140 36.82 73.64 ETR-141 37.46 74.92 ETR-142 36.33 72.66 ETR-143 37.70 75,40 ETR-144 37.01 74.02 ETR-145 41.66 83.32 ETR-146 3'?. 20 74.40 SWARY OF WEIGI(TED AVERAGE. TEI(PERATURES UPPER VOLUME (DEG. F. ) 72.40 LOWER VOLUME (DEG. F.) 73.43 ICE CONDENSER (DEG. F.) 16.76 UPPER VOLUME (DEG. R.) 532.10 LOWER VOLUME (DEG. R. ) 533.13 ICE CONDENSER (DEG. R.) 476.46 COt(TAINHENT VAPOR PRESSURE DATA CHECK CONTAIt(MENT PRESSURES DATA CHECK HILLI- DEtl POINT VAPOR PRESSURE UNCORRECTED CORRECTED llYGROHETER VOLTS (DEG. F. ) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU"1 16.45 32.60 0.0908 PU-1 26.9690 26.7827 VPU-2 0.0 32.00 0.0 PU-2 26.8328 26.8316 Lol(ER: LOWER:
VPL-1 21.00 41.62 0.1295 PL-1 0.0 0.0 VPL-2 18.49 36.61 0.1065 PL-2 26.8153 26.8137 ICE: ICE:
VPI-1 7.29 14.32 0.0383 PI-1 26.8352 26.8343 VPI-2 -1.23 9.86 0.0307 PI-2 26.8496 26.8483 At(DIENT 14.43?3 14.4311 AVERAGE VAPOR PRESSURES SUM((ARY OF CORRECTED AVERAGE PRESSURES UPPER COt(TAINMENT LOt(ER CONTAINMENT ICE CONDENSER (PSIA)
(PSIA)
(PSIA) 0.0908 0.1180 0.0345 AVERAGE AVERAGE UPPER PRESSURE (PSIA)
LOWER PRESSURE (PSIA)
'6.8072 26.8137 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8413 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8207 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3896
RUt( ~f R 23 Fy ELAPSED TIME 42.00 CONTAINMENT TfHPERATURES DATA Cl(ECK UPPER VOLUHE LOWER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F.
ETR-101 39.36 78.72 ETR-122 35.97 71.94 ETR-115 8.69 17.38 ETR-102 37. 33 74.66 ETR-123 36.70 73.40 ETR"116 8.61 17.22 ETR-103 35. 62 71.24 ETR-124 37.33 74.66 ETR-117 8.24 16.48 ETR-104 35.55 71.10 ETR-125 36.02" 72.04 ETR-118 9. 95 19.90 ETR-105 35. 88 ?1.?6 ETR-126 36.16 72.32 ETR-119 8.37 16.74 ETR-106 36. 17 72.34 ETR-127 33.89 67.78 ETR-120 8. 02 16.04 ETR-107 35. 76 71.52 ETR-129 37. 24 74.48 ETR-121 8.34 16.68 ETR-108 35. 74 71.48 ETR"130 35.65 71.30 ETR-109 35. 64 71.28 ETR-131 33.89 67.78 ETR-110 35.50 71.00 ETR-132 37.74 75.48 ETR-ill 35.56 71.12 ETR-134 36.78 73.56 ETR-112 35.58 ?1.16 ETR-135 36.62 73.24 ETR-114 34.83 69.66 ETR-136 36.70 73.40 ETR-128 36.97 73.94 ETR"137 36.36 72.72 ETR-133 34. 37 68.74 ETR-138 36.76 73.52 ETR-113 37.46 74.92 ETR-139 34.02 68.04 ETR"140 36.8). 73.62 ETR-141 37.49 74.98 ETR-142 36.34 72.68 ETR-143 37.70 75.40 ETR-144 37.01 74.02 ETR-145 41.66 83.32 ETR-146 37. 19 74.38 SUMHARY OF WEIGHTED AVERAGE TE)IPERATURES UPPER VOLUME (DEG. F. ) 72.35 LOWER VOLUME (DEG. F. ) 73 43 ICE CONDENSER (DEG. F.) 16.82 UPPER VOLUME (DEG. R.) 532.05 LOWER VOLUME (DEG. R.) 533.13 ICE CONDENSER (DEG. R.) 476.52 COt(TAINHEt(T VAPOR PRESSURE DATA CtlECK CONTAINHEt(T PRESSURES DATA CHECK HILLI- DEW POINT VAPOR PRESSURE UNCORRECTED CORRECTED HYGROHETER VOLTS (DEG. F.) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.46 32.62 0.0908 PU-1 26.9640 26.7778 VPU-2 "0.22 28.04 0.0 PU-2 26.8281" 26.8269 LOWER: LOWER:
VPL-1 0.00 -0.00 0.0 PL-1 0.0 0.0 VPL-2 18.52 36.67 0.106? PL-2 26.8110 26.8094 ICE: ICE:
VPI-1 7.89 15.52 0.0406 PI-1 26.8310 26.8301, VPI-2 1.18 10.?6 0.0321 PI-2 26.8459 26.8446 A!SIENT 14.4276 14.4215 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0908 LOWER COt(TAIt(MENT (PSIA) 0.1067 AVERAGE UPPER PRESSURE (PSIA) 26.8024 ICE CONDENSER (PSIA) 0.0363 AVERAGE LOWER PRESSURE (PSIA) 26.8094 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8374 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8164 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.3949
g~jj/~
RUN ~R Z4 k'.
ELAPSED TINE 42.50 CONTAINHENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD NILLI-VOLTS DEG. F. RTD NIL LI-VOLTS DEG. F.
ETR-101 39.34 78.68 ETR-122 35.97 71. 94 ETR-115 8. 73 17.46 ETR-102 37.32 74.64 ETR-123 36.73 73.46 ETR-116 8.67 17.34 ETR-103 35.63 71.26 ETR-124 37.35 74.70 EQR-117 8.33 16.66 ETR"104 35.57 71.14 ETR"125 36.07 72.14 ETR-118 10. 53 21.06 ETR 105 35.92 71.84 ETR-126 36.15 ?2.30 ETR"119 8.38 16.76 ETR-106 36.17 72.34 ETR-127 33.85 67.70 ETR-120 8.03 16.06 ETR-107 35. 79 , 71.58 ETR-129 37.29 ?4.58 EQR-121 8.34 16.68 ETR-108 35. 74 71.48 ETR-130 35.65 71.30 ETR-109 35.51 71.02 ETR-131 33.89 67,78 ETR-110 35.55 71.10 ETR-132 37.74 75.48 ETR-111 35.56 71.12 ETR-134 36.78 73.56 ETR-112 35.59 71.18 ETR-135 36.67 73.34 ETR-114 34.86 69. 72 ETR-136 36.69 73.38 ETR-128 36. 98 73.96 ETR-137 36.40 72.80 ETR-133 34. $ 6 68.72 ETR-138 36.?4 ?3.48 ETR-113 37.50 75.00 ETR"139 34.03 68.06 ETR-140 36.82 73.64 ETR-141 37.48 74.96 ETR-142 36.33 72.66 ETR-143 37.?0 75.40 ETR-144 37. Ol 74.02 ETR-145 41. 65 83.3P ETR-146 37. 20 74.40 SUt(NARY OF HEIGIITED AVERAGE TEMPERATURES UPPER VOLUHE (DEG. F. ) 72.37 LONER VOLUHE (DEG. Fo) 73.45 ICE CONDENSER (DEG. F. ) 16.94 UPPER VOLUtlE (DEG. R.) 532.07 LONER VOLUHE (DEG. R. ) 533.15 ICE CONDEt(SER (DEG. R.) 476.64 COt(TAINHEHT VAPOR PRESSURE DATA CllECK CONTAINHENT PRESSURES DATA CHECK HILLI- DEH POINT VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROHETER VOLTS (DEG. F.) (PSIA) HANOHETER READING (PSIA) READING (PSIA)
UPPER'- UPPER:
VPU-1 16.48 32.66 0.0910 PU-1 26.9640 26.7778 VPU-2 -0. 20 28. 40 0.0 PU-2 26.8269 26.8257 LONER: LONER:
VPL-1 0.02 0.02 0.0 PL-1 0.0 0.0 VPL-2 18.49 36.61 0.1065 PL-2 26.8099 26.8083 ICE: ICE t VPI-1 7.26 14.27 0.0382 PI-1 26.8300 26.8291 VPI"2 -1.25 9.50 0.0301 PI-2 26.8447 26.8434 AHBIENT 14.4238 14.4177 AVERAGE VAPOR PRESSURES SUHt(ARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0910 LONER COt(TAIM(Et(T (PSIA) 0.1065 AVERAGE UPPER PRESSURE (PSIA) 26.8018 ICE CONDENSER (PSIA) 0.0341 AVERAGE LONER PRESSURE (PSIA) 26.8083 AVERAGE ICE CONDEt(SER PRESSURE (PSIA) 26.8363 AVERAGE CONTAINHENT PRE'."-(tRE (PSIA) 26.8155 AVERAGE COl(TAIM(ENT icrSS'JRE (PSIG) 12.3978 P~g'@~,($
RUHR ELAPSED TIME 43 F 00 CONTAINMENT TEMPERATURES DATA CHECK UPPER VOLUt(E LOWER VOLUHE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD MILLI-VOLTS DEG. F ~ RTD HILLZ-VOLTS DEG. F.
ETR-101 39. 32 78.64 ETR-122 36.01 ?2.02 ETR-115 8. 66 17.32 ETR-102 37.30 74.60 ETR-123 36.71 73.42 ETR-116 8. 66 17.32 ETR-103 35.63 71.26 ETR-124 37.36 74o72 ETR" 117 8. 21 16.42 ETR-104 35.57 71.14 ETR-125 36 F 10 72.20 ETR-118 9. 79 19.58 ETR-105 35.88 71.76 ETR-126 36.16 72.32 ETR-119 8.37 16.74 ETR-106 36.17 72.34 ETR-127 33.86 67.72 ETR-120 8.03 16.06 ETR-107 35. 75 71.50 ETR"129 37.27 74.54 ETR-121 8.32 16o64 ETR-108 35. 75 ?1.50 ETR"130 35.65 71.30 ETR-109 35. 63 ?1.26 ETR-131 33.89 67.78 ETR"110 35.50 71.00 ETR-132 37 '5 36.77 75.50 73.54 ETR-111 35.57 71.14 ETR-134 ETR-112 35.60 71.20 ETR-135 36.59 73.18 ETR-114 34.85 69.70 ETR"136 36.66 73.32 ETR-128 37. 01 74.02 ETR"137 36.38 72.76 ETR-133 34.39 68.78 ETR-138 36.75 73.50 ETR" 113 37.45 74.90 ETR-139 34.03 68.06 ETR-140 36.82 73.64 ETR-141 37.47 74.94 ETR-142 36.33 ?2.66 ETR-143 37. 71 75.42 ETR-144 37.01 74.02 ETR-145 41.67 83.34 ETR-146 37.20 74.40
SUMMARY
OF WEIG((TED AVERAGE TEMPERATURES UPPER VOLUME (DEG. F. ) 72.34 LOWER VOLUME (DEG. F. ) 73.43 ZCE CONDENSER (DEG. F.) 16.80 UPPER VOLUME (DEG. R. ) 532.04 LOWER VOLUME (DEG. R.) 533.13 ICE CONDENSER (DEG. R. ) 476.50 CONTAINMENT VAPOR PRESSURE DATA Ct(ECK CONTAINMENT PRESSURES DNA CHECK t(ILLI- DEH POIt(T VAPOR PRESSURE UNCORRECTED CORRECTED I(YGROHETE R VOLTS (DEG. F. ) (PSIA) MANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.48 32.66 0.0910 PU-1 26.9620 26.7758 VPU-2 -0 '0 28.40 0.0 PU-2 LOWER:
26.8260 26.8248 LOWER:
VPL-1 18.64 36.91 0.1078 PL-1 0.0 0.0 VPL-2 18.50 36.63 0.1066 PL-2 26.8090 26.8074 ICE: ZCE:
VPI-1 7. 68 15.10 0.0398 PI-1 26.8289 26.8280 VPI-2 -1. 21 10.22 0.0312 PI-2 26.8440 26.8427 AMBIENT 14.4257 14.4196 AVERAGE VAPOR PRESSURES SUt(MARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINt(Et(T (PSIA) 0. 0910 LOWER COt(TAZ((MENT (PSIA) 0.1072 AVERAGE UPPER PRESSURE (PSIA) 26.8003 ICE CONDENSER (PSIA) 0.0355 AVERAGE LOWER PRESSURE (PSIA) 26.8074 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8354 AVERAGE CONTAINMENT PRESSURE (PSIA) 26.8144 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3948
RUt( ~R ELAPSED TIHE 26 43.50 CONTAIt(HENT TEHPERATURES DATA CtlECK UPPER VOLUHE LONER VOLUHE ICE CONDENSER RTO llILLI-VOLTS DEG. F. RTD HI LLI "VOLTS DEG. F. RTD NIL LI-VOLTS DEG. F.
ETR-101 39.34 78.68 ETR-122 35. 99 71.98 ETR-115 '.81 17.62 ETR-102 37. 28 74.56 ETR"123 36. 73 73.46 ETR-116 8.50 17.00 ETR-103 35. 62 71.24 ETR-124 37.31 74.62 ETR-117 8. 06 16. 12 ETR-104 35.59 71.18 ETR-125 36.11 72.22 ETR-118 9.43 18.86 ETR-105 35. 89 71.78 ETR-126 36.16 72.32 ETR-119 8.37 16.74 ETR-106 36. 16 72.32 ETR-127 33.87 67.74 ETR-120 8.02 16.0$
ETR-107 35.79 71.58 ETR-129 37.25 74.50 ETR-121 8.31 16.62 ETR"108 35.75 71.50 ETR-130 35.65 71.30 ETR-109 35.65 71.30 ETR-131 33.91 67.82 ETR-110 35.49 70.98 ETR-132 37. 75 75.50 ETR-ill 35.56 71.12 ETR-134 36.72 73.44 ETR-112 35.60 71.20 ETR"135 36.64 73.28 ETR"114 34.86 69.72 ETR-136 36.70 73.40 ETR-128, 37.01 74.02 ETR"137 36.38 72.76 ET R-133 34. 38 68.76 ETR-138 36.76 73.52 ETR-113 37.440 74.80 ETR-139 34.05 68.10 ETR-140 36.82 73.64 ETR-141 37 4I8 ?4.96 ETR-142 36.34 72.68 ETR"143 37.71 75.42 ETR-144 37.02 74.04 ETR-145 41.66 83.32 ETR-146 37.21 74.42 SUHHARY OF HEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F.) 72.35 LONER VOLUHE (DEG. F.) 73.4I!t ICE CONDENSER (OEG. F. ) 16.71 UPPER VOLUHE (OEG. R.) 532.05 LONER VOLUHE (DEG. R.) 533.1$ ICE CONDENSER (OEG. R.) 476.41 CONTAINHENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA C(IECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED llYGROHETER 'OLTS (OEG. F. ) (PSIA) HANOHETER READItlG (PSIA) READING (PSIA)
UPPER:. UPPER:
VPU-1 16.55 32.80 0.0915 PU"1 26.9600 26.7738 VPU-2 LOHERI
-0 '2 28.04 0.0 PU-2 LONER:
26.824IO 26.8228 VPL-1 18.80 37.23 0.1091 PL-1 0.0 0.0 VPL-2 18.51 36.65 0.1067 PL" 2 26.80?5 26o8059 ICE I ICE:
VPI-1 7.?9 15.32 0.0402 PI-1 26.8270 26.8261 VPI-2 -1.20 10.40 0.0315 PI"2 26.8419 26.8406 AHBIENT 14.5920 14.5848 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHENT (PSIA) 0.0915 LONER CONTAIt(ttENT (PSIA) 0.1079 AVERAGE UPPER PRESSURE (PSIA) 26.7983 ICE CONDEttSER (PSIA) 0.0358 AVERAGE LO)(ER PRESSURE (PSIA) 26.8059 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8334 AVERAGE CONTAINHENT PRESSURE (PSIA) 26.8125 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.22?7 Q~!!
p/p, RU R 27 EL ib TIHE 44.00 CONTAIMIENT TEHPERATURES DATA CHECK UPPER VOLUHE LONER VO(JOE ICE CONDENSER RTD NIL LI-VOLTS DEG. F. RTD HILLI-VOL/S DEG. Po RTD NILLI-VOLTS DEG. F.
ETR-101 39. 29 ?8.58 ETR-122 35. 99 71, 98 ETR-115 9.01 18.02 ETR-102 37. 27 74.54 ETR"123 36.72 8.59 17.18 ETR-103 35.65 71.30 p 73.44 ETR-116 ETR-124 37.34 74.68 ETR-117 8.31 16.62 ETR-104 35.58 71.16 . ETR-12$ 36.08 ?2.16 ETR-118 9.49 18.98 ETR-105 35.90 ?1.80 ETR-l26 36.14 72.28 ETR-119 8.37 16.74 ETR-106 ETR-107 36 '5 35.80 72.30 ETI(-127 33.86 67.72 ETR-120 8. 03 16.06 71.60 ETR-129 37.27 74.54 ETR-121 8.33 16.66 ETR-108 35.75 71.50 ETR-130 35. 63 71. 26 ETR-109 35.51 74.02 ETR-131 35.89 67.78 ETR-110 35.55 71.10 ETR-132 37.75 75.50 ETR-ill 35.55 71.10 ETR"134 36.70 73.40 ETR-112 55.57 71.14 ETR-135 36.66 73.32 ETR-g~~ 34.85 69.70 ETR-136 36.65 73.30 ETR-128 37.00 74.00 ETR-137 36.39 72.78 ETR-133 34.38 68.76 ETR-138 36.77 73.54 ETR-113 37.38 74.76 ETR-139 34.06 68. 12 ETR-140 36.83 73.66 ETR-141 37.48 74.96 ETR-142 36.34 72.68 ETR-143 37.71 75.42 ETR-144 37.01 - 74.02 ETR-145 41.67 83.34 ETR-146 37.21 ?4.42 SUNRY OF NEIGIITED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72 '3 LONER VOLUIIE (DEG. F. ) 73.43 ICE CONDENSER (DEG. F.) 16.81 UPPER VOLUHE (DEG. R.) 532.03 LONER VOLUHE (DEG. R.) 533.13 ICE CONDENSER (DEG. R. ) 476.51 COIITAINHENT VAPOR PRESSURE DATA CIIECK CONTAINHEt(T PRESSURES DATA CHECK HILLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED IIYGROIIETER VOLTS (DEG. F. ) = (PSIA) HANOMETER READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.54 32 78
~ 0.0914 PU-1 26.9560 26.7698 VPU-2 "0.21 28.22 0.0 PU-2 26.8203 26.8191 LONER: LONER:
VPL"1 18.92 37.47 0.1102 PL-1 0.0 0.0 VPL-2 18.53 36.69 0.1068 PL-2 26.8041 26.8025 ICE: ICE:
VPI-1 8.08 15. 90 0.0413 PI-1 26.8234 26.8225 VPI-2 -1.32 8. 24 0.0283 PI-2 26.8388 26.8375 AHBIENT 14,4180 14.4119 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHEt(T (PSIA) 0.0914 LONER CONTAINHENT (PSIA) 0.1085 AVERAGE UPPER PRESSURE (PSIA) 26 '945 ICE CONDENSER (PSIA) 0.0348 AVERAGE LONER PRESSURE (: SIA) 26.8025 AVERAGE ICE CONDENSE:: PRESSURE (PSIA) 26.8300 AVERAGE COIITAINHENT PRESSURE (PSIA) 26.8090 AVERAGE CONTAINHENT PRESSURE (PSIG) 12.3971
RUN ~R ELAPSED TIME 28 44.50 lent CONTAINMENT TEHPERATURES DATA CHECK MILLI UPPER VOLUME LONER VOLUHE ICE CONDENSER RTD MILLI-VOLTS DEG. F. RTD "VOLTS DEG. F. RTD MILLI-VOLTS DEG. F.
ETR-101 39.30 78.60 ETR-122 35.97 71.94 ETR-115 8.78 17.56 ETR-102 37. 25 74.50 ETR-123 36. 74, ?3 48 ETR-116 8.50 17.00 ETR-103 35. 63 71.26 ETR-124 37. 30 74.60 ETR-117 8. 11 16.22 ETR-104 35. 59 71. 18 ETR-125 36.10 72.20 ETR-118 9.36 18.72 ETR-105 35.89 71.78 ETR-126 36.15 72.30 ETR-119 8.37 16.?4 ETR-106 36.14 72.28 ETR-127 33.85 67.70 ETR-120 8.03 16.06 ETR" 107 35. 77 71.54 ETR-129 37.28 74.56 ETR-121 8.32 16.64 ETR-108 35. 75 71.50 ETR-130 35.64 71.28 ETR-109 35; 60 71.20 ETR"131 33.89 67.78 ETR-110 35.47 70.94 ETR-132 37.75 75.50 ETR-ill 35.57 71.14 ETR-134 36.71 73.42 ETR-112 35.57 71.14 ETR-135 36.63 73.26 ETR"114 34.84 69.68 ETR-136 36.68 ?3.36 ETR-128 37. 01 74.02 ETR-137 36.35 72.70 ETR-133 34. 37 68.74 ETR"138 36.75 73.50 ETR"113 37.44 74.88 ETR-139 34.06 68. 12 ETR-140 36.82 73.64 ETR-141 37.48 74.96 ETR-142 36.33 72.66 ETR"143 37. 71 75.42 ETR-144 37. Ol 74.02 ETR-145 41.70 83.40 ETR-146 .37.21 ?4.42
SUMMARY
Of HEIGHTED AVERAGE TEMPERATURES UPPER VOLUHE (DEG. F.) 72.33 LOHER VOLUME tDEG. F.) 73.42 ICE CONDENSER (DEG. Fo ) 16.71 UPPER VOLUME (DEG. R. ) 532.03 LONER VOLUME tDEG. R.) 533.12 ICE CONDENSER (DEG. R.) 476.41 COttTAINMENT VAPOR PRESSURE DATA CHECK CONTAINttENT PRESSURES .DATA CHECK HZLLI- DEN POINT VAPOR PRESSURE UNCORRECTED CORRECTED
!lYGROHETER VOLTS (DEG. F. ) (PSIA) HANOMETER READING (PSIA) READING (PSZA)
UPPER: UPPER:
VPU-1 16.46 32.62 0.0908 PU-1 26.9570 26.7708 VPU"2 -0.20 28.40 0.0 PU-2 26.8203 26.8191 LONER: LONER:
VPL<<1 19. 02 37. 67 0.1110 PL-1 0.0 0.0 VPL-2 18.53 36.69 0.1068 PL-2 26.8043 26.8027 ICEt ICE:
VPZ-1 7.71 15.16 0.0399 PI-1 26.8043 26.8034 VPI"2 -1.35 7.70 0.0275 PI-2 26.8385 26,.8372 AHBIENT 14.4199 14.4138 AVERAGE VAPOR PRESSURES SUHMARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINMENT (PSIA) 0.0908 LONER CONTAIttttENT (PSIA) 0.1089 AVERAGE UPPER PRESSURE (PSIA) 26.7950 ICE CONDENSER (PSIA) 0.0337 AVERAGE LONER PRESSURE (PSIA) 26.8027 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8203 AVERAGE COttTAINMENT PRESSURE (PSIA) 26.8060 AVERAGE CONTAINMENT PRESSURE (PSIG) 12.3922
(p~
RUN ~R ELAPSED TIHE
'29 45.00 CONfAINHEtff TEHPERATURES DATA CHECK UPPER VOLUHE (.OWER VOLUHE ICE CONDENSER RTD HILLI-VOLTS DEG. F. RTD HILLI-VOLTS DEG. F. RTD ((ILLI "VOLTS DEG.
ETR-101 39.2? 78.54 ETR-122 35.97 71.94 ETR-115 8.69 F'7.38 ETR-102 37.24 74.48 ETR-123 36.75 73.50 ETR-116 8.54 17. 08 ETR-103 35.62 71.24 ETR-124 37.34 74.68 ETR-117 8. 09 16.18 ETR"104 35.58 71.16 ETR-125 36olO 72.20 ETR-118 9.42 18.84 ETR-105 35.87 71.74 ETR-126 36.16 72.32 ETR-119 8.40 16.80 ETR-106 36.13 72.26 ETR-127 33.85 67.70 ETR"120 8.03 16.06 ETR-107 35.78 71.56 ETR-129 37.29 74.58 ETR-121 8.32 16. 64 ETR-108 35.75 71.50 ETR"130 35.66 71.32 ETR-109 35.60 71.20 ETR"131 33.89 67.78 ETR-110 35.50 71.00 ETR-132 37.75 75.50 ETR-ill 35.55 71.10 ETR-134 36.66 73.32 ETR-112 35.57 71.14 ETR-135 36.64 73.28 ETR-114 34.82 69.64 ETR-136 36.69 73.38 ETR-128 37.02 74.04 ETR-137 36.40 72.80 ETR-133 34.37 68.74 ETR"138 36.75 73.50 ETR-113 37.49 74.98 ETR-139 34.08 68.16 ETR"140 36.84 73.68 ETR-141 37.49 74.98 ETR-142 36.36 72.72 ETR"143 37.71 ?5.42 ETR-144 37.02 74.04 ETR-145 41.69 83.38 ETR-146 37.21 74.42 SUHHARY OF WEIGHTED AVERAGE TEHPERATURES UPPER VOLUHE (DEG. F. ) 72.32 LOWER VOLUHE (DEG. F.) 73.44 ICE CONDENSER (DEG. F.) 16.73 UPPER VOLUHE (DEG. R.) 532.02 LOWER VOLUHE (bEG. R.) 533.14 ICE CONDENSER (DEG. R.) 476.43 CONfAItRENT VAPOR PRESSURE DATA CHECK CONTAINHENT PRESSURES DATA CHECK NILLI" DEW POINf VAPOR PRESSURE UNCORRECTED CORRECTED
! IYGROHETE R VOLTS (DEG. F. ) . (PSIA) HANOHETE8 READING (PSIA) READING (PSIA)
UPPER: UPPER:
VPU-1 16.52 32. 74 0 '913 PU-1 26 '550 26.?689 VPU-2 -0.17 28.94 0.0 PU-2 26.8188 26.8176 LOWER: LOWER:
VPL"1 19.10 37.83 0.1117 PL-1 0.0 0.0 VPL-2 18.51 36.65 0.1067 PL"2 26.8029 '6.8013 ICE: ICE:
VPI-1 8.?3 17. 19 0. 0440 PI-1 26.8219 26.8210 VPI-2 -1.23 9.86 0.0307 PI-2 26 '392 26.8379 AHSIENT 14.4083 14.4023 AVERAGE VAPOR PRESSURES SUHHARY OF CORRECTED AVERAGE PRESSURES UPPER CONTAINHEt(f (PSIA) 0.0913 LOWER COt(TAIt(WENT (PSIA) 0.1092 AVERAGE UPPER PRESSURE (PSIA) 26.7933 ICE CONDENSER (PSIA) 0.0373 AVERAGE LOWER PRESSURE (PSIA) 26.8013 AVERAGE ICE CONDENSER PRESSURE (PSIA) 26.8295 AVERAGE CONTAIt(WENT PRESSURE (PSIA) 26.8080 AVERAGE CONTAINHEtff PRESSURE (PSIG) 12.4057
JJJJJJJJJJ JJJJJJJJJJ ll ill 8888888888 888888888888 2222222222 222222222222 ll ill AAAAAAAAAA JJ JJ llll ll 88 88 88 88 22 22 22-llll ll AAAAAAAAAAAA AA AA JJ JJ ll ll 88 ~
eesssess 88 22 22 ll ll AA AA AA AA JJ JJ ll ll 88 88888888 88 22 22 ll ll AAAAAAAAAAAA AAAAAAAAAAAA JJ JJ JJ JJ ll ll 88 88 88 88 22 22 ll ll AA AA AA AA JJJJJJJJ JJJJJJ llll lll 888888888888 llllllllll 8888888888 1 1 1 222222222222 222222222222 llllllllll llllllllll AA AA AA AA AA AA DELIVER CODE - AEP 07JP %%KKX&f%%%%%%%XKXXKXXKKX%%%%3f%%%%Ã%%
EEEEEEEE NH HN DDDDDDD JOB NAHE ILRI1821 EEEEEEEE NN NN ODDDDDD
%%K% Ef NttH NN DD DD JOB NUttBER - 1821 EE HHN NN DD DD
%XWf% NttttH HN DD DD xxxwt wxwxwf PROGRAttHER -
PROBST ff ttNNH HN DD DD EEEEEEE NH NH NN DD DD ROON NUNBER 07JP EEEEEEE NN NN HN DD DD EE ttH NNttN DD DD SYSOUT CLASS -A ME%%% Ef ttN NNNN DD DD ff tII NNN DD DD PRINT TINE 2.02.03 PH EST EE 'N HNN DD DD EEEEEEEE NN NN DDDDDDD PRINT DATE - Ol OCT 84 EEEEEEEE NN HN DDDDDDD PRINT DEVICE COLUHBUS.COCO.PRIHTR3 KXKXKKXXKX%%%%%%%%%%%%%%%%%%%%%%%E%%
SUMMARY
OF TYPE OF TYPES BSrC TEST RESULTS D. C., COOK PLANT UNIT 2 - 1984
SUMMARY
OF TYPE B CONTAINMENT AIRLOCK LEAK TESTING*
D. C. COOK UNIT 2 TEST OVERALL UPPER OVERALL LOWER COMPLETION AIRLOCK LEAKAGE AIRLOCK LEAKAGE ACCEPTANCE CRITERIA DATE (SCCM) (SCCM)
September 2, 1981 45 75 <5511 SCCM January 16, 1984 900 500 March 5, 1982 520 190 September 4, 1982 650 490 March 3, 1983 1400 100 September 8, 1983 <50 <50 February 15, 1984 '0 June ll, 1984
For period from 1981 ILRT (Type A test) to 1984 ILRT
APPENDIX G TXPE B & C TESTING AUGUST 1984
~ t ~ ~
~ CA
>>oIIITOTT>>o O ~ C ~ COOK NUCLEAR PLANT UNIT NO 2 TYPE "8" AND "C" LEAK RATE TEST OF CONTAINHENT ISOLATION VALVES DURING HAR 198EI OUTAGE ~
I~
~
~W
\ rr ( (I 3I
~
~ >"Ioo
'i Yt'E "t)" ANO "C" LEAK BATE TFST OF CONTAINMENT ISOLATION VALVES DURING HAR 1984 OUTAGE'C "OATA INFORHATION'-'NPUT OATA (UNCORRE CTEO)
TEST OESCR IPT ION TEMP(F) PRESS t PS I G) LHH IND ~ LEAK~ INPUT CODE t
~
~
I CV~>>
CLV <<I wan 7 W -902 3
64.0 2 ' 165 0 '
il ? SCH-901 6 wCk-903 64 ~ 0 12.5 165 '
=
0 CUV <<I WCH-920 6 WCB-922
-SC -923 59.0 '
li 6
19 Cii~ol CUV <<3 VCR oa WCR-928 6 WCR-930 -,
SS.O
'i .
1294 iz.o
' '65 165 le5 ,
0 0.0 i)1'8 57 12 0 20 CUV <<3 WCH-929 6, WCR 931 57 ~ 0 12 ~ 0 165 0~0 27 I IIST Ril. REST WCIc=964460 - 64. 0 120 l94 0 ~ 0 IINST. HHP WFST WCR-965 6 'WCR-967 EX'CR-104 12 ' 194 0~0 32 34 LOWER VENTS IIPPER VER~5. VC~VS 4
6. VCH-204 VC~'0~2, 72 ' 12 ' 194 0 '
9)t 0~0 1 35 PKESS ~ EQUALIZATION VCH-107 6 VCtt-207 t)YUHOGEtt RETURN LINE; ECH-10 6 ECH-?0:
70 F 0 12 ' 194 60 ' 1
' 0'
'5 64 12 =- 194 EC'- 1
'.0 0'SW
~ 0 1 38 ESK-2 ECR-12 6 ECR 22 12 '
. tI4 ~ 0 194 '
39 40 41 FSK-3 ES =4 ESH-5 ECR=14 4 EC~
FCH-13 6 ECH 23 ECR"15 6 ECR 25 64 ~ 0 64 F 0 12 '
12.2 12.3 194 194 194 0
0~0 0~0 0 '
1 1
1 42 ESK-6 ECH-16 6 ECR 26 Ee~ 64 ' 12 ' 194 0~0 1 43 44 ESTI=T ES24-8 ECA=T7 C ECR-18 6 ECH 28 64 ~ 0 tz& 94 1 64 an 12 3 194 L
45
'57 58 ESH-9 GLYCOL SOPPLY GLYCOL BETUHN ECR-19 6 ECR 29 9CR" VCR"20 6 VCH-21 63 F 0 63.0 63 12~9 12
12. 0
' 194 194 o.o 0
=
31 LOWER vENT ~ SUPPLY 'CH"103 6 VCH-?03 73.0 12 ' 193 1300 0
19~5000.0 79 . i P?.
LO'ISEB CONT AIK PAHf HON HAO GAS MON ECH-33 6 ECH-35 tCR-31 6 FCR>>32 70 F 0 70,0 12 F 1 165 2500 ' 1 "116 117
='GLTCGL SGPPCT ETPANSro~~b GLYCOL RtT!!BN FXPANSION
~59 R-157 6 B-158 63,0 12.0 Iz I 165 194
' 1300,0 00 118 6300 12 F 0 194 8000 '
,I i19 POST ACC SAMPLF. HET ~
POST ACC9 S)IE)PC~E~S.C~
NS-357 7200 12 ' 165 0' .
12.5 000 165 0:0 120 POST ACCT SAMPLE SU!3FLY ECR-415 70 ' 12 ~ 0 165 250 '
122
--- CONTAIN!!ENT SAHPLING ECK-535 68 ~ 0 12.5 194 " 20 '
1?3 CON'l'AINMENT-SAf!PEING EC~3 68.0 Izz 194 "200 124 64 71 7?
7tt LOWER RHS RFTUHN FCh-36 CONT ~ SUMP TO HUT REPUEL,li*TE REFUEL CAV. ORAIN ACLUHP SAMiPLE OCB-600 6 OCR-601
~IPTT~S~P=152~ -
SF-ISV 6 S! -160 ICR-5 6 ICR-6
'70 72 an 72 F 0 "72 ~ 0 0
Ii 12 1295 12.
12 12
~93=
S le5 193 193 193
=' 0.0 0
0; 0 0
0 0 29 "
It)ST; RH; VENl SOPPCY 'FC~Ol a VC~O'I .66 0 12'0 '
30 INSTP Rt)0 VFNT ~ SUPPLY VCH-102 6 VCK-202 194 225.0
,66 ~ 0 120 u 194 360 '
70 Pw FOR HX CAY ~ SCRUB QCH-919 6 QCk-920 72 ~ 0', 12 ' 194 0 '
~
A
9 o<<oooosro99 O, C COOK NUCLEAR PLANT) UNIT NO ~ 2 TYPE "8" At<0 "C" LEAK RATE TEST OF CONTAINHENT ISOLATION VALVES DURING HAR 1984 crt DAT~HFO HATI OUTAGE'EST
¹
~ll ¹ STEt'FSCRIPTION INPUT DATA (UNCORRECTED)
TEHP(rl PRESS(PSIGI LHH INDE LEAK~ INPUT CODE 85 NITIIOGEN YO ECCUH. GCR" 19 71 ~ 0 12 ~ 5 193 0~0 61 ICE COND ~ AHU DRAIN ttDH ~ VCR-610 6 611 7390. 12 ' 193 140 ' 1
' 65 LEIOOWrs OCH-300 73 ' 12 ' 193 0~0 1 66 'ETOOwN OCR-$ 0f 7S ~ 0$ fz.o'2 193 30 ' 1 9 HCt'1 WCH-941 6 'ACR-945 54 ~ 0 ), ' 194 0~0 1 10 HCt'rl WCH-951 6 WCH-955 54 0:~ 12 ' 194 0~0 )
2 HCP ¹2 >>CH-942 a WC -946 ee.o 12 ' 194 0~0 22 RCP ¹2 WCH-952 6 'WCR 956 6690 12 ' 194 0 '
23 HCt'J WCH-943 6 WCH-941 66 ' 12 5 194 0 '
113 114 HCP tt3=ttCA=953~~CiFKT CCW TO CFQ-2 CCW TO,CEQ-2 RC~'~C~
CCH-,432 CCH-433 ei.o 68 ';
68 ~ 0 '¹ f2 '
12 '
12 '
~
194 194 194 0~0 0~0 0~0 11 98 0~0
'¹5::
1? RCt ¹4 WCH-954 6 WCR-958 6890 12 ' 193 0~0 GRAB SAtRPLF SH-4 6 SH-6 70 0 12 5 193 0 '
109 110 111
-irS 7
CPN COICS 3~CCII CCW TO CEQ-1 CCW FRVH CFQ-1 cpR-cor~~c71 CUV ¹4 CCH-430 CC CCH-431 CE-WCH-932 6 WCR-934
" 7fl.
68 68.o 68 '
90
12. 8 1295 12 1293 165 193 193 270 '
20 '
40 '
0~0 0~0 8 CUV 44 WCH-933 6 WCH-935 68.0 12 193 280 '
25 IrtST; RH. CasT wtTI=960 a 65.0 I'2.5 0 '
26 INST ~ RHG EAST WCH"961 6 WCR-963 65 ' 12 ' 194 0 '
A~OP '
'8 72.0 105 GRAB SAtsPLE SH-8 6 SH-10 ~ 12 194 090
¹1 SEA~A¹ ER C -9 6 io 65 0~0 47 HCP ¹4 SEAL WATER CS-442-4 65 ' 12 ~ 0 165 0~0 IJ RCt'2 SEAL 'WATER CS-442-2 65 ' 12 165 0~0 RCF f3 SEAl. RATER C "4 65,0, f2-',S L6s 0~0 73 HVT LEG SAHPLES NCR-105 6 NCH-106 ee.o 12 ' 194 0~0 74 PHESS ~ LIQ ~ SAHPLES NCR-107 6 NCH-108 66 ' 12 ' 194 0~0 75 STE'AH'AHPCE 71CR=ITli~c~
f5'93 0~0 1 62 CLV AND CUV DRAIN HOR OCrO-620 6 OCR-62] 73 ' 12 ~ 0 2400 '
108 Ct'N COILS 364 CCW CCW-?43-72 63 ' 12 ' 165 3250 '
3 COt ¹4 lTCR=OT2 W 63i 0 194 0~0 Ct V ¹4 WCH-913 6 WCR-915 63 ~ 0,'- 12 ' '
194 0~0 15 CLV ¹3 >>CH"908 6 WCR-910 63 ~ 0 ~
1294 194 40 '
IG 52 CClf ¹'3 RCR=9II9
~2 00 '
rtIThOGEW TO ACCUHULATORS N-loc.'3 60 12.1 165 0~0 Nl THOGFN TO PRT N-159 60.0 12 ' 165 570 '
SO=GEAR HETGHT EACTRITATOR RP7MSl" 91 53 ' 12.4 165 0~0 101 80HON INJECTION ICH-251 74 0~ 12 ' 193 700 '
102 80rtON INJECTION 'CH-250 ' :
,'4 1291 193 1850 '
TYPE ')" ANO 0~ C COOK NUCLEAR PL "C" LEAK HATE TFST Ol'ONTAINMENT ISOLATION VALVES OUHING MAR
( TE UNIT NO 2 aaaaaaaa<<a 1984 OUTAGE P
,: 0 t P
2 Wi 2"
INPUT DATA (UNCORRECTED)
TF.ST STEI DESCRIPTION TEMP IF ) PRESS <PS IG) LRH INOo LEAK~ INPUT CODE 4 Fc~n~aN~ cn 206 6 nett- 06 73 ' 1204 193 0~0 121 POST ACCT SAMPLE SUPPLY ECH"417 7000 12 F 1 165 300 '
90 CONl PRESS'LARM PPA-310 & PVA-311 74 ' 1205 193 0 '
100 CONT, PRESS'LARM PPA-312 & PPA-3 74 ~ 0 >il
12 ' 193 0 '
92 RX SUPPORTS CCW CCR-$ 57 135 '." 70.0 j,;. 1262 60 '
& CCW",
0', ;193
=
93 HX SUPPORTS CCW . CCR 455 & CCH 456 70 ~ 12 ' 193 40 '
80 NO)7TH SI I SCH ICM-260 7100 12 ' 193 0' SOUTH SI OISCH 81 87 'AFETY INJ ~ TFST LINE ICM-265 SI-171>1722194 7500 73 '
12 ~ 5 12ol 193 193 0~0 0~0 Sb Pw To PR~N%=252
'A" 57.0), 12 ' 193 0 '
I
'93
'A ' '
L 103 WELO CHANNEL PRESS ~ 1815 78 ~ 0 j. 12 0
~ Wl 1 04 ~ WELD CHANNFL PHFSS ~ 181N '- 76 0' 12 ' 193 0 '
68 '
I 0 ~
T7 CGV )E2 )ICIC-9?4 & WCR-926 i2.5 194 0 0 W' I:, 18 . CUV ))2 hCH-925 & WCH-927 68 ' 1265 194 300 '
59 RCUT HEAOFR DCR-203 DCH-207 70 ' ' '
Ni 'lCE&sVENT LEYnONN Nx CCN cc -6 o 6 0 ll 902- 67 ~ 0 6 12 12 '
194 193 300
'i 0 0
~
76 HCDT SAMPLE RCR-100 & RCR-101 6900 12 ' 193 0' 77 'HT SAMPLE OCR-202 & OCH-204 ~ 69 12 ~ 2 193 0' NY YEO 20 PET 68 ' 70 '
.'-.'TNECY Ptf 29 2~5 165 67 HCE SEAL WATER RETUHN OCM-2SO & QCM-350 69 ' 1205 193 0' 63 ' ' 110 '
EY 106 l2 107
'PN CPN COILS 2&5 CCW CPN COICS 2KB CCW=: CCR-440 COILS 2& 5 CCW CCW>>243-25 CCW-244"25 Eit.o:,,
63 ~ 0'(2,,.-'6 "
12 f2.2 12 ~ 2 165 194 165 190 '
20 '
0'
"-' I',
~O~NECS 85 96 iVITROGEN TO PRT PRESS'LARM GCR-301
.acaaEN~P-PPP-301 o
69 ~ Os
?00 72 '
12 ~ 5 2~2 193 194 0~0 r
~600'2 CONT ~ 12 194 0 YN
,i 97 9)I 55 CONT PRESS.
Cot%. PHES5.
ALARM PPP-302 ALA)I~Xi-30 CHARGING TO HEGENo HX ~ CS-321
~
7200 72 62
', 12 12 '
194 194 165 0
0 24000 '
ll CONTROL AIR TO CONT ~ 12 ' 0'
0 4 ~ 83 XCR-100 & .XCF)-101 ~ 193 0
.,l 4 CONTNO~ ~ X M- 12 4
~ 194 540 '
' 12 ' '
Wi'J 121 120 14 POST I~CO 42='LCIFN~~N POST CLV 12 ACC SAMPLE'UPPLY ACCo S~MPLE SuPPLY
)0CH-905 &
RCDT VENT HEADER "
WCR-907'0
-9 N-160 &'CR-201, ECH-4l7 ECH-416
~
64 64 6
, 62 '
~
73 ' )
0<<
12 '
22 ~
1265 1295
~93 194 194 193 194 0
0 60,0 80 '
1650 2
I 66 ' 12 F 1 165 700 0 "21 33 UPPER VENTS SUPPLY VCH 105 & VCR 205 70 ' 12 ' 193 80 ' 2 108 COILS 3&4 CCW-243-72 ' ' 2500 '
51 CPM AIR A'R~ 'EE CCW 66 6600 12 12 '
165 I 65 625 ~ 0 2
1 68 RHH RECIRC ~
'W'CH-306 ICN-305 ~
'2 0 I 12 ' 194 6000 '
69 HHR HECIRC ~ 6240 2.. 1202 194 750 '
( "d" "C" TFo52oo45252oo D ~ C ~ COOK NUCLFAR PLANT ~ Ut)IT NO ~ 2 5245555oooAFoo TYPE. AND LEAK HATE TEST OF CONTAINMENT ISOLATION VALVFS DURING MAR 1984 OUTAGE Y MCTT. DATA INFOR51ATION INPUT DATA 1UNCORRECTFD)
TEST STEP DESCRIPTION TEMP1F) PRESS(PSIG) IN'EAK ~ INPUT CODE
-I ~O".ER-CTIR~O~R.
82 AIH PART ~ RAO GAS MONR ECR-3l 6 ECR-32 ;
62 '
62 ' 12 2 '
94 194 1750 3600 2
2 117 GLYCOL HE.TLIHN EXPANSION R-157 6 H" 158 - 60 ' 12 0 194 0~0 2 50 RELIEF VALVE AEADE~D EF ~ 0, 12.5 165 30RO I II . 53 NITHOGEt) TO PRT N-159 '.
"-~j",.,'. 62)0 12 ' les 2000 ' 3 60 HCUT VENT HEADER N=160'& OCR~201 ' )P'2 12%0. 194 260 0 2 60 ~ 0 2 4 65 27000 ' 3 S3 t)l fi OGf'.t~ TO 1'RT N-159 62 ~ 0 12 ' leS 40 '
55 CHAT<GING TO HEGENA HX ~
'RC)'lL CS-321 62 ~ 0 12 AU les 750 ' 2 90 CCAS. CCW CCM-4~ .4 69 ~ 0 12 ' 193 0~0 1 89 RCP OIL CLRS ~ CCM CCM-45254545458 I, 69 ' 1252 193 5~~5li~EE~~I~
~
0~0 62 CLV At(D CUV DRAIN HDR ~ DCH-620 6 DCH-621 -" '.-" 62 12 ' 193 050 .?
t
.r I
lnl
--IOBsl 51 bOHON INJE.CT Iot1 AlK. PART ~ RAO GAS MONITOR CPN COIL'S3~CT:~ca=%3=72 AIH PART ~ RAO GAS MONITOR ICM-251 SM-1 SM-I 6
76 ~
65FO 66)O ee.
~ 0 0
o 12.O 12 '
12 le.o 1250 194 165 16S 165 20 40 23000 '
2500 booo 0
2 3
68 HHEt RECIRC 'E'CM-305- 74 ' 12 193
~
51 A~Mt'~D ~
4A M N 0 66 ~ 0 1
Ied 0~0 I)050 2 .
4 82 AIM PART ~ RAO GAS MONo ECR-31 6 ECR-32 73 ' 12+2 ~ 193 7000 ~ 0 3 79 '" LOITER CONT ~ MON, ECH-33 6 ECH-35 73 ' 12 F 0 193 26SO ~ 0 3 III BORON IlfJECTTOH: TC~5l 81.0 . 2 ' f93 40 ~ 0 3 102 BOKON ItlJECT ION ICM-.250 8050 '01 12 ' "
193 1200 ' 2 102 BORON INJECTION ICM-250 ~ 0
'I 12 ' 193 Soio 3 108 CPf) COT~~CC 6000 ' 5 I
I lna CPN COILS 364 CCH CC)t-243-72 70 ' 12 ' 165 2900 ' 6 10&
"52 82 CPN COILS 364 CC)t ATR FART. FAR GA5 RM, AIM PAHT. HAD GAS MON.
Cc)t-243-72 ECR=3I~ER=A2 ECR-31 6 ECR-32 70.0 l9 ~
72 '
'TI ~ TE.'~
1250 1254 165 f94 193 120 ~ 0 I'300.o 1250 '
7 4
5 79 LOaER Cot)T. MON. ECR-33 L ECR-35 ' .
'4 12 ' 193 - 1900 ' 4 I?5 PLANl ATR T~OHTATttcIEH~CR- I'2. 5 f0o 0~0 126 PLANT AIR TE) COt)T ~ CHECK VLV~ PA34? 73 ' 12 ' 194 4000 '
aaaaaaaaaa O ~ C ~ COOK NUCLEAH PL ~ UNIT NO ~ 2 TYPE "8" ANO "C" LEAK RATE TEST OF CONTAINHENT ISOLATION VALVES DURING NAR 1984 OUTAGE I~YE "C" DATA INTORNATION I
a
' TEST STEP' IIESCHIPTIO COWHECTEO RESULTS OF VALVF. TESTING fOLINE jNDTCATEO. CORRECTED ;. TEHPERATURE PRESSURE LRN
> .'EAKAGE "" '
LEAKAGE LEAKAGF.
fT) i 1 l CLV tel CLV sl CLV H4 WCR"900 SICk-912 WCH-902 WCH-901 & WCR-903 WCR-914 720 720 C
720 ~ 0 '..f(,' E'0 0 0~0
~ 0 0
0 '
71 '
71 ~ 0 63 '
12 '
12 ~ 5 12 '
165 165 194 CLV H4 WCH-913 & WCH-915 720 ' 0 ' 0 ' 63 ' 12 ~ 4 194 r
CUV 01 WCH-920 & WCH-922 480 ' 0 ' 0 ' 66 ' 12 ' 165 CUV II WCH"921 & WCR-.923 480 ' 0 0 0~0 63 ' 12 ' 165 Y
CUV E 4 WCR-932 & WCH-934 480 ' 0 ' 0~0 68RO 12 ' 193 8 'CUV H4 WCH"933 & WCH-935 480 ' , 280 ' 279 ' 68 ~ 0 12 ' 193' I'0 r HCP RCP Hl Nl HCP a4 WCR-941 WCH-944 WCH-945
'WCH-951 & 'WCR-955 WCH-948 A
'r '
360 360 360,0 0
0 0
0 0
0 54 '
54 ~ 0 6'
12R2 12 '
12 ~ 3 194 194 193 1? RCP H4 WCR-954 & WCH-958 360 ' , 0 ' 0 ' 68 ' 12 ' 1 3 r r ~
\
'0 "" 0 ~ C. COOK NUCLEAR P NT, UNIT NO ~ 2 >+<+>+>o>
TYPE '"8" AND "C" LEAK RATE TEST Of CONTAINMENT ISOLATION VALVES OUHING MAR 1984 OUTAGE PE E CT~AT'A iN~OATION
'COHREC'fED RESULTS Of VALVE TESTING T'EST STjl'c.SCRIPTION GUIOL INE LEAKAGE NDI CATED CORRECTEO TEMPERATURE PRESSURE LRM 1.EAKAGE , LEAKAGE 13 CLV N2 WCH-904 & WCR-906 720+0 60 ' 59 ' 62 ' 12 ' 193 0~
E .14 CLV E12 WCH-905 & WCR-907 720to )
~
80 ' 78 ' 62 ' 12 ' 193 i t 15 CLV a3 WCH-908 & 'WCR-910 720 ' 40 ' 39 ' 63 ' 12 ' 194 16 CLV s3 'WCB-909 & WCR-911 720eo '. 100 ' 99 ' 63 ' 12 ' 194 17 Cuv r2 WCH-924 & WCR-926 480 ' 0~0 0~0 68 ~ 0 12 ' 194 18 CUV s2 WCH-925 & WCR-927 480,0 300 ' 296 ~ 7 68 ' 12 ' 194 CUV s3 tiCk-928 & WCH-930 4eo.o 0~0 0~0 64 ' 12 ' 165 20 CUV a3 WCH-929 & WCR-931 480 ' 0~0 0 ' 64 ' 12 ' 165 21 RCP 112 WCH-942 & WCR-946 360 ~ 0 0~0 0 ' 66 ' 12 ' 194 22 HCP s2 PlCH-952 & WCR-956 360 ' 0~0 0~0 66 ' 12 F 1 194 23 HCP w3 tiCR-943 & WCH-947 360 ' 0~0 0 ' 66 ' 12 ' 194 24 RCP w3 WCH-953 & WCR-957 360 ' 0~0 0~0 66.0 12 ' 194
D~ C~ COOK NUCLEAR PLANTy UNIT NO ~ 2oo++o+"+++
TYf'E 'ff AND "C" LEAK RATE TESI OF CONTAINMENT ISOLATION VALVES DUHING MAR 1984 OUTAGE I
'T E !!C!'ATA INFORf!ATION h k 4
EM STE'ORRECTED RESULTS Of VALVE TESTING NE .
IqKICCCfED; COffAECTED .,TEHP&ATUIfE PRESSURE LRH LEAKAGE- .--"" LEAKAGE , 'EAKAGE:>>y .
25 INST. HNe EAST WCR-960 6 wCR-962 240 0 0 ~0 0~0 es.o l2+5 194 26 INST. HN. EAST wcR-,9el 6.wCR-963 ,
'-.. 2qo;o -,{'= o.'o 0 ~ 0'5 ' 12oS 27 INsT- Hff. wEsT wcH-9e4 6 wcR-9ee 240 ' 0 ~0 0~0 e4.o 12+5 194 INST. HH. wEST wCH-9es 6 wCH-9e7 240 ' 0~0 0~0 64 ' 12 ' 194 29 INST HN ~ VENTS 5UPPLY VCR"101 6 VCR-201 1680 ' 2?5 ~ 0 224 ' ee.o 12 ' 194 INST'H VENT SUPPLY VCR-102 6 VCR-202 1680 0 360 ' 358 ' eeeo 12 ' 194 31 LOWDC VENT ~ SUPPLY . VCR-103 6 VCH-203 2880 0 1300 ' 1303 ' 73 ' 12 ' 193 LOWEH VEIIT~ EXHo VCR-104 6 VCH-20rl 3600 ' 0~0 0,0 72 ' 12 ' 194 33 UPPEH VENT+ SUf'PLY VCH-105 6 VCH-205 3600+0 20000 ' 20018 ' 71 ' 12 ~ 0 194 80 ' 79 7. 70 ' le 2 193, UPPEH VENTS EX'CR 106 f VCH"206 2880 ' 0~0 0~0 72 ' 12 ' 194 f
35 PRFSS ~ EOI/ALIZATION VCR-107 6 VCR-207 1440 ~ 0 60 ' 60 ' 70 ' 12 ' 194 HYDROGEN RETURN LINE ECR 10 6 ECR 20 60 ~ 0 0~0 0~0 64 ~ 0 12 '
TYPE "8" AND "C" ooooee"ceo>> O~ C~
0 COOK NUCLEAR PLANT UNIT NO ~ 2 LEAK RATE TEST OF CONTAINHENT ISOLATION VALVES DURING NAR 1984 OUTAGE C eeC~OATA INFOHNAT ION COHHECTEO HESULTS OF VALVE TESTING TEST STEP ESSCR ON GUIDLINE INDICATED . .CORRECTEO TEHPERATURE PRESSURE LRM LEAKAGF. -
LEAKAGE LEAKAGE 37 ESH-1 FCH"11 6, ECR 21 eo ~ 0 0~0 0~0 'ee. O 12 ' 194 38 ESR-2 ECR-12 & ECR 22 60 F 0 0~0 0~0 64 ' 12 ' 194 ESR-3 ECR-13 6 ECR 23 eo.o 0~0 0 ' 64 F 0 12 ' 194 40 ESR-4 ECR" 14 6 ECR 24 60 ~ 0 0~0 0 ~ 0 '
'4 ' 12 ' 194 41 ESR-5 ECR-15 6, ECH 25 eo ~ 0 0 ' 0~0 64 ~ 0 12 ' 194 42 ESR-6 ECR-16 6 ECR 26 60 ' 0~0 0~0 64 ' 12 ~ 2 194 ESH-7 64 '
ECR-17 6 ECR 27 eo.o 0,0 0~0 12 ' 194 ESR-8 fCR-18 6 -FCR 28 eo.o 0~0 0 ' 64 F 0 12 ' 194 I,I 45 ESR-9 ECR" 19 6 ECR 29 eo.o 0 ' 0 ' 63 ' 12 ' 194 I
ll I
RCP Nl SEAL MATER CS-442"1 120 ' 0~0 0~0 72 ' 12 ' 165
~ ee ee 47 RCP S4 SEAL VIATFH RCP N2 SEAL )AIER CS-442-4 CS-442-2 120 120 0~0 0~0 0~0 0,0 72 72 ~
0'2 12.1 F 0 165 le5 4
D ~ C ~ COOK NUCLEAR PL 'f UNIT NO 2 000350oo0300oiio TYPE "8" AND "C" LEAN RAft'. TEST OF CONTAINHENT ISOLATION VALVES DURING HAR 1984 OUTAGE I Yl'E '5CII DATA INF OHHAT ION RESULTS Of VALVF. TESTING
'OHHECTED TEST STEP UTO~LNE ICAT D CORR T D EN]'ERASURE PRESSURE .
LEAKAGE LEAKAGE LEAKAGE 49 RCP 43 SEAL WATEH CS-442-3 120 ' 0~0 0,0 72 ' 12 ' 165
\
50 HELIE.F VALVE HEADER TO PRT 120 ' f ~~ 30 ' 2998 73 ' 12 ' 165 I
51 AIR PART ~ RAD GAS HONITOR SH-1 60 ' 62590 626 ' 73 ' 12 ~ 0 165 2300090 2295795 ' '
5'00'0.5
. 50f0.1'13
'09 '
72
~
12 12 '
165 165 110 73 12 ' 165 52 NI THullEN TO ACCUHULATORS N-102 eo,o 0~0 0~0 67 ' 12 ~ I 165 NITHDGEN TO PRT N-159 45 ~ 0 570 ' 568,4 e7 o 12 ' 165 70090 70097 73 ~ O. 1201 165 2000.0 1990.1 6990 12 ' 165 40 ~ 0 39.8 e9.o 12+2 165 34 L PHIHAHY WATER TO PRT CHARGING TO RFGEN ~ HX ~
PM-275 CS-321 180 '
180 ~ 0
70 2 9000 ~ 0
' 69 '
23977 ~ 3 75 69.u
' 12
-1290
' 165 165 750 ' 749 ~ 3 69 ' 12 ' )65
. 5e DEao wEIGHT caLIBRAT0R Npx-151-yl 30 ' 0~0 0~0 60 ' 1294 165
~ 0 I
7 GLYCOL SUPPLY VCR-lo & VCH-ll 480 ' 0~0 0 ' 63 ' 12 ' lt4 GLYCOL RFTURN VCH-20 & VCH-21 $ 8050 0~0 0~0 6300 12 ' 1 4 59 HCOT VENT HEADER OCH-203 & DCH-F07 120,0 300 ' 297 ' 70 0 12 ' 194 20 ' 12 ' 193
OOOOCICOOOCOIOOICIa P~ COOK NUCLEAR PLANTS UNIT NO ~ 2 0002000040100000000 TYPE "8" AND "C" LEAK RATE TEST OF CONTAINttENT ISOLATION VALVES DURING HAR 1984 OUTAGE tCtt KAA"~llFO~HTI CORRECTED RESULTS OF VALVE TESTING fEST STFP ~DL HE IHfffCATER COf!HkCT~D'EHPERATURE PRESSURE LHH LEAKAGE LEAKAGE , LEAKAGE 60 HCDT VEttT HEADER N-160 6 l)CR"?01 120 ~ 0 1650 ' 163994 73 ' 12>>5 194 260 ' 258 ' 62 ' 12 ' 194 61 ICE COND. AHU DRAIN HDR.-DCR-610 6 6II 300 ' ' 140 ' 139 ' 73 ' 12 ' 193 CLV DNO CUV DRAIN HDH ~ OCR-620 6 UCR-621 120 ~ 0 2400 ' 2406 ' 73 ' 12 ' 193 0 0 ~ 0' 62 ~ 0 12 ~ 0 193 63 RCDT DRlfTb HOR ~ UCIc=ZQ 07l 13; 0 12>>4 193
~ >>
Ig-- -"-- 64 CONT. SUHP TO HUl OCR=GI~KR- GQ>>0 , 0 ' 0~0
"" 72 12 ' " 193 65 CETDNTt~CR=306 73 ' 12>>l 193 66 LETDORot0 QC~O I'ED.O 30.0 30.1 73 ' 12 ' 193 RCP SEA~TE~ETDR~~5~0C33R1 toITO ~ 0 12 ~ 5 193 IIII e8
'== RHR RECIRC ~ EEO TCH=SO. 1080 891ll 6 "
0 BOUILLI ~
62;0 12,>> 19>>
A 0~0 0~0 74 ' 12 F 1 193 69 ttHR kt CIRC ~ W ~ I CH-306 1080.0 750 ' 741 AS 62 ' 12 ~ 2 194 f Pt FOR RX Cav. SCRUB OCR-919 6 OCR-920 120.0 0 ~ 0 0 ' 72 ' 12 ' 194 71 kEFUEL. WATER TO RX CAV. SF-152 t SF-154 300 ' 0 ' 0~0 72 ' 12 5 193
0 ~ C COOK NUCLEAR PL NT UNIT NO, 2>>4oooooo4 TYPE "8" ANO "C" LEA'k RA1E TESI OF CONTAINHEQT ISOLATION VALVES OURING MAR 1984 OUTAGE
'0 E
47 2
CO~RECTEO RESULTS OF VALVE TFSTING 2 TEST" STEP =DESCfHP 0 ALEE PDICXTE5 CGfQECTEO TEHPEAA/URE. PRESSURE LRH 2.
oI LEAKAGF
LEAKAGE LEAKAGE
,~
3 7? REFUEL CAY ~ ORAIN SF-159 6 SF-160 360 ' 0~0 0~0 72 ' 1295 193 73 HOT LEG SAMPLES NCR-105 6 NCR"106 60 ' b 000 0 ' 66 ' 12 ' 194 4
4',)
PRESS. '
LIO. SAMPLES NCR-107 6 Nck-108 60 ' 0~0 0 ' 66 ' 12 ' 194 75 STEAM SAMPLE NCR" 109 6 NCR-110 60 ' 0 ' 0 ' 66.0 12 ' 194 76 RCOT SAMPLE RCH-100 r RCR-101 ' 69 '
60 ~ 0 0~0 0 12 ' 193
"~ iL'I, 77 PRT SAHPLE OCR-202 6 OCR-204 60 ' OS 0 0 ' 69 ' 12 ' 193 6 78 ACCUM9 SAHPLF. ICR-S 6 ICR-6 60 ~ 0 0 ' 0 ' 72 ' 12 ' 193 I
79 LOMEM CONT ~ HON ~ ECR"33 6 ECR-35 60 ' 2500 ' 2512 ' 77 ' 12 ' 165 F 1700 0 1736,7 62 0 12 0 194 2250 ~ li 2627.6 73.0 72.0 193 L) 1900 ' 1907 ' 74 ' 12 ~ 0 193
)
TL NORTh SI OISCH. ICH-260 240 ' , 0 ' 0 ' 71 ' 12 ' 193
~ 2 SOUTH Sl OISCHo ICM-265 240 ' 0 ' 0 ' 075,0 12 ' IP3 l
5? AIR PART ~ RAO GAS HONo ECk-31 4 ECft-32 120 ' '300 ' 1308 ' 7702 12 '
1/5 0
0 3600 ' 3539 ' 62 ' 12 ~ 5 194 - 'I looo,d 1903,6 73i0 12 ~ 2 193 61 1300 ' 1306 F 1 79 ' 12 ~ 2 194 1
~ II 125000 1243 ~ 1 72 ' 1294 193 4
( O ~ C ~ COOK NUCLEAR PLANTt UNIT NOR 2 aaaaaaaaaa TYPE, "8" ANO "C," LEAK RATE TEST OF CONTAINHFNT ISOLATION VALVES OUHING HAR 1984 OUTAGE AIA IR RRA)IR(4 COHHECTEO RESULTS OF VALVE TESTING TFSl STEP INNNTeT4TE9 CORING.CTI;I~EflPERATIIRE'RESSURE 1.RH LEAKAGF. LEAKAGE I EAKAGE 63 CONTc(OL AIII TO CONT ~ XCH-100 & XCR-101 120 ' 0 ' 0 ' 70 ' 12 ' 193 I;4 CUNTHOL AIR TO CONT ~ ~ XCR-.102 & .XCR-103 120 ' " S)0 ' 531 ' 6240 12 ' 194 I
N I THOGFrl TO PHT GCH-301 4S ~ 0 0 ' 0 ' 69 0 12+5 193 u6 NITROGEN TO ACCUH ~, GCR-314 60AO 0 ' Ot0 71t0 12&5 193 SAFE TY INJ ~ TEST LINE SI 171 t I 12t 19+ 210 ~ U OAO 0 ' 73 ' 12 I 193 88 Pw TO PHT NCH-252 180 ~ 0 .0 ~ 0 Ot0 57 ' 12 ' 193 HCP OIL CLRS. CCW CCH"452t454t458 1200 ' 0 ' 0 ' 69 ' 12 ~ 2 193 HCP OIL CLRS ~ CCW CCH"451 t453t4'b9 1200 ' ' ' 0 ' 69+0 12+2 193
~
(
EXC&tSS LETOOWN HX CCW CCR-460 6, CCH-462 360 ' 0 ' 0 ' 67 ' 12+2 193 HX SUPPORTS CCW CCH-4S7 6 CCW-135 240t0 , 60 ' 59 ' 70 ' 12 ' 193 HX SUPPORTS CCW CCR-455 & CCH-456 240,0 40 ' 39 ' 70 ' 12 ' 193 GRAB SAHPLE SH-4 6 SH,"6 60 ' 0 ' 0+0 70 ' 12 ' 193 41 1
IIIIIIIIIIIIIIIIIIII 0~ C ~ COOK NUCLEAR PLANT UNIT NO ~ 2 TTPE IIBII AND "C" LEAK RAIE TFST Ol'ONTAINHENT ISOLATION VALVES DURING HAR 1984 OUTAGE C2~AT~IT~HTI O -1 COII'RECTED RESULTS OF Val.VE TESTING TEST'TEP ESCRIPTIDH DCINE INDICAl'EO CORRECTED fEHPERAYURE PRESSURE I.RH
=2II LEAKAGE LEAKAGE LEAKAGE CONT ~ PRESS'LARH PPP-300 F 0 0 ' 0 ' 72 ' 12 ' 194
!2 96 CONT ~ PRESS'LARH PPP-. 301. 0~0 0~0 0~0 72 ' l2 ~ I 194 j,
~
I I.I, I'8 CONT. PRFSS~
CO;lT. PRESS.
ALARH PPP-302 ALARH PPP-303 0 '
0+0 0
0~0
' 0 0~0
' 72 72 12 12 '
194 2
'j.
CONT ~ PRESS ~ ALARH PPA-310 6 PPA-311 0~0 0 ' 0 ' 74 F 0 120'5 193 100 CONT ~ PRESS ~ ALARH PPA-312 6 PPA-313 0.0 0~0 0~0 74 ' 12 ' 193 101 BORON INJECTION ICH-251 240 0 700 0 702 ' 74 ' '
~0.0 193 F F 12 40.0 00~
I 0.2 70.0 01 ~ 0 12 '
12.0 194 193
' I I
102 BORON INJFCTTOl~ ~222~
1200 F 0 1206.8 74 '
80 '
I'2 I 1202 193 193 50 0 50 ' 8100 12 ' 193
.103 VELD CHANNEL PRESS. CA-181S 30 ' 0 ' 0~0 78 ' 1225 193 104 ~FLD CtIANNEL PRFSS ~ CA-181N 30 F 0 0 ' 0 ' 7600 1205 3 105 GRAB SAHPl.E SH-8 6 SH-10 60 F 0 0 ' 0 ' 72 ' 12 ' I P4 0
4, 0
l tYPE>>8>> Att0>>C00 ooaaoaoaoo DE CD COOK NUCLEAR PL IT ~ UNIT NO ~
LEAK RAIE TEST OF CONTAIt>t/ENT ISOLATION VALVES DURING MAR 1984 OUTAGE
'YI DATQ JNFORNATION 4
E
'CotERECTED RESULTS OF VALVE TESTING TEST ST DHAE gDTCAAb lloyd CUARECTH~EAPEHATURE PRESSORE LRH LEAKAGE LEAKAGE LEAKAGE lq I
106 CVN 'COILS 2t 5 CCW CCW-243-?5 60 ' 0 109 ' 70 ' 12 ' 165 I,"
107 CPN COILS 2t 5 CCW "CCW-244-25 60 ' 20 ' 1999 7090 12 ' 165 I
108 Catt COILS 3L4 CCH CCW-243-72 3250 ' 3250 ' 70 ' '. 12 ' 165 Jj 2500 ' ?502 ' 73 ' 12 F 1 165 'I 270000.6 2e724.o 67 ~ 0 12 ' 165 4
250090 2507 ' 73 ~ 0- 12 ' 165 26000 ' 26175 ' 77 ' 1290 I b5 AI 29oo,o 2919.e 77.2 12.0 165 12000 120 ~ 8 7 l.2 12 ~ 0 165 IO9 CPW-COZL~C4-CC I
8599 1283 165
=110 '" 'CW IO'EO=1 CCt~ 9'0,0 20,~'9,0 68 '" 1285" 193 0.~0.0 3~ " 12'I" '93
~
CEO~
~
111 112 --
CCW I CPN 00ff COILS ?L~CW CCR~ 60 ' =I'90;O r88 2 60.0 66,0 12 ' 194
'I 113 CC>~0 CEtI~ ~
.If 0.0 60.0 12.2 '94 .0 If r
" 114 CCW hJ CE~ CCF~3 68 ~ 0=
== " 12;3 194 115 CPt4 CQTC~~CCLT CC~ 56 ' 12 ' 194 116 " -
GLYcoL sUppL~pAN 9 00.0 0.0 0 0= " 6300 = = 12 F 1 194
D C ~ COOK NUCLEAR PL iT0 UNIT NO ~ 2 TYPE "8" AND "C" LEAK RATE TEST OF CONTAINMENT ISOLATION VALVES DURING MAR 1984 OUTAGE HFU+MATT Cot4HECTED RESULTS OF VALVE TESTING ES~T I CAT M AAAAtRE PfCSSURE LRH LEAKAGE I LEAKAGE LEAKAGE
~ A&
117 GLYCOL HFTUf4tt EXPANSION R-157 & R-158 60 ' , 8000 ' 7947 ~ 0 63 ' 12 ' ,'
0~0 0 ' 6000 12 '
'0 118 POST ACCT SAMPLE RET ~ NS-357 15 ' ~ A 0~0 0~0 79 ' 12 ' 165 I
1L II? 'OST ACC ~ SAMPLE RET ~ ECR 496 & .tCR 497 15 ' 0 ' 0~0 77 ' 12 ' 165 120 POST ACCT SAMPLE SUPPLY 'CH-rtl6'.'<<- .
f5 ~ 0 I .. 250 ' 251 ' 77 ' 12 ' 165 t
~ I 64.0 12 ' 194 1 7
1<0
~
I 121 "OST 'ACC SAMPCE SUPP~.C- 00. 0 e.o 201 .5=77.
o,o '4.o 2 "12 ~ I 12 '
165 194 1?? Cot tTA INMFtt T SAtsPL ING ECR-535 30 ' 20 ' 19 ' 68 ' 12 ' 194 I I
I 123 CorttalNMENT SAMPLING t.CR-536 30 ' 4 20 ' 19 ' 68 ~ 0 120$ 194 i,'.,
124 LOWEk RMS HETUHN ECH"36 120 ' 0 ~ 0 0 ~ 0 77 ' 1205 165
~ ~
A 125 PLAitl AIH TO CottTAINMENT PCH-40 120 0~0 0~0 73 ' 12+3 194 126 PLANT AIR TO CONT ~ CttECK VLV~ PA342 12o.o 4000 ' 3974 ' 73 ' 12 ' 194 1
0 C COOK NUCLEAR PLANT, UNIT NO ~ 2 o4 TYPE "8" ANO "C" LEAK RAIF TESI OF CONTAINMENT ISOLATION VALVES DURING HAk 1984 OUTAGE
~
g O'IAT~NF O~MT ION
l VOLUMES WHERE GUIOLINE LEAKAGE HAS BEEN EXCEEOFO TEST STKP OESCRIPTION -, GUIOLINE LEAKAGE CORRECTEO LEAKAGE
'r --'-5551 ' AIR PART ~ RAO GAS &lONITOR SH-I 60 ' 109 ' COHPLEft4+o+
CHARGTNG TD REGEH fIX CS N-leo ~ OCR-201 .
371'.. 80+0 '49i3 COMPLETE<<>>
en RCOT VEIIT HEAOFR 120+0 258 ' COHPLE It>+o+
79 8?
LOWER CONT ~ MON ~
PAR~A~~ON FCR-33 I ECR-35 MI ~CR=32 60+0 1907 ' COHPLETEo"o~
AIR ECR 20~0 1243il=
a4 CONTROL AIR TO CONT. XCM-102 L XCR-103 120 ' 531 ' COMPLETEoo
. I
y l06
= 108 " - -. CPN COILS 2L5 CCW Ccw-?43-25 60 ' 109 ' COMPLEItooo" CPN COT~~CCW CCW 243 72 60" 0" 120 ' COMPLETtaooo 109 CPN COILS 364 .CCW CCW"244-72 60.0 372 ~ 5 COHPLETE>>>>
I, 112 CPN COILS 265 CCW CCH-440 60 ' 188 ' COHPLE Ito~4O l2 3974 ' COHPLETEO>>o~
g 1
aaaaaaaaaa 0 ~ Co COOK NUCLEAR PL T ~ UNIT O Q p a a a a a a a a a a TYPE ((B>> AND>>C>> LEAK RATE TEST OF CONTAINHEJT, ISOLATION VALVES DURING HAR 198'UTAGE T~F OTTHH TTO i
TEST VOLUHES THAT HAVE NOT BEEN INITIALLY TESTED TEST STEP DESCRIPTION I,
4a
})
~
'l-
82oooIEONOIIo 0 ~ CD COOK NUCLEAR PL NT UNIT NO ~ 2 TYPE "8" AND "C" LEAK HATE TEST OF CONTAINMENT 'ISOLATION VALVES OURING MAR 1984 OUTAGE
/(6 coMPLETEo TEsT voLUMEs 2
ESl 'DCUtl LEAKAGE RRECI~RIAL NO"RNEN 6 8
LEAKAGE VOLUME PASSED It CLV tI] WCR-900 & WCR-902 720 ' 0~0 1
2 CCV ttl=tii~l) 0~ 0~0 3 CLV tt4 WCH-.912 & WCR"914 720 ' 0~0 4 CLV tt4 WCR-.91'3 & WCH"9]5-+,; 720 ' 0~0
'uv b tt] wcH-921 & wcH-923 480 ' 0~0 I CUV tt4 WCH-932 & WCH-934 480 ' 0 0 CUV tt4=WC~33~CR=93 80' 0 79 ~ 8 9 HCP ttl WCR-941 & WCR 945 .': 36090 0~0 10 RCP tt] 'WCR-951 & WCR-955 360 ' 0~0 C 0~0 12 HCP tt4 WCH-954 & WCH-958 360 ' 0,0 720 ' 59 '
13
]4 15 CLV tt2 CCV CLV tt3 tt~C~O~ WCH-904 Wck-908 WCR"906
'WCH-910-20 720
' 39 ' 36 lb CLV tt3 WCR-.909 (.WCR-9] 1 ."720 ' 99 ' 1(
]7
]tt CUV tt2 tt2 WC~2~
WCR-925 WCR-927 0
480
'0'966
& ~ 0 7 I.E' 19 cuv tt3 'wcR-928 & wcH-930 480 ' 0~0
~
93 eo-.o 0~0 It
('
21 HCP tt2, WCR-942 & WCR"946 36060 'U~~~2~CR 0~0 RCP tt2 WCR-952 & WCR 956 8 36/60 0~0 CP tt3 WCR=94~C 59 ~
24 R CP tt3 WCR-953 & WCH"957 360 ' 0~0 I' 25 I NST ~ HM EAST WCR-96U & WCR-962 240 ' 0~0 26 IN ST .RM .EaST-~~e1~CRWS 40 GRO 27 28 I ttST ~ HMi I NST WEST WEST WCR-9b4 & WCR-966 WCR-964 & WCR-967
~88 240 240 0~0
~
RM 0~0 29 I NS~M 66/ Dt~i. PP~CR=~~~0 30 INST ~ RNi VENT ~ SUPPLY VCR-102 & VCR-202 1680 ~ 0 358 '
31 L'OWER VEttT. SuPPLY VCR-103 & VCR-203 2880 ' 1303 '
RE~EN~~EN=IC~CR=29 'CR-105 0~0 33 UPPER VENT ~ SUPPLY & VCR-205 3600 ' 79 ~ 7 2880 '
34 UPPER VENTS EXHA Vcg-.]06 & VCR-206 ( 0~0 1 (80 ~ 60 ' I 36 ttYOHOGEN RETURN LlttE ECH-]0 & ECH-2O 60 ' 0'
~~
1 3I ESR ECR-ll & ECH 21 60 ' 0 ~ 0 I Jtt ESR-V ~ ECH=T2 60 ' 0 0 1 39 ESH-3 ECH-13 & ECR 23 60 '
40 41 ESR-4 C SR-5 ESR"6 ECH-.M~~
ECH-14 ECH-]6
& ECR 24
& ECH 2b 60 '
606 60 '
0~0 0~0 0~0 1
1 1
0~0 43 ESH-7 ECR-17 & ECR 27 60 ' 0~0 E RAN
TYPE IIO4oo0000<<" 0 ~
<<II<<aND <<C<<LFAK RaTE C ~ COOK NUCLEAR PLANTS UNIT NO ~ 2 TEST OF CONTalNMENT ISPLATI(IN VALVES DURING HaR 1984 OUTAGE E~!C! KAT~FO~MT'IO .
COMPLETED TEST VOLUMES TESl VOLUHE 60TOEL
LEAKAGE . LEAKAGE VOLUME PASSED 44 ESH-8 ECR-18 28 60 '
6 ECR 0 0 ESR=9 EC~ ~@~9- -...-76 60 ' OPO 46 HCP ttl SEAL WATEH ; CS-.442-,l-l-..';" 120 ' 0 47 RCP tt4 SEAL .WATER'S-442-,!. 120 ' 0 20 ~ 0 49 BCP tt3 SEAL WATFH CS-442-3 '
'20 0 '
RELIEF VALVE HFADFH TO VMT 120 ' 29 '
51 AIR PARTo B'A~IIIS HONTTOR 5- 0969 4 52 NITROGEN TO ACCUMULATOHS '-102 e0.0 0 ' 1 SJ. ,NITHOGEN TO PRT . N-159 45 ' 39 '
SA PRTMAR~ATSIT TU"PRl PIPP75 III 69'7 CHAHGING TO REGENT HX ~ CS-321 I 7496 3 2 57 DEAD wEIGHT c/LlfIHATQR GLYCOL SUPPLY 'VCR=I'0 6 VCR-ll NI x-151-vl 4-0 'n I V Il I GLYCOL RETURN 'CR-20 6 VCtt-21 480 ' 0'
~
I RCOT VENT HEADER OCB-203 6 DCH-207 120 ' 19 ' 2 60 RCOT VEN~E7fDEfl ~elf ~CR=20l 58 '
el ICE COND. aHU OBaIN HOR. OCH-elo 6 ell 300 ' 139 ' I 62 CI.V ANO CUV OBAIN HOft ~ UCB-620 6 OCB-621 I 63 "" =RCOT"DBAIN HDRi OCR=ZOS ~CR=2U6 480 ~
0" ""0 0 000 2 1" '
e4 COtlT ~ SUHP TO HUT OCB-600 6 DCR-601 360 ' 0 '
65 LETDOWN QCR"300 120 ' '
0 I 66 LETDOWN OCR=30'I 20 ~ 0 0 ~ 0 1 1 67 HCP SEAL WATER RETURN GCM-250 6 QCH-350 480 ' 000 1 ec e9- Rtfk BECIRC ~
RHH-HEC
~ ES IR~v~~cM=Jve ICH-305 1080 '
I'000' 741 0 '
2 70 PW FOR RX 'CAV ~ SCRUB QCR-919 6 OCR-920 120 ' Oi0 71 REFUELS WATER TO PX CAV ~ SF-,152 6 SF-154 300 ' 0' 72 REFOEI..CAVo DRAGON . SF=IS~5~6 6066 0' 1 73 HQT LEG saHPLEs NcH-I!t5 6 t(cH-106 60 ' 0 ' 1 7>> PRESS L IQ ~ SAMPI.ES NCH-107 6 NCH-108 60 ' 0~0
'" " 1 STEIIH SAMPLE ~
FiiR=TU9 6 tTCB=ITO ASU 0.0" 76 HCOT SAtIPLE RCH-100 6 HCH" 101 60 ' 0 '
1 I
77 PBT SAMPLE OCR-202 6 UCH-204 60 ' 0' 1 Trl AccUrr. 5AMpc~cR=~OR= 6'0 ~ 0 0 1 79 I:0 SI tt3 LOWER CONT ~ HONo NGHTH SI OISCH ~
SOUTIT Sl UISC~CM=06 COtITROL AIR TO CONT ~
ECH 33 6 ECB 35 ICH-2o0 XCR-.100 6IXCR-101 60 240 2IIOTO I?0 '
0 1907 ~ 2
""00 '
4 1
1 1
d4 85-CONTROI. AIH TO'ONT ~, . XCH-102 6 XCR-103 120 ~ 0 531 ' I tIITRQGEN~ 5~ 0' 1 we NI THOGEW TO ACCI/M~ GCK 31 0 60 ' 0' 1 87- SAFETY INJ TEST LINE 'SI-17101720194 27060 0' 1
z4 TYPE "8"
(
>>00o"oo00"00 DE C COOK NUCLEAR PLANT, UNIT NO ~ 2 +"00""+"0000t0 AND "C" LEAK HAfE TEST OF CONfAlNHENT ISOLATION VALVES DURING HAR 1984 OUTAGE COMPLETED TEST VOLUMES W
TEST VODIH CORIKCTED TRIAL No WHEN 04 LEAKAGE LEAKAGE VOLUHE PASSED Gd 89 '= PW To PRT RCP O'IL CCRSe tlCR-?52 CC~C~5~0~08 180 ' 0~0 90 HCP OIL CLHS ~ CCW CGA-45li4530$ 59 1200 ' 0 ~ 0 9l EXCESS LETDOWN.'HX CCW CR-460 & CCR-462 360 ' - 0~0 9 PPO 240 59 '
93 RX SUPPORTS CCW CCR-455 6 CCH-456 '
'40 3906 900 GRAU SAMPLE SM-4 6 SM-6 60 ' o,o 8~0 060 96 CONT. PRESS. ALARM PPP-301 ='- 0~0 000 97 CONT ~ PRESS'LARM PRP >02 "'04 '0 ~ 0 060 98 CON~6R~eZTftt 0 ~ '0 99 CONT PRESS ALARM PPA-310 6 PPA-311 0 ~ 0 0~0 100 CONT ~ VFESS ALARH PPA-312 6 PPA-313 0~0
'01 BOROll
~
ItlJECTTDf~CfP24 40.0 40 0~0
' 3 102 BORON INJECT IOtl ICM-2>0 240 ' 50 as 3 103 104 HELD CIIAtJNEL PRESS ~
HELD CFQNNEC PRES ~
CA 1 8 1S 30 ' 0~0 1 306 boo 105 GIIAtt SAMPLE SH-8 6 SM-10 6000 0 ' I l06 rot '
CI'tl COILS 2o,s CCW ct'N coILs 265 CCW-243-25 ccw=z4~
60 ' 109 ' 1 cc0l lsd' 108 CI'N COILS 364 CC0t CCW-243-72 60 ' .
120 '
I09 CVN COILS 364 CCW CCW-244-72 60 ' 27265 CC~
110'* "
CCW TO CEO=I I'9 ~ '8 Ila '
CCW FIIOM CEO-I CCH-43l 90 ' 39 '
crrl cnrLs 2&5 ccw CCH-440 60 ' 188 '
l13 CCW'O CEO=2 CC~>2 W.0 0;0-114 II&
CCW To CEO-2 AGCY'AMPLE CPN COILS 3&4 CCW 4
CCM-433 CCR-441 90 ' 0~0 4
~16 GLYCOL SUPPCY EXP'ANSIQ~=T56~~ S9 60 0 60 II 0,0 0 0 117 Ird GLYCOL RETURtl EXPANSION H-157 6 H-158 60 F 0 0 '
-119'"
120 POST ACC. SAIIPLF. HFT Vosl ACC=SAHPC~El POST 6
SUPPLY NS-357 tYH=%96~ECR=497 CCR-416 1500 150 0 0
0~
0 0= 2 121 POST ACCT SAMPLE SUPPLY 'FCH 417 15 ~ 0 0' f0"
=--
122 123 124 12S-126 COrlTATtlHFN~AHPCTN~~
CONTAINMENT SAIIPL ING LOWt.tt RMS HETURtl ECR-36 I CANT-AZRWOWDIITmeErn C-t CR-536 PLANT AIR To CONT ~ CIIECK VLV~ PA342 30 '
1?0 ~ 0 120.II
~ 0 19 '
3974 '
'0.0'20 0 '
4 I
~
4
-'-i'j I l I6
DE CD COOK NUCLEAR PL T UNIT NO ~ 2 TYPE 8" aND "C" LEAK RATE TEST OF coNTAINHENT IsoLiaTIPN VALVES DURING HaR 1984 OUTAGE, AFG~MLTf J08 ORDER STATUS REPORT-ORIGINAL J 0 33138 OTOELIR , ,: , CURREC750 SUPPLENENTAC LEAKAGSE 'EAKAGE JeO ~ NO/DATE 33 UPPER TwO VENT ~ SUPPLY VCR-105 & VCk-205 ISOLaTION VaLVES NEED REPalk ON THIS VOLUMF.
3600 ' TRIAL I VCk-105 VCR-205.
'0018 ' 9/14" 10/14-3 3
51 AIR PART ~ RAD GAS MONITOR '-'."TSH-1 60 ~ 0 'TRIAL 1 SH 1 9 ~ ~ y 626 ' -, 24/30- 4
., TRIAL 2 SH-1 ~ ~ ~ ~ 22957 ' 33/ 5- 6
~ ~ ~ ~ Sor4-.1 - 36/ 6- 6 3 NITHOGEN TO PAT
N-159 45 ~ 0 TRIAL 285o 568 F 4 - 18/19-Rl~ N-1S9...
1 N ~ ~
700.7 = 23/26- 4 3
55 CtiARGING TO REGENO HX ~ CS"321 18000 TRIAL 1 CS-321' . 23977 ~ 3 - 21/31" 3 59 Av.
MCDT VENT HEADER Dck-203 6 Dck-207 120 ' TRIAL 1 DCR-207 '9762 19/27- 3
. NCUI YEN'NEAOCI! II-ISO 6 'OCI,=2UI 120,0 ARIA~ II-I69, 1539;4 - 13/14- 3 62 CLV aiVD CUV DHAIN MDko DCR-620 6 Di R-621 126 ~ 0 TRIAL 1 DCR".620 ~ 2406 ~ 8 - 15/19- 3
'00'100LATIOll'AL'VES"NEER REPIISR UIPNNI~OCUNE OCR-621, 15/19- 3 REC INC. ifi ICH-305 1080 ~ 0 TRIAL I ICH-3050 '910 ~ 4 - 26/ 1- 5 LOwER CONT. MON., ECR-33 6, ECR-35 60 ' TRIAL 1 FCR-33 ' 2512,2 8/14-
- 27/ 3 TRIAL 2 ECk"35 1736 7 .
" 1- 5 RIA~ ECR33.35 2657.5 '
34/ 6- 6 Alk PANT ~ FchD GAS MON ~ ECR-31 &, t;Ck-32 1?0.0 TRIaL 1 ECR-31oe 130808 7/14- 3 80itON INJECT I ON I CH-251 240 ~ 0 TRIAL 1 ICH-2510 70296 17/19" 3
,I 702 -8ONON-I N JFC T I O~C~S AO 0 TRTA~ ICN=250 1053 5 '17/19- 3 TRIAL 2 ICM-250 ~ 1206 ' 42/ 8- 6 0 5
CPN Cull.S" 3&4"CCW CClf=243=72 "60 0'0 = TR IAL I CCW24372 3250 ~ 0
" " = 16/19- 3
t. A I) 0
oooaaoaooo O CD COOK NUCLEAR PL T ~ UNIT NO ~ ? o<<ooooaooo TYPE TTHIT ANO "C" LEAK RATE TFSI Of CONTAINMEQT ISOLATION VALVt;S OUNING HAR 1984 OUTAGE J
CEmAA Nra~tt TIO F
TFST SIEY '
OESCRTPTIU JOB ORDER STATUS REPORT-ORIGINAL A
GGIOEL1NE LEAKAGE ; '. J.O. 33138 SALVE CORRECTED
'EAKAGE
= SUPPLENENTAL JeOp NO/OATE 117 ()LYCOL kETURN EXPANSION R-157 & K-Ibtt 60 ~ 0 TRIAL 1 R-157 ~ ~ ~ 7947 ' 6/14- 3
,'J - 1?0 POST'CCT S'AHPCE SUPP~ ECP"4T TABOR-El~El I ~ - 1 I/IA- 3 II 1
.,I 121 POST ACCT SAHPLE SUPPLY 'CH 417: 15 ~ 0 TRIAL 1 ECR"417 ~ 301 ~ 5 I
I!/
~ '
4444444444 D ~ C ~ COOK llUCLEAR Pt. IT0 UNIT NO ~ 2 4444444444 Tvri "I)" AND c" LEAK RaTE TESI OF coNTAINHENT IsoLATIDN VALV).S DURING HaR 1984 OUTAGE
~ rr ETAGE A A fO~HATI 01
~
~
A 0/
A I 3 INPUT DATA (UNCORRECTFO) 0 TEST STEP DESCRIPTION TEHP tF) PRESS )PS IG) LHM IND ~ LEAK~ INPUT CODE I
"'cAHr31 A/ 0'$1/
A
'r I
~ 0 I 00 11l l
~
t. 7 Ict; LOnDING Bt IND FLANGE CPN-57 72 ' 12 ' 165 50 ' 1
" '-' )0 sraHE HENETHATIDN c)'N"67 72 ~ 0 12 ' 193 0 ~ 0 1 FL"OX 'THIHHLE HAOOEI~PtPT6 f2.5 200 '
i I ELEVaTION 612 aIR ELEVaTION 650 aIR.LOCK--'",
TO.O, 70 ~ 0$ "
12 ~ 3 ' '65 193
",3550
, I LOCK;.-"'.
2 80 ". 12 165 0 I
'utL
'0 0'2 3 ZONE 3 PENETR'ATI'0)T 63.0 12.0 1'93 0'0 FUEL TRANSFER BLIND FLANGE CPN-1 68 ' 12 ' '
ll, 5 194 0,;. 32~65 0 1 5 TRANSFER BLIND FLANGE ICt. LOADTNG BCIND FC))7lGE CP~
C)'5-I 66 ' 12 ' 193 0 ' '
4 8 2 50'0 I 8 ICE LOADING BLIND FLANGE CPN-80 72 ' "
12 ' "
193 ' 2 l': EQUIP))ENT HATGH FLANGE I,' : -'72 ~ 0
" '= 12 ~ 2,. 165 0 ' 1 EOOIPHEH 90 0 ~ f'5 12 . PERSONNEL AIHLOCK COVER FLANGE 7200 12 ' 165 120 ' I
,f= 1? PEHSONNEL AIRLOCK COVER FLANtIE 7900 12 ' 194 " 24010 ?
~
12 12 6 " PLANT AIR BCINO FLANGE PEHSONNEL AIRLOCK COVER FLANGE PERSONNEL AIRLOCK COVER FLANGE ZOH~ EHETHATIOH CPA=2 80
~ 0
~ 0 83 '
75 '
'2
=, .323
-'-'", 12 ~ 2 194 193 193
'0 120 120 3
4 10 7 ICE LQADING BLIND FLANGF. cpN-57 : 12 F 4 194 ' 2 ZONE 4 PENETHATIONS 74.0 1200 194 ,. 3))000
" ' "' " 2 4 . ZONE 4 PENETRATION 400 120'1 194 800 ' 3 6 PLANT AIR BLIND FLANGE . CPN-29 74 ' 1202 194 0 ' 3 110 A
1
~0>'I//
00 t'i
<<>>EE<<ET>> O. C. COOK NUCLEAR PLANT UNIT NO. 2 ET>>ETETET>><<
TYPE "8" AND "C" LEAK RATE TESl Ol CONTAINHENT ISOLATION VALVES DURING HAR 1984 OUTAGE P~~C OXt~FO>HAT IO .
THE TOTAL TYPE "C" LEAK RATE IS 13723 ' SCCA+
THE. TUTAL LEAK RATE t IN OTLAEE y IS ' ~ 1245 LAN NOTE': Thb TO CUHPLET ION STATUS v'l V O TOTAL TESTED INITIALLY-" 1 6 TOTAL RETESTED" 16 Al PASSED- 110 PASSED- 15 TOTAL VOCOHE~T 0~'6CEF~E~T- 1 COHPLETION RATE ls 99.2l .,%o) b V
b b
ool0olo0>> D. C. COOK NUCLEAR PL I, ttttlT NO, 2 oooo000000oo TYPE "t<" AND "c" LEAK RATE TE>I 0F coNTAINNENT Isot.ATIDN vALYFs DUfrltgG rtAR )984 PUTAGF YP~8r VA~FOglTA'7I 0 COKRECTED RESULTS OF VALVF. TESTING C I
'TEST" STEP "058CRTPTI'OR, GOTDLTFiE CORRECTED YE'HPERATURE
)NAVIGATED PRESSURE LRH LEAKAGE .- ,'EAKAGE LFAKAGE ~
ELEVATIOtt 6)? AIR LOCK 551 I ~ 0 35 ' 34 ' 70 ' 12 ~ 3 165 ELEVATION 650 AIR LOCK ~
5511 ' 0 ' 0~0 8' )2 ' 165 ZOHE 3 PFHETRATIONS )173 ~ 0 0 ' 0 ' 63 ' 12 ~ 0 193 ZONE 4 PEt!ETRATIONS I 173 ~ 0 20000+0 19852 ~ 7 72 ' 12 ~ 5 194 38000 ' 38)43 ' 74 '
' 12 ~ 0 194 80'0 ~ 0 80)o5 '74 ' )2 ' 194 3
I UEL I RAthSFE.P. BLIND FLAttG~PN-I=. 1200 0 "
0 0 0 0 68 ~ 0 )2 ' 194 0 ' 0 ' 66 ' )2 ' 193 00 PLAINT AIR HLIND FLANGE CPN-29 I?00 ' 0 ' 0 ' 79 ' )2'85 165 10 ~ 0 10 ~ 0 77 ' 12 ~ 3 194 1'
'0
' OiO 74 ' 12 ~ 2 194
'7 'TCE LOADING PLTN~CAHG~PN=57 80 ~ 0 50.0=50.0 80.0 79 '
79 '" ' " 12 ~ 5 12 ~ 4 165'500 194 i) 8 ICE LOADlt4G BLIND FLANGE CPN-80 720 ' 50 ~ 0 50 ' 79 ' 12 ~ 4 165 I
I 30 ' 29 ' 72 ' )2 ' 193 I, ~
I FLUX TttIHRLE ttAtlOLING CPN-76 960 ' 200 ' 198 ~ 2 70 ' 12 '
(I ln SPARE PENETRATION CPN-67 240 ' 0 ' 0~0 72 ' 1' EOult.VErtT HATCtt f'LANGE 5500 0 ' " 0~0
" 79 ' 12 ~ 2 165 "0 ' 0;0 79 ' 12 ~ 3 194
0 ~ C ~ COOK NUCLEAR PL TO UNIT NO ~ 2 Tttttttttt"tttt444 TYPE. "8" ANO "C" LEAK RATE TEST OF CONTAINMENT ISOLATION VALVES DURjNG HAR 1984 OUTAGE I4
,~l. DATA TN ORNATTON t
t 4
l CO".RECTED RESULTS OF VALVE TESTING 1
14 I
ji '
! 5L IAE QD I CCTH~tRIIECTH) TEHPERAAURE PRESSURE LRH 'Ai LEAKAGF. LEAKAGE LEAKAGE
~ ~ 4 I
'r 12 PE.RSUNNEL AIRLOCK COVER FLANGE >5 ' 120 ' 120 ' 12 F 1 165 "I
T 240 0 24042 79 ' 12 ' 194 20 ' 120 ' 80 ' 12 ' 193 I.
120 ' 12140 83 ' 12 ~ 2 193 IJ t
I r 'rI I'I
)If
~ 14
)NIt.'
iI
""ir '
~ I D r.',
44,
"'?~+i)+" D. C ~ COOK NUCLEAR PL T UNIT NO 2 4i)>i?" )?i)i?i)
TYPE "8" AND "C" LEAK RATE TEST f)F CONTAINMENT ISOLATION VALVES DURING MAR I984 OUTAGE M TI r r.
.~i<
VOLUMES WHERE GUIDLINE LEAKAGE HAS BEEN EXCEEDED 'i DESCRIPTION
~,,'f,Q. r r,'UIDLINE LEAKAGE CORRECTED )LEAKAGE jill PERSONNFL AIRLOCK COVER FLANGE 55 ' 121+0 COMPLETE.>>i)>
i
?
0 ~ C COOK NUCLEAR PLANT ~ UNIT NO ~ 2 TYI E "0" AND "C" LEAK RATE TEST Of CONTAINHENT 'ISOLATION VALVES DURING HAR 1984 OUTAGE PE 9~$ fA INf~RMATION TEST VOLUHES THAT HAVE NOT BEEN INITIALLYTESTED TEST STEP DESCRIPTION
~ ~
"oo""oo""" 0 ~ CD COOK NUCLEAR PL T UNIT NO ~ 2 oooooooooo TYf'E "8" AttD "C" LEAK RATE TEST OF CONIAINHENT ISOLATION VALVES DURING HAR 1984 OUTAGE TYPE ttBTE DATA INFORHAT ION COHPLETEO TEST VOLUHFS C>
TEST'OLUHE ES tÃfPTHJIlt GUTOE1.INE LEAKAGE'"',
CONNECTER LEAKAGE
'RTGL
'OLUHE NO RNEN O PASSED
'W &
'9 ELEVATION 612 AIR LOCK 55II ~ 0 34 '
ECE VATI'O~~~C 55H .6 -
. 0.0 i
I, ZONE 3 PENETRATIONS 1173 ' 0 '
1 1
ZONE 4 PENETRATIUNS FOE~TERR
' . 801G5 '173 3
5 C 2'f0. 0~0 2
~ ~ ~N I 5 PLANT AIR BLIND FLANGE Ct'N-29 1200 ' 0 ' 3 7
8 ICE LOADING BLIND FLANGE CPN"57 ICE"LO'ADING BLII'1D FEANGE CPN'-80 480 ' " ' 2 720i0 29G9 2 9 FLUX THIHBLE HANDLING CPN-?6 960 ' 198 ' 1 10 SPARE PENETRATION CPN-67 "240 ~ 0- 0 '
I UTPH 0.0 12 PF.HSONNFL AIRLOCK COVER FLANGE 121 '
>I E
"C" 0.'. COUK NUCLEAR l ANT, UNIT NO. 2 <<<<<<>><<<<>>
TYPE. TTB" ANO LEAK RATE TEST Of CUNTAINNENT ISOLATION VALVES DURING HAR 1984 OUTAGE
~PE 'T,'T OATA INFORMATION IEA JOB OROER STATUS REPORT ORIGINAL 'JPO ~ 33138 TFST'IEP UIOECTN ERECTEO SUPPLEHENTAL LEAKAGE LEAKAGE JPO ~ NO/DATED T
s, &A ~
v" = s I
mrs]
I 0, C ~ COOK NUCLEAR PL I'~ UNIT NO ~ 2 TYI'E "II" AND "C" LEAK RATE TESI Of'ONTAlNMENT ISOLATIOI'I'ALVES OURlfIG HAR 19II< OUTAGE r r t ~NOQHAT I O THC TOTAL 'TYI E "fI" LEAK RATE IS l 265 ~ 2 SCCH ~
THI: TOTAL LEAK fIATEt IN "LA"o IS 0 ~ 0115 LA ~
~ t NOTE': THE TOTAL TIDES ffO~HCLUO~PE '
COHPLETION STATUS r
TOTAL TESTED INITI ALLY- 12" . TOTaL RETESTEO- 7
'ATCE-FAA)- 0 PASSED- IO PASSEO-TOT AL VOCOAE~~~ ZCE~O TEST=-5 COMPLET,ION RATE IS 141 6!,%
"r
~
g I ~
I "4
4444444444 Do Co COOK NUCLEAR PL T6 UNIT NO ~
TYPE "8" AND !'C" LEAK RATF. TEST OF CONTAINMENT ISOLATION VALVES DURING HAR 1986 OUTAGE
~ DATA'N ORHATIOM 6
LEAK RATE SUHHARY H LA TVP~ ".-. 6~ , oTf6 6'C66~ '
TYPE '- 'c~ .,". 13722 ~ 98
'245
,i I .
ill!I~
~
4988. f2 6 g I'366:
6
,t TOTAL TESTFD INIT1ALLY- 138 TOTAL HETESTED- 23
, fL 'FA ICED" PASSED- 120 PASSED-,
22
~~I~OCDH~~
OVERALl'OHPLETION RATE IS 102.90%
6 -, ~ 8~ESTED 46"
'6 I
4
APPENDIX G TYPE B & C 1982 1983
>>>~~>~~>> 0. c. cooK t<ucLEAR PLANT< uNIT t>0. 2 >~<<><<>>
TYPE '8 htlo ~c~ LEaK RATE TEST oF CONTalNMFNT lsoLATlnN yaLYEs ouRING Nov. 19/2 ouTAOF.
~ wc A z od tl) LE'AK RATE MONJTO~ TEgpERATURE CALlBRAT10$ -.
165 32'2i - 77' ~
78i '20', ."'. 12bf t2I JOB ORDER NuMBER j 2806/
I
. (.0 TYPE 8!822 Attn
""<<oo<<4" >> I) C "C" LEAK ttAjf TEST
~ COOK nttcLEAR PLT.
O) CottTAINHENT 1 UNI T Nof 2 82ISETosIStstsY82o LATION yALfygs OURlNG ttOy8 l982 PUTAGE 4
4 2
2 JW'f444',45," '" 'f,.".f-:", %N
." ":" -""'..".I'. y..=' ".':".:~.:-Y';"."!'.4>'2"~-YIp<k~<%l!,"AATA=$NABt!h
~ 4 rr & 4&&44 ~
7 TEST STEP.
2, r'7 4 I '='" (
~
y .. rrc y 4 4 ~ -. 'rl ' "2.4 4 7 10 RcP ttI IJtcR-951 & McR"955 " "'. 74 0* "; "-'-'" l2 a ';.,- I'.193"-'-': -a,a ;-':,".". . '-"'-'-";":"':"-='" .=,
"- Rett tIP~: MICR".,9~PVR)~It fthm~~-aJf .~-
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".~-'. ggP.',$ &~>4)CR~Q(j'7VggjgSggg@g>.t4><~.
P
~p> 4 '7. g .g l.R~Q'4 a; $
4
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"'ICR-924
& ACR-.911; 4 MCR-9?6
.-- ;-, -.",--.'74; 0.,;" =.;
.. 72t9 7
~
0 "Tll ~ -
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- 31 30
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'., '. I,',".','-'=,.;;;1 $ 54."',
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37 EsR-I EcR-.)1 &'CR 21 ' " 2".:.".'-'4gat6';*';,.'.I 2f 0 .;","","" Qqa 38 ESR-2 ECR-12 & ECR 22 .. "-=', 74 2f Q 6q a
'8' .'; . l 40 'Ott.tt;..-ECIl~t~- r,.Kcg'i,.";zt', <"4,y. ',~5 :, ~~. ~jltt>k"~:,< 'p7>p.< ),tl f'
~CII" IS~
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42 ESR 43 ESR"7 ECP-1I & ECR 27 . "-,73,) - 2 ::-
l p 'I 44, 1
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EER"-8, ECR-:79 S.RPg,;'S 4'2'27 J,,y -"., g WI~(P9w~S'2'ii i~~'4.:IY 2<>'. j
- 0'0 IQ.',:TT"'.~ 8'ITQWIi@RE,I6T 4 46 RCR If) SEAS 'ITATFR ~ j >
4v Yf Et
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SF,'A~ATE R
'gs.q42Ttt49%'$'y.9 T~', (P0 y" ~4'~. )g,a'.
CS'=292I2-
~ vgttg+3' t'-9 P4L RELIEF VALVF tIEAOER TO VRT . "- 6680 '-."-; 12f f l65 9a f0 52 tel TROGFtt TO ACCUtlULATORS N-.102 75 j0 .2 1285 165 'Qf 0 1
54 PRIHART IIATER 'TO PR$ PII-275"."..'4'Q~~g3; 'gQ;~4gj ~~2 .2g,".'P@.STPP,IP )>~y~~~ljgytl,A)I'I'gg:.L,R~ t.') g9+Q'Pcggf~+L.: ' 0
'.=
~ .
-6I ICL'onn', Atgt nnhltI IeL--COrtO-.-AHU-ORAIN~IOR i]oR- .'CR- ppq=0 l;.~~-,,H'g~~q<<~ I,pl .,-;;~.tL:lt1>0~==.~)>>>>+~ .QA~:.Aj>'>.~ 4P41~.~+-:)~~l<
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62 CLV Attn CIJV ORAItl HDRY OCR-620 & nc8-.62) 77 0 't 12f2,, =
l94 Oqa o 7
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"i'-" -, INI)IALLY. 12 t '-" .,",-;. ~ "'."$0'fAL ltETE TED,: .', f'4 -; il', 0 'ED-', VW i'll 0 If+if++""++o D C'OOK NUCLEAR PLANT UNIT NO ~ 2 TYPF "8" AND '<C" LEAK RATE TEST OF CONTAINPEQT ISOLATION VALVES OURlNG NOY 1982 OUTAGE I: 4 )2 - PERSONNEL AIRLOCK COVER FLANGE . 81ib! - 12tt ' 198 50 ' ii'I ' I . j '1l!',fijI'ii~~j+gQi, Ii I~P C4A~4W4 '0'c ";:( P$ >:$Z'. fy~W ' ZONE 3 PENETRATIONS . "', ic '-:,%.-"., '='"f:..4.r'4"'0jg ." ""'"~ 2 ~ 5.' -'94 0 ' 4 '. ZONE 4 PENETRATIONS ", " '. '-.--. - '..$ 0 ~ 0 2~2 165 dye '"2 .-I,,'-.jElPAJIQP 65(. AIRLPC(q'-,.~t.;~;.:,,'q', h'".i~(j~~,',a~'-,'I'i~'"'"'.".j','68j0 '."-': -,.'-;: -"..12', .-.;,-'-;.. 195.".-',",'...45~0 ~ f C. gXtf"i I' Pgl, .: ygf Pi +gj~<f ~PJ'S,i 'f 44 ' "' I 4 ~ .I ' ~ ++~"~+++"" O' COOK NUCLFAP PLANT UNIT NO ~ 2 TYPE <<0" AND>>C>> LEAK RATF. TFST OF CONTAINNFklT ISOLATION VaLVES OURING NOV. I982 OUTAGE i P++R.0+ 0> O C COOK l'IUCLEAR P ) UNIT NOy ? TYPE l'0" AOO !~C'! 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Qpp<9p >)~VI $$ Q jiff. 55 gg<7 ~</. %gg P'$X ' 1 1 E t<<,g<<<<<<g<<'rt<< l'; " tq ', ~ = -',' ~, <<A(1<<>g .<<)fg)I)gglgkt't " >,,<< j'jf(<<3$ 5$ %$ $ ~%%$ 1F'I<<ST~fg$ [g'i~ ~ ~iA'Pj>t<<-, +'P<l ~<< ~ t of% ..t<< ~ '<< ! k ( q '4s . ~ 1 t ~ * ' I ~ ~ I<< i 4 0~ O'OOK NUCLEAR PLANTo UN1T NO ~ 2 44"4444444 TYPE !'8" AND "C'< LEAK RATE TEST OF CONTA1NHENT tSOLAT]ON VALVES DURlNG NOV~ 1982 OUTAGE 0 ON 0 ~ C ~ COOK NUCLFAR PLA Tg UNIT NO ~ 2 TYPE "8" AND "C" LEAK RATF. TFST OF CONTAINNFNT I OLATION VALVES OURING NOV I982 OUTAGE '*' "'" - "- ' >.~'-':. ~ ' ":'VQ'Y)al'-AX~"'-'VE"ni.i 'iVes-'": '~'<'. '1 44:e~& "'-pfHtppg$ Q""T~~lo. ,'~I: ~~ZT5$ 75" i'-)'gppkpg, p If) >CY~rE '%4j> 4 a ~ I e 0 YC~(~~P~kC>@P~'PLygj@~E~'.j'"4<EL QAf IP MIP~ 'I/01."g t't I 'I ..5 4: . '; ZONE 4 EENETEETIONE:,. 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." - . ~ "l';;'-..-;'.."=".5!~'-- '-A4g5<qc~V'wr~Ag gppf ~At ~ .4 N> IO~AQ j 7 . X$ ON- '<<4'~ Wc 'I >f ~ ' ~ 4 I I "~ y << "IP>> ~ > ~ 9f '."> >r>w>ie/ ~ > )) '(( ),,- 4>.> i > >, '. f>( >'$( . '* r> P / (( t(~f'(S'f>"; }g'i'+> I S)CQr '>>6>>")~ '~<>Y)" 40<~4&r'"f> "gh'>i .'fi< ~~PC~'i'Pl~( >y4I'P~P~4>i. (":Z'0-"" "~~. (: ' ~~'A( >~ Q>>. '-"<<} '-'/RE' V'fi!">"':~"j a'"( r'<fffy. '~2 )5$ 1'$; "A%4" '4AQ>,".f g 0g +47 g}f >v'34(.'P~ Wggtf'~g~~r4~>4>.. gb w >ijj"."+,w5~Cg> (>'=,'-'.>f> .r '"(,>.p~4+~~74~I' brig $ g ()>, g ( '> (!'VJ +'.5 >("C)~~+>Cb ~ .4 fr+'94')$ '"<$4>tb"A.-~<)r4""T'>W@Lfi<y'~~4'S+>4Pa4 4 ~44K<'~ ~~f(y<'~">~i 'f"'. ~ >-. >6 ~ ':f(" i("(.. 'fff> 'g,','4X4$ 1 I Pqgq~P+(;~]2$ ~Pi>' f.~;.Qtd<l y ",~,-Iv, Phg)EP.>4, ~$ +w4$ Pq,, .s@$ k4(P 'P QVfRALL',COVPLg'ff)N 'Pgg jP ..)ggq ~,,', > I . - '~,'; .;> ~ 'f e APPENDIX H SUMP LEVEL CHANGE CALCULATION A.E.P.S.C. - M.EJL INSTRUMENTATION AND CONTROLS. SECTION ADMINISTRATIVE INSTRUCTION AND DESIGN PROCEDURE ENGINEERING CONTROL PROCEDURE CONTROLLED DISTRlaUTION FOR E.C.P. PACKAGE I v' = INITIALISSUE ( 1o Iecnnical Departnamt I Chemical Sect. Leaal Engineer REYISED THIS ~~ ) ( Ccpies going tea hchnical Deparesent/Eng~ Super}ntendent (2) ( ( ( ) 'taaxbine Sect. Hanaqer ) ) Electrical Generaticn Sect. Electrical ~ a1aglneer Design Sect. teaa( cr ISSUE ~ 4 ~ I ) Hectaanical Design Sect, Hanager CD cr ~ CD ( } I a (: Sectfcn Hanager/File (2) CI CI ) HED Asst. Divisicn Hanager O ) Nuclear Dceraticns C1 CI O ICI ( ) pipi~ a Valves Sect. Stesa Generaticn Sect. Hanager ( ~cal Musaticn Sect. CD co O la) (Q @c~~ ( ) ( ) I I <<r CCI aoa 1'Lre?zcaathm Sect. Hanagez ( ) ) Heaters a Pasaps Sectice Hanager Cn cr O CL arI CI 'O an ) 41 CC (1) C1>> REVISION DESCRIPTION ANO AUTHORIZING DOCUMENT I D. cs CD ILI CL'C O CD 0 Xn,'W;~i ZZZ~Z 1n l"~)DES<. eO 7 <AT la)% Q A/4.>>> <c(<<c>'o~ Zoo Ache~.I~i~ uo(~~oI, Ckc.+g P c(c'~Qg ()g N(A ~ p IwV+ I V~~'om g~ if'g F> ~ ~ KPLKAZ'A'M~~ P I.ANT %. ('- .Cooaa C~l('.M(0.+ io~ 0 Wo~ ZLg7 DWG. I ~-A/0-Q5'HEET F o' PdP')(d/.'F I)FVIRIAH PFCORO Le k~ a.< Yoi~eS 1 OF 7 A.E.P.S.C. CALCULATION MECHANICAL ENGINEERING D!YISION INSTRUMENTATION ANO CONTROLS SECTION-E LP .CALCULATION No. SHEET 1 OF TYPE PRELIMINARY OR FINAL PLANT l).C, Co~~ UNIT /+Z SUBJECT GQMP ANY 7 CALCULATED BY CHECKED BY Ks; I SUPERSEDES CALCULATION NO. APPROVED BY FILE LOCATION AND DATE PRDBLEN DEscRIPYIDN: pQ>>p apeD>>/ou /c/ a fia // zlorAoa c>> z~/opy s>>~y c 2~%>>gr>>~ Je>>k ErPe i J ca a. Jlo+a.3/</4cccf IQJc ~/4fg g ~ yJ~ <Q~ p S A ~ 5+riCS IVIII e~ 4ai ~ a tS/A<4 WO lS AR. Q g ~ J g7 EsIBN BAsls AND REFERENGEs r g/I/E Sec/A 5 o CSLARI Q /Y>>cL +J'C>> (cN. W>>ID>>c hy A, 5 Crr'i ~feoI/ 5 +CD I @ID (97'~</c'< /as4 Zapor/ 4'cr Mc;y f (YY/>> g7-g7 /D7g @I'I l7 T+ +7) E.C.P. REVISION NO CALCULATION CHANGE NO. DATE CHANGE CALCULATION BY/DATE CHECKED BY/DATE APPROVED BY/DATE 7-84,-g SAS C5 +C hC U ~oO ~ SS I ~ QJ CD CS UJ a) CD crP LES Ql O 4k-= cc CD CD SEE SUPERSEDED BY E,C.P. CALCULATION NO. REASON 7223l9.83) FORINT 684(c) ENGINEERING OEPT.. SHEET OF +$ AMERICAN ELECTRIC POWER SERVICE CORP. OAT e Mm /l 'I RIVERSIDE PLAZA COMPANY + oK~S'.O. COLUMBUS, OHIO PLANT '+ SUBJECT PIt I 1'F87 6a.okoc- Coe l~ Qr i>>. Pa>>K P;y Vew>>lc C>>la>> >a.g e>>c I-sVoz-(4 . F ~Z3l~,t-m~' ~Wyy g-7 i~ ~5'esca( >; )z'o x 4 B" x sx>g (esq i lc go[ og x ~ 08,S9g~ '/4 7I'gd s Rc aata ~ Ca e li>>d >ra~i'v *L/'t l(ala>>c= 3(c/ FD P &~a r~ l k pro~ L-S'jZ -//g d k>>>> t/l c'a l Icos li g l/clos 4F ~Ca'Ct 0~% b t4me old dl '>>+a>>>>ie>>(r Saa/F g'g~'x fJc "x 7'g~> PD. 3l HeC'~~'Lmf;b S'4 ~P f~'~ x ~g'e ~ 00+ f4'/3't. z 5"8' Z "D" ZZ.So >a4,." gQCLCW bt Qa.V a'fq 'PIa T'aao! Z~ x 7'h' P'/p/p: P/ 73 Net tea.cbo r <ioo la->>4 Drs,w Waak U.o'lu 30l, Po /iO'Fs- l eI'alf am>>>>e.'.>>> Z~~ 6's'llss>>aa / 7(3, > / ~le g~ g $ g ls>>>> cF>>f +I~la~ Ki>>>>>>IIl ois as oaap >>><( Jedmie 14 e ~a g c d vile Ve<ds >~to 4 e 8o~ eleU~&i'w o 9 +h.e T<efr<~e~& Room,s~wp +kc pl ge $~~~<( ls CD/0 O CZ al Tall t)ega+'a>> A pip& 1 V>>slel $ >>~ /S ~> r~S'7y, T~. i~sgr.~Q oo~ g~g potu.~c Ibad-ld Le disr~ycg > F's />>~e, RFS blahs(t.( s(sz. sav-- / SBA '/) a 2--$ >ZOR-1 7223(e e3l FORM O'E4(C) ENGINEERING OEPT. SHEET AMERICAN EI.ECTRIC POWER SERVICE CORP. OAT l ~~ 8 cc 1 RIVERSIDE PLAZA COMPANY Q.O. COLUMBUS, OHIO PLANT ~N.- L SUBJECT I ldus3a +Q g7 .~ u-<-- l,z.~~, i<<<z~ At/era.ge. <o~&a.-,~~~7 4'~ Ve~crd~rc +0 E ~+0 T4)fc G,l I $+c g,7 C 0w+a.~~~~ P f'c,5s, ~g c. iz.>ss:c. (Zc..> Psalm> '~<<A'r, P:r Q~,zQ 70 I/ Q I QPSXg Q. l 3( 2. Qac' $ Co~+ p,sa~. i~sf L~~ka~~'~stI-a )ass I I >> .l77~ C' ~~ p~~z Icsk )aaQ)a mace = . cScsI $ 7~5( I ZCS) /S ) I,A 3(a.i3( c 9/ps) LB g c @ 4 (.g ~ c-uC csQ ~c ~g Uol~~a. = . I342<P~s )( l7i3.3gfgs ~'~~>s cs~ +~~) +<~~a--= P33, 34 I-I3 ~ ckcc g Ilm ~a c.L~c;u '. '7ZPo Q ~/ a llama-co la icy' u.k ua,a ~shee/ hg 4~i( oe,~ccs a~)4g su.~Is ~ y . 4 +( {~~~ -~ P> ~M ~Q tI +eP, f~ t va(A S ~~/ . < S ~ ~ S ~ '-I'.'.i.-' I Ai J ~ .. 7+Fbi ~) (c5 .. C g'w'i'C a C ~ vtC ~ I > I f 4 s SLC- I 2- +@a- 'rr '4:c:'.r'-C Cc ~ ', 'P '-'cpt ra.l ~ / y h I ~ pa.LC ,l'~ t $ ~a r (e a. 5 ~ ~~~ ~ Ccc C.'~m r lc I CJ0> r Cc e ~.g ~ r WLC .lc, j~l rl.E 5 I) l cc $ & 0 '.~ ! 3 I V:~ ~acg lrtrl,~ ~~cCa (AICCC err C P~i'~~. 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T~ ,d r //4 )r r/y r L ' r f ICi Y m. / ~~<, vugg~ c zd~!/ 5 SC jy w ~ >>cc>2.+ / .e>> V.i< -.5:C.C z g')/.Su;C / Oo5 V$ C , Du/4g c I'A {2/ QSC,/2 ~,dg<+g )./2$ E(2/,7 -pq) ~ i~~ = 5$ C+(,Z ~,o/'/49 // )p (p /qg) d/'3g ) /285(z$ ,7-p ) = ) ~ /~r( (P -I),7) 7) I 4EA I.. P /C, /b74 (/ZSS'a/,7- ) )) = ~ /Z(+ (P /v'7) zc.p gg4+z <<,de5A') ~ Iz.f&(P ~l7 J MC(7 z-Cc >1 (i I . oo /VP ~,/zan(tci7 fg )- . ops.sr ) c."."), (),-~<,7) Zc,w iz -eo-og ~ <<~P~ .g a. ( c L ": 4g ' f I >f'! (7c i I'e 9 5 . . / 7-'f r i( I r J g ~ I L / r I J~ ~/ r / C8 i ~ r.e ~ lI o.j'~,,>Z ~rg.( X~!.-( ~ ~ J g/ /'a 2. . C c,7 -c'T. ~Dc 7 3'S ~i X= /7 , LA 7/c.c z < ~ so 3 If g-,i~(l8,7 I@7) 2, ~ ~6* ~ Hi5$ 2E Ice /~y~~ Clccr 2Cp .'- Q.8. O~-"~ p~,/po SHEET EH GIN E E R IH G D E P T. DATE 7 BY AMERICAN ELECTRIC'OWER SERVICE CORP. COMPANY 180 EAST BROAD STREET PLANT ~ CO LUMB U, S 0 HIO susszcr 2 L. R.T 834~+ S ~r~~ vol ~eke'c. Cl,c g e ',~ g~4;c, Wce+ a f i + &~5~' 7 ~y Gael for 14.c lo~cr C~ S'~, Rcc,c 4~C:~<~,Reactor 6,:Fg Z~puJgy c 7~can S~ 0 Cb~ f~~~ ~~ca 5~~ p / ouse.r & el~ue.4;o~ Sgf'o $1// 54 c$ g~g 0(-.gEcf Z.B3 6~ %ID + Z.33x .P3 9V ggp Ng /8 0 i ~lakioa ~+ w r~ amcl Ao eleVa.k:o abc r ~+<~4a~~M /I ~ 5P'J ~ &Minare( g~ gz jg) +(2..53x+ f33 jz %%u+ FIGURE I CONTAINMENT INTEGRATED IEAK RATE TEST EQUIPMENT INSTRUMENT PARAMETER INSTRUMENT TYPE OUTPUT RANGE ACCURACY (/ FUEL SCALE) Pressure-Upper Volumetrics quartz Manometer 0-100 psi 0.002 Containment Pressure-Lower Mensor quartz Manometers 0-30 psi 0.015 Containment and Ice Condenser Pressure-Atmospheric Penwalt Mercury Manometer 0-800 psi 0.05 Temperature Hy-Cal Engineering Resistance 0-120~F 0.08 Thermal Devices Dewpoint Temperature EGSG Hygrometers-Model 992 0-50 mV 0.03 EGRG Hygrometers-Model 660 -5 to 10V 0.01 Supplemental Test Heise Bourdon Tube Gage 0-30 psig 0.07 Pressure Supplemental Test Flow Brooks Rotameter 0-5.6 scfm 1.0 Data Recording/ Fluke Model 2280A Data Iogger 0 + 64 v and 0.009 Acquisition 0 + 512 mV 0.01 FIGURE II SCHEMATIC ARRANGEHENT OF LEAKAGE RATE HEASUREHENT SYSTEM I OFFICIAL UPPER DATA LOGGING TIME SYSTEM KEEPER COMPARTMENT ATA ENTRY ILR DATA PERSONNEL PROGRAH DISPATCHING UPPERS LONERS AND TEST DATA ICE CONDENSER TAKERS CHECK OUTPUT COHPARTHENTS AND 3) OUTPUT BAROMETRIC PRESSURE MANOMETERS I I I L LONER OMPARTHEN TEMPORARY INSTRUHENTATION ROOM ICE CONDENSER DE C. COOK UNIT 2 REACTOR CONTAINHENT BUILDING 4 ~ ~ ~ ~ 0~ FIGURE IV LEAKAGE RATE TEST'ERSONNEL SCHEMATIC Test Supervisor Interfacing Test Department Computer Instrumentation Time- Error Personnel pplications Specialist keeper Analysis Corporate Data Program Software Collection Data Verification Improvement Personnel Dispatcher Instrumentation Equipment Acquisition Setup/Troubleshooting FIGURE V CONTAINMENT AIRLOCK DOOR SEALING'ECHANISM cQ I'tern N3 Item po N2. Item. Ol "C" CLAtfP ~W ~0 ~0 VALVE DISC "C" CLAl.tP FIGURE VI SUPPLEMENTAL TEST INSTRUMENTATION INSTALLATION UN I T ONE ONLY I-PPP-30?;Ul I->PP- 302- 9l Z.-IoPP-SOa;VI PW. LOWER COh!TAINMKNV Luna. CONTaWgZNT 302. PRES. -5.T.. LOCrIC. PRES;5Z LOGIC, CNP-9I 0 I-pPP 30?- 2-PPP-30?- TLAT VEST PT. pU3vu RE@'ULATING 'VALVE. "%-Z" G Tii iKSV CONNECTION "A" 0-3O PSICI HKI5E CqAQE SUPPLEMENTAL i@5T FLOWMETER FIGURE VII TABULATION OF TEST RESULTS Test Test Parameter Acceptance Section Parameter Value Criteria Pressurization Containment 12.415 psig 12.0 psig( +0.5, Pressure -0.0 psig) Stabilization Period Length 4.5 hours > 4 hours Containment, Press. a) last hour of period 12.4098 12.0 psig (+0.5,-0.0 psig) b) 2 nd last hour of period 12.4049 12.0 psig (+0.5,-0.0 psig) Weighted average hT's -last four hours of stabilization period a) Upper Containment Hour 1 4T -0.0516 F/hr. <0.1'F/hr. Hour 2 hT -0.0514 F/hr. Hour 3 AT -0.0310 F/hr. Hour 4 hT -0.0637 F/hr. b) Lower Containment Hour 1 hT +0.0258'F/hr. <O.l'F/hr. Hour 2 hT +0.0629 F/hr. Hour 3 h,T +0.0285 F/hr. Hour 4 d,T +0.0281'F/hr. TABULATION OF TEST RESULTS Test Section Test Parameter Parameter Value Acceptance Criteria Stabilization C) Ice Condenser* Hour 1 bT +0.1521'F/hr. <0.1'F/hr. 2 bT +0.1983 F/hr. 3 bT +0.0018 F/hr. 4 hT +0.2237 F/hr. Highest containment bT in last hour of . stabilization period

1) Upper containment +0.20 F/hr. <0.5 F/hr.

2) Lower containment -0.14~F/hr.

3) Ice condenser* -1.94'F/hr.

Type A Test Period Length 29.5 hours >24 hrs. Data Convergence (Lam/95-Lam) 0.00470 wt//day < 0.1875 wt//day Measured overall leak rate -0.1362 La >-0.7421 La2 >-0.4251 La3 >-0.137 La Supplemental Measured Leak Rate -0.28835 wt//day -0.3579 wt/+day (Lc) during supple- <Lc <-0.2329 mental /wt/day FIGURE VII

~~Due to cyclic defrost operation and subsequent temperature fluctuations in the ice condenser, this acceptance criteria was waived per **12 THP 4030 STP.202.~~

~~FOOTNOTES TO TABULATION OF TEST RESUITS 1 See Section 4.1 A 2 See Section 4.1 B 3 See Section 4.2 0 vN-g 0}}~~

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4.3 CONCLUSION

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