ML20082G123
| ML20082G123 | |
| Person / Time | |
|---|---|
| Site: | Peach Bottom  |
| Issue date: | 08/23/1983 |
| From: | BECHTEL GROUP, INC. |
| To: | |
| Shared Package | |
| ML20082G113 | List: |
| References | |
| NUDOCS 8311300078 | |
| Download: ML20082G123 (125) | |
Text
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A 4 M 1
Philadelphia Electric Company Peach Bottom Atomic Power Station Unit 3 Docket Number 50-278 REACTOR CONTAINMENT BUILDING INTEGRATED LEAKAGE RATE TEST REPORT August 23, 1983
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l' Submitted to The United States Nuclear Regulatory Commission Pursuant to Facility Operating License No. DPR-44 iO B311300078 831123 PDR ADOCK 05000278 P- PDR
TABLE OF CONTENTS 1-]
I. INTRODUCTION II. TEST SYNOPSIS III. TEST DATA
SUMMARY
A. Plant Information B. Technical Data C. Type A Test Result s D. Type B and C Test Results E. Integrated Leakage Rate Measurement System F. Information Retained at Plant IV. ANALYSIS AND INTERPRETATION APPENDICES
(~) A. Stabilization Summaqr Data V B. ILRT Summary Data C. ILRT Mass Point Analysis D. ILRT Plot-Temperature Versus Time E. ILRT Plot-Pressure Versus Time F. ILRT Plot-Mass Point Calculated Leakage Rate Versus Time G. ILRT Plot-Air Mass Versus Time H. Failed Test Report J. Verification Flow Test Summary Data K. Verification Flow Test Mass Point Analysis L. DTBAT Summary Data Total Time Report and Summary of Measured Data M. Local Leakage Test Summaries N. Description of Bechtel ILRT Computer Program l
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7 y, I. INTRODUCTION-The Reactor Containment Building Integrated Leakage Rate, Type A, Test is performed to demonstrate that leakage through the primary reactor co6tainment and systems and components penetrating primary containment does not exceed the allowable leakage rate specified in the Plant - Technical- Specifications.
The purpose of this report is to provide information pertinent to the activities related to the preparation, test performance, and reporting of the Peach Bottom Atomic Power Station, Unit 3, Integrated Leakage Rate ' Test (ILRT).
The section of this report entitled Test Synopsis,Section II, pre-sents the highlights of activities and events which occurred prior to and during the IIRT.
' Test Data Summary,Section III, contains data and result s necessary to demonstrate containment atmosphere stabilization, acceptable leakage' rate, and successful verification test. In addition, plots provided in Appendixes D and E supply a visual history of contain-ment atmospheric conditions beginning with the 8-hour test period and ending with the verification ' test.
Information in Section IV, Analysis and Interpretation, supplies some of the technical detail associatd with the ILRT computer O erestam and its asseciated hardware as we11 as the instrumentatien used during the ILRT.
The successful periodic Type A and verification tests were per-formed according to the requirements of 'the Peach Bottom Atomic i-Power Station, Unit 3, Technical Specifications and 10CFR50,
-Appendix J. The test method utilized is the Absolute Method des-cribed in ANSI /ANS 56.8-1981, " Containment System Leakage Testing-Requirement s. " Leakage rate was calculated using formulas from ANSI /ANS 56.8-1981 (Mass Point) during the Type A and verification test s. Type A and verification test duration were conducted according to the criteria of Peach Bottom Atomic Power Station, Unit 3, Plant Technical Specifications.
The test results are repcrted in accordance with the requirements of 10CFR50, Appendix J, Section V.B.3.
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(} II. TEST SYNOPSIS
- Prior to containment pressurization on August 21, 1983, and sub-sequent ' to completing the verification test on August 23, 1983, y, . Peach Bottom Atomic Power Station, Unit 3, site test and main-tenance personnel were engaged in activities related to contain-ment leakage. Containment leakage was identified through the Type B and C local leakage rate testing programs and reduced by
' repairs to those systems and containment components having ex-cessive ' leakage. The results of the local leakage rate tests are g - given in Appendix M.
~ The following discussion highlights some of the activities men-tioned above and present some items that were essential to the successful and timely completion of the Type A test. These items have been presented in a chronological order and are considered to be some of the most significant activities encountered during test preparation and execution.
A. Pre pressurization Activities Pre pressurization activities included: Completing all Type B and Type C testing; Type A test procedure review; final li' instrumentation operability checks; final ILRT computer program modifications;, and containment subvolume weighting rN f actor calculation checks. A few of these items are discussed
(_) ~ below to.present pertinent information that impacted in Type A Test activities.
Local Jeakage rate testing at Peach Bottom Atomic Power Station, Unit 3 began on January 6,1983, two weeks prior to start of the refueling. outage. The results of this program are summarized in Appendix M, "Results of Local Leakage Rate Tests".
The' Type A test procedure review was conducted to ensure that all references to Plant Technical Specifications, 10CFR50
, Appendix J, ANSI /ANS 56.8-1981, and the FSAR were accurate and current. In addition to verifying that the procedure was in compliance with the appropriate guidelines, the valve line-up was reviewed to ensure that the containcent systems were in as' close to post-accident arrangement as possible.
Final ILRT instrumentation operability checks were performed to ensure that all instrumentation was operating correctly.
An in situ check, as specified in ANSI /ANS 56.8-1981, Sect ion 4.2.3.1, was conducted to verify that all ILRT instrumentation was working correctly.
B. Containment Pressurization Containment pressurization started at 0525 hr, on August 21, 1983, at the rat'e of 4.95 psi /hr. Two compressors were
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running at about 60 psig. The containment test pressure (s /)
_ was reached at 1530 hrs on August 21, 1983.
C. Containment Atmosphere Stabilization At 1930 hrs on August 21, 1983, all stabilization criteria as specified in ANSI /ANS 56.8-1981, section 5.3.1.6, were satisfied. However, at the end of four hours, the contain-ment temperature was still dropping, due to low chilled water temperature. At 1930 hours0.0223 days <br />0.536 hours <br />0.00319 weeks <br />7.34365e-4 months <br /> on August 21, 1983, it was decided to increase the chilled water temperature. This resulted in increase in the containment weighted average t empe rature. The temperature manipulation of the chilled water was . stopped at 2015 hr. The containment weighted average temperature versus time plot yielded a straight line for data taken af ter 2100 hrs, on August 21, 1983. During this entire period the sensor displays for temperature, dew point, and pressure were carefully monitored to verify correct sensor operability.
D. First Test Period Subs eq uent to reaching a plateau for the weighted average containment temperature, leakage rate analysis began at 2115 hrs, on August 21, 1983.
(f At 2230 hrs, a leak path was discovered on packing of RHR-MO-34A valve. The valve packing was back seated and maintenance on the valve was initiated. Although temperature, dew cell, and pressure data were recorded nt 15 minute intervals during the repair work, the initial test period was considered a failed ILRT.
E. Second Test Period (successful ILRT)
Prior to starting the second primary containment Integrated Leakage Rate Test (ILRT), a hose carrying high pressure service cooling water from a RHR heat exchanger ruptured.
This required shutting down the RHR pump, resulting in a significant increase of reactor water temperature and conse-quently the containment air temperature. This caused a delay the starting time for the ILRT to 1630 hrs on August 22, 1983. Af ter stabilization, the ILRT was successfully completed at 0045 hrs on August 23, 1983. The maximum allow-able leakage rate (La) for the primary containment is 0.5 wt.% per day of contained air mass at the peak test pressure of 49.1 psig. The measured leakage rate based on mass point analysis is 0.058 wt% per day with 95% UCL of 0.081 wt.% per day.
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A successful verification flow test was conducted following the ILRT. It started at 0315 hr on August 23, 1983, and completed at 0715 hr the same day. The calculated imposed leakage rate (Lo) is 0.5 wt.% per day (4.41 scfm). The test result are summarized as follows:
Test Method Measured (Allow.) 95% UCL (Allow.)
- 1. ILRT/ Mass Point (Lam) 0.058 (0.375) 0.081 (0.375)
- 2. Verification / (Lvm) 0.431 (0.428-0.678)
Mass Point-F. Subsequent to the ILRT and the verification test, the Drywell-to-Torus Bypass Area Test (DTBAT) was conducted. The ter -
started at 1112 hr on August 28, 1983 and successfully ce t-
' pleted after I hour. The maximum acceptable bypass ares, as delineated in the PBAPS Technical Specification is equivalent to a 1.00 inch I.D. orifice or 0.785 square inch. The calculated bypass area is 0.098 square inch.
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(~') III TEST DATA
SUMMARY
v A. Plant Information Owner Plant Philadalphia Electric Company Peach Bottom Atomic Power Station, Unit 3 Location Delta, Pennsylvania Containment Type Metal Vessel Suppression Pool NSSS Supplier, Type General Electric, BWR Date Test Completed August 23, 1983 B. Technical Data
- 1. Nominal Containment 293,900 eu. f t.
Net Free Air Volume
- 2. Design Pressure, P 56 psig
- 3. Design Temperature, T 276*F
- 4. Calculated Peak 49.1 psig Accident Pressure, P a
- 5. Containment ILRT Average 4 0-13 5'F s
Temperature Limits
~s
- 6. Calculated Peak 283'F Accident Temperature C. Test Results - Type A Test
- 1. Test Method Absolute
- 2. Data Analysis Technique Mass Point (per ANSI /ANS 56.8-1981)
- 3. Test Pressure 49.1 psig
- 4. Maximum Allowable 0.500 wt.%/ day Leakage Rate, L a
- 5. 7 5% of La 0.375 wt.%/ day
- 6. Integrated Laakage Rate Test Results Mass Point Analysis:
- a. Calculated Leakage Rate wt.%/ day from regression line, L am = 0.0 58 fs b. Upper 95% Confidence (m,) Limit = 0.081 SU-042 5
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"% 7. Verification Test Imposed 4.41 scfm (k-I Leakage Rate (0.5 wt.%/ day) i
- 8. Verification Test Results Mass Point Analysis Leakage Rate 0.431 (wt.%/ day)
- 9. Verification Test Limits Mass Point Analysis Test Limits (wt.%/ day)
- 1) Upper limit (Lo+ Lam +0.25La) 0.678 -
. 2)- Lower limit (Lo+ Lam-0.25La) 0.4 28 '
- 10. Report Printouts '
, The Report Printouts of the Type A and DTBAT verifica-tion test calculations are provided for the Mas's Point Analysis (Appendixes B through N). Stabilization data are also provided (Appendix A).
D. Test Results - Types B and C Tests Refer to Appendix M for a summary of local leakage rate test results since the last ILRT performed in 1981. ,
E. Integrated Leakage Rate Measurement System j 1. Absolute Pressure (one main plus one backup)
Range 0-100,000 counts ,
Repeatability 0.001 psia Accuracy 0.015% F.S.
Resolution 0.001 psia i Range. 0-100 psia Sensitivity. 0.001 psia Texas Instuments Model 145-02 Precision Pressure Instrument, Serial No. 2604 Bourdon Capsule (Type 2) Serial No.10381 .
Calibration Date: June 24,1983 Spare: Instrument Serial No. 2605 and Bourdon Capsule Serial No. 10380
- 2. Drybulb Temperature (12 plus 6 spares)
' Resistance Temperature Detectors - Omega Engineering 1000 Platinum Resistance Temperature System, Model CAT-PR-13 100-1/4-5 1/2-E Accuracy: j;0.5'F l Repeatability: + 0.01'F j] Static Resistance: 100 ohms
\_/ Sensitivity: < 0.l*F
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Readout - Fluke Digital Display, (x_'/} Cat. No. 2180A. ,
I Calibration Date: April 11, 1983 Calibration Standard - Philadelphia Electric Company Instrument Number 5557
- 3. Dewpoint Temperature (6 sensors)
Dewpoint Temperature Probes - General Eastern, Model 1200APS Accuracy: 1 2'F Repeatability: 0.l'F Sensitivity: 1 0.5'F Dew Cell assemblies (calibration date: April 21,1983)
S/N 1269 S/N 1275 S/N 1271 S/N 1277 S/N 1273 S/N 1279
- 4. Verification Flow (1 channel)
Flowmeter - Brooks hi-accuracy full view rotameter, fS Model 1110-08K2A1A, Serial No. 8302H05424 V
Range: 0.95 - 9.7 scfm Accuracy: 1 1% Full Scale Calibration Date: March 3,1983
- 5. Overall Instrumentation Selection Guideline (ISG) Value (from ANSI / ANS-56.8-1981 based on ILRT instrumentation and an eight hour minimum test duration = 0.032
- 6. Drybulb and Dewpoint Temperature Sensor Volume Fractions see Procedure retained at jobsite.
F. Information Retained at Plant The following information is available for review at the facility:
- 1. Access control procedures that were established to limit ingress to containment during testing.
- 2. A listing of all containment penetrations, including the -
total number of like penetrations, penetration size, and f unction.
- 3. A listing of normal operating instrumentation used for
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" A system lineup (at time of test), showing required valve positions and status of piping systems.
- 5. A continuous, sequential log of events from initial survey of containment to restoration of all tested systems.
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Documentation of instrumentation calibrations and standards.
Included with documentation should be an error analysis of instrumentation.
- 7. Data to verify temperature stabilization criteria as estab-lished by test procedure (Appendix A). f
- 8. The working copy of test procedure that would include signature sign-off of procedural steps.
- 9. The procedure and all data that would verify completion of penetrations and valve testing (B&C-type tests),
including as-found leak rates, corrective action taken, and final leak rate.
- 10. Computer printouts of Integrated Leakage Rate Test Data and manual data accumulation along with summary descrip-
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tion of computer program (Appendixes B through C).
> . 11. The Quality Assurance audit plan or checklist that was
- j. (s) used to monitor-ILRT with proper sign-offs.
, 12. A listing of all test exceptions including changes in containment system boundaries instituted by licensee to conclude successful testing.
- 13. Description of sensor malfunctions, repairs, and methods used to redistribute volume fractions to operating instru-mentation.
- 14. >
A review of confidence limits of test results with accom-panying computer printouts where applicable.
- 15. Description of method of leakage rate verification of
- instrument measuring system (superimposed leakage), with l
calibration information on flowmeters along with calcula-tions that were used to measure the verification leakage rate (Appendixes I through K).
- 16. Plots presenting ILRT data obtained during the test (Appendixes D through G).
- 17. The P& ids of pertinent systems readily available.
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i IV. ANALYSIS AND INTERPRETATION ,
- Several corrections must be added to the calculated result ' of the Unit 3 ILRT.
Additions to ILRT total as a result of repairs and adjustments made ;
during the Unit 3 refueling outage (leakages are in SCC / min):
1
- 1. Penetration N-7A MSIV 80A, 86A '
As found penetration leak rate 2178
. . As left ' penetration leak rate 20 Addition to ILRT total 2158 t
- 2. Penetration N-7B MSIV 808,.86B As found penetration leak rate 3295 As lef t penetration leak rate 1974 Addition to ILRT total 1321
- 3. Penetration N-7C L
MSIV , . 8 0C, 86C As found penetration leak rate 669
- As lef t penetration . leak rate 300 j Addition to'IURT total 369
- 4. Penetration N-7D MSIV, 80D, 86D
, As found penetration leak rate 2035 As lef t penetration leak rate 591 Addition to ILRT total 1444 I
- 5. Penetration N-8 MO 2-74, 2-77 As found penetration leak rate 450 As left penetration leak rate- 115 Addition to ILRT total 335 L
4 6.- Penetration N-9A *1 ,
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- 8. Penetration N-14 *1
- 9. Penetration N-18 A0 2-82, 2-83 As found penetration leak rate 200 As lef t penetration leak rate 35 Addition to ILRT total 165
- 10. Penetration N-26 *1
- 11. Penetration N-51A SV-3671E, 3978E As found penetration leak rate 310 As lef t penetration leak rate 20 Addition to ILRT total 290 12.
() Penetration N-51B SV-3671D, 3978D As found penetration leak rate 150 As left penetration leak rate 40 Addition to ILRT total 110
- 13. Penetration N-51C
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- 14. Penetration N-51D *1
- 15. Penetration N-52F *1
- 16. Penetration N-203 *1 SV-3671B, 3978B As found penetration leak rate 59 As lef t penetration leak rate 40 Addition to ILRT total 19
- 17. Penetration N-211f.
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( 18. Penetration N-211B (RBR) *2
- 19. Penetration N-211B (CAD) *1
- 20. Penetration N-212 *1
- 21. Penetration N-214 *1
- 22. Penetration N-2178 MO-5245 As found penetration leak rate 1220 As lef t penetration leak rate 65 Addition to ILRT total 1155
- 23. Penetration N-218B *1
- 24. Penetration N-218C O As found penetration leak rate As left penetration leak rate Additica to ILRT total 95 10 85
- 25. Penetration N-221 *1
- 26. "A" RHR sample *1
- 27. "D" RHR sample As found penetration leak rate 333 As lef t penetration leak rate 30 i
Addition to ILRT total 303 28.. Scram discharge volume vents CV 2-32B, 2-35B As found penetration leak rate 230 As lef t penetration leak rate 150 Addition to ILRT total 80 O
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() 29. Scram discharge volume drains CV 2-33, 2-36
- 3 NOTES:
- 1 -- As lef t penetration leak rate was no better than as found, even af ter repairs. No addition to ILRT is required.
- 2 -- LLRT changes to ECCS system which are normally pressurized during the ILRT should not be added to the "as lef t" ILRT since leakage on these valvas would, in no way, affect ILRT results.
- 3 -- Water sealed during accident conditions. No addition to ILRT total is required.
Total addition to ILRT as a result of repairs and adjustments: 7834 sec/ min Several corrections must be added to the calculated result of the Unit 3 ILRT. The following valves were not in the normal positon 1
for accident condition:
RBCC W'ter a 273 SCC / min
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Chilled Water Valves Shutdown Cooling Valves 3500 SCC / min 500 SCC / min
[ ILRT Test Valves 40 SCC / min TOTAL 4313 Drywell sump level increased during the test. This resulted in a volume decrease equivalent to 943 SCC / min. CRD accumulator in leakage per ST 12.5.1 Appendix N was 736 SCC / min. The above corections total 13,826 - SCC / min or 0.055 %/ day. The corrected test results are summarized as follows:
, Lam 95% UCL I II III I II III__
- 1. ILRT/ Mass Point 0.058 0.113 0.375 0.081 0.136 0.375
- 2. Verification / 0.431 0.486 0.428-0.678 Mass Point where Column I =
Leak rate corresponding to that reported in pre-liminary report dated August 23, 1983 m
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for posttest LLRTs, CRD accumulator leakage, ,
and drywell sump level change Column III = Allowable leak rates The Integrated Leakage Rate Test res*dts at the upper 95% conf 1-dence level, L am = 0.136 wt.%/ day (Mass Point analysis) satisfy the acceptance criterion of L a = 0.375 wt.%/ day, at Pa
= 49.1 psig (-0 psi, + 1 psi)am < 0.75L .
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i APPENDIX A r STABILIZATION
SUMMARY
DATA t
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(_)
PEACH BOTTOM UNIT 3 ILRT
SUMMARY
DATA ALMAX = .500 VOLUME = 293900.
VRATET = .392 VRATEM = .381 TIME DATE TEMP PRESSURE VPRS VOLUME 1530' 821 541.135 63.9841 .3690 293700.
1545 821 540.808 63.9635 .3657 293900.
1600 821 540.592 63.9636 .3645 293900.
1615 821 540.437 63.9698 .3633 293900.
1630 821 540.279 63.9774 . 3617 293900.
1645 821 540.140 63.9879 .3603 293900.
1700 821 539.988 63.9645 .3596 293900.
1715 821 539.869 63.9449 .3582 293900.
1730 821 539.738 63.9252 .3579 293900.
1745 821 539.642 63.9077 .3574 293900.
1800 821 539.544 63.8891 .3571 293900.
1815 821 539.451 63.8742 .3560 293900.
1830 821 539.373 63.8574 .3557 293900.
1845 821 539.315 63.8410 .3552 293900.
1900 821 539.238 63.8272 .3549 293900.
1915 821 539.176 63.8142 .3540 293900.
f~T U 1930 821 539.195 63.8050 .3551 293900.
m Asl
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r PEACH BOTTOM UNIT 3 ILRT TEMPER' 'RE ST ABILIZATION
-Os FROM A STARTINL AND DATE OF: 1530 821 1983 TIME TEMP ANSI BN-TOP-1 (HOURS) (OR) AVE AT AVE AT DIFF AVE T (4 HRS) (1HR) (2 HRS)
. 00 541.11
. 25 540.79
. 50 540.57
. 75 540.42 1.00 540.26 1.25 540.12 1.50 539.97
- 1.75 539.85 2.00 939.72- .700*
2.25 539.62 .584*
2.50 . 539.52 .525*
2.75- 539.43 .493*
3.00 539.35 .453*
3.25 539.29 .413*
i 3.50 539.22 .375*
3.'75 539.15 .347*
4.00 539.17 . 486 .179 . 31* .136*
().
- INDICATES TEMPERATURE STABILIZATION HAS BEEN SATISFIED
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SUMMARY
OF MEASURED DATA AT 1530 821 I) TEMP TEMP 1
2
=
=
554.5500 556.5980
(
(
94.650 96.700
)
)
TEMP 3 = 537.1060 ( 77.100 )
TEMP 4 = 537.1130 ( 77.790 )
TEMP 5 = 534.6660 ( 74.940 )
TEMP 6 = 534.4380 ( 74.430 )
TEMP 7 = 529.7720 ( 69.940 )
TEMP 8 = 528.0860 ( 68.250 )
TEMP 9 = 527.0440 ( 67.420 )
TEMP 10 = 544.2390 ( 84.730 )
TEMP 11 = 544.4620 ( 84.700 )
TEMP 12 = 544.4330 ( 85.080 )
PRES 1 = 64.3421 ( 64344.0 )
PRES 2= 64.3534 ( 64355.0 )
VPRS 1 = .2489 ( 59.200 )
VPRS 2= .2419 ( 58.600 )
VPRS 3= .2384 ( 58.800 )
VPRS 4= .2376 ( 58.900 )
VPRS 5= .5048 ( 80.600 )
VPRS 6= .5567 ( 83.600 )
7,
SUMMARY
OF CORRECTED DATA
)
( TIME = 1530 DATE = 821 TEMPERATURE (DEGREES R.) = 541.1350 CORRECTED PRESSURE (PSIA) = 63.9748 VAPOR PRESSURE (PSIA) = .3673 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 937E4.5
,. \
%s A-4
SUMMARY
OF MEASUREC DATA AT 1545 821
,,m
( ) TEMP 1 = 554.2090 ( 94.310 )
'~'
TEMP 2 = 556.3480 ( 96.450 )
TEMP 3 = 536.9660- ( 76.960 )
TEMP 4 = 536.6750 ( 77.350 )
TEMP 5 = 534.3670 ( 74.640 )
TEMP 6 = 534.1480 ( 74.1/O )
TEMP 7 = 529.7320 ( 69.900 )
TEMP 8 = 528.3360 ( 68.500 )
TEMP 9 = 526.9640 ( 67.340 )
TEMP 10 = 543.8780 ( 84.370 )
TEMP 11 = 543.8830 ( 84.120 )
TEMP 12 = 543.9440 ( 84.590 )
PRES 1 = 64.3171 ( 64319.0 )
PRES 2= 64.3295 ( 64331.0 )
VPRS 1 = .2471 ( 59.000 )
VPRS 2= .2384 ( 58.200 )
VPRS 3= .2359 ( 58.500 )
VPRS 4= .2350 ( 58.600 )
VPRS 5= .4996 ( 80.300 )
VPRS 6= .5532 ( 83.400 )
SUMMARY
OF CORRECTED DATA
/~')
\/ TIME = 1545 DATE = 821 TEMPERATURE (DEGREES R.) = 540.8080 CORRECTED PRESSURE (PSIA) = 63.9532 VAPOR PRESSURE (PSIA) = .3640 VOLUME (CU.FT.)
~
= 293900.0 AIR MASS (LBM) = 93809.6 O
G A-5
SUMMARY
OF MEASURED DATA AT 1600 821
,m
( )
~~' TEMP 1 = 553.9690 ( 94.070 )
TEMP 2 = 556.0280 ( 96.130 )
TEMP 3 = 536.7960 ( 76.790 )
TEMP 4 = 536.6750 ( 77.350 )
TEMP 5 = 534.2070 ( 74.480 )
TEMP 6 = 533.9390 ( 73.930 )
TEMP 7 = 529.5230 ( 69.690 )
TEMP 8 = 528.0560 ( 68.220 )
TEMP 9 = 526.9250 ( 67.300 )
TEMP 10 = 543.6180 ( 84.110 )
TEMP 11 = 543.6240 ( 83.860 )
TEMP 12 = 543.6940 ( 84.340 )
PRES 1 = 64.3141 ( 64316.0 )
PRES 2= 64.3285 ( 64330.0 )
VPRS 1= .2454 ( 58.800 )
VPRS 2= .2376 ( 58.100 )
VPRS 3= .2342 ( 58.300 )
VPRS 4= .2342 ( 58.500 )
VPRS 5= .5013 ( 80.400 )
VPRS 6= .5497 ( 83.200 )
SUMMARY
OF CORRECTED DATA
[^')
- /
TIME = 1600 DATE = 821 TEMPERATURE (DEGREES R.) = 540.5920 CORRECTED PRESSURE (PSIA) = 63.0513 VAPOR PRESSURE (PSIA) = .3628 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93844.4 7
\m/
'A-6
SUMMARY
OF MEASURED DATA AT 1615 821
() ,
TEMP 1 = 553.8280 ( 93.930 )
TEMP 2 = 555.8180 ( 95.920 )
TEMP 3 = 536.6760 ( 76.670 )
TEMP 4 = 536.3660 ( 77.040 )
TEMP 5 = 533.9380 ( 74.210 )
TEMP 6 = 533.8290 ( 73.820 )
TEMP 7 = 529.4230 -( 69.590 )
TEMP 8 = 528.0960 ( 68.260 )
TEMP 9 = 526.7550 ( 67.130 )
TEMP 10 = 543.4980 ( 83.990 )
TEMP 11 = 543.4650 ( 83.700 )
TEMP 12 = 543.5440 ( 84.190 )
PRES 1 = 64.3201 ( 64322.0 )
PRES 2= 64.3335 ( 64335.0 )
VPRS 1 = .2445 ( 58.700 )
VPRS 2= .2367 ( 58.000 )
VPRS 3= .2333 ( 58.200 )
VPRS 4= .2333 ( 58.400 )
VPRS 5= .4979 ( 80.2 ,
VPRS 6= .5497 ( 83.Lvv )
,s
SUMMARY
OF CORRECTED DATA
() TIME = 1615 DATE = 821 TEMPERATURE (DEGREES R.) = 540.4370 CCARECTED PRESSURE (PSIA) = 63.9585 VAPOR PRESSURE (PSIA) = .3616 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93881.8
. !3(
Y, A-7
SUMMARY
OF MEASURED DATA AT 1630 821
() TEMP TEMP 1
2
=
=
553.6080 555.7980
(
(
93.710 95.900
)
)
TEMP 3 = 536.3860 ( 76.380 )
TEMP 4 = 536.3470 ( 77.020 )
TEMP 5 = 533.7180 ( 73.990 )
TEMP 6 = 533.7890 ( 73.780 )
TEMP 7 = 529.3630 ( 69.530 )
TEMP O = 527.5560 ( 67.720 )
TEMP 9 = 526.7350 ( 67.110 )
TEMP 10 = 543.3270 ( 83.820 )
TEMP 11 = 543.2950 ( 83.530 )
TEMP 12 = 543.4140 ( 84.060 )
PRES 1 = 64.3291 ( 64331.0 )
PRES 2= 64.3395 ( 64341.0 )
VPRS 1 = .2436 ( 58.600 )
VPRS 2= .2367 ( 58.000 )
VPRS 3= .2325 ( 58.100 )
VPRS 4= .2317 ( 58.200 )
VPRS 5= .4945 ( 80.000 )
VPRS 6= .5479 ( 83.100 )
-s
SUMMARY
OF CORRECTED DATA l*' ^) TIME = 1630 DATE = 821 TEMPERATURE (DEGREES R.) = 540.2790 CORRECTED PRESSURE (PSIA) = 63.9691 VAPOR PRESSURE (PSIA) = .3600 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93924.8 r.,
V A-8
SUMMARY
OF MEASURED DATA AT 1645 821
,m
() TEMP TEMP 1
2
=
=
553.4480 555.5580
(
(
93.550 95.660
)
)
TEMP 3 = 536.2160 ( 76.210 )
TEMP 4 = 536.1380 ( 76.810 )
TEMP 5 = 533.7880 ( 74.060 )
TEMP 6 = 533.5490 ( 73.540 )
TEMP 7 = 529.2040 ( 69.370 )
TEMP 8 = 527.6460 ( 67.810 )
TEMP 9 = 526.6750 ( 67.050 )
TEMP 10 = 543.1670 ( 83.660 )
TEMP 11 = 543.1350 ( 83.370 )
TEMP 12 = 543.2750 ( 83.920 )
PRES 1 = 64.3371 ( 64339.0 )
PRES 2= 64.3484 ( 64350.0 )
VPRS 1 = .2427 ( 58.500 )
VPRS 2= .2367 ( 58.000 )
VPRS 3= .2325 ( 58.100 )
VPRS 4= .2325 ( 58.300 )
VPRS 5= .4910 ( 79.800 )
VPRS 6= .5444 ( 87.900 )
SUMMARY
OF CORRECTED DATA I)
TIME = 1645 DATE = 821 TEMPERATURE (DEGREES R.) = 540.1400 CORRECTED PRESSURE (PSIA) = 63.9786 VAPOR PRESSURE (PSIA) = .3585 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93962.9
,f ~3
\_Y A-9
SUMMARY
OF MEASURED DA1A AT 1700 821
(,) TEMP 1 = 553.2770 ( 93.380 )
TEMP 2 = 555.2680 ( 95.370 )
TEMP 3 = 536.1960 ( 76.190 )
TEMP 4 = 535.6700 ( 76.340 )
TEMP 5 = 533.5590 ( 73.830 )
TEMP 6 = 53.3.6490 ( 73.640 )
TEMP 7 = 529.1040 ( 69.270 )
TEMP 8 = 527.7360 ( 67.900 )
TEMP 9 = 526.5750 ( 66.950 )
TEMP 10 = 543.0270 (, 83.520 )
TEMP 11 = 542.9260 ( 83.160 )
TEMP 12 = 543.1150 ( 83.760 )
PRES 1 = 64.3111 ( 64313.0 )
PRES 2= 64.3245 ( 64326.0 )
VPRS 1 = .2419 ( 58.400 )
VPRS 2= .2342 ( 57.700 )
VPRS 3= .2308 ( 57.900 )
VPRS 4= .2308 ( 58.100 )
VPRS 5= .4927 ( 79.900 )
VPRS 6= .5444 ( 82.900 )
SUMMARY
OF CORRECTED DATA
() TIME = 1700 DATE = 821 TEMPERATURE (DEGREES R.) = 539.9880 CORRECTED PRESSURE (PSIA) = 63.9532 VAPOR PRESSURE (PSIA) = .3579 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93952.1 rm
> t
%)
A-10 L.
SUMMARY
OF MEASURED DATA AT 1715 821
()
-- s TEMP 1 = 553.1070 ( 93.210 )
TEMP 2 = 555.0980 ( 95.200 )
TEMP 3 = 535.9060 ( 75.900 )
TEMP 4 = 535.8790 ( 76.550 )
TEMP 5 = 533.5090 ( 73.780 )
TEMP 6 = 533.4290 ( 73.420 )
TEMP 7 = 529.1040 ( 69.270 )
TEMP 8 = 527.5360 ( 67.700 )
TEMP 9 = 526.5050 ( 66.880 )
TEMP 10 = 542.8960 ( 83.390 )
TEMP 11 = 542.7860 ( 83.020 )
. TEMP 12 = 542.9950 ( 83.640 )
PRES 1 = 64.2911 ( 64293.0 )
PRES 2= 64.3030 ( 64305.0 )
VPRS 1 = .2410 ( 58.300 )
VPRS 2= .2333 ( 57.600 )
VPRS 3= .2308 ( 57.900 )
VPRS 4= .2300 ( 58.000 )
VPRS 5= .4893 ( 79.700 )
VPRS 6= .5427 ( 82.800 )
SUMMARY
OF CORRECTED DATA I TIME = 1715
~
DATE = 821 TEMPERATURE (DEGREES R.) = 539.8690 CORRECTED PRESSURE'(PSIA) = 63.9347 VAPOR PRESSURE (PSIA) = .3564 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93945.5
/~'s U
A-ll
SUMMARY
.0F MEASURED DATA AT 1730 821 7)%
(_ TEMP 1 = 552.8760 ( 92.980 )
TEMP 2 = 554.9780 ( 95.080 )
TEMP 3 = 535.8460 ( 75.840 )
TEMP 4 = 535.6300 ( 76.300 )
TEMP 5 = 533.3390 ( 73.610 )
TEMP 6 = 533.3790 ( 73.370 )
TEMP 7 = 529.0140 ( 69.180 )
TEMP 8 = 527.4760 ( 67.640 )
TEMP 9 = 526.3850 ( 66.760 )
TEMP 10 = 542.7660 ( 83.260 )
TEMP 11 = 542.6370 ( 82.870 )
TEMP 12 = 542.8750 ( 83.520 )
PRES 1 = 64.2686 ( 64270.0 )
PRES 2= 64.2831 ( 64285.0 )
VPRS 1 = .2410 ( 58.300 )
VPRS 2= .2325 ( 57.500 )
VPRS 3= .2376 ( 57.800 )
VPRS 4= .2300 ( 58.000 )
VPRS 5= .4932 ( 79.800 )
VPRS 6= .5409 ( 82.700 )
SUMMARY
OF CORRECTED DATA
()
TIME = 1730 DATE = 821 TEMPERATURE (DEGREES R.) = 539.7380 CORRECTED PRESSURE (PSIA) = 63.9252 VAPOR PRESSURE (PSIA) = .3579 VOLUME (CU.FT.) = 293900.0
, AIR MASS (LBM) = 93954.5
,m.
.s A-12
SUMMARY
OF MEASURED DATA AT 1745 821 jm
(
'~'
) TEMP 1 = 552.8060 ( 92.910 )
TEMP 2 = 554.8580 ( 94.960 )
TEMP 3 = 535.7160 ( 75.710 )
TEMP 4 = 535.5210 ( 76.190 )
TEMP 5 = 533.3090 ( 73.580 )
TEMP 6 = 533.1000 ( 73.090 )
TEMP. 7 = 528.9150 ( 69.080 )
TEMP G = 527.6060 ( 67.770 )
TEMP 9 = 526.3750 ( 66.750 )
TEMP 10 = 542.6860 ( 83.180 )
TEMP 11 = 542.5270 ( 82.760 )
TEMP 12 = 542.7750 ( 83.420 )
PRES 1 = 64.2496 ( 64251.0 )
PRES 2= 64.2651 ( 64267.0 )
VPRS 1 e .2401 ( 58.200 )
VPRS 2= .2317 ( 57.400 )
VPRS 3= .2367 ( 57.700 )
VPRS 4= .2292 ( 57.900 )
VPRS 5= .4932 ( 79.800 )
VPRS 6= .5409 ( 82.700 )
()
SUMMARY
OF CORRECTED DATA TIME = 1745 DATE = 821 TEMPERATURE (DEGREES R.) = 539.6420 CORRECTED PRESSURE (PSIA) = 63.9077 VAPOR PRESSURE (PSIA) = .3574 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93945.5 r
A-13
SUMMARY
OF MEASURED DATA AT 1800 821 TEMP 1 = 552.5960 ( 92.700 )
TEMP 2 = 554.5370 ( 94.640 )
TEMP 3 = 535.7460 ( 75.740 )
TEMP 4 = 535.5010 ( 76.170 )
TEMP 5 - 533.1900 ( 73.460 )
TEMP 6 = 533.0500 ( 73.040 )
TEMP 7 = 528.8850 ( 69.050 )
TEMP 8 = 527.4460 ( 67.610 )
TEMP 9 = 526.3550 ( 66.730 )
TEMP 10 = 542.6260 ( 83.120 )
TEMP 11 = 542.4070 ( 82.640 )
TEMP 12 = 542.6760 ( 83.320 )
PRES 1 = 64.2297 ( 64231.0 )
PRES 2= 64.2462 ( 64248.0 )
VPRS 1 = .2401 ( 58.200 )
VPRS 2= .2317 ( 57.400 )
VPRS 3= .2367 ( 57.700 )
VPRS 4= .2292 ( 57.900 )
VPRS 5= .4916 ( 79.700 )
VPRS 6= .5409 ( 82.700 )
SUMMARY
OF CORRECTED DATA TIME = 1800 f( ) DATE = 821 TEMPERATURE (DE8REES R.) = 539.5440 CORRECTED PRESSURE (PSIA) = 63.8891 VAPOR PRESSURE (PSIA) = .3571 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93935.2
(~')
v A-14
SUMMARY
OF MEASURED DATA AT 1815 821 f; TEMP 1 = 552.5060 ( 92.610 )
TEMP 2 = 554.4970 ( 94.600 )
TEMP 3 = 535.4060 ( 75.400 )
TEMP 4 = 535.4310 ( 76.100 )
TEMP 5 = 533.1000 ( 73.370 )
TEMP 6 = 532.9800 ( 72.970 )
TEMP 7 = 528.8050 ( 68.970 )
TEMP 8 = 527.5060 ( 67.670 )
TEMP 9 = 526.2450 ( 66.620 )
TEMP 10 = 542.5460 ( 83.040 )
TEMP 11 = 542.3080 ( 82.540 )
TEMP 12 = 542.5960 ( 83.240 )
PRES 1 = 64.2117 ( 64213.0 )
PRES 2= 64.2302 ( 64232.0 )
VPRS 1 = .2393 ( 58.100 )
VPRS 2= .2317 ( 57.400 )
VPRS 3= .2359 ( 57.600 )
VPRS 4= .2283 ( 57.800 )
VPRS 5= .4900 ( 79.600 )
VPRS 6= .5392 ( 82.600 )
SUMMARY
OF CORRECTED DATA
(~ TIME = 1815 k- ' DATE = 821 TEMPERATURE (DEGREES R.) = 539.4510 CORRECTED PRESSURE (PSIA) = 63.8742 VAPOR PRESSURE (PSIA) = .3560 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93929.4 r~.
v A-15
SUMMARY
OF MEASURED DATA AT 1830 821 g
(,) TEMP 1 = 552.3750 ( 92.480 )
TEMP 2 = 554.5270 ( 94.630 )
TEMP 3 = 535.3260 ( 75.320 )
TEMP 4 = 535.3420 ( 76.010 )
TEMP 5 = 533.0900 ( 73.360 )
TEMP 6 = 532.8800 ( 72.870 )
TEMP 7 = 528.7650 ( 68.930 )
TEMP 8 = 527.0360 ( 67.200 )
TEMP 9 = 526.2550 ( 66.630 )
TEMP 10 = 542.4860 ( 82.980 )
TEMP 11 = 542.2580 ( 82.490 )
TEMP 12 = 542.5360 ( 83.180 )
PRES 1 = 64.1958 ( 64197.0 )
PRES 2= 64.2132 ( 64215.0 )
VPRS 1 = .2393 ( $8.100 )
VPRS 2= .2308 ( 57.300 )
VPRS 3= .2350 ( 57.500 )
VPRS 4= .2283 ( 57.800 )
VPRS 5= .4900 ( 7?.600 )
VPRS 6= .5392 ( 82.600 )
SUMMARY
OF CORRECTED DATA bs) TIME = 1830
~ DATE = 821 TEMPERATURE (DEGREES R.) = 539.3730 CORRECTED PRESSURE (PSIA) = 63.8574 VAPOR PRESSURE (PSIA) = .3557 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93918.3 r9 h
'%)
A-16
SUMMARY
OF MEASURED DATA AT 1845 821 y,
(' ~ i TEMP 1 = 552.2850 ( 92.390 )
TEMP 2 = 554.3870 ( 94.490 )
TEMP 3 = 535.4860 ( 75.480 )
TEMP 4 = 535.3220 ( 75.990 )
TEMP 5 = 533.0200 ( 73.290 )
TEMP 6 = 532.6310 ( 72.620 )
TEMP 7 = 528.7450 ( 68.910 )
TEMP 8 = $27.1460 ( 67.310 )
TEMP 9 = 526.1750 ( 66.550 )
TEMP 10 = 542.4160 ( 82.910 )
TEMP 11'= 542.1980 ( 82.430 )
TEMP 12 = 542.4660 ( 83.110 )
PRES 1= 64.1788 ( 64180.0 )
PRES 2= 64.1962 ( 64198.0 )
VPRS 1 = .2384 ( 58.000 )
VPRS 2= .2308 ( 57.300 )
VPRS 3= .2350 ( 57.500 )
VPRS 4= .2275 ( 57.700 )
VPRS 5= .4883 ( 79.500 )
VPRS 6= .5392 ( 82.600 )
7._s
SUMMARY
OF CORRECTED DATA
( ) TIME = 1845 DATE = 821 TEMPERATURE (DEGREES,R.) = 539.3150 CORRECTED PRESSURE (PSIA) = 63.8410 VAPOR PRESSURE (PSIA) = .3552 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93904.2 f
+
( !
A-17
SUMMARY
OF MEASURED DATA AT 1900 821
,3
( ) TEMP 1 = 552.2250 ( 92.330 )
TEMP 2 = 554.2170 ( 94.320 )
TEMP 3 = 535.2160 ( 75.210 )
TEMP 4 = 535.1130 ( 75.780 )
TEMP 5 = 532.9500 ( 73.220 )
TEMP 6 = 532.6710 ( 72.660 )
TEMP 7 = 528.6950 ( 68.860 )
TEMP 8 = 527.1360 ( 67.300 )
TEMP 9 = 526.1350 ( 66.510 )
TEMP 10 = 542.3750 ( 82.970 )
TEMP 11 = 542.1380 ( 82.370 )
TEl1P 12 = 542.4160 ( 83.060 )
PRES 1 = 64.1658 ( 64167.0 )
PRES 2= 64.1822 ( 64184.0 )
VPRS 1 = .2384 ( 58.000 )
VPRS 2= .2300 ( 57.200 )
VPRS 3= .2350 ( 57.500 )
VPRS 4= .2267 ( 57.600 )
VPRS 5= .4883 ( 79.500 )
.VPRS 6= .5392 ( 82.600 )
SUMMARY
OF CORRECTED DATA l > TIME = 1900 DATE = 821 TEMPERATURE (DEGREES R.) = 539.2380 CORRECTED PRESSURE (PSIA) = 63.8272 VAPOR PRESSURE (PSIA) = .3549 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93077.4 r~s, Li' A-18
SUMMARY
0F MEASURED DATA AT 1915 821' L# 'T TEMP 1 = 552.0150- ( 92.120 )
~# - -TEMP ~ 2 = 554.2570 ( 94.360 )
TEMP .3 = 535.0860 ( 75.080-)
TEMP 4 = 534.9740 (' 75.640 )-
' TEMP 5 = 532.7610 ( 73.030 )
TEMP- 6 = 532.'6610 ( 72.650 )
TEMP 7 = 528.5860 ( 68.750 )
-TEMP 8 = 527.2360 ( 67.400 )
TEMP 9'= 526.0850 ( 66.460 )
' TEMP 10 = 542.3450 ( 82.840 )
' TEMP 11'= 542.1280 ( 82.360 )
TEMP 12 = 542.3669 -( 83.010-)
PRES. 1 =- 64.1509 ( 64152.0 )
PRES- 2'= 64.1682 ( 64170.0 )
~
VPRS 1= .2376 ( 57.900 )
VPRS 2= .2300 ( 57.200 )
^
VPRS' 3= .2342 ( 57.400 )
VPRS 4= .2267 ( 57.600 )
- VPRS 5= . 4867 ( 79.400 )
VPRS 6= . 5374 (- 82.500 )
~
SUMMARY
OF. CORRECTED DATA TIME = 1915
[ - (b-}'
DATE = 821 TEMPERATURE (DEGREES R.) = 539.1760
, CORRECTED PRESSURE (PSIA)l= -63.8142 VAPOR PRESSURE (PSIA) = .3540 VOLUME (CU.FT.) = 293900.0
' AIR MASS (LBM) = 93889.0 i-4 A-19
SUMMARY
OF MEASURED D4TA AT 1930 821
-i p) TEMP 1 = 551.9350 ( 92.040 )
TEMP 2 = 554.2870 ( 94.390 )
TEMP 3'= 535.3260 ( 75.320 )
TEMP 4 = 535.0630 ( 75.730 )
TEMP- 5 = 532.8200 ( 73.090 )
TEMP 6 = 532.6900 ( 72.680 )
TEMP 7 = 528.7250 - ( 68.890 )
TEMP 8 = 527.1660 ( 67.330 )
TEMP 9 = 526.2050 ( 66.580 )
TEMP 10 = 542.2950 ( 82.790 )
TEMP 11 = 542.0980 ( 82.330 )
TEMP 12 = 542.3360 ( 82.980 )
PRES 1 = 64.1479 ( 64149.0 )
PRES 2= 64.1602 ( 64162.0 )
VPRS 1 = .2393 ( 58.100 )
VPRS 2= .2308 ( 57.300 )
VPRS 3= .2359 ( 57.600 )
VPRS 4= .2283 ( 57.800 )
VPRS 5= .4883 ( 79.500 )
VPRS 6= .5374 ( 82.500 )
SUMMARY
OF CORRECTED DATA
'(3)'
TIME = 1930 DATE = 821 TEMPERATURE (DEGREES R.) = 539.1950 CORRECTED PRESSURE (PSIA) = 63.8050 VAPOR PRESSURE (PSIA) = .3551 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93872.3 A-20
, b l
- i. APPENDIX B 1
SUMMARY
DATA :
i.
4.
i I~
I l
}
i 1
4 i
t e
9 h
t' f
i 9
i 1
1 1
1 l
J B-1 ,
t
-,,wwa-me-,---,,---., w-,v+-. r,-.~ .,w. ----,r-._n.---r-
n-i'q,)1 PEACH BOTTOM UNIT 3 ILRT
SUMMARY
DATA ALMAX = .500 VOLUME = 293900.
VRATET = .392 VRATEM = .381 TIME DATE TEMP PRESSURE VPRS VOLUME 1630 822 540.244 64.0914 .3837 293900.
1645 822 540.274 64.0916 .3845 293900.
1700 822 540.271 64.0920 .3841 293900.
1715 822 540.265 64.0930 .3851 293900.
1730 822 540.282 64.0939 .3852 293900.
1745 822 540.294 64.0955 .3856 293900.
1800 822 540.309 64.0977 .3854 293YOO.
1815 822 540.301 64.0974 .3857 293900.
1830 822 540.301 64.0983 .3858 293900.
1845 822 540.283 64.0971 .3860 293900.
1900 822 540.296 64.0974 .3857 293900.
1915 822 540.297 64.0944 .3867 293900.
1930 822 540.274 64.0887 .3864 293900.
1945 822- 540.241 64.0822 .3869 293900.
2000 822 540.266- 64.0784 .3867 293900.
2015 822 540.258 64.0777 .3864 293900.
[^}
t/
2030 822 2045 822 540.298 540.289 64.0782 64.0809
.3859
.3862 293900.
293900.
2100 822 540.291 64.0843 .3868 293900.
2115 822 540.336 64.0873 .3858 293900.
2130 822 540.409 64.0921 .3860 293900.
2145 822 540.429 64.0974 .3857 293900.
2200 822 540.456 64.1028 .3853 293900.
2215 822 540.478 64.1062 .3859 293900.
2230 822 540.460 64.1083 .3868 293900.
2245 822 540.556 64.1131 .3860 293900.
2300 822 540.594. 64.1157 .3874 293900.
2315 822 540.587 64.1202 .3879 293900.
2330 822 540.601 64.1241 .3870 293900.
2345 822 540.638 64.1281 .3870 293900.
O 823 540.666 64.1318 .3873 293900.
15 823 540.655 64.1356 .3875 293900.
30 823 540.710 64.1396 .3875 293900.
45 823 540.770 64.1422 .3889 293900.
Oy>
B-2
SUMMARY
OF MEASURED DATA AT 1630 822 f' ~) TEMP 1 = 551.5140 ( 91.620 )
TEMP 2 = 553.2970 ( 93.400 )
, TEMP 3 = 535.9660 ( 75.960 )
TEMP 4 = 535.7990 ( 76.470 :
TEMP 5 = 534.0780 ( 74.350 )
TEMP 6 = 534.0080 ( 7." 000 )
TEMP 7 = 531.0190 ( 71.190 )
TEMP- 8 = 528.9850 ( 69.150 )
TEMP 9 = 530.0520- ( 70.430 )
TEMP 10 = 543.2070 ( 83.700 )
TEMP 11 = 543.3550 ( 83.590 )
TEMP 12 = 543.7740 ( 84.420 )
PRES 1 = 64.4712 ( 64473.0 )
PRES 2= 64.4751 ( 64477.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .4965 ( 80.000 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA TIME = 1630
[~}
L' DATE = 822 TEMPERATURE (DEGREES R.) = 540.2440 CORRECTED PRESSURE (PSIA) = 64.0914 VAPOR PRESSURE (PSIA) = .3837 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94110.5 p.
' NJ' B-3
SUMMARY
OF MEASURED DATA AT 1645 822
[ ')
TEMP 1 = 551.6740 ( 91.780 )
TEMP 2 = 553.4470 ( 93.550 )
TEMP 3 = 536.0260 ( 76.020 )
TEMP 4 = 535.8090 ( 76.480 )
TEMP 5 = 533.9480 ( 74.220 )
TEMP 6 = 533.8790 ( 73.870 )
TEMP 7 = 531.0090 ( 71.180 )
TEMP S = 529.2250 ( 69.390 )
TEMP 9 = 530.0220 ( 70.400 )
TEMP 10 = 543.2370 ( 83.730 )
TEMP 11 = 543.3850 ( 83.620 )
TEMP 12 = 543.8240 ( 84.470 >
PRES 1 = 64.4732 ( 64475.0 )
PRES 2= 64.4761 ( 64478.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2663 ( 62.100 )
VPRS 5= .5015 ( 80.300 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
[# s TIME = 1645
\- DATE = 822 TEMPERATURE (DEGREES R.) = 540.2740 CORRECTED PRESSURE (PSIA) = 64.0916 VAPOR PRESSURE (PSIA) = .3845 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94105.6
/~
Y)) .
B-4
SUMMARY
OF MEASURED DATA AT 1700 822
[!
TEMP 1 = 551.4140 ( 91.520 )
TEMP 2 = 553.3770 ( 93.480 )
TEMP 3 = 535.3360 ( 75.830 )
TEMP 4 = 535.7890 ( 76.460 )
TEMP 5 = 534.1080 ( 74.380 )
TEMP 6 = 533.9390 ( 73.930 )
TEMP 7 = 531.0890 ( 71.260 )
. TEMP 8 = 529.2550 ( 69.420 )
TEMP 9 = 530.1020 ( 70.480 )
TEMP 10 = 543.2570 ( 83.750 )
TEMP 11 543.4050 ( 83.640 )
TEMP 12 = 543.8340 ( 34.480 )
PRES 1 = 64.4722 ( 64474.0 )
PRES 2= 64.4761 ( 64478.0 )
VPRS 1= .2818 ( 62.700 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2663 ( 62.100 )
VPRS 5= .4998 ( 80.200 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CL'RRECTED DATA
/,_T TIME = 1700
\~ DATE = 822 TEMPERATURE (DEGREES R.) = 540.2710 CORRECTED PRESSURE (PSIA) = 64.0920 VAPOR PRESSURE (PSIA) = .3841 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94106.6
\_)
B-5
SUMMARY
OF MEASURED DATA AT 1715 822 I
TEMP 1 = 551.5240 ( 91.630 )
'~
TEMP 2 = 553.3170 ( 93.420 )
TEMP 3 = 535.7660 ( 75.760 )
TEMP 4 = 535.7500 ( 76.420 )
TEMP 5 = 53!.9380 ( 74.210 )
TEMP 6 = 533.9790 (. 7:'. 970 )
TEMP 7 = 531.0390 ( 71.210 )
TEMP. 8 = 529.0550 ( 69.220 )
TEMP 9 = 530.0520 ( 70.430 )
TEMP 10 = 543.2770 ( 83.770 )
TEMP 11 = 543.4550 ( 83.690 )
TEMP 12 = 543.9240 ( 84.570 )
PRES 1 = 64.4722 ( 64474.0 )
PRES 2= 64.4781 ( 64480.0 )
VPRS 1 = .2808 ( 62.600 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2663 ( 62.100 )
VPRS 5= .5031 ( 80.400 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
/') TIME = 1715
\' DATE = 822 TEMPERATURE (DEGREES R.) = 540.2650
- CORRECTED PRESSURE (PSIA) = 64.0930 VAPOR PRESSURE (PSIA) = .3851 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94109.2 l
(~h l
B-6 l
SUMMARY
OF MEASURED DATA AT 1730 822 I)
TEMP 1 = 551.3430 ( 91.450 )
TEMP 2 = 553.2470 ( 93.350 )
TEMP 3 = 535.9760 ( 75.970 )
TEMP 4 = 535.7200 ( 76.390 )
TEMP 5 = 533.9680 ( 74.240 )
TEMP 6 = 534.0780 ( 74.070 )
TEMP 7 = 531.0190 ( 71.190 )
TEMP 8 = 529.2250 ( 69.390 )
TEMP 9 = 530.0520 ( 70.430 )
TEMP 10 = 543.2970 ( 83.790 )
TEMP'11 = 543.4840 ( 83.720 )
TEMP 12 = 543.8840 ( 84.530 )
PRES 1 = 64.4742 ( 64476.0 )
PRES 2= 64.4791 ( 64481.0 )
VPRS 1 = .2808 ( 62.600 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5031 ( 80.400 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
/ TIME = 1730 k ') DATE = 822 TEMPERATURE (DEGREES R.) = 540.2820 CORRECTED PRESSURE (PSIA) = 64.0939 VAPOR PRESSURE (PSIA) = .3852 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94107.6 i
O.
N..)
B-7
SUMMARY
OF MEASURED DATA AT 1745 822 f'~) TEMP 1 = 551.5340 ( 91.640 )
TEMP 2 = 553.2770 ( 93.380 )
TEMP 3 = 535.8560 ( 75.850 )
TEMP 4 = 535.6900 ( 76.360 )
TEMP 5 = 533.9790 ( 74.250 )
TEMP 6 = 534.0780 ( 74.070 )
TEMP 7 = 530.9890. ( 71.160 )
TEMP 8 = 529.1050 ( 69.270 )
TEMP 9 = 530.0420 ( 70.420 )
TEMP 10 = 543.3270 ( 83.820 )
TEMP 11 = 543.5240 ( 83.760 )
TEMP 12 = 543.9240 ( 84.570 )
PRES 1 = 64.4742 ( 64476.0 )
PRES 2= 64.4811 ( 64483.0 )
VPRS 1= .2808 ( 62.600 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
(~}
\/
TIME = 1745 DATE = 822 TEMPERATURE (DEGREES R.) = 540.2940 CORRECTED PRESSURE (PSIA) = 64.0955 VAPOR PRESSURE (PSIA) = .3856 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94107.8 (b
v B-8
i
SUMMARY
OF MEASURED DATA AT 1800 822 I ')
\ ^
TEMP 1 = 551.5340 ( 91.640 ) '
TEMP 2 = 553.2270 ( 93.330 )
TEMP 3 = 535.8060 ( 75.800 )
TEMP 4 = 535.7400 ( 76.410 )
TEMP 5 = 534.0780 ( 74.350 )
TEMP 6 = 534.0280 ( 74.020 )
TEMP 7 = 531.0290 ( 71.200 )
TEMP 8 = 529.2450 ( 69.410 )
TEMP 9 = 530.0720 ( 70.450 )
TEMP-10 = 543.3170 ( 83.810 )
TEMP 11 = 543.5140 ( 83.750 )
TEMP 12 = 543.9730 ( 84.620 )
PRES 1 = 64.4752 ( 64477.0 )
PRES 2= 64.4831 ( 64485.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2663 ( 62.100 )
VPRS 5= .5031 ( 80.400 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA l'~T TIME = 1800
\2 DATE = 822 TEMPERATURE (DEGREES R.) = 540.3090 CORRECTED PRESSURE (PSIA) = 64.0977 VAPOR PRESSURE (PSIA) = .3854 VOLUME'(CU.FT.) = 293900.0 AIR MASS (LBM) = 94108.4 s.
B-9 k
,7_
L./
SUMMARY
OF MEASURED DATA AT 1815 ,822 TEMP 1 = 551.3730 ( 91.480 )
TEMP 2 = 553.1770 ( 93.280 )
TEMP 3 = 535.9160 ( 75.910 )
TEMP 4 = 535.7200 ( 76.390 )
TEMP 5 = 533.9180 ( 74.190 )
TEMP 6 = 534.0580 ( 74.050 )
TEMP 7 = 531.0490 ( 71.220 )
TEMP 8 = 529.1950 ( 69.360 )
TEMP 9 = 529.9920 ( 70.370 )
(~ TEMP 10 = 543.3570 ( 83.850 )
A-}- TEMP 11 = 543.5540 ( 83.790 )
TEMP 12 = 543.9830 ( 84.630 )
PRES 1 = 64.4791 ( 64481.0 )
PRES 2= 64.4831 ( 64485.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5031 ( 80.400 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA i TIME = 1815 DATE = 822 TEMPERATURE (DEGREES R.) = 540.3010 CORRECTED PRESSURE (PSIA) = 64.0974 VAPOR PRESSURE (PSIA) = .3357 VOLUME (CU.FT.) = 293900.0 AIR T1 ASS (LEri) = 94109.4 x_,
)
B-10
_ _ _. . . - _ , , _ _ _ _ _ . . _ , . . - - - - , _ . _ . _ _ _ _ _ - ~ , - - . _ . . . _ _ _ . . , , . . _ _ _ . . . - - - -_ _
SUMMARY
OF MEASURED DATA AT 1830 822
()
f -YEMP TEMP 1
2 =
= 551.4540 553.1570
(
(
91.560 93.260
)
)
TEMP 3 = 535.8760 ( 75.870 )
TEMP 4 = 535.7400 ( 76.410 )
TEMP 5 = 533.9180 ( 74.190 )
TEMP 6 = 533.9990 ( 73.990 )
TEMP 7 = 531.0490 ( 71.220 )
TEMP 8 = 529.0850 ( 69.250 )
TEMP 9 = 530.0520 ( 70.430 )
TEMP 10 = 543.3770 ( 83.870 )
TEMP 11 = 543.5740 ( 83.810 )
TEMP 12 = 543.9930 ( 84,640 )
PRES 1 = 64.4761 ( 64478.0 )
PRES 2= 64.4841 ( 64486.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2663 ( 62.100 )
VPRS 5= .5031 ( 80.400 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
^
> TIME = 1830 k -} DATE = 822 TEMPERATURE (DEGREES R.) = 540.3010 CORRECTED PRESSURE (PSIA) = 64.0983 VAPOR PRESSURE (PSIA) = .3858 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94110.7
[
v B-11
t I
_ /~')
Lj
SUMMARY
OF MEASURED DATA AT 1845 822 TEMP 1 = 551.2730 ( 91.380 )
TEMP 2 = 553.1270 ( 93.230 )
TEMP 3 = 535.7560 ( 75.750 )
TEMP 4 = 535.7000 ( 76.370 )
TEMP- 5 = 533.9480 ( 74.220 )
TEMP 6 = 533.9790 ( 73.970 )
TEMP 7 = 531.0390 ( 71.210 )
TEMP 8 = 529.1650 ( 69.330 )
TEMP 9 = 530.0420 ( 70.420 )
TEMP 10 = 543.3970 ( 83.890 )
(~}/
TEMP 11 = 543.5840 ( 83.820 )
TEMP 12 = 543.9830 ( 84.630 )
PRES 1 = 64.4791 ( 64481.0 )
PRES 2= 64.4831 ( 64485.0 )
VPRS 1 = .2808 ( 62.600 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= . 5048 ( 80.500 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA TIME = 1845 DATE = 822 TEMPERATURE (DEGREES R.) = 540.2830 CORRECTED PRESSURE (PSIA) = 64.0971 VAPOR PRESSURE (PSIA) =
.3860 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94112.0
,O B-12
V
SUMMARY
OF MEASURED DATA AT 1900 822 TEMP 1 = 551.3430 ( 91.450 )
TEMP 2 = 553.1270 ( 93.230 )
TEMP 3 = 535.7560 ( 75.750 )
TEMP 4 = 535.7100 ( 76.380 )
TEMP 5 = 533.9380 ( 74.210 )
TEMP 6 = 534.0090 ( 74.000 )
TEMP 7 = 531.0590 ( 71.230 )
TEMP 8 = 529.2550 ( 69.420 )
TEMP 9 = 530.0020 ( 70.380 )
IT
\/
TEMP 10 = 543.3970 ( 83.890 )
TEMP 11 = 543.5540 ( 83.790 )
TEMP 12 = 544.0230 ( 84.670 )
PRES 1 = 64.4781 ( 64480.0 )
PRES 2= 64.4831 ( 64485.0 )
VPRS 1 = .2808 ( 62.600 )
VPRS 2= .2682 ( 61.500 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2663 ( 62.100 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA TIME = 1900 DATE = 822 TEMPERATURE (DEGREES R.) = 540.2960 CORRECTED PRESSURE (PSIA) = 64.0974 VAPOR PRESSURE (PSIA) = .3857 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94110.2 e'%
\ -
]
B-13
SUMMARY
-OF MEASURED DATA AT 1915 922
[D TEMP 1 = 551.4140 ( 91.520 )
TEMP 2 = 553.1170 ( 93.220 )
TEMP 3 = 535.7760 ( 75.770 )
TEMP 4 = 535.6500 ( 76.320 )
TEMP 5 = 533.9480 ( 74.220 )
TEMP 6 = 533.9590 ( 73.950 )
TEMP 7 = 531.0490 ( 71.220 )
TEMP 8 = 529.2650 ( 69.430 )
TEMP 9 = 530.0020 ( 70.380 )
TEMP'10 = 543.4280 ( 83.920 )
TEMP 11 = 543.5540 ( 83.790 )
TEMP 12 = 544.0130 ( 84.660 )
PRES 1 = 64.4752 ( 64477.0 )
PRES 2= 64.4811 ( 64483.0 )
VPRS 1 = .2808 ( 62.600 )
VPRS 2 =' .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
(~~T TIME = 1915
\__) DATE = 822 TEMPERATURE (DEGREES R.) = 540.2970 CORRECTED PRESSURE (PSIA) = 64.0944 VAPOR PRESSURE (PSIA) = .3867 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94105.7
,s B-14
SUMMARY
~OF MEASURED DATA AT 1930 822
['- 't TEMP. 1 = 551.2530 ( 91.360 )
TEMP 2 = 553.0970 ( 93.200 )
TEMP 3 = 535.7260 ( 75.720 )
TEMP 4 = 535.6400 ( 76.310 )
TEMP 5 = 533.8980 ( 74.170 )
TEMP 6 = 534.0580 ( 74.050 )
TEMP- 7 = 531.0590 ( 71.230 )
TEMP 8 = 529.2650 ( 69.430 )
TEMP 9 = 530.0020 ( 70.380 )
TEMP 10 = 543.4380 ( 83.930 )
TEMP 11 = 543.5040 ( 83.740 )
TEMP 12 = 543.9730 ( 84.620 )
PRES 1 = 64.4652 ( 64467.0 )
PRES 2= 64.4751 ( 64477.0 )
VPRS 1 = .2818 ( 62.700 )
-VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
[~}
\/
TIME = 1930 DATE = 822 TEMPERATURE (DEGREES R.) = 540.2740 CORRECTED PRESSURE (PSIA) = 64.0887 VAPOR' PRESSURE (PSIA) = .3864 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94101.2
! (D s_;
I B-15
SUMMARY
OF MEASURED DATA AT 1945 822
[}
TEMP 1 = 551.2330 ( 91.340 )
TEMP 2 = 552.9370 ( 93.040 )
TEMP 3 = 535.9160 ( 75.910 )
TEMP 4 = 535.8090~ ( 76.480 )
TEMP 5 = 533.6780 ( 73.950 )
TEMP 6 = 533.9890 ( 73.980 )
TEMP 7 ='531.0190 ( 71.190 )
TEMP 8 = 529.1050 ( 69.270 )
TEMP 9 = 529.9920 ( '70.370 )
TEMP 10 = 543.4280 ( 83.920 )
TEMP 11 = 543.4840 ( 83.720 )
TEMP 12 = 543.9140 ( 84.560 )
PRES 1 = 64.4592 ( 64461.0 '
PRES 2= 64.4691 ( 64471.0 )
VPRS 1 = .2808 ( 62.600 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS. 4= .2663 ( 62.100 )
VPRS 5= .5098 ( 80.800 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
[~') TIME = 1945
- ' DATE = 822 TEMPERATURE (DEGREES R.).=. 540.2410 CORRECTED PRESSURE (PSIA) = 64.0822 VAPOR PRESSURE (PSIA) = .3869 VOLUME (CU.FT.) = 293900.0 AIR MASS (LEM) = 94097.5 IO
%_ ,)
B-16
SUMMARY
OF MEASURED DATA AT 2000 822
[
'#'~
'l TEMP 1 = 551.3530 ( 91.460 )
TEMP 2 = 553.1170 ( 93.220 )
TEMP 3 = 535.8260 ( 75.820 )
TEMP 4 = 535.6800 ( 76.350 )
TEMP 5 = 534.0080 ( 74.280 )
TEMP 6 = 534.1080 ( 74.100 )
TEMP 7 = 531.0090 ( 71.180 )
TEMP 8 = 529.2150 ( 69.380 )
TEMP 9 = 529.9720 ( 70.350 )
TEMP 10 = 543.3870 ( 83.880 )
TEMP 11 = 543.4250 ( 83.660 )
TEMP 12 = 543.8740 ( 84.520 )
PRES 1 = 64.4582 ( 64460.0 )
PRES 2= 64.4651 ( 64467.0 )
, VPRS 1 = .2808 ( 62.600 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
~') TIME = 2000 DATE = 822 TEMPERATURE (DEGREES R.) = 540.2660 CORRECTED PRESSURE (PSIA) = 64.0784 VAPOR PRESSURE (PSIA) = .3867 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94087.6
(
LJ B-17
SUMMARY
OF MEASURED DATA AT 2015 822
(;
TEMP 1 = 551.5140 ( 91.620 )
TEMP 2 = 553.0970 ( 93.200 )
TEMP 3 = 535.8160 ( 75.810 )
TEMP 4 = 535.7300 ( 76.400 )
TEMP 5 = 533.9680 ( 74.240 )
TEMP 6 = 534.0880 ( 74.080 )
TEMP 7 = 531.0490 ( 71.220 )
TEMP 8 = 529.0350 ( 69.200 )
TEMP 9 = 529.9920 ( 70.370 )
TEMP 10 = 543.3870 ( 83.880 )
TEMP 11 = 543.3950 ( 83.630 )
TEMP 12.= 543.8440 ( 84.490 )
PRES 1 = 64.4552 ( 64457.0 )
PRES 2= 64.4641 ( 64466.0 )
VPRS 1 = .2808 ( 62.600 )
VPRS 2= .2682 ( 61.500 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2663 ( 62.100 )
VPR9 5= .5098 ( SO.800 )
VFRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
(]
A--
TIME = 2015 DATE = 822 TEMPERATURE (DEGREES R.) = 540.2580 CORRECTED PRESSURE (PSIA) = 64.0777 VAPOR PRESSURE (PSIA) = .3864 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94088.0 af"*'
i
, l B-18
SUMMARY
CF MEASURED DATA AT 2030 822 I)
TEMP 1 = 551.6840 (. 91.790 )
TEMP 2 = 553.3770 ( 93.480 )
TEMP 3 = 535.9760 ( 75.970 )
TEMP 4 = 535.8590 ( 76.530 )
TEMP 5 = 534.0380 ( 74.310 )
TEMP 6 = 534.0680 ( 74.060 )
TEMP 7 = 53C.9990 ( 71.170 )
TEMP 8 = 529.2150 ( 69.380 )
TEMP 9 = 530.0620 ( 70.440 )
TEMP 10 = 543.3570 ( 83.850 )
TEMP 11 = 543.3550 ( 83.590 )
TEMP 12 = 543.7640 ( 84.410 )
PRES 1 = 64.4552 ( 64457.0 )
PRES 2= 64.4641 ( 64466.0 )
VPRS 1 = .2808 ( 62.600 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
(')d TIME = 2030 DATE = 822 TEMPERATURE (DEGREES R.) = 540.2980 CORRECTED PRESSURE (PSIA) = 64.0782 VAPOR PRESSURE (PSIA) = .3859 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94081.6
,es N,,_.
B-19
SUMMARY
OF MEASURED' DATA AT 2045 822
/ TEMP 1 = 551.7140
) ( 91.820 )
TEMP 2 = 553.3970 ( 93.500 )
TEMP 3 = 535.8460 ( 75.840 )
TEMP 4 = 535.8090 ( 76.480 )
TEMP 5 = 534.0780 ( 74.350 )
TEMP 6 = 534.1480 ( 74.140 )
TEMP 7 = 531.0690 ( 71.240 )
TEMP 8 = 529.2750 ( 69.440 )
TEMP 9 = 530.0620 ( 70.440 )
TEMP 10 = 543.3370 ( 83.830 )
TEMP 11 = 543.3050 ( 83.540 )
TEMP 12 = 543.7240 ( 84.370 )
PRES 1 = 64.4592 ( 64461.0 )
PRES 2= 64.4671 ( 64469.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
(~') TIME = 2045
' - -' DATE = 822
~ TEMPERATURE (DEGREES R.) = 540.2890 CORRECTED PRESSURE (PSIA) = 64.0809 VAPOR PRESSURE (PSIA) = .3862 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94087.2 pMw v
B-20
m
SUMMARY
OF MEASURED DATA AT 2100 822
~
/) TEMP 1 = 551.5840 ( 91.690 )
TEMP 2 = 553.5570 ( 93.660 )
TEMP 3 = 535.8160 ( 75.810 )
TEMP 4 = 536.0180 ( 76.690 )
TEMP 5 = 533.9980 ( 74.270 )
TEMP 6 = 534.1280 ( 74.120 )
TEMP 7 = 531.1090 ( 71.280 )
TEMP 8 = 529.4050 ( 69.570 )
TEMP 9 = 530.0220 ( 70.400 )
TEMP 10 = 543.3270 ( 83.820 )
TEMP 11 = 543.2950 ( 83.530 )
TEMP 12 = 543.6640 ( 84.310 )
PRES 1 = 64.4612 ( 64463.0 )
PRES 2= 64.4711 ( 64473.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2749 ( 61.900 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5098 ( 80.800 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
(;'
'ss TIME = 2100 DATE = 822 TEMPERATURE (DEGREES R.) = 540.2910 CORRECTED PRESSURE (PSIA) = 64.0843 VAPOR PRESSURE (PSIA) = .3868 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94091.8 Y.
B-21
SUMMARY
OF MEASURED DATA AT 2115 822 1'T TEMP 1 = 551.9140 ( 92.020 )
\
TEMP 2 = 553.6670 ( 93.770 )
TEMP 3 = 536.1660 ( 76.160 )
TEMP 4 = 536.0080 ( 76.680 )
TEMP 5 = 534.1870 ( 74.460 )
TEMP 6 = 534.0680 ( 74.060 )
-TEMP 7-= 531.0990 ( 71.270 )
TEMP 8 = 529.2550 ( 69.420 )
TEMP 9 = 530.0620 ( 70.440 )
TEMP 10 = 543.3170 ( 83.810 )
TEMP 11 = 543.2550 ( 83.490 )
TEMP 12 = 543.6340 ( 84.280 )
PRES 1 = 64.4662 ( 64468.0 )
PRES 2= 64.4731 ( 64475.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS' 2= .2692 ( 61.600 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
(~3 TIME = 2115
(/ DATE = 822 TEMPERATURE (DEGREES R.; = 540.3360 CORRECTED PRESSURE (PSIA) = 64.0873 VAPOR PRESSURE (PSIA) = .3858 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94088.3 q
B-22
SUMMARY
OF. MEASURED DATA AT 2130 822 t '$ TEMP 1 = 552.1050 (
kl 92.210 )
TEMP 2 = 554.1270 ( 94.230 )
TEMP 3 = 536.3060 ( 76.300 )-
TEMP 4 = 536.1770 ( 76.850 )
TEMP 5 = 534.1370 ( 74.410 )
TEMP 6 = 534.2080 ( 74.200 )
TEMP 7 = 531.1880 ( 71.360 )
TEMP 8 = 529.4650 ( 69.630 )
TEMP 9 = 530.1020 ( 70.480 )
TEMP 10 =-543.3070 ( 83.800 )
TEMP 11 = 543.2250 ( 83.460 )
TEMP 12 = 543.5740 ( 84.220 )
PRES 1 = 64.4722 ( 64474.0 )
PRES 2= 64.4781 ( 64480.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2701 ( 61.700 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
()
\_/
TIME = 2130 DATE = 822 TEMPERATURE (DEGREES R.) = 540.4090 CORRECTED PRESSURE (PSIA) = 64.0921 VAPOR PRESSURE (PSIA) = .3860 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94082.7
- Y B-23
SUMMARY
OF MEASURED DATA AT 2145 822
[' ')' '_ TEMP 1 = 552.0850 ( 92.190 )
TEMP 2 = 554.1170 ( 94.220 )
TEMP 3 = 536.3360 ( 76.330 )
TEMP 4 = 536.2470 ( 76.920 )
TEMP 'S = 534.2270 ( 74.500 )
TEMP 6 = 534.3480 ( 74.340 )
TEMP 7 = 531.1380 ( 71.310 )
TEMP 8 = 529.5250 ( 69.690 )
TEMP 9 = 530.1620 ( 70.540 )
TEMP 10 = 543.2970 ( 83.790 )
TEMP 11 = 543.2050 ( 83.440 )
TEMP 12 = 543.5540 ( 84.200 )
PRES 1 = 64.4761 ( 64478.0 )
PRES 2= 64.4831 ( 64485.0 )
VPRS 1 = .2828 ( 62.800 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2682 ( 62.300 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
(~Ni -TIME = 2145 k/ DATE = 822 TEMPERATURE (DEGREES R.) = 540.4290 CORRECTED PRESSURE (PSIA) = 64.0974 VAPOR PRESSURE (PSIA) = .3857 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94087.1
(~T L)
B-24
SUMMARY
OF MEASURED DATA AT 2200 822
[]
TEMP 1 = 552.2150 ( 92.320')
TEMP 2 = 554.3970 ( 94.500 )
TEMP. 3 = 536.1660 ( 76.160 )
TEMP 4 = 536.3570 ( 77.030 )
TEMP 5 = 534.4170 ( 74.690 )
TEMP 6 = 534.3280 ( 74.320 )
TEMP 7 = 531.1580 ( 71.330 )
TEMP 8 = 529.5050 ( 69.670 )
TEMP 9 = 530.1520 ( 70.530 )
TEMP 10 = 543.2870 ( 83.780 )
' TEMP 11 = 543.1850 ( 83.420 ) .
TEMP 12 = 543.5240 ( 84.170 )
PRES 1= 64.4811 ( 64483.0 )
PRES 2= 64.4881 ( 64490.0 )
VPRS 1" = .2828 ( 62.800 )
VPRS 2= .2701 ( 61.700 )
VPRS 3= .2769 ( 62.100 )
.VPRS _4 = .2682 ( 62.300 )
VPRS 5= .5031 ( 80.400 )
VPRS 6= .5549 ( 83.500 )
SUMMARY
OF CORRECTED DATA
' 's(~ TIME = 2200.
DATE = 822' TEMPERATURE (DEGREES R.). = 540.4560 CORRECTED PRESSURE (PSIA) = 64.1028 VAPOR PRESSURE (PSIA) = .3853 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94090.3 l
l l
, ?
a B-25 s
u, _ _ _ _ _ _ _ _ _ . _ _ _ . _ _ . _ _ . . . - - . - .
SUMMARY
OF MEASURED DATA AT 2215 822 TEMP 1 = 552.3950 92.500 )
[#)
TEMP 2 = 554.5470
(
( 94.650 )
TEMP 3 = 536.3060 ( 76.300 )
TEMP 4 = 536.3270 ( 77.000 )
TEMP 5 = 534.3970 ( 74.670 )
TEMP 6 = 534.3180 ( 74.310 )
TEMP 7 = 531.1980 ( 71.360 )
TEMP 8 = 529.6850 ( 69.850 )
TEMP 9 = 530.1920 ( 70.560 )
TEMP 10 = 543.2570 ( 83.750 )
TEMP 11 = 543.1550 ( 83.390 )
TEMP 12 = 543.4740 ( 84.120 )
PRES 1 = 64.4831 ( 64485.0 )
PRES 2= 64.4921 ( 64494.0 )
VPRS 1 = .2838 ( 62.900 )
VPRS 2= .2701 ( 61.700 )
VPRS 3= .2769 ( 62.100 )
VPRS 4= .2692 ( 62.400 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5549 ( 83.500 )
SUMMARY
OF CORRECTED DATA T'T TIME = 2215 l DATE = 822 TEMPERATURE (DEGREES R.) = 540.4780 CORRECTED PRESSURE (PSIA) = 64.1062 VAPOR PRESSURE (PSIA) = .2959 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94091.5
/~3 V
B-26
StJMMARY OF MEASURED DATA AT 2230 822
[')
\-"
TEMP 1 = 552.6260 ( 92.730 )
TEMP 2 = 554.4170 ( 94.520 )
TEMP 3 = 536.3260 ( 76.320 )
TEMP 4 = 536.0780 ( 76.750 )
TEMP 5 = 534.3970 ( 74.670 )
TEMP 6 = 534.3080 ( 74.300 )
TEMP 7 = 531.2080 ( 71.380 )
TEMP 8 = 529.4750 ( 69.640 )
TEMP 9 = 530.2120 ( 70.590 )
TEMP 10 = 543.2670 ( 83.760 )
TEMP 11 = 543.1550 ( 83.390 )
TEMP 12 = 543.4740 ( 84.120 )
PRES 1 = 64.4881 ( 64490.0 )
PRES 2= 64.4951 ( 64497.0 )
VPRS 1 = .2838 ( 62.900 )
VPRS 2 =- .2711 ( 61.800 )
VPRS 3= .2769 ( 62.100 )
VPRS 4= .2692 ( 62.400 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA TIME = 2230
(~')N
(- DATE = 822 TEMPERATURE (DEGREES R.) = 540.4600 CORRECTED PRESSURE (PSIA) = 64.1083 VAPOR PRESSURE (PSIA) = .3868 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94097.8 B-27
SUMMARY
OF MEASURED DATA AT 2245 822 l ID TEMP 1 = 552.6760 ( 92.780 )
~ TEMP 2 = 554.9780 ( 95.080 )
TEMP 3 = 536.3260 ( 76.320 )
TEMP 4 = 536.4060 ( 77.080 )
TEMP 5 = 534.5170 ( 74.790 ) 7 TEMP 6 = 534.4680 ( 74.460 )
TEMP 7 = 531.2100 ( 71.390 )
TEMP 8 = 529.7550 ( 69.920 )
TEMP 9 = 530.2720 ( 70.650 )
TEMP 10 = 543.2770 ( 83.770 )
TEMP 11 = 543.1250 ( 83.360 )
TEMP 12 = 543.4540 ( 84.100 )
PRES 1 = 64.4931 ( 64495.0 )
PRES 2= 64.4991 ( 64501.0 )
VPRS 1 = .2838 ( 62.900 )
VPRS 2= .2711 ( 61.800 )
VPRS 3= .2769 ( 62.100 )
VPRS 4= .2692 ( 62.400 ) '
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5549 ( 83.500 )
SUMMARY
OF CORRECTED DATA
[],
TIME = 2245 DATE = 822 TEMPERATURE (DEGREES R.) = 540.5560 CORRECTED PRESSURE (PSIA) = 64.1131 VAPOR PRESSURE (PSIA) = .3860 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94088.0
[~)
v B-28
SUMMARY
OF MEASURED DATA AT 2300 822
()
TEMP TEMP 1
2
=
=
552.9570 554.8380
(
(
93.060 94.940
)
)
l
{
TEMP 3 = 536.5460 ( 76.540 )
TEMP 4 = 536.2970 ( 76.970 )
TEMP 5 = 534.7060 ( 74.980 )
TEMP 6 = 534.5180 ( 74.510 )
TEMP 7 = 531.2680 ( 71.440 )
TEMP 8 = 529.9450 ( 70.110 )
TEMP 9 = 530.2920 ( 70.670 )
TEMP 10 = 543.2670 ( 83.760 )
TEMP 11 = 543.0860 ( 83.320 )
TEMP 12 = 543.4240 ( 84.070 )
PRES 1 = 64.4971 ( 64499.0 )
PRES 2= 64.5031 ( 64505.0 )
VPRS 1 = .2838 ( 62.900 )
VPRS 2= .2720 ( 61.900 )
VPRS 3= .2779 ( 62.200 )
VPRS 4= .2692 ( 62.400 )
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
(~;l TIME = 2300 ks CATE = 822 TEMPERATURE (DEGREES R.) = 540.5940 CORRECTED PRESSURE (PSIA) = 64.1157 VAPOR PRESSURE (PSIA) = .3874 VOLUME (CU.FT.) = 293900.0 AIR MACS (LBM) = 94085.1 B-29
SUMMARY
OF MEASURED DATA AT 2315 822
('~ j TEMP 1 = 552.7960 ( 92.900 )
TEMP 2 = 554.8580 ( 94.960 )
TEMP 3 = 536.4960 ( 76.490 )
TEMP 4 = 536.5460 ( 77.220 )
TEMP 5 = 534.7060 ( 74.980 )
TEMP 6 = 534.3980 ( 74.390 )
TEMP 7 = 531.3080 ( 71.480 )
TEMP O = 529.8450 ( 70.010 )
TEMP 9 = 530.3220 ( 70.700 )
TEMP 10 = 543.2770 ( 83.770 )
TEMP 11 = 543.0860 ( 83.320 )
TEMP 12 = 543.4140 ( 84.060 )
PRES 1 = 64.5021 ( 64504.0 )
PRES 2= 64.5081 ( 64510.0 )
VPRS 1 = .2848 ( 63.000 )
VPRS 2= .2711 ( 61.800 )
VPRS 3= .2779 ( 62.200 )
VPRS 4= .2701 ( 62.500 )
VPRS 5= .5098 ( 80.800 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
(~', TIME = 2315
(/ DATE = 822 TEMPERATURE (DEGREES R.) = 540.5870 CORRECTED PRESSURE (PSIA) = 64.1202 VAPOR oRESSURE (PSIA) = .3979 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94093.0
,e f l N, /
B-1)
)
I l
l
SUMMARY
OF MEASURED DATA AT 2330 822 (l TEMP 1 = 552.9770 ( 93.080 )
\- TEMP 2 = 555.1580 ( 95.260 )
TEMP 3 = 536.5060 ( 76.500 )
TEMP 4 = 536.2770 ( 76.950 )
TEMP 5 = 534.6360 ( 74.910 )
TEMP 6 = 534.5280 ( 74.520 )
TEMP 7 = 531.2980 ( 71.470 )
TEMP 8 = 529.9450 ( 70.110 )
TEMP 9 = 530.3620 ( 70.740 )
TEMP 10 = 543.2470 ( 83.740 )
TEMP 11 = 543.0760 ( 83.310 )
. TEMP 12 = 543.3940 ( 84.040 )
PRES 1 = 64.5061 ( 64508.0 )
PRES 2= 64.5111 ( 64513.0 )
VPRS 1 = .2848 ( 63.000 )
VPRS 2= .2720 ( 61.900 )
VPRS 3= .2779 ( 62.200 )
VPRS 4= .2701 ( 62.500 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
(" TIME = 2330 k- DATE = 822 TEMPERATURE (DEGREES R.) = 540.6010 CORRECTED PRESSURE (PSIA) = 64.1241 VAPOR PRESSURE (PSIA) = .3870 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94096.4
\.)
B-31
SUMMARY
OF MEASURED DATA AT 2345 822
(~'J - TEMP 1 = 553.0970 ( 93.200 )
lEMP 2 = 555.2480 ( 95.350 )
TEMP 3 = 536.6960 ( 76.690 ) s TEMP 4 = 536.3070 ( 76.~980 )
TEMP 5 = 534.6860 ( 74.960 )
TEMP 6 = 534.6180 ( 74.610 )
TEMP 7 = 531.3080 ( 71.480 )
TEMP 8 = 529.7350 ( 69.900 )
TEMP 9 = 530.3720 ( 70.750 )
TEMP 10 = 543.2670 ( 83.766 TEMP 11 = 543.0960 ( 83.330 )
. TEMP 12 = 543.3940 ( 84.040 )
PRES 1 = 64.5101 ( 64512.0 )
PRES 2= 64.5151 ( 64517.0 )
VPRS 1 = .2848 ( 63.000 )
VPRS 2= .2720 ( 61.900 )
VPRS 3= .2779 ( 62.200 ) s VPRS 4= .2701 ( 62.500 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
("N k-TIME = 2345 DATE = 822 TEMPERATURE (DEGREES R.) = 540.6380 CORRECTED PRESSURE (PSIA) = 64.1281 VAPOR PRESSURE (PSIA) = .3870 VOLUME (CU.FT.) = 293900.0 AIR MASS (LDM) = 94A95.8
/~T V
B-32
- r?
SUMMARY
OF MEASURED DATA AT 0 823
'~'; TEMP 1 = 553.1570 ( 93.260 )
t/ TEMP 2 = 555.2480 ( 95.350 )
TEMP 3 = 536.7160 ( 76.710 )
TEMP 4 = 536.3570 ( 77.030 )
TEMP 5 = 534.7660 ( 75.040 )
TEMP 6 = 534.6380 ( 74.630 )
TEMP 7 = 531.2780 ( 71.450 )
TEMP 8 = 529.9850 ( 70.150 )
TEMP 9 = 530.3720 ( 70.750 )
TEMP 10 = 543.2870 ( 83.780 )
TEMP 11 = 543.~0760 ( 83.310 )
TEMP 12 = 543.3940 ( 84.040 )
PRES 1 = 64.5141 ( 64516.0 )
PRES 2= 64.5191 ( 64521.0 )
VPRS 1 = .2858 ( 63.100 )
VPRS 2= .2720 ( 61.900 )
VPRS 3= .2789 ( 62.300 )
VPRS 4= .2701 ( 62.500 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CCRRECTED DATA
(~') TIME = 0
(_ -
DATE = 823 TEMPERATURE (DEGREES R.) = 540.6660 CORRECTED PRESSURE (PSIA) = 64.1318 VAPOR PRESSURE (PSIA) = .3873 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94096.3
[u B-33
SUMMARY
OF MEASURED DATA AT IL 823
.()
\/
TEMP 1 = 553.2570 ( 93.360 )
TEMP 2 = 555.3280 ( 95.430 )
TEMP 3 = 536.5760 ( 76.570 )
TEMP 4 = 536.3070 ( 76.980 )
TEMP 5 = 534.7760 ( 75.050 )
TEMP 6 = 534.5880 ( 74.580 )
TEMP 7 = 531.3780 ( 71.550 )
TEMP G = 529.9050 ( 70.070 )
TEMP 9 = 530.3820 ( 70.760 )
TEMP 10 = 543.2370 ( 83.730 )
TEMP 11 = 543.0560 ( 83.290 )
TEMP 12 = 543.4140 ( 84.060 )
PRES 1 = 64.5201 ( 64522.0 )
PRES 2= 64.5231 ( 65325.0 )
VPRS 1 = .2858 ( 6T.100 )
VPRS 2= .2730 ( 62.000 )
VPRS 3= .2789 ( 62.300 )
VPRS 4= .2711 ( 62.600 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA t); TIME = 15
(_ DATE = 823 g
TEMPERATURE (DEGREES R.) = 540.6550 i CORRECTED PRESSURE (PSIA) = 64.1356 VAPOR PRESSURE (PSIA) = .3875 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94103.8 3
(V B-34
SUMMARY
OF MEASURED DATA AT 30 623
- (-) TEMP 1 = 553.3170 ( 93.420 )
TEMP 2 = 555.5380 ( 95.640 )
TEMP 3 = 536.7160 ( 76.710 )
TEMP 4 = 536.4760 ( 77.150 )
TEMP 5 = 534.8060 ( 75.080 )
TEMP 6 = 534.7170 ( 74.710 )
TEMP 7 = 531.3580 ( 71.530 )
TEMP B = 529.8550 ( 70.020 )
TEMP 9 = 530.4420 ( 70.820 )
TEMP 10 = 543.2570 ( 83.750 )
TEMP 11 = 543.0760 ( 83.310 )
TEMP 12 = 543.4040 ( 84.050 )
PRES 1 = 64.5240 ( 64526.0 )
PRES 2= 64.5271 ( 64529.0 )
VPRS 1 = .2858 ( 63.100 )
VPRS 2= .2730 ( 62.000 )
VPRS 3= .2789 ( 62.300 )
VPRS 4= .2711 ( 62.600 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5567 ( 83.600 )
SUMMARY
OF CORRECTED DATA
(~')
%/
TIME = 30 DATE = 823 TEMPERATURE (DEGREES R.) = 540.7100 CORRECTED PRESSURE (PSIA) = 64.1396 VAPOR PRESSURE (PSIA) = .3875 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94100.0 (a
B-35
SUMMARY
OF MEASURED DATA AT 45 823 TEMP 1 = 553.4480 ( 93.550 )
['>')
TEMP 2 = 555.6280 ( 95.730 )
TEMP 3 = 536.6260 ( 76.620 )
TEMP 4 = 536.6750 ( 77.350 )
TEMP 5 = 534.9460 -( 75.220 )
TEMP 6 = 534.7770 ( 74.770 )
TEMP 7 = S31.4180 ( 71.590 )
TEMP 8 = 530.0650 ( 70.230 )
TEMP 9 = 530.4620 ( 70.840 )
TEMP 10 = 543.2870 ( 83.780 )
TEMP 11 = 543.0760 ( 83.310 )
TEMP 12 = 543.4240 ( 84.070 )
PRES 1 = 64.5260 ( 64528.0 )
PRES 2= 64.5311 ( 64533.0 )
VPRS 1 = .2869 ( 63.200 )
VPRS 2= .2730 ( 62.000 )
VPRS 3= .2798 ( 62.400 )
VPRS 4= .2711 ( 62.600 ) '
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
(^'s TIME = 45 kJ DATE = 823
' TEMPERATURE (DEGREES R.) = 540.7700 CORRECTED PRESSURE (PSIA) =
64.1422 VAPOR PRESSURE (PSIA) = .3889 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94093.4 o
B-36
O APPENDIX C ILRT MASS POINT ANALYSIS O
O C-1
t's
' N.
PEACH BOTTOM UNIT 3 ILRT LEAKAGE RATE (WEIGHT PERCENT / DAY)
MASS POINT ANALYSIS TIME AND DATE AT START OF TEST: 1630 822 1983 TEST DURATION: 8.25 HOURS TIME TEMP PRESSURE CTMT. AIR MASS LOSS AVERAGE MASS (R) (PSIA) MASS (LBM) (LBM) LOSS (LBM/HR)
-- _ _ _ _ . _ ._ = _ - - - - -
1630 540.244 64.0914 94110.
1645 540.274 64.0916 94106. 4.9 19.5 1700 540.271 64.0920 94107. -1.1 7.7 1715 540.265 64.0930 94109. -2.6 1.7 1730 540.282 64.0939 94108. 1.6 2.9 1745 540.294 64.0955 94108. .3 2.1 1800 540.309 64.0977 94108. .6 1.4 1815 540.301 64.0974 94109. .9 .6 1830 540.301 64.0983 94111. -1.3 .1 1845 540.283 64.0971 94112. -1.4 .7 1900 540.296 64.0974 94110. 1.9 .1 1915 540.297 64.0944 94106. 4.5 1.7 1930 540.274 64.0887 94101. 4.5 3.1
(')
\'
1945 540.241 2000 540.266 64.0822 64.0784 94097.
94088.
3.7 9.9 4.0 6.5 2015 540.258 64.0777 94088. .4 6.0 2030 540.298 64.07e2 94082. 6.3 7.2 2045 540.289 64.0809 94087. -5.6 5.5 2100- 540.291 64.0843 94092. -4.7 4.1 2115 540.336 64.0873 94088. 3.5 4.7 2130 540.409 64.0921 94083. 5.6 5.5 2145 540.429 64.0974 94087. -4.3 4.5 2200 540.456 64.1028 94090. -3.3 3.7 2215 540.478 64.1062 94092. -1.2 3.3 2230 540.460 64.1083 94098. -6.3 2.1 2245 540.556 64.1131 94088. 9.8 3.6 2300 540.594 64.1157 94085. 2.0 3.9 2315 540.587 64.1202 94093. -7.9 2.6 2330 540.601 64.1241 94096. -3.4 2.0 2345 540.638 64.1281 94096. .6 2.0 0 540.666 64.1318 94096. .5 1.9 15 540.655 64.1356 94104. -7.5 .9 30 540.710 64.1396 94100. 3.8 1.3 45 540.770 64.1422 94093. 6.6 2.1 FREE AIR VOLUME USED.(CU. FT.) = 293900.
REGRESSION LINE INTERCEPT (LBM) = 94107.
SLOPE (LBM/HR) = -2.3
()
MAXIMUM ALLOWABLE LEAKAGE RATE 75% OF MAXIMUM ALLOWABLE LEAKAGE RATE
=
=
.500
.375 THE UPPER 95% CONFIDENCE LIMIT = .081 THE CALCULATED LEAKAGE RATE = .058 C-2 j
(D )
I I
l APPENDIX D ILRT PLOT-TEMPERATURE VERSUS TIME ,
I b
a I
f i
t G
9 f
I D-1 1
r i
w,---m- w_w,w. _ew e . --e ~ w m ---p w,-m p o on ,-m p s
O PEACH BOTTOM UNIT 3 ILRT TEMPERATURE DEGREES F 80.571 80.615 80.659 80.703 80.747 80.791 80.835 80.880 80.924 80.968 81.012 81.056 81.100
,_______..+ + .+. ...+ + . + +.---+.----+ +-.- +.----.+
1630 !+
1645 l +
1700 1 +
1715 1 +
'173) l +
1745 1 +
- 1800 1 +
1815 1 +
1830 1 +
1845 ! +
1900 1 +
1915 1 +
1930 1 +
1945 +
2000 1 +
2015 1 +
2030 1 +
2045 1 +
i 2!00 1 +
2115 1 +
2130 1 +
2145 1 +
.2200 i +
2215 1- +
2230 1 +
2245 ! +
2300 1 +
2315 i +
2330 1 +-
2345 1 +
01 +
15 3 +
30 ! +
45 1 +
O D-2
O 0,PPliNDIX E It.R1 FiOT-PRESSURE VERSUS TIME i
O O
F 1
l.
l-O PEACH BOTTOM UNIT 3 ILRT PRESSURE PSIA 64.078 64.083 64.088 64.094 64.099 64.105 64.110 64.115 64.121 64.126 64.131 64.137 64.142
+ .+.... .+. _..+ _ .,_. +. , + . _ , + _ ..,- .+. . ,
1630 1 +
1645-l +
- 17H I +
1715 1 +
1730 1 +
1745 1 +
1800 1 +
1815 1 +
1830 1 +
1845 i +
1900 1 +
1915 1 +
1930 1 +
1945 1 +
2000 1+
2015 + 4 2030 1+
2045 1 +
O' 2100 1 2115 1
+
+
2130 1 +
2145 1 +
2200 1 +
2215 1 +
2230 1 +
2245 i +
2300 1 +
2315 1 +
2330 1 +
2345 1~ +
01 +
15 1 +
30 1 +
45 1 +
0 E-2
e O
APPENDIX F ILRT PLOT-MASS POINT CALCULATED LEAKAGE RATE VERSUS TIME O
O F-1
O PEACH BOTTOM UNIT 3 ILRT MASS POINT LEAKAGE RATE (+) AND UCL(%)
.038 .M2 .034 .070 .1% .142 .178 .214 .250 .2N .322 .358 .394
+ + _ .+ .+._._+_+.w+.++._,. +.... +
IMO I 1 1645 1 1 17M i 1 1715 1 + 1 1730 1 + 1 1745 i + 1 1800 1 + 1 1815 I .+ 1 1830 1 + 1 1845 + 1 1900 1+ 1 1915 1 + 1 1930 1 + 1 1945 1 + 1 2M01 + 1 2015 1 + 1 2030 1 + 1 2045 I + 1
+ 1 0 2l00 2115 1 i + 1 2130 1 + 1 2145 1 + 1 2200 1 + 1 2215 1 + 1 2230 1 + 1 2245 i + 1 2300 l + 1 2315 1 + 1 2330 1 + 1 2345 1 + 1 01 + 1 15 I + 1 30 l + 1 45 1 + 1 i O
F-2
O APPENDIX G ILRT PLOT-AIR MASS VERSUS TIME O .
O G-1
O PEACH BOTTOM UNIT 3 ILRT AIRMASS LBM X 1000 93.999 93.999 94.010 94.020 94.030 94.040 94.051 94.061 94.071 94.001 v4.092 94.102 94.!!2
+ _ __ + ..,___. + +__ + .__+.__. ,.____ + _
+.__ __..+ ___+. __ __,
1630 1 +
1645 I +
1700 1 +
1715 1 +
17301 +
1745 1 +
18M i +
1815 I +
1830 1 +
l 1845 i +
1900 1 +
1915 1 +
19301 +
1945 1 +
20M i +
2015 1 +
2030 1 +
2045 i +
+
. O 2!00 21151i +
2130 1 +
2145 i +
2200 1 +
2215 1 +
2230 1 +
2245 I +
l 2300 1 +
2315 +
2330 i e 2345 1 +
0i +
15 1 +
30 1 +
45 8 +
O l c-2
i I
h l
I i
i APPENDIX H !
f FAILED TEST REPORT .
l '
t i
I I
J f
l i
O l a
I i
t I
a
! I I
- n e
t E
e H-1 t
.n.,-,
f O
PEACH BOTTOM UNIT 3 ILRT LEAKAGE RATE (WEIGHT PERCENT / DAY)
MASS POINT ANALYSIS TIME AND DATE AT START OF TEST: 2115 821 1983 TEST DURATION: 1.25 HOURS i
TIME ' TEMP PRESSURE CTMT. AIR MASS LOSS AVERAGE MASS (R) (PSIA) MASS (LBM) (LBM) LOSS (LBM/HR)
. 2115 539.888 63.8625 93836.
2130 539.917 63.8610 93829. 7.3 29.4 2145 539.939 63.8582 93821. 7.8 30.3 2200 539.963 63.8556 93813. 8.0 30.9 2215 539.972 63.8525 93807. 6.2 29.4 2230 539.985 63.8489 93799. 7.6- 29.6 FREE AIR VOLUME USED (CU. FT.) = 293900.
REGRESSION LINE INTERCEPT (LBM) = 93836.
SLOPE-(LBM/HR) = -29.6 MAXIMUM ALLOWABLE. LEAKAGE. RATE = .500
. 75% OF MAXIMUM ALLOWABLE LEAKAGE RATE = .375
\]'
/ THE UPPER 95% CONFIDENCE LIMIT THE CALCULATED LEAKAGE RATE
=
=
.783
.757 0:
H-2
SUMMARY
OF MEASURED DATA AT 2115 821
/~'T TEMP 1 = 552.7660 ( 92.870 )
't l TEMP 2 = 554.6970 ( 94.800 )
TEMP 3 = 536.3060 ( 76.300 )
TEMP 4 = 536.2570 ( 76.930 )
TEMP 5 = 534.3070 ( 74.580 )
TEMP 6 = 533.7590 ( 73.750 )
TEMP 7 = 530.3010 ( 70.470 )
TEMP 8 = 528.7650 ( 68.930 )
TEMP 9 = 529.8120 ( 70,190 )
TEMP 10 = 542.2650 ( 82.760 )
TEMP 11 = 542.0980 ( 82.330 )
TEMP 12 = 542.3260 ( 82.970 )
PRES 1 = 64.2237 ( 64225.0 )
PRES 2= 64.2401 ( 64242.0 )
VPRS 1 = .2798 ( 62.500 )
VPRS 2= .2682 ( 61.500 )
VPRS 3= .2740 ( 61.800 )
VPRS 4= .2663 ( 62.100 )
VPRS 5= .4900 ( 79.600 )
VPRS 6= .5392 ( 82.600 )
SUMMARY
OF CORRECTED DATA
('s, TIME = 2115
't_/ DATE = 821 TEMPERATURE (DEGREES R.) = 539.8880 CORRECTED PRESSURE (PSIA) = 63.8625 VAPOR PRESSURE (PSIA) = .3776 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93836.2
.f 3
'\
SUMMARY
OF MEASURED DATA AT 2130 821
()
TEMP TEMP 1
2
=
=
552.7360 554.8180
(
(
92.840 94.920
)
)
TEMP 3 = 536.2760 ( 76.270 )
TEMP 4 = 536.3470 ( 77.020 )
TEMP 5 = 534.4470 ( 74.720 )
TEMP 6 = 533.8290 ( 73.820 )
TEMP 7 = 530.4400 ( 70.610 )
TEMP 8 = 528.7050 ( 68.870 )
TEMP 9 = 529.8720 ( 70.250 )
TEMP 10 = 542.2850 ( 82.780 )
TEMP 11 = 542.0880 ( 82.320 )
TEMP 12 = 542.2860 ( 82.930 )
PRES 1= 64.2227 ( 64224.0 )
PRES 2= 64.2391 ( 64241.0 )
VPRS 1= .2808 ( 62.600 )
VPRS 2= .2692 ( 61.600 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2663 ( 62.100 )
VPRS 5= .4900 ( 79.600 )
VPRS 6= .5392 ( 82.600 )
SUMMARY
OF CORRECTCD DATA
()
k>
TIME = 2130 DATE = 821 TEMPERATURE (DEGREES R.) = 539.9170 CORfCCTED PRESSURE (PSIA) = 63.8610 VAPOR PRESSURE (PSIA) = .3782 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93828.9
,n, w;
H-4
SUMMARY
OF MEASURED DATA AT 2145 821
[) TEMP 1 = 552.5360 ( 92.640 )
TEMP 2 = 554.7080 ( 94.810 )
TEMP 3 = 536.4160 ( 76.410 )
TEMP 4 = 536.4260 ( 77.100 )
TEMP 5 = 534.4070 ( 74.680 )
TEMP 6 = 533.9390 ( 73.930 )
TEMP 7u 530.4600 ( 70.630 )
TEMP 8 = 528.9750 ( 69.140 )
TEMP 9 = 529.9220 ( 70.300 )
TEMP 10 = 542.2850 ( 82.780 )
TEMP 11 = 542.0980 ( 82.330 )
TEMP 12 = 542.3060 ( 82.950 )
PRES 1 = 64.2217 ( 64223.0 )
PRES 2= 64.2371 ( 64239.0 )
W'RS 1 = .2818 ( 62.700 )
VPRS 2= .2701 ( 61.700 )
VPRS 3= .2759 ( 62.000 )
VPRS 4= .2673 ( 62.200 )
VPRS 5= .4916 ( 79.700 )
VPRS 6 = .5392 ( 82.600 )
SUMMARY
OF CORRECTED DATA TIME = 2145
(~')
ks DATE = 821 TEMPERATURE (DEGREES R.) = 539.9390 CORRECTED PRESSURE (PSIA) = 63.8582 VAPOR PRESSURE (PSIA) = .3789 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93821.1
,/ ~
N/'
H-5
4 i
, *y
SUMMARY
OF MEASURED DATA AT 2200 821
()
TEMP TEMP 1
2
=
=
552.7060 554.8880
(
(
92.810 94.990
)
)
' TEMP 3 = 536.3060 ( 76.300 )
. TEMP 4 = 536.4260 ( 77.100 )
TEMP 5 = 534.3670 ( 74.640 )
TEMP 6 = 534.0780 ( 74.070 )
TEMP 7 = 530.5100 ( 70.680 )
TEMP 8 = 528.8750 ( 69.040 )
TEMP 9 = 529.9420 ( 70.320 )
TEMP 10 = 542.2850 ( 82.780 )
TEMP 11 = 542.0980 ( 82.330 )
TEMP 12 = 542.3260 ( 82.970 )
PRES 1 = 64.2197 ( 64221.0 )
PRES 2= 64.2352 ( 64237.0 )
VPRS 1 = .2818 ( 62.700 )
VPRS 2= .2701 ( 61.700 )
VPRS 3= .2769 ( 62.100 )
VPRS 4= .2682 ( 62.300 )
' VPRS 5= .4932 ( 79.800 )
VPRS 6= .5392 ( 82.600 )
SUMMARY
OF CORRECTED DATA
/~'S TIME = 2200 kl DATE = 821 TEMPERATURE (DEGREES R.) = 539.9630 CORRECTED PRESSURE (PSIA) = 63.8556 VAPOR PRESSURE (PSIA) = .3796 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93813.0 4
'v' s
H-6 i i
.s v
SUMMARY
OF MEASURED DATA AT 2215 821
(~
TEMP TEMP 1 = 552.7964
.2 = 554.8380
(
(
92.900 94.940
)
)
TEMP 3 = 536.2860 ( 76.280 )
TEMP 4 = 536.3570 ( 77.030 )
TEMP 5 = 534.4470 ( 74.720 )
TEMP 6 = 534.0880 ( 74.080 )
TEMP 7 = 530.5400 ( 70.710 )
TEMP 8 = 529.0350 ( 69.200 )
TEMP 9 = 529.9720 ( 70.350 )
TEMP 10 = 542.2650 ( 82.760 )
TEMP 11 = 542.0980 ( 82.330 )
. v ,- , , , TEMP 12 = 542.3160 ( 82.960 )
_s PRES 1 = 64.2167 ( 64218.0 )
.s, .
PRES 2= 64.2322 ( 64234.0 )
s
., y VPRS 1 = .2828 ( 62.800 )
f / <" VPRS 2= .2711 ( 61.800 )
,a , j- VPRS 3= .2779 ( 62.200 )
_I VPRS 4= .2682 ( 62.300 )
VPRS 5= .4916 ( 79.700 )
VPRS 6= .5392 ( 82.600 )
SUMMARY
OF LORRECTED DATA
[]
k#
TIME = 2215 DATE = 821 TEMPERAfURb kD' GREES R. ) = 539.9720 CORRECTED PRESSURE (PSIA) = 63.8525 VAPOR PRESSURE (PSIA) = .3796 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93806.9
- 4
(
( -
1 H-7
_m
SUMMARY
OF MEASURED DATA AT 2230 821
,-m
- l TEMP 1 = 552.7060 ( 92.810 )
TEMP 2 = 554.5370 ( 94.640 )
TEMP 3 = 536.3860 .( 76.380 )
TEMP 4 = 536.5260 ( 77.200 )
TEMP. 5 = 534.5960 ( 74.870 )
TEMP 6 = 534.0180 ( 74.010 )
TEMP 7 = 530.6300 ( 70.800 )
TEMP 8 = 529.0350 ( 69.200 )
TEMP 9 = 530.0320 ( 70.410 )
TEMP 10 = 542.2850 ( 82.780 )
TEMP 11 = 542.0980 ( 82.330 )
TEMP 12 = 542.3360 ( 82.980 )
PRES 1 = 64.2107 ( 64212.0 )
PRES 2= 64.2281 ( 64230.0 )
VPRS 1 = .2828 ( 62.800 )
VPRS 2= .2711 ( 61.800 )
VPRS 3= .2779 ( 62.200 )
VPPS 4= .2682 ( 62.300 )
VPRS 5= .4900 ( 79.600 )
VPRS 6= .5392 ( 82.600 )
SUMMARY
OF CORRECTED DATA
( ') TIME = 2230 DATE = 821 TEMPERATURR (DEGREES R.) = 539.9850 CORRECTED PRESSURE (PSIA) = 63.8489 VAPOR PRESSURE (PSIA) = .3793-VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93799.3 r%
\ ,/
H-8
l-O APPENDIX J VERIFICATION FLOW TEST
SUMMARY
DATA O
t
)
i O
J-1 i
I j
~.%,-- , - - , - . . . - _ _ _ _ _ _ . _ . _ _ , . , _ , , , , _ _ , _
b, PEACH BOTTOM UNIT 3 VERIFICATION
SUMMARY
DATA ALMAX = .500 VOLUME = 293900.
VRATET = .547 VRATEM = .553 TIME DATE TEMP PRESSURE VPRS VOLUME 315 823 540.917 64.1420 .3891 293900.
330 823 540.927 64.1420 .3891 293900.
345' 823 540.962 64.1405 .3896 293900.-
400 823 541.006 64.1379 .3902 293900.
415 823 541.004 64.1369 .3902 293900.
430 823 541.000 64.1353 .3908 293900.
445 823 541.035 64.1350 .3911 293900.
500 823 541.033 64.1355 .3906 293900.
515 823 541.075 64.1340 .3911 293900.
530 823 541.079 64.1326 .3915 293900.
545 823 541.080 64.1315 .3916 293900.
600 823 541.098 64.1315 .3916 293900.
, 615 823 541.111 64.1313 .3918 293900.
630 823 541.167 64.1307 .3914 293900.
645 823 541.165 64.1301 .3910 293900.
700 823 541.201 64.1288 .3923 293900.
() 715 823 541.197 64.1288 .3923 293900, t
v J-2
SUMMARY
OF MEASURED DATA AT 315 823
( #) TEMP 1 = 553.~9990 ( 94.100 )
TEMP- 2 = 556.2380 ( 96.340 )
TEMP 3 = 537.0760 ( 77.070 )
TEMP 4 = 536.6850 ( 77.360 )
TEMP 5 = 535.0450 ( 75.320 )
TEMP 6 = 534.9070 ( 74.900 )
TEMP 7 = 531.5270 ( 71.700 )
TEMP 8 = 529.8950 ( 70.060 )
TEMP 9 = 530.6920 ( 71.070 )
TEMP 10 = 543.3470 ( 83.840 )
TEMP 11 = 543.1350 ( 83.370 )
TEMP 12 = 543.4240 ( 84.070 )
PRES 1 = 64.5270 ( 64529.0 )
PRES 2= 64.5311 ( 64533.0 )
JPRS 1 = .2889 ( 63.400 )
VPRS 2= .2759 ( 62.300 )
VPRS 3= .2818 ( 62.600 )
VPRS. 4 = .2730 ( 62.800 )
VPRS 5= .5031 ( 80.400 )
VPRS 6= .5585 ( 83.700 )
F
SUMMARY
OF CORRECTED DATA T. TIME = 315
(~J
\- DATE = 823 TEMPERATURE (DEGREES R.) = 540.9170 CORRECTED PRESSURE (PSIA) = 64.1420 VAPOR PRESSURE (PSIA) = .3891 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94067.6 LJ J-3
, __m________ . . _ . _ . _ _ _ _ . _
SUMMARY
OF MEASURED DATA AT 330 823 I~3 TEMP 1 = 554.0990 ( 94.200 )
k/ TEMP 2 = 556.3680 ( 96.470 )
TEMP 3 = 536.8460 ( 76.840 )
TEMP 4 = 536.7250 ( 77.400 )
TEMP 5 = 535.0750 ( 75.350 )
TEMP 6 = 534.8870 ( 74.880-)
TEMP 7 = 531.5870 ( 71.760 )
TEMP 8 = 529.9150 ( 70.080 )
TEMP 9 = 530.6720 ( 71.050 )
TEMP 10 = 543.3470 ( 93.840 )
TEMP 11 = 543.1550 ( 83.390 )
TEMP 12 = 543.4340 ( 84.080 )
PRES 1 = 64.5270 ( 64529.0 )
PRES 2= 64.5311 ( 64533.0 )
VPRS 1 = .2889 ( '63.400 )
VPRS 2= .2749 ( 62.200 )
VPRS 3= .2818 ( 62.600 )
VPRS 4= .2740 ( 62.900 )
VPRS 5= .5031 ( 80.400 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA S TIME = 330
(~J k DATE = 823 TEMPERATURE (DEGREES R.) = 540.9270 CORRECTED PRESSURE (PSIA) = 64.1420 VAPOR PRESSURE (PSIA) = .3891 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94066.0
,r's
\ _/
J-4
SUMMARY
OF MEASURED DATA AT' 345- 823
(~') TEMP 1 = 554.0690 ( 94.170 )
k/ TEMP 2 = 556.4180 ( 96.520 )
TEMP 3 = 537.0360 ( 77.030 )
TEMP 4 = 536.7150 ( 77.390 )
TEMP 5 = 535.1450 ( 75.420 )
TEMP 6 = 534.9970 ( 74.990 )
TEMP 7 = 531.4880 ( 71.660 )
TEMP 8 = 530.0350 ( 70.200 )
TEMP 9 = 530.7020 ( 71.080 )
TEMP 10 = 543.3470 ( 83.840 )
TEMP 11 = 543.1850 ( 83.420 )
TEMP 12 = 543.4340 ( 84.080 ).
PRES 1 = 64.5270 ( 64529.0 )
PRES 2= 64.5301 ( 64532.0 )
VPRS 1 = .2889 ( 63.400 )
VPRS 2= .275Y ( 62.300 )
VPRS 3= .2818 ( 62.600 )
VPRS 4= .2740 ( 62.900 )
VPRS 5= .5048 ( 80.500 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRECTED DATA
(/~T TIME = 345
,) DATE = 823 TEMPERATURE (DEGREES R.) = -540.9620 CORRECTED PRESSURE (PSIA) = 64.1405 VAPOR PRESSURE (PSIA) = .3896 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94057.6 (3
L.]
J-5 l
SUMMARY
OF MEASURED DATA AT 400 823 p
- 1 TEMP 1 = 554.3390 ( 94.440 )
'~
TEMP 2 = 556.4180 ( 96.520 )
TEMP 3 = 537.0560 ( 77.050 )
TEMP 4 = 536.7150 ( 77.390 )
TEMP 5 = 535.0150 ( 75.290 )
-TEMP' 6 = 535.0670 ( 75.060 )
TEMP 7 = 531.5570 ( 71.730 )
TEMP 8 = 530.5250 ( 70.690 )
TEMP 9 = 530.6920 ( 71.070 )
TEMP 10 = 543.3570 ( 83.850 )
TEMP 11 = 543.1850 ( 83.420 )
TEMP 12 = 543.4440 ( 84.090 '
PRES 1 = 64.5220 ( 64524.0 )-
PRES 2= 64.5281 ( 64530.0 )
VPRS 1 = .2889 ( 63.400 )
VPRS 2= .2749 ( 62.200 )
VPRS 3= .2818 ( 62.600 )
VPRS 4= .2740 ( 62.900 )
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5585 ( 83.700 )
SUMMARY
OF CORRCCTED DATA
["T TIME = 400 DATE = 823 TEMPERATURE (DEGREES R.) = 541.0060 CORRECTED PRESSURE (PSIA) = 64.1379 VAPOR PRESSURE (PSIA) = .3902 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94046.1
_)
J-6
SUMMARY
OF MEASURED DATA AT 415 823
!n
/ TEMP 1 = 554.3090 ( 94.410 )
TEMP 2 = 556.5080 ( 96.610 )
TEMP 3 = 537.0560 ( 77.050 )
TEMP 4 = 536.6950 -( 77.370 )
TEMP 5 = 535.0050 ( 75.280 )
TEMP 6 = 535.0570 ( 75.050 )
TEMP 7 = 531.6070 ( 71.780 )
TEMP 8 = 530.3050 ( 70.470 )
TEMP 9 = 530.7320 ( 71.110 )
TEMP 10 = 543.3770 ( 83.870 )
TEMP 11 = 543.1850 ( 83.420 )
TEMP 12 = 543.4540 ( 84.100 )
PRES 1 = 64.5230 ( 64525.0 )
PRES 2= 64.5271 ( 64529.0 )
VPRS 1 = .2889 ( 63.400 )
VPRS 2= .2749 ( 62.200 )
VPRS 3= .2818 ( 62.600 )
VPRS 4= .2740 ( 62.900 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
[i TIME = 415
# DATE = 823 TEMPERATURE (DEGREES R.) = 541.0040
. CORRECTED PRESSURE (PSIA) = 64.1369 VAPOR PRESSURE (PSIA) = .3902 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94045.0 e
wA*
Cl J-7
SUMMARY
OF MEASURED DATA AT 430 823
-'"[) TEMP TEMP 1
2
=
=
554.2790 556.4080
(
(
94.380 96.510
)
)
TEMP 3 = 537.1960 ( 77.190 )
TEMP 4 = 536.7250 ( 77.400 )
TEMP 5 = 535.0450 ( 75.320 )
TEMP 6 = 535.0470 ( 75.040 )
TEMP 7 = 531.6270 ( 71.800 )
TEMP 8 = 530.0550 ( 70.220 )
TEMP 9 = 530.7820 ( 71.160 )
TEMP 10 = 543.3770 ( 83.870 )
TEMP 11 = 543.1950 ( 83.430 )
TEMP 12 = 543.4440 ( 84.090 )
PRES 1 = 64.5201 ( 64522.0 )
PRES 2= 64.5261 ( 64528.0 )
VPRS 1 = .2899 ( 63.500 )
VPRS 2= .2759 ( 62.300 )
VPRS 3= .2818 ( 62.600 )
VPRS 4= .2740 ( 62.900 )
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA i TIME = 430
[^J
'- DATE = 823 TEMPERATURE (DEGREES R.) = 541.0000 CORRECTED PRESSURE (PSIA) = 64.1353 VAPOR PRESSURE (PSIA) = .3908 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94043.3
('l
\)
3-8 P
h m i
SUMMARY
OF MEASURED DATA AT 445 823
[} TEMP 1 = 554.3290 ( 94.430 )
TEMP 2 = 55S.5780 ( 96.680 )
TEMP 3 = 537.1160 ( 77.110 )
TEMP 4 = 536.7740 ( 77.450 )
TEMP 5 = 535.2450 ( 75.520 )
TEMP 6 = 535.0470 ( 75.040 )
TEMP 7 = 531.6070 ( 71.780 )
TEMP 8 = 530.0550 ( 70.220 )
TEMP 9 = 530.7620 ( 71.140 )
TEMP 10 = 543.3870 ( 83.880 )
TEMP 11 = 543.2050 ( 83.440 )
TEMP 12 = 543.4740 ( 84.120 )
PRES 1 = 64.5220 ( 64524.0 )
PRES 2= 64.5261 ( 64528.0.)
VPRS 1 = .2899 ( 63.500 )
~
VPRS 2= .2769 ( 62.400 )
VPRS 3= .2818 ( 62.600 )
VPRS 4= .2749 ( 63.000 )
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
(~'; TIME = 445 N'
DATE = 823 TEMPERATURE (DEGREES R.) = 541.0350 CORRECTED PRESSURE (PSIA) = 64.1350 VAPOR PRESSURE (PSIA) = .3911 VOLUME (CU.FT.) = 293900.0 AIR MASS (LEM) = 94036.9 f'N
'\ _)
J-10
SUMMARY
OF MEASURED DATA AT 500 823 I)
\
TEMP 1 = 554.4090 ( 94.510 )
TEMP 2 = 556.7280 ( 96.830 )
TEMP 3 = 536.9760 ( 76.970 )
TEMP 4 = 536.7840 ( 77.460 )
TEMP 5 = 535.0750 ( 75.350 )
TEMP 6 = 535.0870 ( 75.080 )
TEMP 7 = 531.6370 ( 71.810 )
TEMP O = 530.0350 ( 70.200 )
TEMP 9 = 530.7720 ( 71.150 )
TEMP 10 = 543.3970 ( 83.890 )
TEMP 11 = 543.2050 ( 83.440 )
TEMP 12 = 543.4840 ( 84.130 )
PRES 1 = 64.5220 ( 64524.0 )
PRES 2= 64.5261 ( 64528.0 )
VPRS 1 = .2899 ( 63.500 )
VPRS 2= .2759 ( 62.300 )
VPRS 3= .2828 ( 62.700 )
VPRS 4= .2740 ( 62.900 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5603 ( 83.800 )
~
SUMMARY
OF CORRECTED DATA
/
\s ')' TIME = 500 DATE = 823 TEMPERATURE (DEGREES R.) = 541.0330 CORRECTED PRESSURE (PSIA) = 64.1355 VAPOR PRESSURE (PSIA) = .3906 VOLUME (CU.FT.) =
293900.0 AIR MASS (LBM) = 94037.9 uj J-ll
SUMMARY
OF MEASURED DATA AT 515 823 I'
TEMP 1 = 554.4500 ( 94.550 )
TEMP 2 = 556.5580 ( 96.660 )
TEMP 3 = 537.0560 ( 77.050 )
TEMP 4 = 536.8840 ( 77.560 )
TEMP 5 = 535.2450 ( 75.520 )
TEMP 6 = 535.0970 ( 75.090 )
TEMP 7 = 531.6470 ( 71.820 )
TEMP 8 = 530.3850 ( 70.550 )
-TEMP 9 = 530.7720 ( 71.150 )
TEMP 10 = 543.3970 ( 83.890 )
TEMP 11 = 543.2150 ( 83.450 )
TEMP 12 = 543.5040 ( 84.150 )
PRES 1 = 64.5171 ( 64519.0 )
PRES 2= 64.5251 ( 64527.0 )
VPRS 1 = .2899 ( 63.500 )
VPRS 2= .2759 ( 62.300 )
VPRS 3= .2828 ( 62.700 )
VPRS 4= .2749 ( 63.000 )
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5603 ( 83.800 )
SUt1 MARY OF CORRECTED DATA '
[~}
TIME = 515 DATE = 823 TEMPERATURE (DEGREES R.) = 541.0750 CORRECTED PRESSURE (PSIA) = 64.1340 VAPOR PRESSURE (PSIA) = .3911 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94028.5 C'"3 !
J-12
SUMMARY
OF MEASURED DATA AT 530 823
.f )
TEMP TEMP 1
2
=
=
554.5200 556.6990
( 94.620 )
( 96.800 )
TEMP 3 = 537.1660 ( 77.160 )
TEMP 4 = 536.8440 ( 77.520 )
TEMP 5 = 535.3250 ( 75.600 )
TEMP 6 = 534.9970 ( 74.990 )
TEMP 7 = 531.6270 ( 71.800 )
TEMP 8 = 530.0750 ( 70.240 )
TEMP 9 = 530.8720 ( 71.250 )
TEMP 10 = 543.3970 ( 83.890 )
TEMP 11 = 543.2250 ( 83.460 )
TEMP 12 = 543.5040 ( 84.150 )
PRES 1 = 64.5171 ( 64519.0 )
PRES 2= 64.5241 ( 64526.0 )
VPRS 1 = .2899 ( 63.500 )
VPRS 2= .2769 ( 62.400 )
VPRS 3= .2828 ( 62.700 )
VPRS 4= .2740 ( 62.900 )
VPRS 5= .5098 ( 80.800 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
/~T TIME = 530
\-) DATE = 823 TEMPERATURE (DEGREES R.) = 541.0790 CORRECTED PRESSURE (PSIA) = 64.1326 VAPOR PRESSURE (PSIA) = .3915 VOLUME (CU.FT.) = 293900.0 AIR. MASS (LBM) = 94025.7 O
J-13
SUMMARY
OF MEASURED DATA AT 545 823 f)
TEMP 1 = 554.5200 ( 94.620 )
TEMP 2 = 556.8690 ( 96.970 )
TEMP 3 = 537.06o0 ( 77.060 )
TEMP 4 = 536.8140 ( 77.490 )
TEMP 5 = 535.2450 ( 75.520 )
TEMP 6 = 534.9570 (- 74.950 )
TEMP 7 = 531.6670 ( 71.840 )
TEMP S = 530.1550 ( 70.320 )
TEMP 9 = 530.7920 ( 71.170 )
TEMP 10 = 543.4280 ( 83.920 )
TEMP 11 = 543.2350 ( B3.470 )
TEMP 12 = 543.5040 ( 84.150 )
PRES 1 = 64.5161 ( 64518.0 )
PRES 2= 64.5231 ( 64525.0 )
VPRS 1 = .2909 ( 63.600 )
VPRS 2= .2759 ( 62.300 )
VPRS 3= .2828 ( 62.700 )
VPRS 4= .2749 ( 63.000 )
VPRS 5= .5098 ( 80.800 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
/~S TIME = 545 5- DATE = 823 I
TEMPERATURE (DEGREES R.) = 541.0800 CORRECTED PRESSURE (PSIA) = 64.1315 VAPOR PRESSURE (PSIA) = .3916 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94023.8
/^\
U J-14
f
SUMMARY
OF MEASURED DA TA AT 600 823 I' ')
TEMP 1 = 554.6700 ( 94.770 )
TEMP 2 = 556.9290 ( 97.030 )
TEMP 3 = 537.0560 ( 77.050 )
TEMP 4 = 536.7840 ( 77.460 )
TEMP 5 = 535.2450 ( 75.520 )
TEMP 6 = 535.0370 ( 75.030 )
TEMP 7 = 531.6270 ( 71.800 )
TEMP 8 = 530.1950 ( 70.360 )
TEMP 9 = 530.8220 ( 71.200 )
TEMP 10 = 543.4280 ( 83.920 )
TEMP 11 = 543.2250 ( 83.460 )
TEMP 12 = 543.5140 ( 84.160 )
PRES 1 = 64.5161 ( 64518.0 )
PRES 2= 64.5231 ( 64525.0 )
VPRS 1 = .2899 ( 63.500 )
VPRS 2= .2769 ( 62.400 )
VPRS 3= .2828 ( 62.700 )
VPRS 4= .2749 ( 63.000 )
VPRS 5= .5098 ( 80.800 )
VPRS 6= .5603 ( 83.300 )
SUMMARY
OF CORRECTED DATA
(~t TIME = 600
' + '
DATE = 823 TEMPERATURE (DEGREES R.) = 541.0980 CORRECTED PRESSURE (PSIA) = 64.1315 VAPOR PRESSURE (PSIA) = .3916 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94020.7 v
J-15
SUMMARY
OF MEASURED DATA AT 615 823 TEMP 1 = 554.5600 94.660 )
I)
TEMP 2 = 556.9790
(
( 97.080 )
TEMP 3 = 537.0160 ( 77.010 )
TEMP 4 = 536.8640 ( 77.540 )
TEMP 5 = 535.0750 ( 75.350 )
TEMP 6 = 535.0770 ( 75.070 )
TEMP 7 = 531.7170 ( 71.890 )
TEMP 8 = 530.3850 ( 70.550 )
TEMP 9 = 530.8220 ( 71.200 )
TEMP 10 = 543.4480 ( 83.940 )
TEMP 11 = 543.2750 ( 83.510 )
TEMP 12 = 543.5140 ( 84.160 )
PRES 1 = 64.5171 ( 64519.0 )
PRES 2= 64.5231 ( 64525.0 )
VPRS 1 = .2909 ( 63.600 )
VPRS 2= .2769 ( 62.400 )
VPRS 3= .2028 ( 62.700 )
VPRS 4= .2749 ( 63.000 )
VPRS 5= .5081- ( 80.700 )
VPRS 6= .5620 ( 83.900 )
~
SUMMARY
OF CORRECTED DATA
(} TIME = 615
\' DATE = 823
, TEMPERATURE (DEGREES R.) = 541.1110 CORRECTED PRESSURE (PSIA) = 64.1313 VAPOR PRESSURE (PSIA) = .3918 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94018.3 r's
(
J-16 m-
SUMMARY
OF MEASURED DATA AT 630 823 TEMP
( )
TEMP 1
2 =
= 554.6600 556.9890
(
(
94.760 97.090
)
)
TEMP 3 = 537.3960 ( 77.390 )
TEMP 4 = 536.8840 ( 77.560 )
TEMP 5 = 535.2850 ( 75.560 )
TEMP 6 = 535.1870 ( 75.180 )
TEMP 7 = 531.6670 ( 71.840 )
TEMP 8 = 530.3050 ( 70.470 )
TEMP 9 = 530.8820 ( 71.260 )
TEMP 10 = 543.4380 ( 83.930 )
TEMP 11 = 543.2450 ( 83.480 )
TEMP 12 = 543.5440 ( 84.190 ~)
PRES 1 = 64.5151 ( 64517.0 )
PRES- 2= 64.5221 ( 64524.0 )
VPRS 1 = .2909 ( 63.600 )
VPRS 2= .2769 ( 62.400 )
VPRS 3= .2828 ( 62.700 )
VPRS 4a .2749 ( 63.000 )
VPRS 5= .5081 ( 80.700 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA I TIME = 630 k ') DATE = 823 TEMPERATURE (DEGREES R.) = 541.1670 CORRECTED PRESSURE (PSIA) = 64.1307 VAPOR PRESSURE (PSIA) = .3914 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94007.7 (D
v J-17
SUMMARY
OF MEASURED DATA AT 645 823
()
TEMP TEMP 1
2
=
=
554.6200 556.9990
(
(
94.720 97.100
)
)
TEMP 3 = 537.3260 ( 77.320 )
TEMP 4 = 536.8740 ( 77.550 )
TEMP 5 = 535.2250 ( 75.500 )
TEMP 6 = 535.1470 ( 75.140 )
TEMP 7 = 531.7070 ( 71.880 )
TEMP 8 = 530.4350 ( 70.600 )
TEMP 9 = 530.8420 ( 71.220 )
TEMP 10 = 543.4680 ( 83.960 )
TEMP 11 = G43.2650 ( 83.500 )
TEMP 12 = 543.5440 ( 84.190 )
PRES 1 = 64.5151 ( 64517.0 )
PRES 2= 64.5211 ( 64523.0 )
VPRS 1 = .2909 ( 63.600 )
VPRS 2= .2769 ( 62.400 )
VPRS 3= .2828 ( 62.700 )
VPRS 4= .2749 ( 63.000 )
VPRS 5= .5065 ( 80.600 )
VPRS 6= .5603 ( 83.800 )
SUMMARY
OF CORRECTED DATA
["')
k
TIME = 645 DATE = 823 TEMPERATURE (DEGREES R.) = 541.1660 CORRECTED PRESSURE (PSIA) = 64.1301 VAPOR PRESSURE (PSIA) = .3910 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 94006.9 (3
NY J-18
SUMMARY
OF MEASURED DATA AT 700 823
('-)' TEMP 1 = 554.7500 TEMP 2 = 556.9690
(
(
94.850 97.070
)
)
TEMP 3 = 537.2860 ( 77.280 )
TEMP 4 = 536.9930 ( 77.670 )
TEMP 5 = 535.4150 ( 75.690 )
TEMP 6 = 535.3270 ( 75.320 )
TEMP 7 = 531.6870 ( 71.860 )
TEMP 8 = 530.2750 ( 70.440 )
TEMP 9 = 530.8820 ( 71.260 )
TEMP 10 = 543.4680 ( 83.960 )
TEMP 11 = 543.2650 ( 83.500 )
TEMP 12 = 543.5440 ( 84.190 )
PRES 1 = 64.5151 ( 64517.0 )
PRES 2= 64.5211 ( 64523.0 )
-VPRS 1 = .2909 ( 63.600 )
VPRS 2= .2769 ( 62.400 )
VPRS 3= .2838 ( 62.800 )
VPRS 4= .2749 ( 63.000 )
VPRS 5= .5098 ( 80.800 )
VPRS 6= .5620 ( 83.900 )
SUMMARY
OF CORRECTED DATA f~) TIME = 700 DATE = '?3 TEMPERATURE (DEGP" 3.) = 541.2010 CORRECTED PRESSURL >IA) = 64.1288 VAPOR PRESSURE s. '3I A) = .3923 VOLUME i CU. F T. ) = 293900.0 AIR MASS (LBM) = 93999.0
,, \
N.j J-19
SUMMARY
OF MEASURED DATA AT 715 823
,~.
i ) TEMP 1 = 554.7200 ( 94.820 )
TEMP 2 = 557.0990 ( 97.200 )
TEMP 3 = 537.2760 ( 77.270 )
TEMP 4 = 536.8840 ( 77.560 ) ,
TEMP 5 = 535.2450 ( 75.520 )
TEMP 6 = 535.2070 ( 75.200 )
TEMP 7 = 531.7370 ( 71.910 )
TEMP 8 = 530.4850 ( 70.650 )
TEMP 9 = 530.8520 ( 71.230 )
TEMP 10 = 543.4880 ( 83.980 )
TEMP 11 = 543.2950 ( 83.530 )
TEMP 12 = 543.5640 ( 84.210 )
PRES 1 = 64.5151 ( 64517.0 )
PRES 2= 64.5211 ( 64523.0 )
VPRS 1 = .2909 ( 63.600 )
VPRS 2= .2769 ( 62.400 )
VPRS 3= .2838 ( 62.800 )
VPRS 4 = .2749 ( 63.000 )
VPRS 5= .5098 ( 80.800 )
VPRS 6= .5620 ( 83.900 )
SUMMARY
OF CORRECTED DATA
/~N TIME = 715
\- DATE = 823 TEMPERATURE (DEGREES R.) = 541.1970 CORRECTED PRESSURE (PSIA) = 64.1288 VAPOR PRESSURE (PSIA) = .3923 VOLUME (CU.FT.) = 293900.0 AIR MASS (LBM) = 93999.7 i
J-20
.,.L + e - - - - , . --- a M w N 4 -- 4-A= a- m ---u J O
APPENDIX K l O
f VERIFICATION FLOW TEST MASS POINT ANALYSIS f
h 8
t O
- O K-1 M*W*mmW-P P 'Br**e .g*eM-w verN re- .,ww*T---*- __wwNwww-*N'evud-w eww *w- mw.. --"-
Ix-PEACH BOTTOM UNIT 3 VERIFICATION LEAKAGE RATE (WEIGHT PERCENT / DAY)
MASS POINT ANALYSIS TIME AND DATE AT START OF TEST: 315 823 1983 TEST DURATION: 4.00 HOURS TIME TEMP PRESSURE CTMT. AIR MASS LOSS AVERAGE MASS (R) (PSIA) MASS (LBM) (LBM) LOSS (LBM/HR) 315 540.917 64.1420 94068.
330 540.927 64.1420 94066. 1.7 6.6 345 540.962 64.1405 94058. 8.4 20.0 400 541.006 64.1379 94046. 11.5 28.7 415 541.004 64.1369 94045. 1.1 22.6 430 541.000 64.1353 94043. 1.7 19.5 445 541.035 64.1350 94037. 6.4 20.5 500 541.033 64.1355 94038. -1.0 17.0 515 541.075 64.1340 94028. 9.5 19.6 530 541.079 64.1326 94026. 2.8 18.6 545 541.080 64.1315 94024. 1.9 17.5 600 541.098 64.1315 94021. 3.2 17.1 615 541.111 64.1313 94018. 2.3 16.4
/ 630 541.167 64.1307 94008. 10.7 18.5 k- 645 541.165 64.1301 94007. .7 17.3 700 541.201 64.1288 93999. 8.0 18.3 715 541.197 64.1288 94000. .7 17.0 FREE AIR VOLUME USED (CU. FT.) = 293900.
REGRESSION LINE INTERCEPT (LBM) = 94065.
SLOPE (LBM/HR) = -16.9 MAXIMUM ALLOWABLE LEAKAGE RATE = .500 75% OF MAXIMUM ALLOWABLE LEAKAGE RATE = .375 THE UPPER 95% CONFIDENCE LIMIT = .459 THE CALCULATED LEAKAGE RATE = .431 K-2
4 0
APPENDIX L DBAT
SUMMARY
DATA TOTAL TIME REPORT AND
SUMMARY
OF MEASURED DATA O
L-1
l.-
m
(_) PEACH BOTTOM UNIT 3 BYPASS TEST
SUMMARY
DATA ALMAX = .785 VOLUME = 127700.0 COD = .600 TIME DATE DRYTMP DRYPRS DRYVAP TORTMP TORPRG TORVAP VOL 1112. 828 543.013 16.130 .171 543.282 14.759 .555 '127700.0 1117- 828 542.137 16.125 .171 543.362 14.768 .554 127700.0 1122 828 542.114 16.122 .171 543.216 14.773 .553 127700.0 1127 828 542.083 16.119 .171 543.166 14.775 .553 127700.0 1132 828 542.084 16.116 .'171 543.146 14.781 .553 127700.0 1137 828 542.194 16.114 .170 543.152 14.785 .552 127700.0 1142 828 542.048 16.110 .168 543.136 14.789 .551 127700.0 1147 828' 542.057 16.107 .168 543.129 14.794 .544 127700.0 1152 828 542.045 16.040 .167 543.136 14.799 .551 127700.0 1157 828 542.037 16.101 .166 543.133 14.804 .550 127700.0 1202 828 542.067 16.100 .165 543.133 14.809 .551 127700.0 1207 828 542.054 16.096 .166 543.123 14.814 .551 127700.0 1212 828 542.059 16.094 .165 543.136 14.818 .551 127700.0 O
d
~j L-2
O PEACH BOTTOM UNIT 3 BYPASS TEST BYPASS AREA (SOUARE INCHES)
-TOTAL TIME ANALYSIS TIME AND DATE AT START OF TEST: 1112 828 1983 TEST DURATION: 1.00 HOURS TIME DRYTMP DRYPRS DRYVAP TORTMP TORPRS TORVAP AREA 1112 543.013 16.130 .171 543.282 14.759 .555 1117 542.137 16.125 .171 543.362 14.768 .554 .14068 1122 542.114 16.122 .171 543.216 14.773 .553 .15840 1127 542.083 16.119 .171 543.166 14.775 .553 .22566 1132 542.084 16.116 .171 543.146 14.781 .553 .12389 1137 .542.194 16.114 .170 543.152 14.785 .552 .11631 1142 542.048 16.110 .168 543.136 14.789 .551 .11575 1147 542.057 16.107 .168 543.129 14.794 .544 .12885 1152 542.045 16.040 .367 543.136 14.799 .551 .10905 1157 542.037 16.101 .166 543.133 14.804 .550 .10985 1202 542.067 16.100 .165 543.133 14.809 .551 .10490 1207 542.054- 16.096 .166 543.123 14.814 .551 .10425 1212 542.059 16.074 .165 543.136 14.818 .551 .10123 TORUS VOLUME (CU. FT.) = 127700.0 COEFFICIENT OF DISCHARGE = .600 MEAN OF THE MEASURED BYPASS AREAS = .120 MAXIMUM ALLOWABLE BYPASS AREA = .785 THE LOWER 95% CONFIDENCE LIMIT = .089 THE UPPER 95% CONFIDENCE LIMIT = .107 THE: CALCULATED BYPASS AREA = .098 O
x>
L-3
--J - ~ ,-A' -- ma .a - w
>ss.a-.-= _
u_,
4 APPENDIX M LOCAL LEAKAGE TEST SUMMARIES f
I l
l O
O SU-042 M-1
. . _ . . _ _ _ _ _ . . ... - _ __ __ _ ,-~
e APPENDIX PEACH BOTTOM UNIT 3 TYPE B TEST
SUMMARY
(./
P
} ' l' p.YS it;M u.t unscnIPTtgN l H r.? M d.;:, n Si*
' um g7 g ,.
DATi! Scc /,tt f ii SCC.' M ' t<
Dryw' ell Head 8-19-83 10 t 10 10 RPV Stabilizer Manways 2-18-83 i 50 10 A through H 50 N-1 Equipment AcceLs Hatch 8-19-83 35 10 35 N-2 Personnel Airlock '10-5-8) 906 50
{ 10-22-81 Offscale
, 10-23-81 495 1 50 2-10-82 462 1 50 4-9-82 461 i 50 Airlock O' ring 7-20-83 10 i 10 471 N-4 Head Access 3-1-83 10 1 10 10 N-6 CRD Hatch 9-25-81 20 t 10 10-20-81 20 i 10 4-4-82 10 t 10 8-20-83 20 10 20 al M-7A Main Steam Line Bellows *l-total for N-7A, 7E ,2-15-R3 215 i 50 1 7C, 7D, 9A, & 9B is 215 *1 reported under N-7A j 6
M-2
APPENDIX PEACH BOTTOM UNIT 3
-s TYPE B TEST
SUMMARY
l' u' ' l' aY.Y.i.N un og.sca1PT y,3 g g,g d . ,"
-1 NO. i 6nbf .. t a h s u .1: Pin T 15, i DATM SCC /,tt f n SCCN tr N-7B Main Steam Line Bellows '
2-15-83 *1
- 1 N-7C Main Steam Line Bellows 2-15-83 *1
- 1 N-7D Main Steam Line Bellows 2-15-83 *1
- 1 N-ll HPCI Steam Line Bellows *2-total for N-11,12, 2-26-83 85 10 13A, 14, 16A, & 17 85 is reported under N-ll
^-
ll .
N-12 RHR Suction Line Bellows ;-26-83 *2
- 2 M-3
APPENDIX PEACH BOTTOM UNIT 3 TYPE B TEST
SUMMARY
r V
4 2, r ST tt.: ud od5caleTivs ] g,ggge - ..h S i' a.m.a e y g-0.\T:s Sec/:.;;d
. SCC.' N t !*
N-13B RHR Injection Line Bellows *3-total for N-13B 2-26-83 150 t 10 and 16B is report- 150 ed under N-13B N-14 RWCU Su-tion Line Bellows 2-26-83 *2
- 2
.m N-16A Core Spray Bellows 2-26-83 *2
- 2
~
N-16B Core Spray Bellows 2-26-83 *3
- 3 N-17 Ilead Spray Bellows 2-26-83 *2
- 2 N-25 AO-3505, 3519, 3520 5-2-83 40 ! 10 0-rings 40 N-26 AO-3506, 3507 4-11-83 10 10 0-rings 10 N-35A-G Tip Penetration 3-21-83 20 t 10 0-rings 20 M-4
APPENDIX PEACH BOTTOM UNIT 3
,m TYPE B TEST
SUMMARY
)
P 's en wit.y us occa w riu.',
, 1 un ass, ---
.. .m ,, c , g , , . g,y . 7 IWi'i? SCC /:.I I H SCC.'M I N N-100A Electrical *4-total for N-100A, 1-24-83 20 ! 10 100C, 104A, 104B, 20 *4 104C, 104D, 105A, 105B, 106A, 106B, 107 & 220 is re-ported under N-100A N-100C Electrical 1-24-83 *4
- 4 1 -
- 5 N-100D Electrical *5-total for N-100D, 1-25-83 20 t 10
'00E, lOlC, 101D, 20 *5 101E, 103B, 104E, 104F, 104G, 104H, 105C, 105D, 106C 106D is reported under N-100D N-100E Electrical 1-25-83 *5
- 5
- O N-101A Electrical *6-total for N-101A. 1-24-83 20 i 10 101B, 101F, 231A, ,
- 6 g & 231B is report-ed under N-101A M-5
e APPENDIX PEACH BOTTOM UNIT 3 TYPE B TEST
SUMMARY
U I'id* ' s K).
SYSTDI Od OiiSCftiPT!ut, ] H r. '.M d 'ih i hb~ ,,i;,g g , w. t:
PdN'? ,
N-101B Electrical 1-24-83 *6
- 6 N-101C Electrical 1-25-83 *5
- 5 N-101D Electrical 1-25-83 *5
- 5 N-101E Electrical 1-25-83 *5
- 5 N-101F Electrical 1-24-83 *6
=
- 6 N-103B Electrical 1-25-83 *5
- 5 N-104A Electrical 1-24-83 *4
- 4 N-104B Electrical 1-24-83 *4
- 4 e
M-6
l l
APPENDIX PEACH BOTTOM UNIT 3 l
(
(
TYPE B TEST
SUMMARY
P hid ' T SYSTEM Od OdSCRIPTtu,N f g r. M. d Aa' '
NO. -
e hs ;- ,,g g ,g , ,; g g,7 )g ; .
DATE SQ1/;1[h SCC. Mis N-104C Electrical 1-24-83 *4
- 4 N-104D Electrical 1-24-03 *4
- 4 N-104E Electrical 1-25-83 *5
- 5 i - N-104F Electrical 1-25-83 *5 t
- *5 N-104G Electrical 1-25-83 *5
- 5 i
M-104H Electrical 1-25-83 *5
- 5 N-105A Electrical 1-24-83 *4
- 4 N-105B Electrical 1-24-83 *4
- 4 6
M-7
4 k APPENDIX I
PEACH BOTTOM UNIT 3 TYPE B TEST
SUMMARY
O l' t h ' t SYSTEM utt DEbCfllPTt0N 'I REMAM5 NO. '
TEST Lt,u,w ti PtN'T 10TA DATF SCC /:1IN SCC / MIN 1
i l
N-105C Electrical 1-25-83 *5
- 5 N-105D Electrical '
l-25-83 *5
- 5 N-106A Electrical 1-24-83 *4
- 4 j == N-106B Electrical 1-24-83 *4
- 4 N-lO6C Electrical 1-25-83 *5
- 5 N-106D Electrical 1-25-83 *5
- 5 N-lO7 Electrical 1-24-83 *4
- 4 N-150 Test Nozzle Double O-ring 2-22-83 20 i 10 l
20 9
M-8
1 APPENDIX l PEACH BOTTOM UNIT 3 p TYPE B TEST
SUMMARY
(_/ 1 P h* ' 1 SYSTEM ud DESCRIPTION l KEMAd45 -
NO. 'CSF LCAKabh PEN'T 10is DATE SCC / MIN
. SCC /N b N-200A Torus Manway NE 8-20-83 20 10 8-28-83 20 10 20 M-200B Torus Manway SW 9-21-81 20 ! 10 9-30-81 20 10 7-20-83 20 10 8-20-83 20 10 20
- 7 N-201A Torus Vent Bellows *7-total for N-201A 1-24-83 71 1 10
& 201B is report- 71 *7 ed under N-201A 4
N-201B ToruAVent Bellows 1-24-83 i *7
- 7 a
u N-201C Torus Vent Bellows '
- 8-total for N-201C & 1-24-83 20110 _
201D is reported 20 *8 inder N-201C N-201D Torus Vent Bellows 1-24-83 *8
- 8 _
6 M-9
e APPENDIX PEACH BOTTOM UNIT 3
.s TYPE B TEST
SUMMARY
(
PL:4 T SYSTEM ud DESCRIPTt0N 1 HEMARAS NO. TEST Lc,d,W ii DATE PEN'T TCil
. SCC / MIN SCC / MIN l N-201E Torus Vent Bellows *9-total ~for N-201E, u
1-24-83 111 10
& 201F is report- 111 *9 ed under N-2ClE l l N-201F Torus Vent Bellows 1-24-83 *9
- 9 M-201G Torus Vent Be?;ows *10-total for N-201G l-24-83 20 ! 10 4 20lH is re-20 *10 i
.m ported under N-20lG l
l j N-20lH Torus Vent Bellows 1-24-83 *10 t
- 10 M-205A AO-35023 Replaced with a wdwe 8-83 --
l that does not have --
O-rings.
N-205B AO-3502A & VAC BKR 26A 8-19-83 10 + 10 0-rings AO-3521A & 3521B 5-2-83 30 i 10 llh O-rings 40 M-10
1 APPENDIX PEACH BOTTOM UNIT 3 i
TYPE B TEST
SUMMARY
l'hti ' i SYSTEM ud DESCRIPTION ! R cMA rt.tS NO. TEST Lc,unu li PEN'T TOT-DATR SCC / MIN SCC /NIN N-206A,B Torus Level Instruments 2-24-83 35 1 10 35 M-213A Torus Construction Drain j 9-16-81 20 i 10 1-31-83 20 i 10 20 N-213B Torus Construction Drain 1-31-83 20 10 20 M-219 A0-3511 and 3512 0-rings 8-16-83 200 50 200 N-220 Electrical 1-24-83 *4
- 4 M-231A Electrical 1-24-83 *6
- 6 M-231B Electrical 1-24-83 *( --
- 6 9
s M-ll
APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
- ' nli t h(hTtn tat os s c a l e rg y,,
. ;) , I -] g g,g"., --
A lib i. I,ba hab i:
IMTH PdN'T TC S( (1/'_1 [ N SCC /MJ l
N-7A MSIV 80A and 86A 80A 1 2-14-83 l 522, 742
{
i 86A 2-14-83 2178 i 450 '
8SA 3-16-83 6279 1 450 86A 3-19-83 5615 i 450 80A 3-22-83 738 ! 50 80A 3-27-83 20 10
_ 86A 3-27-83 5072 i 450 86A 5-10-83 20 i 10 20 m
N-7B MSIV 80B and 86B 80B 2-14-83 3295 1 450 86B 2-14-83 6536 450 86B 3-10-83 1958 45C 86B 3-27-83 1974 1 450 _
3315 N-7C MISV 80C and 86C 80C 2-15-83 40,996 86C 2-15-83 669 50 86C 3-12-83 3685 1 450 80C 3-23-83 289 ! 50 80C 3-28-83 300 ! 50 3705 l I M-12
A f
APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
l i'im ' T 5(dihN OK OESCRIPTIv.N T.'q . [ K r..'u d a b '-
' li l
.1:a h nb l: Ppg
N-7D MSIV 80D and 86D 80D 2-14-83 )850,000 86D 2-14-83 2035 ! 450 86D 3-11-83 422 1 50 80D 3-19-83 > 850,000 80D 3-27-83 ) 850,000 80D 4-1-83 > 850,000 86D 4-5-83 591 i 50 80D 4-~16-83 607 1 50 607 N-8 Main Steam Line Drain MO-74 2-15-83 45,260 MO-77 7-12-83 450 ! 50 7-15-83 1511 450 8-20-83 229 ! 50 l __
229 N-9A Feedwater Chk 28A 2-23-83 1513 450 MO-2-38A, Feed Chk 96A, & 2-24-83 5860 1 450 Mo-23-19 4-21-83 4504 1 450 6-13-83 3203 1 450 3213 t
M-13
e APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
O_/
w Ph,., r T';, terSTEN Ud OESCHAPTauti [ gesg,<^^.
n hb. i' t,t,u,u d: P94
N-9B Feedwater Chk 28B 2-23-83 990 1 50 MO-2-38B, Feed Chk 56B, MO-68 only 4-4-82 60 i 10 FO-13-21, MO-12-68 2-24-83 39, 609 5-14-83 1111 450 6-15-83 3253 450 96B only 8-13-83 851 ! 50 4364 N-10 RCIC Steam Supply 3-10-83 20 1 10 20 N-ll HPCI Steam Supply 3-14-83 771 1 50 1
~
771 1
l l
N-12 Shutdown Cooling 4-6-83 1282 450 1282 N-13A LPCI Injection 4-23-81 20 i 10 3-16-83 671 1 50 3-17-83 400 t 50 671 M-14 v
e APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
l'LN'. S s h .~t.M Ud DEh C R I PT i u,N N'O .
l Mr.*M ddh 6C'SI L t:a h,u,1: Pen T 1g;f iMTR SCC /l1 Ti1 SCC /M t .'
tt-21 Service Air Inboard valve 8-20-83 35 10 Outboard Valve 8-20-83 360 1 50 370 N-22 Instrument N2 AO-3969A 3-3-83 55 i 10 Check Valve 3-3-83 10 1 10 55 N-23,24 RBCCW to/from Drywell MO-3373 5-4-83 > 10,000 j . MO-3374 5-4-83 1078 1 450 MO-3373 5-16-83 3657 450 MO-3374 5-16-83 253 ! 50 MO-3373 5-20-83 20 1 10 27?
)
/
N-25 Drywell / Torus Inerting 1-6-83 262 + 50 4-15-83 160 ! 10 One inch make-up 3-2-83 115 ! 10 275 N-26 Drywell Vent 9-25-81 30 ! 10 4-12-83 110 i 10 ,
M-16 '/
.. _ _ _ _ _ _ _ _ . _ _ l
e APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
U PhM i MSTEN Ud OdS C R I P T i o,N [ g.u g '- ."' -..
4C, S f xl0 . ..t,t h,u . fi P d p; - ( 10; DATi; SCC /.'.1 [ H SCC' MIN Drywell Cad Vent 3-7-83 160 + 10 8-18-83 310 50 PCAC Sample 1-31-83 70 10 CAD Ayalyzer Isolation 3-2-83 45 10 Valves 535 N-32C ILRT Test Valves 2-28-83 20 i 10 20 N-32D ILRT Test Valves 2-28-83 10 + 10 10 N-39A CAD Injection 2-4-83 '
20 ! 10 6-29-83 20 i 10 Containment Spray 3-16-83 531 1 50 561 N-39B CAD Injection 1-28-83 23 i 10 6-28-83 20 + 10 l Containment Spray 3-11-83 90 10 120 M-17
4 APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
O le t;;. t
.3YSstM ud Oc5CHIPTtUN f M r.M A rt .ib NO. I iliS T ..c a h a t , i: PdN'? 10i/
DATii SCC /:.i!iv $CC M N N-41 Recirc Sample 2-21-83 20 i 10 20 N-42 Standby Liquid Control 7-21-83 40 i 10 40 N-47 ADS Backup N2 Supply 5-19-82 15 i 10 3-2-83 10 ! 10 10 N-51A PCAC Sample 2-2-83 310 1 50 l
8-10-83 1211 i 450 8-17-83 400 50 8-18-83 410 1 50 8-28-83 20 i 10 20 1
1 N-51B PCAC Sample 2-2-83 180 1 10 _
6-6-83 65 ! 10 8-10-83 20 10 8-16-83 40 + 10 65 l
l P
l M-18
e APPENDIX PEACH BOTTOM UNIT 3 f'^, TYPE C TEST
SUMMARY
(>'
l*le ' i 6YS'7t.N UK OdS C R I PT t 0.N NO.
f g ggg g ^,^
..h5 i. .,b a h,w h DATi Pin
- 7 ]Q f S CC /.'.1 I N SCC /MtN N-51C PCAC Sample 2-3-83 20 10 6-6-83 20 1 10 CAD Analyzer Isolation i 1-31-83 260 50 Valves 280 N-51D PCAC Sample Return Chk Valve 1-25-83 305 50 SV - 3980 1-25-83 48 10 Chk Valve 4-27-83 770 50 Chk Valve 6-16-83 1101 + 450 Chk Valve 8-19-83 140 i 10 __
140 N-52F Instrument N2 AO-3969B 3-2-83 360 1 50
( Chk Valve 3-2-83 '
10 t 10 t -- _
AO-3969B 4-6-83 160 10 Chk Valve 4-6-83 10 t 10 1 160 N-53 Drywell Chilled Water MO-3201B 6-4-81 1348 450 5-4-63 1378 450 1378 P '
M-19 I-
4 APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
((. s at 't 2, ( S ',~ r..' t u d Od.%CRI F f t VN NC. I ttt;v.Ad AS ThST i,c,t h,ta n P P:' T 10 i LMTR SCC /;.1 IN SCC.'M I N N-54 Drywell Chilled Water MO-32008 6-4-81 > 10,000 8-13-81 20 10 5-4-8. 20 + 10 j 20 N-55 Drywell Chilled Water MO-3200A 6-4-81 590 1 50 5-4-83 20 i 10 20 M-So Drywell Chilled Water MO-3201A 6-4-81 1938 1 450 5-4-83 2082 1 450 2082 N-57 Main Steam Sample 2-19-83 20 10 20 N-102B ADS Backup N2 ADS 3-2-63 20 + 10 a yw0l1
$$$$f{j$d A Breathing Air 3-12-83 65 t 10 95 N-203 PCAC Sample 2-3-83 59 ! 10 6-3-83 90 t 10 8-9-83 40 10
~'
8-16-83 80 10 es
)
M-20
e APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
Phn'4 t,(biLM ud ud SC R I PT i u,.
,\!u . [ g ,, ya ,< ,;3
- kUI i,1; A N u ,4; P gj ' ? J Q_i DATi! SCC /:!!h SCC / Nit CAD Anaylzer 1-26-83 55 10 Isolation Valves 135 M-205A Torus Vacuum Breaker 8-18-83 611 1 50 8-25-83 631 ! 50 631 N-205B Torus Vacuum Breaker 8-19-83 390 1 50
)
390 l 1 P N-211A Torus Cooling 3-16-83 7647 450 4-20-83 473 1 50 34 B & 38B only 8-5-83 170 10 8-19-83 547 i 50 CAD Injection 1-26-83 10 i 10 6-27-83 10 t 10 557 f
N-211B Torus Cooling 2-28-83 7323 1 450 t
34A & 38A only 3-9-83 8627 1 450 l
3-10-83 8942 1 450 34A & 38A only 8-4-83 636 ! 50 M-21
a -
\
APPENDIX PEACH BOTTOM UNIT 3
-m TYPE C TEST
SUMMARY
- 'h!' ' 6' N (h ir.N Uit Od 5C R I PT t U:' l H r;
- Ir\ rt ^' a'
- w. . h S a' t,c ,s h,m si pgn.7 7g; DX7H SCC /:-:IIt SCC /MtN CAD Injection 1-31-83 5052 ! 450 2-2-83 5052 ! 450 Chk Valve Only 6-27-83 20 ! 10 971 N-212 RCIC Exhaust 2-19-83 > 10,000 3-15-83 5872 ! 450 4-25-83 3663 450 7-8-83 406 50 RCIC Exhaust Drain 2-19-83 36 ! 10 f i
Stop Check 0-ring 2-17-83 10 10 1
452 l l . .
N-214 HPCI Exhaust 2-16-83 1712 1 450
-q HPCI Exhaust Drain 2-16-83 > 10,000 4-23-83 y 10,000 5-23-83 501 _ + 50 l
Stop Check 0-ring 2-17-83 701 ! 50 2914 l
llh l
M-22 '
e APPENDIX PEACH BOTTOM UNIT 3 TYPE C iEST
SUMMARY
l' Lii' ' ' liYSTEM Uit OdhCitlPTiuN
\!C l g g, gg ,<"' ' -
' h 's. 4.
l 1 L,thM.1: Pdn
- 7 ]Q; i ' DATH Sec/llIN SCC /M i i, N-217B RCIC Exhaust Vacuum Relief 1-26-83 121 1 10 HPCI Exhaust Vacuum Relief 1-27-83 1220 1 450 6-16-83 20 t 10 8-3-83 65 i 10 186 N-218A Torus Instrument N2 ,
3-22-83 340 ! 50 340 N-218B PCAC Sample 2-3-83 20 i 10 6-3-83 20 10 20 N-218C ILRT Test Valves 2-28-83 t 95 1 10 4-29-83 10 1 10 10 N-219 Torus Vent 9-21-81 170 1 10 8-16-83 230 i 50 Torus CAD Vent 3-17-83 290 1 50 8-16-83 260
- 50 ,
f M-23
APPENDIX PEACH BOTTOM UNIT 3 TYPE C TEST
SUMMARY
v Pht ' a M b Ti::: Ud OE5CHIFTsuN f F r.
- a d ~ N T,'O 'hS4- 1.t:. t h ale s: PdN*T TQ[A DATH SCC /l1Th SCC.'N I N PCAC Sample 2-4-83 45 10 8-20-83 65 ! 10 Cad Analyzer Isolation 1-26-83 45 f 10 Valves 600 N-221 RCIC Vacuum Pump 2-17-83 343 57 Discharge 2-21-83 21 i 10 21
^
I
" N-223 HPCI Exhaust Drain 2-16-83 20 1 10 20 N-225 RCIC Pump Suction 2-21-83 59 ! 10 Torus Water Cleanup 1-31-83 90 10 149 N-227 HPCI Suction 2-21-83 925 ! 50 925 N-234B Post Accident Sampling 4-29-83 20 1 10 Return 20 M-24 "g
e APPENDIX FEACH BOTTOM UNIT 3 p) l
\s TYPE C TEST
SUMMARY
- ' t 'T tu.YJL:l ud U2aCHI FT i v . I ut sag,;3 ;u;;-
g ,, gg,7 g; IMTE SCC /i.t r H SCC /M i r.
a N-9A HPCI Pump Discharge 2-22-83 223 50 5-7-83 100 i 10 N-9B RCIC Pump Discharge 3-16-83 20 i 10 Scram Discharge Volume CV-32A 4-16-83 30 1 10 Vents and Drains CV-35A 4-16-83 10 i 10 CV-32B 4-16-83 230 t 40
.m CV-35B 4-16-83 4004 i 450 CV-35B 5-17-83 711 1 50 CV-35B 5-24-83 150 i 10 CV-33 3-19-83 2104 i 450 CV-36 3-19-83 2419 i 450.
CV-33 5-16-83 '
20 ! 10 CV-36 5-16-83 > 10,000 CV-36 5-26-83 583 1 50 798 N-35F Tip Purge 6-23-83 20 i 10 20 t
O ---
I M-25 ,i.
e APPENDIX PEACH BOTTOM UNIT 3 fm TYPE C TEST
SUMMARY
id ' 4 Py'U. te rSTf:t-1 Urt OsbCHiF i't uN ] g g ;, g ,; ..,
N
- R ,,> I t,lm h at . l: Ptyt
- r ]Q_;
L_ NOTE: All leak rates are reportec using the format specified in Ansi /Ans 56.8 - 1981, which requi2es that a leakage rate deviation be specifi 3d .
Total leakage: 38,210 i 1515 sec/ min M-26 , %
/
, . _ - ~ . ... .. , _ - . _ _ - - ._ . ~ ..- - ,
i N. APPENDIX N '
DESCRIPTION OF BECL8TEL ILRT COMPUTER PROGRAM !
l A. PROGRAM AND REPORT DESCRIPTION l
- 1. The Bechtel ILRT computer program is used to determine the inte-grated leakage rate of a nuclear primary containment structure. 1 The program is used to compute leakage rate based on input values of time, free air volume, containment atmosphere total pressure, drybulb temperature, and dewpoint temperature .(water vapor pressure). Leakage rate is computed using the Absolute Method as defined in ANSI /ANS 56.8-1981, " Containment System Leakage Testing Requirements" and BN-TOP-1, Rev 1, " Testing D Criteria for Integrated Leakage Rate Testing of Primary Containment Structures for Nuclear Power . Plants." The program l- is designed to allow the user to evaluate containment leakage rate test results at the jobsite during containment leakage testing. Current leakage rate values may be obtained at any
' time during the testing period using one of two computational methods, yielding three different report printouts. l
- 2. The first printout is the Mass Point Report and is based on ,
the Mass Point Analysis Technique described in ANSI /ANS 56.8-1981, ' " Containment System Leakage Testing Requirements."
The mass of dry. air in the containment is computed at each data point (time) using the Equation of State, from current values of containment atmosphere drybulb temperature and partial-pressure of dry air. Contained mass is " plotted" versus time F
and -regression line is fit to the data using the method of
' least squares. Leakage rate is determined from the statistically derived. slope and intercept of the regression line.
3.
' The second printout, the Trend Report, is a summary of leakage rate values based on Total Time and Mass Point computations presented i
as a function of number of data points and elapsed time (test i'
i duration). The Trend Report provides all leakage rate values
' required for comparision to the acceptance criteria of BN-TOP-1 for conduct of a short duration test.
- 4. ' The program is written in a high level language and is designed '
for use. on a micro-computer. Brief descriptions of program use, formulae used for leakage rate computations, and program logic are provided in the following paragraphs.
4 "OL SU-042 N-1
- . 2 _. - . . . . . . . . . . , - - - _ , . _ . . - - . . . - _ . - _ . - . . .. .- ..,, .,_ - - - -
i 1
B. EXPLANATION OF PROGRAM
- [')
- 1. The Bechtel ILRT computer program is written, for use by experi-enced ILRT personnel, to determine containment integrated leakage ,
rates based on the Absolute Method described in ANSI /ANS 56.8-
'1981 and BN-TOP-1.
- 2. Information loaded into the program prior to or at the start of the test:
- a. Number of containment atmosphere drybulb temperature sensors, dewpoint temperature (water vapor pressure) sensors and ,
pressure gages to be used in leakage rate compotations for the specific test
- b. Volume fractions assigned to each of the above sensors
- c. Calibration data for above sensor, if required
- d. Calibration data for' pressure sensor
- e. Test title
- f. Test pressure
- g. Maximum allowable leakage rate at test pressure.
[J"'g
- 3. Data received from the data ' acquisition system during the test, .
and used to compute leakage rates: r
- a. Tine and date i
- b. Containment atmosphere drybulb temperatures
- c. -Containment atmosphere pressure (s)
- d. ' Containment atmosphere dewpoint temperatures
- e. . Containment free air volume.
- 4. Af ter all data at a given time are received, a Summary of Measured Data report (refer to " Program Logic," Paragraph D,
" Data" option command) is printed.
- 5. If drybulb and dewpoint temperature _ sensors should fail during the test, .the data from the sensor (s) are not used. The volume fractions for the remaining sensors are recomputed and reloaded
.into the program for use in ensuing leakage rate computations.
?
, (_-
- SU-042- N-2 4
-.n, _,,..-.,,e. - . , - - y-,mw - p,,,.e-,p., v.e- y . w e v en my .m 3 - .y ., ,..,,.-,,y,y, , p y, -
C. LEAKAGE RATE FORMULAE
- 1. Computation using the Total Time Method
- a. Measure leakage rate from data:
P1i V = W 1RTt (1)
PVi i = WiRTi (2) 2400 (W1-W) i Li =
(3) at Wt1 Solving for W1 and Wi and substituting equations (1) and (2) into (3) yields:
~
2400 l- TPV1ii Li = 1- (4) ati TiPgV1 Where:
p W,Wi 1 = Weight of contained mass of dry air at times t1 and
.d ti respectively, ibm.
14, Ti = Containment atmosphere drybulb temperature at times ti and ti respecitve , "R.
P,Pi 1 = Partial pressure of the dry air compon,.nt of the containment atmosphere at times ti and ti respectively, psia.
V,V 1 i = Containment tively, (constant free air volume atduring or variable times' the ti and ti res test), f tpc-ti, c1 = Time at 1st and ith data points respectively, hours.
ti = Elapsed time from ti to t i, hours.
R = Specific gas constant for air = 53.35 f t. lbf/lbm.*R
, Li = Measured leakage rate computed during time interval tt to i ,t wt.%/ day.
To reduce truncation error, the computer program uses the following equivalent formulation:
-2400 aW1 att W1 SU-042 N-3
where:
=
AWi Wi-W1 W1 W1 AP AV AV i t+ g+APpV i P1 V1 PV1i T1 A Tj 1+
Ti api =Pi-P1 AVi=Vi-VI ATi=Ti-T1
- b. Calculated leakage rate from regression analysis:
L=a+batN (5)
Where:
L = Calculated leeakage rate, wt.%/ day, as detennined f rom O the regression line.
a = (E Li - bm ti)/N (6)
N(E Lpi t ) - (E L t )(B ti )
2 N(B t1 ) - (Ei t t)2 N = Number of data points N
=E i=1
- c. Calculated leakage rate at the 95% confidence level.
595 = a + la tN+S - (8)
L Where:
h5 = Calculated leakage rate at the 95% confidence level, wt%/ day, at elapsed time a t N-O SU-042 N-4
\,
, .i For a tN 24 S_ = t0.025;N-2 IL i - AILf - BELg at t )/(N-2)] N x L
11 + 1 + (A Nt -67)2/ (Zatf 2 - (M t y)2/N]1/2 (93)
,N where:
t0 I .0253N-2 = 1.95996 + 2.37224 + 2.82250 N-2( (N-2)4 For AtN 124 S_ = t0.025;-2 IL i - aI Lt - b IL A g t g)/(N-2)]1/2 x L
[1, + (6 Nt 47) /(TAtg2 - (Itg)2/N]l/2 (9b)
N where:
- 1. 6449 ( N-2 )2+3. 5283 ( N-2 )+0. 85602 (N-2)2 + 1.2209(N-2) - 1.5162 Li = Calculated leakage rate computed using equation (5) at total elapsed time att, %/ day O
Iati t" --
- 2. Computation using the Mass Point Method
- a. Contained mas of dry air from data: '
W1 = 144 (10)
RT1 where:
All symbols are previously defined.
O '
SU-042 N-5 s
k a - - - -
e e
6 g
- b. Calcu ated leakage rate from regression analysis, s
j W = a 4-bat!
L = -2400 6 a
Where:
L = Calculated leakage rate, wt.%/ day, as determined from the regression line a = ( I61 -bIi ti)/N (12) t N(Bi ati) - ( Bi )(E ti)
N(Btg2 ) - (Ety)2 ati = Total elapsed time at time of ith data point, hours N = Number of data ponts W1 = Contained mass of dry air at ith data point, Ibm, as computed from equation (10).
N E=I i=1 Inorder to reduce truncation error, the computer program uses the following equivalent formulation:
AWi b a- W 1+(t - mt i)/N 1
W1 W1 N (I AWi AWi )
atf) - I mt g Wi Wi b= W 2
N( mtf ) - ( I&tt)2 W
Ai (q/ where, W1 is as previously defined.
SU-042 N-6
- c. Calculated leakage rate at the 95% confidence level.
-2400 195 = (b - Sb) (14) a Where:
L95 = calculated leakage rate at the 95% confidence level,
! wt%/ day.
SN1 /2 8b"t0.025;N-2
[Nmtg 2 - ( m tt )2jl/2
- 1. 6449 ( N-2 ) 2+3 . 5283 ( N-2 ) 2+0 . 85602
- ** 0.025;N-2 "
(N-2)2 + 1.2209 (N-2) - 1.5162
-E[Wg - (a + bati )] D @
N-2 s=W 1 t(aW1 /W 1 ) - I E(6Wi /W 1 )] /N -
1 N-2
[ E(AW i /W t )att - E(AW 1 /W g )(mti )/N]2 I/2 Z
E(at1)-(mt)Z/N- t _
O SU-042- N-7
D. PROGRAM LOGIC s_/ 1. The Bechtel ILRT computer program logic flow is control'1ed by a set of user cptions. The user options and a brief description of their associated function are presented below.
OPTION COMMAND FUNCTION Af ter starting the program erecution, the user either enters the name of the file containing previously i
entered data or initializs a new data file.
l DATA Enables user to enter raw data. When the system requests values of time, volume, temperature, pressure and vapor pressure, the user enters the i
appropriate data. Af ter completing the data entry, a summary is printed out. The user then verifies I
that the data were entered correctly. If errors are detected, the user will then be given the opportunity to correct the errors. After the user verifies that the data were entered correctly, a Corrected Data Summary Report of time, data, average temperature, partial pressure of dry air, and water vapor pressure is printed.
-~
TREND A Trend Report is printed.
V TOTAL A Total Time Report is printed.
MASS A Mass Point Report is printed.
TERM Enables user to sign-off temporarily or permanently.
All data is saved on a file for restarting.
CORR Enables user to correct previously entered data. '
LIST A Summary Data Report is printed.
PLOT Enables user to plot summary data, individual sensor data or air mass versus time.
DELETE Enables user to delete a data point.
INSERT Enables user to reinstate a previously deleted data point.
VOLFRA Enables user to change volura fract ions.
TINE Enables the user to specify the time interval for a report or plot.
VERF
-( ) Enables the user to input imposed leakage rate and calculated 1LRT leakage rates at start of verification test.
SU-042 N-8 1
_ _ _ - - _ _ _ - _ _ _