ML19316A227
| ML19316A227 | |
| Person / Time | |
|---|---|
| Site: | Oconee  |
| Issue date: | 07/14/1970 |
| From: | Koehler R, Stafford P, Wilson R DUKE POWER CO. |
| To: | |
| References | |
| JOB-6210, NUDOCS 7912030343 | |
| Download: ML19316A227 (175) | |
Text
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, 4 INTEGRATED LEAK RATE TEST OF THE REACTOR CONTAINMENT BUILDING
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OCONEE NUCLEAR STATION DUKE POWER COMPANY
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PERFORMED BY DUKE POWER COMPANY WITH TECHNICAL ASSISTANCE BY BECHTEL CORPORATION i JOB 6210 Prepared by: [ Patrick M. St # ord
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- Approvei by: \N '
Robert M. Koehler Tech. Support Engr. (-< Lt 2 '
' Richard L. Wilson
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Performance Engr. <
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- i TABLE OF CONTENTS Section Page 1 FINAL REPORT
SUMMARY
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1.2 INTRODUCTION
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- 1. 3 CONCLUSIONS . . . . .... . .. . .. . . . . . ... . . . 1-2 -
2 REACTOR BUILDING ILRT PROCEDURE AND MEASUREMENT SYSTEM . . . . 2-1 2.1 TP 1 A 150 3.4 REACTOR BUILDING INTEGRATED LEAK RATE TEST. 2 2.2 INITIAL TEST CRITERIA . .. . . .. .. . . . . . . . . . . 2-2 2.3 MEASUREMENT SYSTEM ... .. ... . . . . . . . . . . . . 2-2 2.4 INSTRUMENTATION ERROR ANALYSIS . . . . . . . . . . . . . . 2-6 2.5 PRESSURIZATION SYSTEM . . . . . . . . . . . . . . . . . . . 2-8 2.6 AIR RECIRCULATION SYSTEM . . .. . .. . . . . . . . . . . . 2-10 2.7 STRUCIURAL INTEGRITY AND iLRT ORGANIZATION . . . . . . . . 2-10 2.8 STRUCTURAL INTEGRITY ANL INTEGRATED LEAK RATE TESTS PRESSURE CYCLE . . . . . . . . . . . . ... .. .. . . . . . .. . . 2-10 3 COMPUIER PROGRAM , , , ..,. . ,., . .. . . .. . . . . . 3_3 3.1 INTR 3 DUCTION. . . . . ... . . . . .. . . , . . . . . . . 3-1 3.2 EXPLANATION OF PROGRAM. . . . . . . . . . . . . . . .. . . 3-2 3.3 DEMONSTRATION OF PROGRAM , . . .. .. . . . . . . .. . . 3-5 4 FINAL TEST REPORTS,
SUMMARY
DATA AND CURVES. . . . . . . . . . 41 4.1 29.5 PSIG ILRT. . . . .. . . . . . . .. . . . . . . . . . 4-1 4.2 29.5 PSIG VERIFICATION TEST . . . . . . .. . . . . . . . . . 4-1 4.3 59 PSIG ILRT . . . . .. .. .. . . . .. . . . . . . . . . 4-1 4.4 59 PSIG VERIFICATION TEST , . . . . . . . . . . . . . . . . 4_1 5 IDCAL LFAK TESTS . . . . .. . . . .. . . . . . . . . .. . . 5-1 5.1 LOCAL LEAK TEST
SUMMARY
. . . . .. . . .. . . . . . . . . . 5-1 5.2 PERSONNEL AND EMERGENCY LOCK LEAK RATE TEST PROCEDURE . . . 5-5 5.3 RB ISOLATION HYDROSTATIC TEST PROCEDURE . . . . . . . . . . 5-12 5.4 RB ISOLATION PNEUMATIC LEAK TEST PROCEDURE. . . . . .. . . 5-13 5.5 ELECTRICAL PENETRATION LLAK TEST PROCEDURE. . . . . . . . . 5-14 i
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Section < Page 1 FINAL REP 0lti
SUMMARY
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1.1 SYNOPSIS 1-1
1.2 INTRODUCTION
1-1 1.3 -CONCLUSIONS 1-2
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1 FINAL REPORT
SUMMARY
1.1 SYNOPSIS The initial Integrated Leak Rate Test (ILRT) of the Reactor Building was completed with satisfactory results on August 2, 1971. Interpretation and final analysis of test data show results well within the specified . limits for this building,which has a maximum allowable leak rate (La) of 0.25 weignt percent per day of building atmosphu re at design pressure of 59 psig. The leakage rates for the Oconee 1 containment structure were found to be I +0.0147%*at 29.5 psig and +0.0475%* at 59 psig. l 1, The initial integrated leak rate test was completed within a time period of 5 days, which included building pressurization, depressurization and conducting the structural integrity test at a pressure of 67.8 psig. Prior to conducting the ILRT, a series of local leak tests were performed to verify reactor building integrity. Local leak tests were performed on piping system isolation valves which became part of the building boundary under MHA I conditions, electrical penetrations, the personnel locks, the equipment hatch, l 1, and the fuel transfer tubes. The Integrated Leak Rate Test was performed by Duke Power Company with the technical assistance of Bechtel Corporation. 1.2 'NTRODUCTION
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The successful Reactor Building Integrated Leak Rate Test (ILRT) was performed in accordance with Test Procedure TP 1A 150 3.4 approved for use July 28, 1971. This test procedure is based on specifications provided by Bechtel Corporation. The 'following, deviations to the procedure were made during the test; this does not include minor valve lineup changes which did not affect the integrity of the reactor building boundary:
- 1. The test was performed using the " Absolute Pressure 3kthod" only due to failure of instrumentation required to perform the " Reference Vessel Method" prior to initiating the Integrated Leak Rate Test. (Differential Pressures shown on computer printout of test results are invalid).
- 2. ILRT Test durations were reduced to a time period of ten (10) hours which provided sufficient data to calculate the twenty four (24) hour leak rate.
- 3. Reactor Building auxiliary and cooling unit fans were run during the reduced p ress ure (29.5 psig) test in order to aleviate potential condensation.
Reactor Building auxiliary fans only were run during the peak pressure (59 psig) test. s The allowable integrated leakage rate is as follows: 1. Conditicas W ight % Per Day of Tern Containment Atmosphere Maximum Allowable Integrated Leakag La 0.25 Rate at Test Conditions 39 psig
- Includes leakage rate measured from 2 penetraticns tested after the Integrated y, Leak Rate Test 7-
^1 a Rev. I pril 21,1972
. .. (Refer to .0conee Technical Specification 4.4.1) The instrumentation provided for the ILRT, consisted of one (1) precision pressure sensor, twenty four (24) building temperature sensors, and two (2) vapor pressure sensors which measure building atmospheric conditions during the performance of the ILRT. One of the vapor pressure sensors became unusable during the 59 psig test due to failure of a sample pump providing flow thru the dewpoint sensor. The effect of the loss of this sensor presented no appreciable change or variations on the test due to the fact that before failure both sensors had consistently given identical results which were representative of moisture conditions in the reactor building. The leakage rate data was recorded at fifteen (15) minute intervals for a period of 10 hours for both the 29.5 psig and 59 psig ILRT's. Reactor building atmospheric conditions were allowed to stabilize prior to commencing each 1G hour ILRI. Following each 10 hour ILRT, an instrument verification was conducted by imposing a controlled leak through a calibrated flow meter for a period of 5 hours. The controlled leak was established by setting the air leaking through the flow meter at a known, predetermined value. System accuracy and leakage rate results were validated by these tests. The method used,to calculate the reactor building integrated leak rate based on the recorded data is in accordance with proposed standard ANS 7.60. All calculations, summaries and reports showing calculated test results were performed by the Bechtel computer located in San Francisco with input data from a remote terminal located at Oconee.
1.3 CONCLUSION
S As shown in the computer printouts and graphs in Section 4 of this report, the calculated leak rates for both the reduced pressure test (29.5 psig) and the peak pressure test (59 psig) are well within the allowable leakage rate, and verify that the reactor building is extremely tight with an in-tegrated leak rate approximating zero. For purposes of establishing a base for future tests, the measured leak rate for this initial-test is +0.0147* weight % per day of building atmosphere
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for the reduced test pressure (29.5) and +0.0475 weight % per day of building 1. atmosphere for the peak test pressure (59 psig) . These calculated leak rates were -obtained by using a linear least -squares fit of the fifteen (15)' minute leak rate data over a period of 10 hours. These calculations are based on the total time methos . The ratio of Lem as defined in Technical Specification 4.4.1 is .309 and is 1, Lpm within an acceptable range. The allcwable leak rate ~ for -future tests is l . calculated to be .0773 weight % per day of building atmosphere for reduced l 1, pressure tests (29.5 psig).
- Includes leakage rate measured.frem 2 penetrations tested'after the Integrated
- Leak Fate Test-l-2 Rev. 1 April.21, 1972
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The verification test imposing a known leak at the end of the ILRT for each pressure level both prove out test result.) and verify the instrumentation used. Illustrating this on the Integrated Leak Rate Test, the following reasoning can be applied. Tha imposed leakage at 29.5 psig, 0.125 weight % of atmospheric air in the reactor building amounts to 5.025 standard cubic feet per minute. For the 59 psig verification test, an imposed leakage of 0.134% or 8.325 was established for a period of approximately 5 hours. This was Lccomplished using a precision flow meter throughout this period. Comparis on of the imposed known leakage and the calculated leakage for each test is as follows: Reduced Test 0.147'% Calculated Pressure (29.5 psig) +0.125 % Imposed 0.1397% - Total 0.157 % Calculated During Verification Test
! Peak Test 0.475 % Calculated l 1.
Pressure (59 psig) +0.134 % Imposed l 0.1815 % Total l1. 0.186 % Calculatea During Verification Test Comparison of the above showing a very small difference between the total of the caluclated and imposed and that calculated during the verification test is attributed to the fact that the sensitivity of the leak rate measuring system is greater than the sensitivity of the flowmeter. The close correl-ation between the leak rates provides sufficient information to validate the Integrated Leak Rate Test results. The data and results of these tests correlate closely with results of four (4) previous tests on prestressed concrete Reactor Building structures (Palisades, Point Beach 1 & 2 and Turkey Point) . Therefore, we are confident that the results obtained during the ten (10) hour test durations are valid and the leak rates at both test pressures approximate zero. 6 .
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h 1-3 Rev. 1 April 21, 1972
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TABLE OF CONTENTS Section Pm 2 REACTOR BUILDING ILRT PROCEDURE AND MEASUREMENT SYSTEM 2-1 2.1 TP 1 A 150 3.4 REACTOR BUILDING INTEGRATED LEAK RATE TEST 2-1 2.2 INITIAL T GT CRITERIA 2-2 l l i , 2.3 MEASUREMENT SYSTEM 2-2 l
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2.4 INSTRUMENT ERROR ANALYSIS 2-6 2.5 PRESSURIZATION SYSTEM 2-8 2.6 AIR RECIRCULATION SYSTEM 2-10 l , ! 2.7 STRUCTURAL INTEGRITY & ILRT ORGANIZATION 2-10 2.8 STRUCTURAL INTEGRITY AND INTEGRATED LEAK RATE TESTS PRESSURE 2-10 i CYCLE i s A
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. , 2-1 Instrumentation Characteristics 2-3 1 2-2 RID Locations- and Associated Volume Fractions 4
'2-3 Pressurization System Equipment 2-9 , !
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LIST OF FIGURES , Figure No. Title 2-1 Precision Pressure Gage Calibration Chart 2-2 Calibration Report for RTD/ Digital Temperature System 2-3 RTD Locations El. 787' 2-4 RID Locations El. 830' 4 2-5 RID Locations El. 850' 2-6 RID Locations El. 866' 2-7 RTD Locations El. 923' - El. 970' 2-8 Dew Point Hygrometer 332 Certificate of Traceability 2-9 Dew Point Hygrometer 333 Certificate of Traceability 2-10 Dew Point Hygrometer 332 Thermometer Calibration Data 2-11 Dew Point Hygrometer 333 Thermometer Calibration Data 2-12 Keactor Building Air Recitculation System 2-13 Leak Rate Test Panel i 2-14 Leak Rate Measurement System 2-15 Reactor Building Pressurization System 2-16 Structural and Integrated Leak Rate 2-17 Test Organization Structural and Integrated Leak Rate Tests Pressure Cycle
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1-2 REACTOR '3UILDING ILRT PROCEDURE AND MEASUREMENT SYSTEM 2.1 TP 1 A 150 3.4 REACIOR BUILDING INTEGRATED LEAK RATE TEST
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Following is a copy of the test procedure used for the conduct of the test. Data sheets are not enclosed as they would add significantly to the bulk of the material in this report. They may be seen at Oconee Nuclear Station.
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TEST PROCEDURE RLCORD OF APPROVAL, CllANCES AND IFST PERFORMANCE TE"T PROCEDI;RF ?. UMBER TP 1 A 150 3.4 m.,. . . . - , . . TEST P'wCEURE TITLE Reactor Bldg. Integrated _ ..
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- s CONTROL COPY FINAL OCONEE NUCLFAR STATION TP 1 A 150 3.4 REACTOR BUILDING IhTEGRATED LEAK RATE TEST 1.0 Purpose 1.1 To measure reactor building leakage rate at design peak pressure (59 psig) and at design peak pressure (29.5 psig) .
1.2 To compare the measured leakage rate to the allowable leakage rate as given in Oconee FSAR, Section 15.4.3, (Ref. 2.1). 1.3 L 11tiate a performance history for future integrated leak rate tests.
- 1,4 To compare the results of the full-pressure and half-pressure integrated leak rate tests.
2.0 References 2.1 Oconee FSAR, Section 5.6.1.2; 5.6.1.3; 15.4.3. 2.2 DPC Dwg. 0-472. 2.3 PO-101-B, Diagrammatic Layout of HP Injection System. 2.4 PO-102-A, Diagrammatic Layout of LP Injection and Core Flooding System. 2.5 PO-103-A, Diagrammatic Layout of RB Spray System. 2.6 P0-107-A, Diagrammatic Layout of Coolant Storage System,
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(Quench Tank Portion) . 2.7 PO-107-B, Diagrammatic Layout of Liquid Waste Disposal System, (Miscellaneous Waste Portion). 2.8 P0-107-D, Diagrammatic Layout of Auxiliary Building High Activity Sump Drains System. 2.9 PO-110-A, Diagrammatic Layout of Chenicci Addition and Sampling System. 2.10 PO-116-A, Diagrcmmatic _ Layout of Reactor Building Purge and Penetration Room Ventilation System. 2.11 PO-144-A, Diagratuatic Layout of Component Cooling System. 2.12 0-422n-8 through 0-422R-13, Inctrument Details. 2.13 React or nullding Struct ural Integrity Tent TP 1 A 150 2.4. -- 150/3 4 Rev. 4 July 27, 1971 i
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3.0 Tine Required 3.1 Seven Days
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4.0 Prerequisite Tcsts 4.1 TP/1/B/150/1, RB Leak Detection Instrumentation Preoperational Calibration. 4.2 TP/1/A/150/4, Equipment Hatch Leak Test. 4.3 TP/1/A/150/5, RB Electrical Penetration Leak Test. i 4.4 TP/1/A/150/6, RB Isolation Pneumatic Leak Test. 4.5 TP/1/A/150/7, RB Isolation Hydro Leak Test. 4.6 TP/1/A/150/8, Personnel and Emergency Lock Leak Test. 4.7 TP/1/A/150/9, Reference Vessel Leak Test. - 5.0 Test Equipment 5.1 Air Compressors (2 compressors 2300 cfm each). 5.2 After Ccoler (4600 cfm) . 5.3 Air Dryer (4'600 c fm) . " 5.4 Reference Vessel System. , 5.5 Flowmeter. 5.6 Hygrometer System. 5.7 Barometer. , 5.8 Micromanometer. . 5.9 Pressure Gauges (2). 5.10 RTD's (28). 5.11 Precision Pressure Gauge (optional for absolute pressure measure- .
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5.12 Electric Heaters (for depressurization). 5.13 Microwave tower weather instruments (for information only and not required for conduct of this test). For-Details, Sec TP/1/B/150/1. 6.0 Limitations and Precautions 6.1 The activities in this procedure shall be coordinated with the (2)
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' 7-27-71 structural test and.related programs. It will be necessary to
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provide hold periods at the pressure levels requirec' to conduct the structural integrity test and surveillance programs in addition to hold periods for the leak rate measurements. 6.2 Personnel access restrictions are given in Enclosure 13.1. 6.3 Reactor building air temperature.should be kept above 60 F and above the dev point. 6.4 Personnel designated to work inside the reactor building while it is under pressure shall be medically certified for work in pressurized air.' The maximum allowable pressure for work inside the reactor building is 14 psig. , V 6.5 !!B vent unit fans and RB auxiliary fans should be operated only at half-speed. 6.6 Prevent helium gas from contacting the Texas Instrument pressure sensor. Helium can penetrate the sensor crystal and cause it to beco.ae inoperative. M S 6.7 Remove all fire extinguishers, bottled gas, and flammable liquids from RB prior to pressurization. MIS 6.8 Remove all lights from inside the Fuel Transfer Canal and from the polar crane prior to pressurization. . [ b 6.9 Turn off unnecessary cicctrical power to the RB.
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' 7.0 Required Plant Status b/lkf 7.1 Core Flooding Tanks are empty and vented to the RB atmosphere.
@)lk7.2 The Qucnch Tank is empty and vented to the RJ atmosphere.
G A 7.3 The Hp and LP Injection Systems isolation valves'are closed. ,
@Mk7.4 The Conponent Cooling System isolation valves are closed.
6 N 7.5 The LPSU System is operating to provide cooling uatcr for the RB vent unit coolers, temporary air compressors, and temporary aftercoolers. . Nk7.6 RB Spray System isolation valves are closed. . Obk7.7 Gascous Radioactivity lionitoring System and RB Purge System isolation valves are closed. b/ 7.8 Fuct Traner er Tubes are -f n -isolation state. Gr}( 7.91 nn Sump isolation valves are clotcd and 18" dinneter emergency cump lines are capped. . " (3)
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7-27-71 7.10 m ~ n d r h. r/1/A/1;;/ ouvuiu um in , er lir: " * -i r i _ n'_._.,. 7.11 Vent instrument transducers to and closed structural syste:.s to RB atmos. 2 857.12 Remove area radiation monitors RIA-2, RIA-3, and RIA-5 from the RB. N b 7.13 Remove portable TV Equipment from RB. , h [7.14 Steam Generator secondary handholes and instrument connections visually inspected for seal tightness. 7.15 RV vented to RB atmosphere 8.0 Prerequisite System Conditions 8.1 The RB is structurally complete. Penetrations are sealed and
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the leak rate from each testable penetration has been deter-mined. 8.2 All Integrated Leak. Rate Test Equipment located inside the RB is installed and cal'ibrated prior to the start of this test. Test panel located in Room 507.
/// 8 8.3 RB Vent unit fans are able to recirculate air within tha RB at h speed and the vant unit coolers are available for temperature reduction.
.4 RB heating coils are installed and available for heat input ,
to RB.
/ 8.5 RB auxiliary fans are operable and available to recirculate air in the upper region of the RB.
b 8.6 Blind flanges on leak rate test pressurination line and compressed air supply line are removed. 8.7 Reference vessel system Icak tested and prescurized to 35 psig with dry' air. 8.8 Temporary air compressors installed and LPSU cooling water con-nected to compressors and aftercoolers. Operation of compressors checked. . 8.9 The precsurication system and Icak rate r.ieasurement. system should , l be inctalled as shown on Dwgs. 0-4 22 R-fi /00422R- 13.
.10 A temperature survey of the RB should be trade establishing any localized areas uhcre temperature gradient s may dif fer from the
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RB average. This should be done both wi;h the ventilation system operating, and af ter the ventilation system has been
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shutdown. RID's should be located on the basis of this survey. 8.11 Individual penetrations have been tested and the Leak Rate , through all has been determined. . 9.0 Test Method -
- The RB leakage rate will first be determined at 29.5 psig. During the pressure increase, at about 10 psig, a short informal leak test will be performed and the building will be entered for leakage detection. This is done so that any large-scale leakage can be detected and repaired prior to increasing pressure. A known leak .
, will be imposed on the building at 29.5 psig to check the ability to accurately measure leakage. Both the " reference-vessel method" and the " absolute pressure method" will be used. The " absolute-pressure method" is preferred in the case of different results. After the leakage rate has been determined at 29.5 psig, the pressure will be increased in the RB to 67.8 psig (115% of design pressure) and the structural test run. After the structural test has been completed, reduce the RB pressure to 59 psig for the second part of
' the leak rate test. This will be performed like the reduced pressure , test, and'a known leak rate will be introduced to check the ability to accurately measure leakage.
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I 10.0 Data Required 10.1 RB air humidity 10.2 RB air temperature
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10.3 Dif ferential pressure between the reference vessel and the RB. (Temperature corrected) . 10.4 Barometer reading (temperature c'orrected) . 10.5 Flot: meter reading during "known leak". . 10.6 RB absolute pressure (^ 7 < '" - 10.7 RB liner temperature.
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10.8 Outside air temperature (DB). * (5)
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11.0 Acceptance Criteria 11.1 For the integrated leak rate test acceptance criteria, refer to re ference 2.1. Leak rate calculations are outlined in Enclosure 13.2. 12.0 Test Procedure
/f 12.1 Dewater all low points. Adjust valve positions to those shown on Enclosure 13.4.
RJ 12.2 Verify that all safety precautions and site clearances have been ratisfied. 12.3 Close inner doors on both locks. Leave outer doors open. _O 12.4 Verify that LRT-16 is closed, h 12.5 Record the data called for on Enclosure 13.3. [ M 12.6 St?r: RB vent unit fans and auxiliary fans at speed.
$ M 12.7 Start water flow through coolers if and when required by temp-erature limitations. ,
12.8 Open valves LRTI 3, LRT-10, LRT-13, LRT-15, and LRT-17. Start temporary compressors and begin pressurization of the PB. 2.9 _ _ DuringpressurizationandudthesA'urization, u.c record the cata m called for on Enclosure 13.3 " 'r or more often if conditions are close to the limits of 6.3. 10 L' hen RB pressure reaches approximately 10 psig, close LRT-17 and LRT-15 and turn of f the temporary compressors and fans. , ' 2.11 At this pressure, an informal Icak test will be performed as a check on the lenkage from the building and on the instrumentation used for the test. This Icak rate test will run concurrently
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with the outside and inside~ penetration leak checks. 12.12 Inspect pcuctrations for Icakat;c. Inspect all gaskets of the equipment hatch and inner lock doors. (6)
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entry into the reactor building may be made using the following procedures: 12.13.1 Enter lock and ciose outer door and equalizing valve. 12.13.2 Slowly prcssurize lock by opening inner door equalizing valve. t 12.13.2 When lock becc=es pressurized, open inner door and enter the reactor building. 12.14 Inspect suspect leak areas inside the reactor building. Exit from the reactor building may be accomplished by the reverse of the entry procedure. After exiting, close the outer' doors on both air locks. M/A 12.15 if teoks are found which cannot be repaired with the reactor i building pressurized, the building should be depressurized by opening valves LRT-16 and LRT-17, and the leak should be repaired. A 10 paig retest should then be done, bhL12.16 If significant leaks are not found, resume pressurization by starting the compressors and opening valves LRT-15 and LRT-17. Start building fans. 2.17 When RB pressure reaches 29.5 + 2, -0 psig, close LRT-15 and , LRT-17 and stop compressors. ' '
/ 12.18 Equalize reference vessel pressure to RB pressure by opening valves LRT-34 and LRT-35. When pressures equali::c, close LRT-34 and LRT-35.
12.19 connect the differential manometer by opening valves LRT-28 and LRT-33. , 12.20 Read and record the following instrument readings every 15 minutes (Enclosure 13.3.) 12.20.1 RTD's 12.20.2 Micromanometer and temperature at manomqters. 12.20.3 Texas Instrument pressure gauge. .
'
'
12.20.4 Dew Point Sensors. 12.20.5 Bare eter cad tce;erature at barc teter. (7)
4 50/3 4
/-27-71 ,
h 12.21 Record the following instrument readings hourly (all found in microwave towers):
"
12.21.1 Outside air temperature sensors (DB and WB). , 12.21.2 Wind Velocity. 12.21.3 Wind Direction. 12.22 Calculate the leakage rate from the procedure given in Enclosure 13.2. Continue leak rate testing. k 12.23 At the end of the test period, superimpose a leak on the RB by lla opening valves IA-M, IA-90. - > " The flow rate through ISO the flowmeter should be controlled by IA-K to be approximately , equal to the allowable leakage rate. l 11.2d / 3. 3 / 12.24 Record data as in 49,4ila and 4uh44. u.o Gm volve. LZ 2 2 - ' ' 2T 2 2.
-
b 12.26 Pressurize the reference vessels to 68 psig. thru valves LRT-36 h L12.27 At the conclusion of the verification test, resume pressurization by starting the compressors and cpening the valves LRT-15 and LRT-17. Start auxiliary and vent unit fans. h 2.28 When RB pressure reaches 68 psig i .2 psig, close LRT-15 and LRT-17 and stop compressors. Main:ain this pressure for one hour minimum, k/h12.29 Reduce RB pressure to 59 psig by opening valves LRT-16 and LRT-17. Energize electric heaters as required to satisfy tenperature requirements. O312.30 When EB pressure reaches 59 + 2, -0 psig, close valves LRT-16 and LRT-17. Stop fansg'cx QI d d h MA' "5 " 2.31 Reduce reference vessel pressure to RB pressure by opening valves LRT-34 and LRT-35. .! hen pressures equalize, close valves LRT-34 and LRT-35.
- .- 150/3 4 7-27-71 42.32- C;.. ;;; the dif fer::ti:1 :=::::c. L; ep -5g '1"a L.~" -28
-
M. dalVC. sh tranomb ocr_o rdm* b hosure. /5.(m. , -
, # 2 2 / .33 12 Read and record the following instru=ent readings every 15 minutes.
(Enclosure 13.3) 12.33.1 RID's 12.33.2 Micromanometer and temperature at cancmeter. 12.33.3 Texas Instrument Pressure Cauge. 12.33.4 Dew Point Sensors.
, -12.34 Record the following instrument readings hourly 12.34.1 Outside Air Temperature Sensor.
12.34.2 Wind Velocity. l l 7 12.34.3 Wind Direct.on. l
-12.35
-
_r Calculate the leakage rate from the procedure given in Enclosure j d lea
- Jo ,
13.2, continue leak rate testing for ghours. N 12.36 At the end of the test period, superimpose a leak on the RB by opening valves IA-89, IA-90, and IA-91. The flow rate through the flowmeter should be controlled by IA-89 to be approximately equal to the allowable leakage rate. kc ok- ic.asb 5 ko0TS . 12.37 Record data as in 12.33 and 12.34 3 -
-
k 12.38 At the conclusion of the verification, open valves LRT-16 and LRT-17 and begin depressuri:ation. Operate RB heaters if required to meet air temperature requirements. Start fans. 12.39 Continue depressurization to atmospheric pressure. Stop fans.
$ f,, /
/ M " / 12.40 Inspect the RB internally and the equipment within the RB to
.
determine if any damage has been done by the pressure. tost. 13.0 Enclosures
/
13.1 Personnel Access Restrictions 13.'o M L e o.e_. de.sse_\ ond bomeher 13.2 Leakage Rate Calculations- k
.
*13.3 Data Sheet 13.4 Valve Checklist
-
> 13. 5_ RB pressure Profile
. _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _
. 150/J 4 ,
,
7-27-71
'
- R[EACTOR BUILDING LEAK RATE TEST
_
~
pER'SONNEL"A'CCESS REST,RICTIONS CONTROL COPY 5 TEST PERSONNEL ;S.I.TE _PERSONN EL
.
.70 __
.
'
ADMIN. CONTR OL PER$0NNEL REMAIN OF PkNETil. hR'EAS OUTSIDE NO ENTRY TO.. FENCED l AREA
'PENETR. AREAS 9 60_._ '
h b W b til . . PERSONNEL g !502.- REMAIN to OUTSIDE
$ FENCED lE a ]^ #h b
o 40___ d o 03 ADMIN.C 'NTROL
~
ACCESS ALLOWED h OF PENETR.
^ % UNFiESTRICTED j , j ASSIGNED WORK $ 30 _ ACCESS />>>
g i I / / ll r ! l 20_- l l ACCESS ALLOWED FOR . ASSIGNED WOR K, 10 . .. l , t. UN41LM RIC TC D ACCI S5
.
I \" y ENr.l.OSUllE 13.1
._..--.......n.,c
_ _ _ _ _ _ _ _ _ _ . - - _ _ _ _ -
.
- *
~
150/3 4
- 7-27-71 REACTOR BUILDING LEAK RATE TEST
'
CONTROL COPY dBSOLUTE PRESSURE
' GAUGE READING
.
iT.O.B. E'.CONSTAN.T* , fTRUE
, PRESSURE CORRECTED = PT = -
.
. PSI.A
--
--
--
. l l
. . _ . . _ . . . .
GAUGE PRESSURE
. . . . .
! BAROMETER . . . . .
. I_HgA P
'IEiVIP CORRECTION -
.
=
c
- GRAVITY ~CO'R R ECTION -
- ' -
e
= , x.49I2 I
,PBAR =- .pg, e
PT e
, PGAR G= PSIG
'
,
.
.
- CALIDRATION DATA SUPPLIED BY THE r. ANUFACTURER
"^E CALCULNiiON BY ENCI.OSURE C.2 OCONEE UNIT ONE '
SilEET 1 Ol; G
150/3 4 * . 7-27-71
' REACTOR BUILDING LEAK RATE TEST
,
CONTROL COPY DIFFERENTI AL PRESSURE
-
i 5 P iMICROMANOMETER j
- TEMP CORRECTION TO 40C -
.
_ _ . , CORRECTED I . . - - - . L_6'P_
. Ln H2O
[~x'_0.03G13
,
! E.P = . PSIG DEW POINT TEMPER ATURES DPT1 _
. .
,
DPT2 = ,
*
'
.
TOTAL :=
- e 2
p ,_ PARTIAL PRESSURE OF
- 0 PSIA WATER FROf.1 STEAM TABLES , .
DATE CALCU L ATION BY __. ... ENCLOGUl:E 13.2 OCONEE UNIT ONE S11EET 2 OF G
. - - _ _ _ _ _ _ - _ _ _ _ - _ - _ _
. .
. . - .
150/3 4
- 7-27-71 REACTOR BUILDING LEAK RATE TEST
{~
! REACTOR BUILDING TEMPERATURES ,
X =
.T1--- . . .
T2
-
X = .
. . ,
T3 . X . .
-
.T4 X .
< . . T5 X = l. .
. .
X :
- TG . .
,
X : Ti.
-
. . .
T8 . i x . l= 1 .I i T.9 ~l X . .
.
-
X =
- T.10 . . .
iT 1'1 X ,: .
. . . .
_,_ .. X = T12 . . . X = T'3-1 . .
.
,
.
T-14 X : . a
. .
T'5 1
,
X , , X = T1G , ,
,
.T17 .
X . . T18 X . .
.
T10 . Xi . l .
,
T20
. L .
=!. .
T21 . X ll ,. h=]. . T_OTAL
.
'
=
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T22 X 4 5 9 G 0
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.
,- 7_
-
T23 , ll X d Ii = ;!l ,! Ta ,
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T24 _l x e;,; jj = 4i,.
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DATE_. CALCULATION UY . OCONilE UNIT ONE ENCLOMU;E 13 ;, SHEET 3 OF G.
!
1 193/3 4 ' I 7-27-71 l
,
-
\
~ "
l REACTOR BUILDING LEAK RATE TEST I l
~
~
CONTROL C0P p_ : PARTIAL PRESSURE __ _,
"
pyT P?
-
l OF RB AIR
!
- PT l[v - 0
.
il. . PSIA
~
-
UR = 2400
"
3_ P2T1 ABSO' LUTE PRE'S SURE I_T_,,_ g -- {1,T2 ,
,
tMETHOD P2 !Ti X
. .
l X
- . .
- P1 T2 1 0 0 0 0 0 0
.
-
0 0 0 9 _- 2400 0 0 0 0 X
. .T
_
.
LR = 0 O %/ DAY
,
DATE.- - CALCULATION BY - l ENCLOSullE 13.2 OCONEE UNIT ONE
.....,..n- ,~
.
.
150/3 4
- 7-27-71 .
REACT,OR BUILDING LEAK RATE TEST (REFERENCE VESSEL METHOD CONTROL COPY .
~
~ ~
~~L'R = 2dd0 i
~
I T1 (AP2 + Pv2 ) . ([P -~~~$1 1 +P )
-T. PT1 - PV1 T2 .
;PT. ,
- 0
'.P- .
ibI~$ ~~ , psi AP
.
.P'y
--
Y 0 e
- - -
A .P + Py .pgg
.- . . . - . .
lX
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.
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,T2
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A P1' + Pv1' ,
. . . - . .
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0 X
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2 4 0 1
- LR = -
;
X - e . I l 0 %/Df Y
,_) 0 l DATE CALCULATION 13Y . __
i OCONEE UNIT ONE f ENCLOSUliE 13.2 StiEET 5 OF G i I l
.
.
, -
150/3 4
.
7-27-71
' REACTOR BUILDING LEAK RATE TEST
- ~
.
CONTROL COPY IP I 5 ~ ~5 6' 3 X g.,_ , 1
,
.x_._106
. .
T
.
Y! = . !x.- 1d5 LBm~ ~ ~ '
- - - . . . .
~
..... LR 'x W L.R ' = 2400 LR' = 0 0 X
. .
2 4 0 0 l ! ! !
.
LR'= .
._ _
l LB/HR 1 D AT E - - -- -- CALCul.ATION BY __ -._ ENCLOCUi1E 13.2 OCON!:E UiJIT ONf.
i! [ $ . .
-
NE
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he
=
e _ cm_e m e m
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=-
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e w
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s i s i s t e i s i s i s R E o t A C R T E O T A R o C B T U O I L R B D I E it N N e U C I L G D I L O I N si N T
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A R sT IR A 1 T 3 T E 3 E M D L t P E E u R A A K T R iT U A a R T . E E T E et S s T . _ '
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_ _ _ f u %. _ _. _ _ iT e 1
e 1 Y 2 e 1 2
SO HC T E O E i s T N E 2 E t U r O F IN 3 T 3 O t N r a E
'
-
,9 150/3 4
-
'
7-27-71
.
EEdCTOR ' BUILDING INTEGR ATEd1EAK II ATE'TE'ST
. . . - - - Lif4ER FLATE TEMPER ATURE
-. . DATA
. _ .DATE. . TIME RECORDER TA TB TC TD f i
-
!
_
'
l . l l l 1 i a L_ -l l l-i :
'1 ! i
-- ! --l l j
t
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; i l l
- . _ _ . _ _ , - l I I ~! l I ENCLOSul;E 13.3 OCONEE UNIT O. '
SHEET 3 OF 3
-. - _
- . . . . .
.
.
*
- Sheet 1 of f L/
Enclosure 13.4 Duke Power Company Oconee Nuclear Station VALVE CHECKLIST . Unit #1 VALVE NO. VALVE NAME CONTROL COB._YTION INITIAL CC-1 letdown Cooler "A" Inlet Open h[k CC-2 Letdown Cooler "B" Inlet Closed hh[ CC-3 R.C. Pump "Bl" Coole r Outlet Open h[ CC-4
'
R.C. Pump "B2" Cooler Outlet Closed h[ CC-5 R.C. Pump "Al" Cooler Outlet Open h k CC-6 R.C. Pump ,"A2" Cooler Outlet Open (7 h k CC-7 CC Return Penetracion (54) Inside Block Closed (3.88 CC-8 CC Return Penetration (54) Outside Block Closed h[h CC-10 Pump "A" Suction Open [h CC-21 Supply lleader Penetration (3) Drain Closed h[h _ CC-22 Supply lleader Penetration (3) Vent Closed hMh
- C-23 Supply lleader I'enetration (3) PX Closed GFO CC-37 R.C.P. "B2" Cooler Shell Inlet Check Open .
CC-41 Letdown Cooler "A: Shell Drain Closed h[ _ CC-42 Letdown Cooler "A " Shell Ve'nt Closed h[ CC-44 Letdown Cooler "A" Shell Outlet Open hgk CC-45 Letdct:n Cooler "B" Shell Drain Closed hhk CC-46 Letdown Cooler"B" Shell Vent Closed Q{{ CC-48 Letdoten Cooler "B" Shell Outlet Open h[ CC-49 Quench Tank Cooler Shell Inlet Open h [[ _ CC-51 Quench Tank Cooler Shell Drain Closed h[ CC-52 Quench Tank Cooler Shell Vent Closed _h [ CC-53 l Quench Tank Cooler Shell Outlet _ Open {{ CC-56 Return Penetration (54) Drain Closed hAk 150/3 Rev. 4 July 27, 1971
.
~ -
'
- Shsst2of1y Enclosure 13.4 Duke Power Company Oconee Nuclear Station VALVE CHECKLIST l ALVE NO. VALVE NAME CONTROLC'i*1O.0 ITION INITIAL CC-55 Retum Penetration (54) Closed h[h CC-56 Return Penetration (54) PX . Closed h[h CC-67 Supply Penetration (3) Inside Test Drain Closed hN CC-68 Supply Penetration (3) Inside Test Vent closed h6O CC-69 Supply Penetration (3) Inside Test PX Closed hN CC-78 CRD Cooling Supply Closed' hh CC-79 CRD Cooling Retum Closed h[k CC-80 CRD Header Penetration (44) Vent Closed h['h CC-31 CRD Header Penetration (44) PX Closed , h. [O CC-82 CRD Header Penetration (44) Drain Closed h[h CC-83 CRD Header Penetration (44) Inside Test Vent Closed h[[
CC-84 CRD Header Penetration (44) Inside Test PX Closed h[h CC-85 CFD Header Penetration (44) Inside Test Drain Closed hgk CC-86 Shell Line Drain (Letdown Cooler "A") Closed gfQ CC-87 i Shell Line Vent (Letdown Cooler "A") Closed ]fy ; CC-88 Shell Line Drain (Letdown Cooler "B") Clcsed hg CC-89 Shell Line Vent (Letdown Cooler "B") Clased {p CC-25 RCP "Al" Cooler Shell Inlet Check Open CC-29 RCP "A2" Cooler Shell Inlet Check Open CC-100 CRD Cooling Supply Closed (-- CC-101 Cooling Return Closed [hf CC-95 Quench tank cooler Inlet Vcat Closed [ [ CC-p
,
Quench Tank Cooler Outlet drain Closed 'f g CC-102 Vent _ Closed 150/3 Rev. 4 July 2 7, '.9 71 4
.-
<
.
Shnt 3 of l Enclosure 13'.4 Duke Power Company Oconee Nuclear Station VALVE CHECKLIST Unit #1 VALVE NO. VALVE NAME C03 TROL COPISm0N mTm CC-103 Vent Closed hR CC-97 Return Penetration (54) Drain Closed GAR CC-98 Return Penetration (54) Vent Closed hhk CC-99 Return Penetration (54) PX Closed CC-70 , Inlet header isolation (inside) (3) Closed CF-18 Tank "B" Vent Throttle valve Open h CF-1 Tank A outlet Open CF-2 Tank "B" outlet Open b CF-3 Tank "A" Sample and Drain Clotad CF-4 Tank "B" Sample And Drain Closed -- CF-5 Tank "A" Vent Open Ph CF-6 Tank "B" Vent Open hh CF-7 Core Flood Bleed to Waste Holdup Tank Closed h CF-16 Tank "A" Vent Throttle Valve Open kh CF-19 Sample Block Closed C-N CF-20 Tank "A" drain to Coolant Storage Closed Q. [h CF-21 Tank "A" drain to Coolant Storage Closed h_[h CF-22 Tank "B" drain to Coolant Storage Closed h. f h CF-23 Tank "B" drain to Coolant Storage Closed [,7 f h _ Tank "A" CF-24 outlet test connection Closed h[ CF-25 Tank "A" outlet test connection Closed [[ CF-26 Tank "B" Tank "B" outlet test connection Closed h[k CF-27 outlet test connection Closed hg _ CS-3 Quench Tank outlet Open [ [_. . . _ . . 150/3 Rev. 4 July 27, 1971
-
. ~..
Shast 4 of Enclosure 13'.4 Duke Power Company Oconee Nuclear Station VALVE VA LVE NO. CHECKLISdONTROLPOSITIQU VALVE NAME COP"T # - 1 INITIAL CS-5 (ES Component Drain Header (pent. Isolation) Closed CS-6 (ES Component Drain Header (pent. Isolation) Closed Tb CS-13 Quench tank cooler inlet open - CS-14 Quench tank cooler outlet Clesed CS-23 Component Drain Header penetration (#29) Drain Closed b CS-24 Component Drain Header penetration (#29) Vent closed [b CS-25 Component Drive Header penetration (29) PX, closed. [b fSS .6 ;mdi Iank woM Llet - -Closec~ /
.C6 41 Qunnnh rank enn1 r Outlet- Glesed C. [Gfe CS-145 Quench Tank Cooler yenetration (38) Drain Closed h CS-146 Quench Tank Cooler penetration (38) Vent Closed h CS-147 Quench Tank Cooler penetration (38) PX Closed 6 CS-17 - Quench Tank Cooler Penetration (38) Drain Closed k[
CS-18 Quench Tank Cooler Penetration (38) Vent l Closed g{ CS-19 Quench Tank Cooler penetration (38) PX Closed // ( DW-90 Quench Tank Outlet Header Cicaed /f// Q "J~ BS-1 A Header RB Isolation Closed. l [C 55-2 B Header.RS Isolation Closed l[C BS-12 A' Pump Discharge l Closed 7C BS-13 A Pump Test Closed [( 3S-17 B Pump Discharge Closed .[d 3S-13 3 Pump. Test Closed- [{ SS-21 -lTestlinetoBWSTBlock l Clcsed j
. _ . - _.
.
._ _
, ,
3S-22 . Closed l g p .f
.. --
l Air Test Connection l -
. .
150/3 Rev. 4 July 17. IM1-
.__ . ._ . _ _ _ _ _ . . . . _ _ -
,
_ _ _ , Shrt 5 cf /4 Enclosure 13.4 Duke Power Company Oconee Nuclear Station VALVE CHECKLIST Unit #1 VALVE NO. VALVE NAME O ITION INITIAL BS-23 Air Test Connection Closed [f2 BS-15 Drain Closed f.f[ BS-20 Drain Closed 6S N-128 Core Flood Tank A Supply Closed hMR N-130 Core Flood Tank B Supply Closed Ph LWD-1 RB Normal Sump Penetration (5) Isolation Closed /C LWD-2 RB Normal Sump Penetration (5) Isolation Closed [C LUD-27 RB Normal Sump Penetration (5) Drain
.
Closed [C LWD-28 RB Normal Sump Penetration (5) Vent closed .[( LWD-29 RB Normal Sump Penetration (5) PX Closed [b LWD-99 Emerg. Sump Drain Penetration (40) Block Closed [( LWD-103 Emergency Sump Drain Penetration (40) Block Closed [b. CJD-10 CWD-ll Quench Tank Vent Penetration (18) Vent Closed [h[ Quench Tank Vent Penetration (18) Vent Closed [O/ CWD-12 Quench Tank Vent Penetration (18) Inside Closed '~C
/
CWD-13 Quench Tank Vent Penetration (18) Outside FDW-105 St. Cen. A Sample Penetration (2) Isolation Closed [{ Closed 70 P FDW-106 St. Gen. A Sampic Penetration (2) Isolation FDW-107 St. Gen. B Sample Pen (58) Isolation Closed [][ Closed [p [ FDW-10S St. Gen. B Sample Pen (58) Isolation Closed [O FDW-117 St. Gen. A Sample Pen (2) Vent Closed [y[ FDW-llS St. Gen. A Sample Pen (2) Drain Closed [g[ FDh'-119 St. Gen. A Sample Pen (2) PX Closed 7g[ FDW-122 St. Gen. B Sample Pent (58) Vent Closed j 150/3 Re v. 4 July 27. 1971
' '
Shrst 6 of 14
,
Enclosure 13'.4 Duke Power Coc;pany Oconee Nuclear Station
'
VALVE CHECKLIST #1
/A..VE NO. VALVE NAME CONTROL C0'h X. TIONINITIAL FDV-123 fSt.~ Gen. B Sample Pen (58) Drain Closed /O FDW-124 St. Gen. B Sample Pen (58) PX Closed [O GW-130 Emerg. Feed Vent Closed FDW-131 Ecierg. Feed Drain Closed .
FUW-132 Emerg. Feed PX Closed . [, FDW-38 Emerg. Feed Inlet Closed CA3
- FDW-268 Drain on energ. Feed line to lA S/G. Closed FDW-248 'f1AS/GFeedHeaderDrain Closed ,N' FDW-269 ' 1A S/G Feed Hender Vent Closed [d1 FDW-247 1A S/G Feed Header Vent Closed / ,!
FDW-245 1A S/C Feed Header Vent Closed ,
,
FDW-127 1A S/G Feed Header Drain Closed G. FDW-31 1A S/G Feed H'eader Isol. Valve Closed ggy FDW-36 1A S/G Feed Header Isol. Valve l Closed gj FDW-219 Penetration 17 Closed j p [,
\
FDW-220 Penetration 17 l Closed ,- .
-
FIN-221 Penetration 17 Closed l ,
'
FD'!272 Penetration 17 l Closed
\ Feed Water System FDW-47 Penetration 17 l Closed dQ FDU-270 ' Penetration 25 PO 121-B Closed f FDW-253 Penetration 25 Closed- l /9 6[
FDW-254
,
Penotration 25 . Closed M FD'!-256 ' Penetration 25 Closed
!}6 7D'4-251
/ i closed 1 n l' /_/. g l Penetration 25 ;
_ 150/3 4 Rev. 4 July 27,-197'. E
l
.
,
Sh ^,t 7 of 18/- Enclosure 13.4 Duke Power Company
. Oconee Nuclear Station VALVE CHECKLIS # l-VALVE NO. VALVE NAME POSITION INITIAL EDW-216 Penetration 25 N Closed (h3 FDW-40 Penetration 25 _
Closed C Cd 3 FDW-45 Penetration 25 P 21-B Closed (wg FDW-103 Penetration 43 Closed A , FW-104 Penetration 4 Closed LP-1 RC Return Block Closed LP-2 RC Return Block Closed [h. LP-3 Return Line Penetration Block Closed [h LP-17 LP (A Line) to RC Building Isolation Closed , LP-18 LP (B Line) to RC Building Isolation Closed LP-19 RB Emerg. Sump. Isolation (line A) Closed hfk LP-20 RB Emerg. Sump Isolation (Line B) Closed
$h LP-23 RC Return Line Vent Closed ,h h LP-24 Transfer Canal Drain to LP Closed _. 70,P LP-62 B Header Priming Closed [p[
LP-63 A Header Priming Closed j[g[ LP-64 Priming Line Block Closed [g[ LP-65 Drain to D2 from Loop B Closed Q[[ LP-66 Drain to D2 fr m LO PA Closed Q LP-67 - Penetration 57 Closed 6h LP-80 FS /1/70A/43 Penetration 57 Closed Q _ "7-5 P re s s . Steam Sample Bld. Isol. Closed RC-7 Press. Sample (Bldy. Isol.) Closed /</ 1
-
[ _ RC-39 Press. Sample Penetration Vent closed _ h _ 150/3 Rev. 4 July 27., 1971
__ -
-,
Sh2st 8 of /4 Enclosure 13'.4 Duke Power Company Oconee Nuclesc Statien VALVE CHECKLIST t d' VALVE NO. VALVE NAME CONTROL Y Oti1 TION 1MITIAL RC-50 Press. Sample Penetration Drain Closed b RC-51 Press. Sample Penetration PX Closed b RC-6 Pressurize water space sample line Closed [ S F-1 Transfer Tube A Isolation S F-2 Closed N[ Transfer Tube B Isolation Closed S F-60 Canal Fill Penetration (55) Block Closed h[ S F-61 S F-62 Canal Fill Penetration (56) Block Closed [ Incore Instrument Tank Fill SF-63 Closed [k Incore Instrument Tank Fill Closed h[[ PR-1 RB Purge Outlet (RB) P R-2 RB Purge Outlet. (PR) Closed h[ PR-3 RB Purge Control Closed [ Closed g[
'R-4 RB Purge Inlet Closed
[[ P R-5 RB Purge Inlet (PR) Closed g2) PR-6 RB Purge Inlet (RB) Closed g P R-7 RB Radiation Monitor Inlet Closed fgh PR-8 RB Radiation Monitor Inlet Closed P R-9
]
R3 Radiation Monitor Inlet Closed [/ 1 1 g/ P R-10 RB Radiation Monitor Inlet Closed PR-21 IR.B.PurgeSupplyLineBleed
, f Closed' gy .PR-22 R.B. Purge Exhaust Line Bleed-Closed
[o PR-23 R.B. Sample Inlet Penetration (#60) Test closed Id PR-24 R.B. Sample Inlet Penetration (#60) Test _ . - - -
--
Closed h;y
. -.--
PR-25 R.B. Sample Return Penetration (#61) Test Closed-
] f_ .
.. .
150/3 4 Rev. 4 . July 27. Irl
. __
,
Sh rt 9 of if Enclosrue 13.4 Duke Power Comapny
. Oconee Nuclear Station VALVE NO.
VALVE CHECKLIS' CONTROL VALVE NAME O ITION INI TI AL PR-26 R.B. Sample Return Penetration (#61) Test closed M[ P R-2 7 R.B. Purge Exhaust Penetration (#20) Test Closed ,[ 3 h PR-28 R.B. Purge Exhaust Penetration (#20) Test Closed Mh PR-29 R.B. Purge Supply Penetration (#19) Test Closed h[t) PR-30 R.B. Purge Supply Penetration (#19) Test Closed [$ Q) HP-3 Letdown Cooler A Outlet Closed pD7 IIP-4 Letdown Cooler B Outlet Closed [C HP-5 Letdown Isolation Closed {{ HP-20 RC Pump Seal Return (RB) Closed Q/ O
!!P-21 RC Pump Seal Return (Outside RB)
.
Closed g
!!P-26 RC Loop A Injection Closed Jgf I!P-27 RC loop B Injection Closed [g/O HP-31 RC Pump Seal Pressure Control Closed /~gp _
HP-36 Letdown Penetration (6) Vent Closed '-j ~gf HP-37 Letdown Penetration (6) Drain Closed gj O HP-38 Letdown Penetration (6) PX Closed j-- HP-68 Seal Return Penetration (7) Vant Closed TOP llP-69 Seal Return Penetration f7) Drain Closed - o HP-70 Seal Return Penetration (7) PX Closed -- ~ jg _ _ _ _ llP-119 stC Volume Control Inlet Closed gg
--- . _ .-
HP-120 RC Volume Control Closed g HP-121 RC Voluee Control Outlet ,0 pen {g y _.
!!P-122 RC Volume Control Bypass Closed O 11P-123 RC Loop A Injection Penetration (9) Vent Closed g 150/3 Rev. 4 July 27,1971
,
.
,
Shsst 10 of ty.
'
Enclosure 13'.4 Duke Power Coc:pany Oconee Nuclear Station
, VALVE CHECKLIST Unit #1
'
VALVE NO. VALVE NAME ITION INITIAL EP-124 RC Loop A Injection Penetration (9) Drain Closed [O[ HP-125 RC Loop A Injection Penetration (9) PX Closed TOP BP-13SS Seal Pressure Control (HP-31) Inlet Open 7~O k HP-139 Seal Pressure Control (HP-31) Outlet Open [hP HP-140 Seal Pressure Control Bypass Closed l / h/O i HP-149 RC Loop B Injection Penetration (52) Vent Closed h/ HP-150 RC Loop B Injection Penetration (52) Drain' Closed DF HP-151 RC' Loop B Injection Penetration (52) PX Closed 7D[ HP-155 Closed Core Flooding Tank A Fill lh[/] l HP-156 Core Flooding Tank B Fill Closed [O HP-202 RCP A2 Seal Supply Pen Vent Closed []/C HP-203 RCP A2 Seal Supply Vent PX Closed 7g[ HP-204 RCP A2 Seal Supply Pen Drain
- Closed [g[
HP-209 RCP Al Seal Supply Pen Vent Closed [g/O HP-210 RCP Al Seal Supply Pen PX Clcsed ![g[ j HP-211 RCP Al Seal Supply Pen Drain Closed l [g f HP-216 RCP B2 Seal Supply Pen Vent l Closed f7pp HP-217 RCP B2 Seal Supply Pen PX Closed f 7pj'D H P-2.' 8
.
RCP B2 Seal Supply Pen Drain Closed ![pf l HP-223 RCP B1 Seal Flow Supply Pen Vent Closed l7p
'P-224 i
.RCP B1 Seal Supply ren PX Closed l7yp HP-225
; RCP B1 Seal Supply Pen Drain l Closed '[g[
HP-235
._
lLoopA2NozzleWarmingThrottle la ,ially
.
- g ,g l l
IIP-236 l Loop A2 Nozzle Warming Check l Closed [[ 150/3 Rev. 4 July 2', 1971 I l
- ,
. Shz t 11 of 14 Enclosure 13'.4 Duke Power Company Oconee Nuclear Station VALVE CHECKLIST Unit #1 VALVE NO. VALVE NAME P SITION INITIAL HP-237 Loop A2 Nozzle Warming Pen Vent Closed [h[
HP-238 Loop A2 Nozzle Warming Pen PX ' Closed b/ HP-239 Loop A2 Nozzle Warming Pen Drain Closed [D/ HP-241 Loop Al Nozzle Warming Throttle Open 7[[ HP-242 Loop Al Nozzle Warming Check Closed 7~D P HP-243 Loop Al Nozzle Warming Pen Vent closed [D[ HP-244 Loop Al Nozzle Warming Pen PX Closed Q[ HP-245 Loop Al Nozzle Warming Pen Drain Closed [D[ HP-333 Drain - Letdown Closed hh HP-253 A2 Nozzle Warming Check Closed h[[ HP-254 Al Nozzle Warming Check Closed [[[ HP-322 Al Injection Drain Closed
$[[
HP-323 A2 Injection Drain Closed f[[ HP-126 A2 Inlet Stop Check Closed {f HP-127 Al Inlet Stop Check Closed gf IIP-152 B2 Emerg. Stop Check Closed Q[ HP-lS3 B1 Emerg. Stop Check Closed HP-326 B1 Emerg. Injection Drain Closed { HP-327 B1 Emerg. Injection Drain Closed g/ g/g HP-328 B2 Emerg. Injection Drain Closed HP-334 B2 Emerg. Injection Drain Closed HP-144 A2 Seal Injection Stop Check (Inside) Closed , ;g HP-145 Al Seal Injection Stop Check (Inside) Closed l (.j (r g HP -146 B2 Seal Injection Stop Check (Inside) Closed ,. (. , 150/3 Rev. 4 July 27, 1971
.
- Shret 12 of 14 Enclosure 13'.4 Duke Power Company Oconee Nuclear Sts; ion VALVE CHECKLIST L' nit J1 VALVE NO. VALVE NAME e ITION INITIAL HP-147 l 31 Seal Injection Stop Check (Inside) f Clesed l \N' \M $
i HP-283 Outside Al Seal Supply Stop Check , Closed HP-284 Outside A2 Seal Supply Stop Check Closed [ HP-285 Outside B1 Seal Supply Stop Check Closed 7[ HP-286 Outisde B2 Seal Supply Stop Check Closed f 7f LRT-3 Temporary Compr. #1 Outlet Block gg r p f [jf/$ LRT-6 Temporary Compr. #2 Outlet Block gg closed l[JM LRT-7 After Cooler Drain Block open l [[[ LRT-8 Af ter Cooler Drain Control [ [ ,I [ y [ ! N -
<
# GW LRT-10 Af ter Cooler Outlet Block [[[[[
-
, ,
LRT-13 Air Dryer Ontlet Block [ hgg I C M ,l[ip/ LRT-15 Pressurization Control pg M M f /gg LRT-16 Depressurization Control Closed l,j/jff p i LRT-17 Pressurization Block Closed l gg/f g
+:RT-20 frenvuuulLvvi 31vuk [ ,, ; - Ofen -h LRT-25 RB Pressure Line Outer Block Open { jg/3 LRT-27 Absoi tte Pressure Cauge Block -
v
~
/
~[ ( .
-
. - N/)'
.v Cpen !_
.(,n8 1Y,Y
,
LRT-28 Differential Manometer RB Pressure Block Closed ; g LRT-33 Dif ferential Manometer Ref. Vessel Block Closed LRT-34 Differential Manoineter Equalization Closed { LRT-35 Differential Manometer Equalization Closed [g LRT-36 Reference Vessel Pressurization Closed [ Closed LRT737 ; Reference Vessel Pressurization _ [[ . _ _ . LRT-38 P.eference Vessel Outer Isolation Open [/ [ 150/3 Rev . 4 July 27. 'Mi
, _ _ .
__. _ . _ - _.
. . _ _ _ _ _ . _ _ _ _ ._
,
,
~32- Shint 13 of 14 Enclosure 13.4 Duke Power Company Oconee Nuclear Station VALVE NO. V V A lE CONTRdL C0k$T10s imm LRT-39 Reference Vessel Inner Isolation Open hM LRT-40 Reference Vessel Low Point Drain Closed [/f/g
_ LRT-41 Reference Vessel Low Point Drain Closed [M LRT-42 Reference Vessel Low Point Drain Closed [# LRT-43 Reference Vessel Low Point Drain Closed [///$ LRT-44 Reference Vessel Low Point Drain Closed [ LRT-45 Reference Vessel Low Point Drain Closed [g3 LRT-24 R.B. Pressure Inner Block Open [[h ' LRT-47 Dif f. Manometer R.B. Press. Bicek Open [gg LRT-48 Absolute Press. Gauge Block Open [yj LRT-40 Dif f. Manometer R.B. Press. Block Open [g[ LRT-50 Dif f. Manometer R.B. Press. Block Isolation Closed [$$ LRT-51 Dif f. Manometer R.B. Press. Block Isolation Open gj LRT-52 Reference Vessel Press-Air Regulator Open
$
f[ LRT-53 Re ference Vessel Press. Block : Open g CCW-104 Feed f rom Sw. pump to 1A S/G Closed N[N A>
/
fa CCW-lC8 Feed f rom SW. pump to IB S/G Closed
'
;//
BA-S Penetration 48 Breathing Air-Outside valve Closed p BA-32 Penetration 48 Breathing Air-Inside Valve FS/1/19/7 Closed j MS-141 Penetration-26 1A S/G Vent Closed gr y - MS-142 Penetration-26 1A S/G Vent Closed
'~~
~
MS-143 Penetration-26 1A S/G Vent , Closed /j'1 _ - .4 --.- MS-144 Penetration-26 1A S/G Vent Closed [_ _
..{. -~~
MS-145 Penetration-28 1B S/G Vent Closed 150/3 Rev. 4 July 27, 1971
-
* .g Enc]ozura 13.4 Duke Power Ccecany Oconee !!uclear Station VALVE CHECKLIST thit d 1 V A LVE !! O . VALVE !! AMP. I ! 0!i I!;I TI AL MS-146 Penetration-28 1B S/G Vent Cicsed l/? [[
.-
MS-147 Penetration-28 IB S/G Vent Closed f ji[,[ MS-148 Penetration-28 1B S/G Vent Closed fj4 y LPSW-7
\ Closed _,g f/) P LPSW-8 Closed ,g//)7 LPSW-9 Closed g/g?[
LPSW-10 Sic.e ei , ./ ..J [ _ LPSW-il Closed ' 3,fg/)[
,
LPSW-12 Closed ,4:/),T LPSW-13 Closed ! ,y /),P . i LPSW-14 Closed f f g',I
/
LPSW-15
"_"l$ti n 21 & 22 closed [. .
LPSW-6 Cicsed //, LPSW-144 Closed TM[[ LPSW-145 Closed ,j, , . LPSW-146 Closed j7 LPSW-141 Closed 7 jf ,)j LPSW-142 Closed j/ , LPSW-143 ' Closed ,;fgj PR-36 Inlet to R.B. H2 Purge System Closed f,9,p>
- _
FDOHn
"
"A" OTs (L 3 he ll lk d eksei i>lP EDw-ist W 0 T5 L 5 he ll % n t- l closed _!LP cn L f' ! ;l f cA-74 , _
_
.____m &_ _ .__ 5_ _ _ . .
"N s- +
Fw-64
- \ dd 7'P g/o3eg 'g bw ~Q\ c) cad b;,\ q
.
. .
-- - . . '
aencroa eUitoimG eneSS""' "" "' "
.,,
_ 67.8 PSIG-CONTROL COPY 4 40 HRS 3
,
'60__ - 59 PSIG
.,
- 4 HRS ,
50 _ i
!
40__ 6 g ,
'
b 40 HRS m 4 > CC D E m 30__ [ 29.5 PSIG
'
20 _ _
.
Y
;
10- - 10_PSIG i l
. l TIME (HOURS) )
*-
0-i i i i i e i i i i i
'
, . . . i , , ---- l - -
8 16 24 32 40 48 '56 64 83 104 112 152 72 11 0 DG 120 128 130 144 i i. ] ENCI 9URE 13.5 GCO.*. : e i;y , - .,: -
.
NTS 1 a
r
. -
Parameter 7" ** al brated " '" Model Range Repeatability Accuracy No. Absolute 0-100 PSIA Precision Texas + 0.0009 psi ns " Or - 0.001% 47.64 Pressure gd 100,000 counts " "" 4 (.015% of Reading) Gauge Full Scale
.
Barometric Pressure PRINC0 26-32 IN. HG. + 0.01 IN.HG. ( 0700401 PSI) m Leeds & Northrup Temperature O TO 150*F R . 1 12*F 1773462. y System to U _L- _ _ _ _ T N h ' y Merian ,
,l5 Inches 110 34FB2 .l j
2 2 0 TO 20 IN. i 0.001 1120 0582010 7
"
$ Manometer "
4 1
#es re p, Heise 0-100 Psig 0.1 psi 0.1 psi Eetter Than-Flow 1110-09123GlA 0 TO 10.45 1/4% of Inst.
1 0.1 cfm 7004-39848 Reading
.
Dewpoint Cambridge -100*F System to + .5*F Temperature ~ 332 6 333 992-Cl +200'F .
- - -. -
a
. .
2.2 INITIAL TEST CRITERIA Pressures:
- 1. Design Pressure 59 psig
- 2. 115% of Design Pressure 67.8 psig
- 3. Peak Test Pressure 59 psig
- 4. Redtesd Test Pressure 29.5 psig
, Leak Rate: Maximum Allowable (La) 0.25%/ day by weight Temperature: 60*F Minimum Volume:
- 1. Containment Internal Free Volume 1,910,000 Cu.Ft.
2.3 MEASUREMENT SYSTEM The instrumentation used for the Oconee nD it 1 Leak Rate Test is similar to those used on previous tests conducted by the Bechtel Corporation. A sunnary of instrumentation characteristics is given by Table 2-1. Reactor building pressure was measured by a Texas Instrument precision pressure gage. The unit was factory calibrated before the test and will be recalibrated after the test. The pretest calibration chart is shown as Figure 2-1. Reactor building temperature was measured by 24 calibrated KID's and read on a L & N Numation digital readout device. The factory calibration report is shown as Figure 2-2. Each RTD was assigned a fraction of the total containment volume to represent. In the calculation of Reactor Building air temperature each RTD output was weighed by 1.s appropriate volume fraction. The RID locations and volume fractions are described in Table 2-2 and illustrated in Figures 2-3 through 2-7. In addition to the 24 KID's used for. the calculation of RB temperature, four additional KID's were used to measure temperatures at i miscellaneous points for information. ! 1
!
l 2-2 _ -
- - - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - -
.-
.
' - Sh2Gt 1 of 2 TABLE 2-2 INTEGRATED LEAKRATE TEST UNIT # 1 RTD LOCATIONS AND ASSOCIATED VOLUME FRACTIONS Basement Floor Level - Elev. - 787 Ft. RTD #
- Location Vol. Fract.
1 (180 ) under center' of access opening 0.03 11 10 ft. south-south-west of Steam Gener-ator 1B 0.02 12 15 ft. from Primary Shielding at 324 (placed in opening in secondary shielding) 0.02 2 8 ft. North-East of Steam Generator LA 0.'02 13 Just North of access to Reactor Cavity 0.01 Intermediate Floor - Elev. - 830 ft. RTD # Location Vol. Fract. 3 Between Pressurizer and Reactor Pump 1A1 0.02 14 Between Steam Generator 1B and Reactor pump 1B2 0.02 4 (180 ) on railing of open hatchway 0.05 15 Just west of core flood tank 1B 0.02 5 Inside incore instrument-tank 0.02 Operating Floor - Elev. - 850 Ft. RTD # Location Vol. Fract. 6 Just South of open hatchway 0.03 7 Just South of Steam Generator lA 0.01 20 Just North of Reactor Pump 1B1 0.01 16 Just East of Incore Instrumentation tank top 0.01 , 21 Above core flood tank 1B 0.01 8 Inside refueling canal near Reactor Head 0.08 2-4 __ ..
-.
.
. .
Sheet 2 of 2 Top of Shielding Floor - Elev. - 866 Ft. RTD # Location Vol. Fract. 9 Top of removable shield section East 0.05 10 Top of removable shield section West 0.05 17 Above grading at 0 near Reactor Building '
,
wall 0.05 Polar Crane - Elev. - 923 Ft. RTD # Location Vol. Fract. 18
- On East end of polar crane about 25' from Reactor Building wall 0.09 22
- On West end of polar crane about 25' from Reactor building wall 0.09 0 RTD # 18 and 22 vill be stored on the polar crane access platform until just prior to the Integrated Leak Rate Test to allow use of polar crane up until test.
Spray Header - Elev. - 943 Ft. RTD # Location Vol. Fract. 23 On Reactor Building Spray Header at 0 with a radius af 30 f t. from center 0.11 19 On Reactog Building Spray Headee at 180 with a radius of 30 Ft. from center. 0.11 Top of Dome - Elev. - 970 Ft.
-RTD # Location Vol. Fract.
24 In center of Reactor Building Dome at at an elevation of 970 Ft. 0.07 Miscellaneous RTD's RTD # Location 25 -Next to Lower Reference Vessel 26 In front of compressed Air Inlet Pipe (penetration #51) 27 On Reactor Building liner plate near-electrica? cenetration EB-11. 28 ~Next to Upper Reference Vescel. 2-5
.
_ _
. ,
l i
.
Reactor Building dew point temperature was measured by 2 Cambridge Des Point Hygrometers both traceable to the NBS. Air samples for the two dew point sensors came from two of the auxiliary fans which continually circulated air in the Reactor Building during the leak rate tests. Certificates of traceability and the integral RID calibration data are ) shown in Figures 2-8 through 2-11. The relative location of the humidity sensors is shown on Figure 2-12. The accuracy of the leak rate test measurement system was verified by a 0-10 Scfm Brooks rotameter which is shown on Figure 2-13 mounted on the leak rate test panel. The reference vessel method of leak rate test measurement initially was available for use. However, as the differential manometer was being cut in for use, it was accidentally broken and was subsequently not able to be used. The leak rate test measurement system is shown schematically in Figure 2-14. 2.4 INSTRUMENTATION ERROR ANALYSIS
- The leakage rate in weight percent per day is computed using the absolute method by the formula:
LR = 2400 H [ l - To P) T Po (1) i > l Where l l l ' Po = Initial Reactor Building absolute pressure corrected for ; water vapor pressure. P = Final Reactor Building absolute pressure corrected for water vapor pressure. To = Initial Reactor Building mean absolute temperature. T = Final Reactor Building mean absolute temperature l
- Analysis technique based on equation (3) verified by K. Joroschek and E. Weipport, " Tightness Investigations on Reactor Safety Pressure Vessels" Vol. 13 No. 3 March 1961.
The change or uncertainty interval in LR due to uncertainties in the measured variables is given by: oLR = 2400 [( dLR op)2 + ( dLR o Po)2 + (dLR~ _e To)2 + dT (dLR Ta )2 3 1/2(2) H dP dPo dTo Where o is the standard error for each variable. The error in LR after differentiating is: eLR = 2400 2 + (To. epo) ((_ ToTPo_ ep)T-Po ' P 2 + (- P e g)2 + (To P eT)2]l /2 3) H TPo 2 T p3 2-6
..
,
-
Where e p = op e, p
=
o, p
" #
"To To e "
T T However, for small values of LR, T ~ To P E Po and
"
*T "To The equation then simplifies to e 2 e 2 e 2 e 2 LR = ((- ) + ( ) + (~ ) + ( ) ]
H of
*P "T !
+ ] (4)
LR = g2400 [ 2 (7) 2 (7)
= error in pressure which accounts for the error in the Wheree$1uteprssuremeasurementinstrument abs (ePT) and the water vapor measurement system (eg)
*P = [ (eg) + (eg) ] ! (5) e PT
= absolute pressure instrument accuracy error ep = Dew point sensor accuraev error
[ number of sensors] 1/2 To develop a numerical value for e LR tw be assumed that.
- 1) -H = 10 hours
- 2) RB mean absolute pressure = 60 psig 3)l RB mean absolute temperature = 539.6*R - (80*F) based on 24 volume
. weighed dew point temperature. sensors.
~
- 4) : RB mean dewpoint temperature' = 70*F based on 2 volume weighed-dewpoint temperature sensors.
2-7
-_ . _ - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - _ _ _ _ . . .
. . Substituting the instrument accuracy values given in Section 2.3 into the above equations yields: ePT = i (0.001% full scale *) (100 psi full scale ePT = 10.001 psi) epy = 1 5'F = 10.353*F { from the ASME Steam Tables at 70*F e.py = .00437 psi
- Value of repeatability used. This number is more significant for the error analysis than the absolute accuracy.
e p=1 (.0010 psi)2 + (.00437 psi)2 ep = 1 00448 psi eT = 1 0.12*F 24 e T = 1 0245'F Substitution into equation e .0245 1/2 2400 LR
=1[2( *N 74.7)2 + 2 ( 539.6 )2 ) 10 e = 1 0.0256%/24 hours LR 2.5 PRESSURIZATION SYSTEM Reactor building pressurization was accomplished by two electric motor-driven air compressors operating in parallel. These compressors, purchased for pressurization of the Oconee Reactor buildings also include after-coolers as integral equipment. The discharge from the compressors passes through a single air dryer which reduces the moisture content in the air prior to its ,
entry into the reactor building. The specifications for these components are I given in Table 2-3. l Three valves, LRI-15, LRT-16 and LRT-17 are used to control pressurization I and depressurization of the reactor building. The controls for these valves l are located in the test panel shown in Section 2.3. The pressurization system is shown schematically on Figure 2-15. l l 2-8
.
_ ~ . _ . __ __
.
.
Table 2-3 PRESSURIZATION SYSTEM EQUIPMENT No. Req'd Description 2 Air Compressor-Electrically Driven Centrifugal Type. Capacity of 2300 i scfm @ 80 psia. Joy Turbo-Air 20V2. I 2 After cooler (integral to compressors) Capacity of 2100 SCFM @ 14.4 PSIA, type "ES" - Fixed Tubesheet. Design pressure 150 psig; Basco: Size 22048 1 Air Dryer - Refrigerator type with inertial impingement separator. Capacity of 3750 scfm (100*F (sat.) Inlet) @ 100 Psig. Haa'e ison Model H-15. F 4
.
2-9
-
.
2.6 AIR RECIRCULATION SYSTEM The reactor building air recirculation system consists of four auxiliary fans and three reactor building cooling fans. The auxiliary fans take suction through ducts in the upper region of the reactor building and circulate it downward. The reactor building cooling fans take air from mid height in the reactor building and exhaust it through ductwork down to the lower levels in the reactor building. This is shown schematically in Figure 2-12. In addition to the above units which are normally availa';1e for air recir-culation, 8 reactor building heating units were temp :arily installed to , maintain RB temperature during depressurization. These units having capacity of 50 kw each were located on the ground level for ease of installation and removal. 2.7 STRUCTURAL INTEGRITY AND ILRT ORGANIZATION l l The personnel organization used for the Structural Integrity and ILRT Tests is shown on Figure 2-16. l 2.8 STRUCTURAL INTEGRITY AND INTEGRATED LEAK RATE TESTS PRESSURE CYCLE i 1 The pressure cycle for the Structural Integrity and ILRT Tests is shown on Figure 2-17. t i 2-10
* ~
, e i
TEXAS INSTRUM ENTS i I INCORPORATED 3eos aWPFaLo SPCEOway P O. DOE 64027 MOusTON. TEI AS ??OOG
, A. C. 7t a sPM, 939 6419 PRECISION PRESSURE GAGE CAllBRAil0N CHART ,,-..,..e BOURDoN Tutt CAPSULE ll PREClllON PRESSURE GAGE sense 6 as Openarske amasswas names sensa6 MO. *scoak NO esamine
._._4.264 _ _ _ _ o-lOQ_P.SIA Ovsm pag 3Swas itSTED TO 1888 1% 1:1 TYPE Ca6sSR4 TION STANDa#O 2 150 PSI P-16Qh-3121 C 'JCULaE ou T est.R*40=s
. c 6.t.Tg e... r "
nam 44.0 Derts .C
'
F. Dourtlac ! h/11/70
*TRUE TUst
- TRut Tugg i t TI l t 78
' PRE 55URE *oaRQ pgg$ g6 PRt55Unt CONSTANT ESS Rs l CONSTANT PSTA **"' "'**'"' 'P S H '" PSH ***'"'**'""
M H '' I 0_,0000 0,900 99.8224 98.560 1.01291 4 9911 4m888 1.02109 __9.9829 Q.781 1.02058 l 14.4734 14.677 1.02019 . 19 96h6 19 580 1 01964 _24.9557 24.487 1.01910
= 29. 9469., 2S_,393 1.01881 i
34.9380 134 alo 1.01830 i i _39.9292 39<226 1.01793 :
!
44.4209 44.148 1.01749 49.9112 49.072 1.01710 I _5h9023 54.000 1.01671 _ _59m8 334 l58 935 . 1.01626 64.8846 I 63.876 1.01579 69.8757 !68.816 1.01540
!
l 74,_8668 I 73.762 t ko_1498 i 7918579 l8_.Il0 I L .0 1 4 5 8
- i i '
_84.84901 83.663 > 1.01418I i ! l _89.8402 : 88.623 ' 1.01373 '
-
I 9h8313_93,584 ! 1. 01333.. I NOTES: ' True corrected pressures have been cerrected to stonderd grovity 980.665 cm / sec.a. Units of mercury are corrected to O' C. Un.ts cf 'woter are corrected to 20' C. . t Shou d '.nc Gage thermometer reading ever change odiust the temperature set poent potentiometer (refer to monuoi maintenance sectsoni er odd 0.013 ea of c ;c ecoding per deorce of centigrade positive deviction from the col.brot.on temperature and
. subtract for negative deviction. FIgg 3 1 -
. . .
., ,
. ,
*
* .
- p. i ..
.
.
Fivnters in Prect ion
~
.CCDC & NCMTHREJF COMPANV SUMNEYTOWN PlKE NORTH W/.LES. PA 19454*215 643 2ooo
*
. CALIBRAT10:1 REPORT
. .4 FOR .
,
,
RTD/ DIGITAL TEllPERATURE SYSTEM ,
~
. .o0o_
LT,N Order flo. 49201_ Duke Power Co. No. V-8149 . ,
.
The above designated-temperature measuring system, including l Lt,Il fluma tron, Ser ial flo. 1773462, HP 6181B Power Supply, Serial !!o.
.
.
OB0373, and 28 resistance thermometers, was adjusted in accordance with Section 3 3 0.0 of the supplied Operation lianual. Calibration was com-pleted July, 1970 by placing each of the resistance thermometers in a
- constant temperature bath in close proximity with a standard platinum
- resistance thermometer. Simultaneous readings of bath temperatures at approximately 60* F and 120* F measured with the platic.um resistance thermometer (Std. Temp. Deg. F) and the corresponding system digital read out (Temp. Deg. F) for cach of the resistance thermometers were found to be as follows:
Resistance Std. Temp. Temp. Diff. Std. Temp. Temp. Diff.
- Thermometer Dcg. F Deg. F Deg. F Deg. F Deg. F Dcg. F
,
.
-
'-[ 59.917 59 98 -;+0.06,3 120.000 120.06 +0.060 .
120.000 120.03 ' 4 60.005 10.11 +0.103 +0.030 59 997 60.11 120.000 120.01 +0.010 !. ,3 ' +0.113
/ 59 997 ,60.10 120.000 120.04 +0.040
-
,4 .
+0.103
,. ' 60.014 60.08 +0.066 120.000 120.06 +0.060 5'/ 60.08 120.000 120.04 +0.040
-
6 .59 984 +0.096 59 986 65.10 +0.11 4 120.000 120.05 +0.050 ! 7 4 J 59 965 60.05 120.000_ 120.11 +0.110
-
+0.085 59 986 60.09 +0.104 120.000 120.00 +0.'000 9
10' 59 956 60.01- +0.054 120.000 120.05 +0.050 l
'l l 60.041 60.08 +0.039 120.000 120.01-
,
+0.010 st 2 65.041 60.11 +0.06g 120.000 120.09 +0.090 120.09
'
1 60.043 60.14 ,+0.097 120.000 +0.090 l
,
60.043- 60.08 120.000 120.10 +0.100
,f 14 +0.037 2 Sheets FIGURE 2-2 Sheet il .
- C ADLE A DDR ES5 "LE E Df.MOftT H**
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. Duke' Power Co. No. W-8149 L6N Order No. 49201
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Resistance .Std. Temp *. Temp. Diff. Std. Temp. Temp. Diff. Thermometer Deg. F Dog. F. Deg. F Deg. F Deg. F D'eg. F
'
-16 60.059 60.I1 +0.05 120.000 120.09 40.09o I6
- 60.059 60.11 +0.051 120.000 120.07 +0.070 A7 60.036 60.06 +0.024 120.000 120.05 +0.050
! 48 60.041 60.13 120.000 120.08
+0.089 +0.080
-19 60.041 60.11 120.000 120.04 *
+ 0 063 +0.04o
~20 60.046 60.05 120.000
+0.004 119 96 -0.04o v2I . 59 996 60.04 +0.044 120.000 120.I1
"* +0.I1o 59 940 59 99 +0.05o 120.000 120.07 +0.07o
, . 23 59 970 60.00 +0.03o 120.000 120.05 +0.050
- 24 59 970 60.04 +0.070 120.000 120.11' +0.110
-25 59 963 60.04 +0.077 120.000 120.12 +0.120
,26 59 935
, 60.03 +0.095 120.000 120.10 40.100
~
27 60.011 60.12 +0.109 120.000 120.04
.
+0.040 28 60.014 60.10 120.000
+0.086 120.08 +0.080
- s 4.
The above calibration is, traceable to reference standards main-1 ~
,
tained by this Company and calibrated at regular intervals by the National Burcau of Standards. The applicable reference standards'were calibrated in July, 1969; N. B. S. Test No. 211.01/198737, December, 1969; Test No. , 199743 and September, 1969; Yest No. 211.02/199266.
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For the Executive Vice President - Operations >
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4
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R vig R. H. Verity Manager, Standards Laboratory
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2 Sheets
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Sheet #2
. July 21, 1970
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Tho'rmometer Serial No. 4502 Used on Mode 1992-52 Serial No.' 416-P '
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-100 70.696
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-90 72.945
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90 112.723 45.07
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100 114.898 50.01 110 117.068 -
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120 119.236 130 121.400 140 123.559: '
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150 125.716 . . 160 . 127.869
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170 130.018 . 180 132.164 , , ,
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190 134.306 j ', 200 , 136.445 , .
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( proper worLenanship soe rerted w i* hout anir to the Purda,cr on any m go Cambribe Speem. instrumeni rceurncJ to th tauon. tra.upurearson pre-pa J. wi:hin niner> Jas . of shipment. Dui: to the pretinon nature of C" .
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7 f Cambnhe spiem. instrumenet it 4. the prAc) of the Compang to pse atmost consideration in .mv et sose whsress the user is m t recessirg satn-f " factor) sersise froci the in.rtument purch.t cJ (, Cornronent, not nianufastur J b> Cambrid.:e %.<cm, .us h a, s acuum tubes. condensers lamp. weher in trumente etc . are not cosered S3 this estranry Q
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Howeser. such comroncati are carefu!!> sefeced and inspeceJ before use v, This warranty i af.o so J on an> instrument suhtected to mun e tampenng -^
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TABLE OF CONTENTS Section Pg 3 COMPUTER PROGRAM 3-1 i
3.1 INTRODUCTION
3-1 3.2 EXPLANATION OF PROGRAM 3-2 3.3 DEMONSTRATION OF PROGRAM 3-5 4 4 j , p 3-1
, __ -
. _
_ _
. 3 COMPUTER PROGRAM
'
3.1 INTRODUCTION
ine Contavunent Intecrated Leak Rate Program calculates the leak rate for a .us lear reas tar containment vessel. The program computes the leak rate a- a given time from input values of pressure, temperature, and vapor pres-sure. The leak rate, as a function of time, is determined by elemen:ary linear least-square methods. The Containment integrated Leak Rate Program is designed to allow the user to evaluate containment leak rate test results at the jobsite during contain-ment leak rate testing. Interim leak rate tes't reports may be obtained at anf time durini; the testing period. Each interim report consists of three
.
printouts. The first printout, called the total-time method, used the first and latest input data to compute leak rate. Each computed leak rate is stadstically averai:ed using a linear least-squares fit. Early in the test this method of computation gives indication as to whether or not the leak rate is ac c e ptable. A second printout, called the point-to-point computation, is also provided. The point-to-point method uses the data at a given hour and the data from the previous reading to compute leak rate. Each individually computed leak rate is then statistically averaged using a linear least-squares fit. The results of the two methods used indicates that either method is a satisfactory method for computing containment integrated leak -rates. Both methods of computing the containment leah rate are presented in ANS 7. 60. Standard far l Leakage-Rate Testing of Containment Structures. 'sowever, the total-time i method is recomme nded by the latest revision of INS 7. 60 and is designated j as the containment leak rate. ' The third printout is the trend report which gives a more concise and timely
- c. esc ription of test r.esults. In this printout the leak rate, reported as a funcion of time after the start of the test, is the least squarcs-fitted value at each reported time. For example, the leak rate at six hours .ts the,least squares -
fitted value computed for the total time method from all test data taken in the first six hours of the test. This report shows the trend ot' the data towards some predictable value.
.
'
P00R BR M 3-1
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3.2 LXlit.ANATION OF PROGRAM The Containment Integrated Leak Rate computer program computes contain-ment 14 ak rate usine the Absolute Method as outlined in ANS 7. 60, Standard for Leakaec Rate Testing of Containment Structures. At the sta n c! the program the basic data is entered which consists of:
- 1. Test title.
- 2. Number of report variables.
- 3.
- Report variable names.
- 4. Number of containment temperature points, vapor pressure points, and absolute pressure points to be entered.
- 5. Absolute pressure sensor tube constant.
- 6. Volume fractions assigned to each temperature and vapor pressure sensor.
The recorded data, which is used to compute the leak rate, is then entered. Recorded data consists of:
- 1. Temperature
.
- 2. Vapor pressure
- 3. Absolute pressure Temperature, pressure, and -apor pressure values are entered as read at the test panel, i. e. each temper .ure point is ente. red in F, pressure is entered in PSIA uncorret*ed for tubu constant, and each vapor pressure point is entered ,
in hygrometer meter units. If a temperature or vapor pressure sensor becomes i inoperable during the course of the te st, a value of zero is entered for that ! sensor's reading. The program will i:etect the zero reading and eliminate that sensor from the leak rate computation. After all data for a given time step is entered, a print-out summary of the measured data is provided. In the . Summary of Measured Data each temperature entry is printed out in F and each pressure and vapor pressure entry is printed out in PSIA. At this point the user is given an opportunity to check the data and correct any errors. If :.orrection of errors is not required the values of the repert variables may be entered, if desired.
- The report variable velues, such as outside temper ature, relative humidity
, , and 3 weather,.,ar,e,.ven.tered for information purpose.s only and do not enter
.. .
L t r.to:; th. . -e eontaintpentslea'k rate computations. ! j f B . s .' , s *# * * ! 3-2
-
.
Following the entry of report variables a Corrected Data Summary is printed out. This summary consists of the date, time, one average contain-ment temperature (corrected for volume fractions) and one average contain-n mt air pressure (corrected for vapor pressure and volume fractions). ' i bese corrected values of temperature and pressure are the values used in the containment leak rate computations. Basically the leak rate is computed as follow 3: PV = WgRTg (1) g , PY * # 2RT W 2 3
% leakage 24 (W i - V.' ) ) x 100 (3)
= L =
4 24 hours at Wi Substituting equation (1) and (2) into (3) yields: 7 2400 T1 P (4) L = (1 T2P2) at t
! where -
Wy, W2: weight of contained air at time ti and t2 respectively. T,T t 2
= absolute temperature of containment volume at time ti and t2 respectively.
P,P g
= absolute containment air pressure (corrected for vapor 2
pressure) at times ty and.t3 respectively, a = t2-tt in hours. Linear least-squre fitting is used to establish the value of leak rate at 24 hours. The leak rate as a linear function of time is: L a
- bt where -
2
" ' kL$t i g
-
$tg$t g Lg
-i i i i d
N$ti i
- ($ t i)2
.
3-3
-
.
b = N $ Li ti i
-g Li $t i
i d NQti - ( $ ti)4 i i Li calculated leak rate from equation (4) above at time t i. N number of leak rate calculations.
.
i ! l 3-4 i
_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . .
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3.3 DEMONSTRATION OF PROGRAM To enter the 13echtel CE635 time share system, dial the current telephone number and place the telephone receiver in the acoustical coupler on the data terminal. Enter the user ID and password as requested and continue sign or. procedure as illustrated in Figure ZA. The return key on the terminal is hit after each entry and is also used as a "NO" answer. If at any time an error is entered and detected prior to hitting the return key, it may be corrected by hitting an "@". This deletes the previous character. If multiple characters are to be corrected enter the appropriate number of "i 's " . For example, an entry of XYZ@sTU is equivalent to XTU. (See Figure 2D, T3). Also, prior to a carri' age return, the entire line may be deleted by depressing the " CTRL" key and then, holding the " CTRL" key down, depressing the "X" key. (See Figure 2F, TS). When entering the time use military time, i. e. , 1345 for 1:45 p.m. The date is entered in four digits; the first two are the month, the last two the day. For example, 0704 is July 4th. The general flow of user's decisions is shown in the flow chart in Figure 1. The first decision to be made is whether or not a restart of the previous problem is desired. If the previous, run terminated normally and the sign-off was properly executed, the run may te continued by entering more data. If a restart is requested, the next keyboard entry will be current values of time, date, temperatures, pressure and vapor pressure. A new problem start requires that basic data be supplied to the system. This basic data includes title information, number of report variables, name of report variables, number of temperature points, number of pressure points, pressure constant, number of vapor pressure points and volume fraction associated with each temperature and vapor pressure point. After entering the basic data, it is possible to enter averaged values of temper-ature and pressure from previous runs. (See Figure 2H. ) If this option is selected, enter data as directed by the system. After ertry of this data, the user may request an interim or trend report. After each report the user may select a new first data point for least-square data fitting. This is accomplished by entering the new start time as directed by progr'am output to the terminal typewriter. When the system requests current values of time, temperature, and pressure. the user enters data as directed by the program. After completing data entry. a summary is printed out for the user's verification of data correctness. If there are errors detected by the user, the user will be given the opportunity to correct the errors. After the user certifies the data as entered, a summary repvrt of time, average temperature, and average pressure is crinted. This 3-5
__
.
.
.
!
is the data to be used in subsequent runs if the option to enter previous data is selected. After entry and certification of data, the user is given the option to obtain an interim report, trend report, or terminate. If he selects a report, a report in the format of Figure 2N is produced. After each report the user may choose to terminate the run or continue by entering more data. EXAM PLE Figure No. 2 is an example of program utilization for computing containment leak rate. The initial sign-on procedure changes' periodically. Consult Bechtel Startup personnel for information. When the asterisk appears "RUN" is entered. Since this example is an initial start, a reatart is not possible and the basic data is entered. (See Figure 2A. ) Recorded values of containm,ent temperature, pressure and vapor pressure are entered as requested for the given time. The user is then given the option to change any data. A Summary of Measured Data is the printed. The user is again given the option to change any data. Report variables are then entered if desired. The Corrected Data Summary values are then printed (See Figure 2C). The above procedure is repeated until termination of the program or until a report is requested. In Figure 2G the program is terminated. Previous data is not saved. The program is started again in Figure 2H. Since data was not saved from the previous run a restart is not possible. The basic data is re-entered. Previous data is entered from the " TEMP. AND PRESS. CORRECTED DATA
SUMMARY
" printouts on Figures 2C, 2E and 2G. Additional data points are entered for times 1800 and 1830. An Interim Report is requested. This report includes the previous data plus the additional data. Following the Interim Report new data is again added. (See Figure 2L. ) An Interim and Trend Report is requested which includes the latest data. (See Figures 2N and 20. ) An Interim Report is then requested using a new start time (Figure 2P). The program is then terminated. To facilitate program restarts, the basic data and previous summary data can be put on tape. When basic data or previous data is called for in the program the tape is run thereby saving considerable time. It is not feasibic to demonstrate all possible combinations of the user's input
- requests. However, the typewriter data terminal instructions to the user are
, an adequate guide for proper use of the program. f
.
r l 3-6
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CONTAINh1ENT INTEGRATED LEAK RATE TEST PROCEDURE COMPUTER PROGRAM LOGIC DIAGRAhi SIGN ON (Figure 2A) 1r NO ( RESTART 7 ' , [ 1r w E N I Elt TIME, DA TF/ EN TER BASIC DATA [ ] OF LAST DA TA (Fieure 2A) q, ENT ER NEXT T Eh1P, qr * ^ " NO (Figure 2B) ENTER PREVIOUS /'
^
V A LUES? YES 1r 3 ENTER CORREC r!ON
,r ( ERROR? ]
ENTER CORRECTED gg @\ (Figure 2E) ,{
SUMMARY
DATA (Ficure 2H) ir
SUMMARY
OF MEASURED ,
'
j [ T 1r DATA (Figure 2B) I TREND REPORT?] NO i 1r 1r j
, TR E'JD ( ERROR ]YES
! R E POR '! NO 1r NO (INTERIUM REPORT? \ ENTER REPOI E V ARIAB LES/
YES 1r V jIN FERIUM REPORT CORRECTED DATA (Figure 2K)
SUMMARY
(Figure 2C) . l [ RESPONSE] R EQUIR EDJ NEW STA T TIME?) D.PUT YES R EQU IR E D 1r GTER NEW STAR
- l TIME (Figure 2N) 1r 1r ( li>RINFO'Tl j
;
'
(T ER MINA T E' ]O
; YES i
1r l i SIGN OFF (Figure 2(is
;
e Figure 1
_ - _ _ _
.
USER ID- J L PASSWORD-- SECC5BMBEFUR SYSTEM ? FORT OLD OR neb- SIGN
"#
REA DY ORUN I F THI S I S A RESTART ENTER YES
= 9 ENTER TITLE OF LESS THAN 28 CHARACTERS J b = DEMONSTRATION OF PROGRAM ENTER NO. OF VARIABLES TO BE PRINTED ON EACH INTERIM REPORT = 2 ENTER 2 VARI ABLE NAMES OF LESS THAN16 LETTERS ENTER VARI ABLE I a OUTSIDE TEMP ENTER VARI ABLE 2
- WEA TH ER ENTER NO.0F TEMPERATURE POINTS
= 5 ENTER TH E NO . OF PRESSURE POINTS = 1 ENTER PRESSURE CONSTANT 8A##C = DATA EN T ER TH E N O . OF VAPOR PRESSURE POINTS a 2 ENTER VOLUME DECIMAL ASSOCI ATED WITH EACH TEMP ERATURE VOL . FRAC. TEMP. I a .400 VOL. FRAC. TEMP. 2 = .200 VOL. FRAC. TEMP. 3 = .200 VOL. FRAC. TEMP. 4 s .100 VOL. FRAC. TEMP. 5
, = 100 ENTER VOLUME DECIMAL ASSOCI ATED WITHVAPOR PRESSURE VOL. FRAC. VAPOR PRESS. I a .600 VOL. FRAC. VAPOR PRESS. 2 if e .400 ENTER PREVIOUS VALUES OF TIME AND AV. TEMP. AND PRESS. ? IF SO ENTER YES o l l l , Figure 2A
-
.
.
ENTER PRE' 10US VALUES OF TIME AND AV. TEMP. AND PRESS. ? IF SO ENTER YES
=
!.'J ! E P TIME,DATE
= 1600,0620 INTER S TEMP. READ.
! l
= l *e *V T 3
= ..N T 3
= (**.03 T 4
= ,,.c T 5
= 75.n3 ENTER 1 PRESS. IN PSIA P 1
= 9C.966 ENTER 2 VAP. PRESS. IN MILV VP 1
= 4 65 VP 2
= 4 70 CHANGE ANY DATA? IF SO ENTER YES
=
SUMMARY
OF MEASURED DATA AT TIME 1600 620 d TEMP 1 = 79 92 TEMP 2= 80 0/ TEMP 3= 79 65 summMY Oc M AsuffD MM , TEMP 4 = 76 82 1
'
TEMP 5= 75.03 TPRS 1 = 44.767 VPRS 1 = 0 331 VPRS 2= 0 210 9 , l CHANGE ANY DATA? IF SO ENTER YES s l ENTER REPORT VARI ABLES OUTSIDE TEMP
= 68 W EA Tn ER
= P A R TLY CLOUDY Figure 2B
,
.
-
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1600 DATE = 620 , TEMP = 79 100711 PRES = 44 484020. 9 TERMINATE 7 IF SD ENTER YES a TREND REPORT? IF SD ENTER YES
=
INTERIM REPORT? IF SO ENTER YES
=
ENTER TIMES DATE
= 1630 0620 ENTER S TEMP. R EA D.
T 1
= 80 21 T 2 8 80 25 T 3 a 79,82 T 4 = 76 79 T 5 7S.17 ENTER I PRESS. IN PSIA P 1 = 90 988 ENTER 2 VAP. PRESS. IN MILV VP 1 = 4 68 VP 2 s 4 72 CHANGE ANY DATA? IF SO ENTER YES a ,
SUMMARY
OF MEASURED DATA AT TIME 1630 620 l l I TEMP 1 = 80 21 ' TEMP 2= 802b TEMP 3= 79 82 ' TEMP 4= 76 79 TEMP 5= 75 17 TPRS I = 44 778 VPRS i = 0 335 VPRS 2= 0 212 Figure 2C l
.
- ,
CHANGE ANY DATA? IF SO ENTER YES
=
ENTER REPORT VARI ABLES OUTSIDE TEMP
= 67 b.EA TH ER ,
= PARTLY CLO UDY TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1630 CATE = 620 TEMP = 79 295071 PRES = 44 491686 TERMINATE? IF SO ENTER YES
=
j TREND REPORT 7 IF SO ENTER YES
=
INTERIM REPORT? IF SO ENTER YES
=
ENTER TIME,DATE
= 1700,0620 ENTER S TEMP. READ.
T 1
HO.34 T 2
= 80 98 T 3
= 19 8869 ctter cwre rso esa was - 7 f. 88
(*****r** "~'**'* " 79.89 T 4 %
= 77,16 '
T 5
'
= 7be42 ENTER I PRESS. IN PSIA P 1
= 91 010 ENTER 2 VAP. PRESS. IN MILV VP 1 .
= 4 66 VP 2-
= 4.73 Figure 2D
-
._ _ _ _
, .
U CHANGE ANY DATA? IF SO ENTER YES = YES EN TEli VARI ABLE NAME ( TIME TEMP, PRES, VAPS, TBASE), ITS NUM6ER (1,2,...), AND I TS VALUE. FOR EXAMPLE: TEMP,3,9 5 3 OR TIME, 1100,0927 OR TBASE,,74 0 aW44rc no4/ IF TEMP RASE CHANGE ENTER FIRST.bHEN FINISHED ENTER LAST,, = TEMP, 4,77 16 = LAST , y CHANGE ANY DATA? IF SO ENTER YES =
SUMMARY
OF MEASURED DATA AT TIME 1700 620 TEMP I = 80 34 TEMP 2= 80.d4 TEMP 3= 79 89 TEMP 4 = 77 16 TEMP 5= 75 42 TPRS 1 = 44 789 VPRS I = 0 333 VPRS 2 = 0 213 CHANGE ANY DATA? IF S3 ENTER YES a ENTER REFORT VARIABLES OUTSIDE TEMP
= 65 kEA TH ER a CL EAR TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1700 DATE = 620 TEMP = 79 427569 PRES = 44 503709 TERMINATE? IF SO ENTER YES REND REPORT? IF SC ENTER YES INTERIM REPORT 7 IF SD ENTER YES o Figure 2E
. -_-_ _. _ _ _ _ _ _ - - - - _ _ _ _ _ . _ _ _ _ _ _ _
* -
,
.3 ENTER TIMEsDATE
= 1730,0620 ENTER S TEMP. READ.
1 I
= 30 25 T 2
= 80 43 T 3
= 80 13 T 4
= 77 30 T S
- 72 5 DEL 79 DEL VAtur HL 7 f os 7f,2G f mnt a Dm M .
15 26 ENTER 1 PRESS. IN PSIA .
- P 1
= 91 030 EN TER 2 VAP. PRESS. IN MILV VP 1
= 4 69 VP 2
= 4.73 CHANGE ANY DATA? IF SD ENTER YES l
SUMMARY
OF MEASURED DATA AT TIME 1730 620
,
TEMP 1 = 80 25 TEMP 2= 80 43
- TEMP 3= 80 13 TEMP 4= 77 30 TEMP 5= 75 26 TPRS 1 = 44 798 #
VPRS 1 = 0 336 VPRS 2= 0 213 CHANGE ANY DATA? IF SD ENTER YES
=
ENTER REPORT VARI ABLES OUTSIDE TEMP
= 62
. WEA TH ER
= CLEAR Figure 2F
.
__. _ _ _ _ _ _ _ _
.
.
9 I i T EMP . AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1730 DATE = 620 1 TEMP = 79 467552 PRES = 44 511171
<
d , TERMINATE 7 IF SO ENTER YES
= YES PROGRAM STOP AT 2590
- BYE o
coTIME SHARING 8FF AT 15 324 ON 07/09/70
,
t
.
d l ! l , t I I l i Figure 2G l l
. . _ _
*
,
. USER 10 - PASSh0RD-- 33BETBwTEPSA SY STEM ? FORT CLD JR NEh- . READY sRGN IF TH I S IS A RESTART ENTER YES ENTER TITLE OF LESS THAN 28 CHARACTERS
= DEMONSTRATION OF PROGRAM ENTER NO. OF VARI ABLES TO BE PRINTED ON EACH INTERIM REPORT
= 2 ENTER 2 VARI ABLE NAMES OF LESS THAN16 LETTERS ENTER VARIABLE 1
= OUTSI DE TEMP 2
,
ENTER VARIABLE
= L EA TH ER ENTER NO.0F TEMPERATURE POINTS )
= 5 1 EN TER TH E NO . OF PRESSURE POINTS
.
- I ENTER PRESSURE CONSTANT EN TER TH E NO . OF VAPOR PRESSURE POINTS
=2 ENTER VOLUME DECIMAL ASSOCI ATED WITH EACH TEMP ERA TURE VOL. FRAC. TEMP. 1
= .400 VOL. FRAC. TEMP. 2
= 200 VOL. FRAC. TEMP. 3
= 200 VOL. FRAC. TEMP. 4
= .100 VOL. FRAC. TEMP. 5
= .300 ENTER VOLUME DECIMAL ASSOCI ATED WITHVAPOR PRESSURE VOL. FRA C . VAPOR PRESS. 1
= .600 VOL. FRAC. VAPOR PRESS. 2
= .400 ENTER PREVIOUS VALUES OF TIME AND AV. TEMP. AND PRESS.? IF SO ENTER YE
= YES ENTER TIME, DATE, TEMP, PRESS kHEN FINISHED ENTER 9999,,,, FNTER PREVaAs
= 1600,0620,79 100711,44 484020 VALUES
= 1630,0620,79 295071, 44 491686
= 1700,0620,79 427569,44 507 DEL 1700,0620,79 427569, 44 503709
= 1730,0620,79 467552, 44 511171 9
= 9999,,,,
ThENC REPORT? IF S0 . ENTER YES fMTERIM REPORT? IF S0 ENTER YES 3 Figure 2H
.
d ENTER TICE DATE o 1800,CC80 ' ENTER -5 TEMP. R E.A D . T I
= 80 00 T 2 '
a 80 56 Y 3
,
80.lb T 4
'
a 77 49 T 5 ^
= 75 56 EN TER I PRESS. IN PSI A P 1
'
= 91 0 48 ENTER 2 VAP. PRESS. IN MILV VP 1 a 4 68 VP 2
= 4 75 CHANGE ANY DATA 7 IF SO ENTER YES a
SUMMARY
OF MEASURED DATA AT TIME 1800 620 T EMP 1 = 80 60 TEMP 2= 80 56 TEMP 3= 80 15 TEMP 4= 77 49 T EMP 5= 75 56 TPRS I = 44 807 VPRS 1 = 0 335 VPRS 2= 0 215
'
.
{HANGE ANY DATA 7 IF SO ENTER YES ENTER REPORT VARIABLES OUTSI DE TEMP a 60 WEATH ER a CL EAR
.
TEMP
- AND PRESS. CORRECTED DATA
SUMMARY
'
TIME 1800 . DATE = 620 TEMP = 79 684725
-PLES = 44 520042 Figure 21
- _ _ _ _ _ _ _ _ _ _ _ _
_ .-
.
. TERMINATE 7 IF SO ENTER YES .
=
Th'EN D REPCRT? ~ I F SO ENTER YES INTERIM REPORT? IF SO ONTER YES ENTER TIME,DATE
= 1830,0620 ENTER S TEMP. READ.
T 1
= 80 65 T 2
= 80 70 T 3
= 80 31 T 4
= 77.b6 T 5
= 75 4S EN TER 1 PRESS. IN PSIA P 1
= 91 065 ENTER 2 VAP. PREbS. IN MILV VP 1
= 4.7 VP P
= t. 7 5 CHANGE ANY DATA? IF SO ENTER YES
=
SUMMARY
OF MEASURED DATA AT TIME 1830 620 TEMP 1 = 80 65 TEMP 2= 80 70 T EMP 3= 80 31 TEMP 4= 77 56 T EMP 5= 75 45 TPRS 1 = 44 816 VPFS 1 = 0 338 VPRS 2= 0 215
.
CHANGE ANY DATA? IF SO ENTER YES
=
ENTER REPORT VARI ABLES OUTSI DE TEMP
= 58-KEATHER
= CLEAR Figure 2J
.
.
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1830 DATE = 620 -
^ '
TEMP = 79 761937 PRES = 44 526821
.
TERMINATE? IF SO ENTER YES
=
THEND REPORT 7 IF SO ENTER YES a INTERIM REPORT? IF SO ENTER YES a YES DEMONSTRATION OF PROGRAM OUTSI DE TEMP = 58 WEATH ER = CL EAR TIME AFTER START OF TEST = 2 500 HR CONTAINMENT AVERAGE TEMPERATURE = 79 762 F CONTAINMENT AVERAGE PRESSURE = 44 527 PSI L EAK RATE BASED ON CONDITIONS AT 16 00 620 TIME TEMPERATURE PRESSURE LEAK RATE L EAK RATE 9 5% CONFIDENCE MEASURED CALCULATED LIMITS 16 50 79 30 44 49 0 904E+00 0 672E+00 -0 2 7 E+ 0 0 0 16E+01 17 00 79 43 44 50 0 39 4E+00 0 535E+00 - C . 31 E+ 0 0 0 14E+01 0 12E+ 01 ' 17 50 79 47 44 51 0.ll3E+00 0 399E+00 -0 42E+00 18 00 79 68 44 52 0 329 E+00 0 262E+00 -0 59 E+ 0 0 0 11 E+01 18 50 79 76 44 53 0 254E+00 0 12 6E+ 00 -0 82E+00 0 11 E+01 I F I T I S A SSUM ED TH A T TH E L EAK RATE IS CONSTANT: ' TH E M EAN IS 0 399E+00 1 THE STANDARD DEVIATION IS 0 121E+00 SXEW I S POSITIVC THE CALCULATED LEAA RATE AFTE3 2 50 HOURS CF TEST IS 0 126E+00 i: r w . e. ik i
-
.
.
9 L EAK RATE BASED ON POINT-TO-POINT CALCULATIONS PRESSURE L EAK RATE LEAK RATE 9 5% CONFIDENCE TIME T EMP ERATURE M EASURED CAL CUL ATED LIMITS 79 30 44.49 0 90 4E+00 0 415E+00 -0 24E+01 0 32E+01 16 50 0 29 E+ 01 17 00 79 43 44 50 -0 117E+00 0 335E+00 -0 22E+01 17 50 79 47 44 51 -0 449 E+00 0 254E+00 -0 22E+01 0 27E+01 18 00 79 68 44 52 0 977E+00 0 17 4E+00 -0 2 4E+ 01 'O.27E+01 44 53 -0 436E-01 0 9 40E-01 -0 2 7 E+ 01 0 29 E+ 01 18 50 79 76 IF I T I S ASSUM ED TH AT TH E L EAK RATE IS CONSTANT: TH E M EAN IS 0 254E+00 THE STANDARD DEVI ATION IS 0 258 E+00
$<EW IS POSITIVE TH E CALCULA TED L EAK RAlf AFTER 2 50 HOURS OF TEST IS 0 9 40 F-01 IF YOU WANT TEST DATA STARTING AT TIME OTHER THAN 16 00 ENTER YES
=
TERMINATE? IF SO ENTER YES
=
TREND REPORT? IF SO ENTER YES NTERIM REPORT 7 IF SO ENTER YES
=
ENTER TIME,DATE
= 1900,0620 ENTER S TEMP. READ.
T 1
= 80 67 i T 2
= 80 84 T 3
= 80 32 T 4
= 77 73 T 5
= 75 63 i ENTER 1 PRESS. IN PSIA l
' .
P 1
= 91 082 ENTER 2 VAP. PRESS. IN MILV
. VP 1
= 48 VP 2
= 48
.
Figure 2L
--
.
>
CHANGE ANY DATA? IF SO ENTER YES
=
SUMMARY
OF MEASURED DATA AT TIME 1900 620 T EMP 1 = 80 67 T EMP - 2= 80 84 TEMP 3= 80 32 TEMP 4 = 77 73 TEMP 5= 75 63 TPRS 1 = 44 824 VPRS 1 = 0 353
, VPRS 2= 0 220
! CHANGE ANY DATA? IF SO ENTER YES
=
ENTER REPORT VARI ABLES OUTSI DE TEMP
= $7 W EATH ER = CL EAR i-I
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
I TIME = 1900 DATE = 620 , TEMP = 79 836794
- l
, PRES = 44 524414 , TERMINATE? IF SO ENTER YES TREND REPO R T? IF SD ENTER YES 8 YES
.
>
--
. . . .. ,g Figure 2M
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.
DEMONS 1RA110N OF PROGRAM TI M E, DATE STAR 1 0F TEST 16 00 620 TIME AFTER START OF TES1 = 3 000 HR CONTAINMENT AVERAGE TEMPERATURE = 79 837 F CONTAINMENT AVERAGE PRESSURE = 44 524 PSIA ) 1 RENDS BASED ON TO TAL TIME CALCULATIONS HOURS DATA MEAN OF C AL C UL A T ED OF 1EST ENTRIES CALC. LR L EAK RATE 1 50 4 0 470E+00 0 746E-01 2 00 5 0 435E+00 0 134E+00 2 50 6 0 399E+00 0 126E+00 3 00 7 0 393E+00 0 187E+00 THE CALCULATED LEAK RATE IS 0 18 7E+ 00 THE MAXIMUM ALL0kABLE LEAK RATE IS 0 250E+00 THE LAST 0 DATA POINTS ESTABLISH A NEGATIVE SL OP E IF YOU WAN I 1SST DATA S1 ARTING AT TIME 01HER THAN 16 00 ENTFR YES . TERMINA1F IF S0 ENTER YES a TREND REPORl IF SO EN1ER YES
=
INTERIM REPCRT IF SD ENTER YES
= YES Figure 2 N , _ ,
.. . .. _ .-
-
DEMWNSTRAT193 SF PR80 RAM
- l ~
* ! OUTSIDE TEMP = 57 WEATH ER = CL EAR i
TIME AFTER START OF TEST = 3 000 HR CONTAINMENT AVERAGE TEMPERATURE = 79 837 F
= 44. 524 PSI CONTAINMENT AVERAGE PRESSURE-L EAK RATE BA3ED ON CONDITIONS AT 16 00 620 TIME T EMP ERATURE PRESSURE LEAK RATE L EAK RATE 9 5% CONFIDENCE MEASURED CALC UL A TED L IM I TS 16 50 79 30 44 49 0 904E+00 0 600E+00 -0 23E+ 00 0 14E+01 17 00 79 43 44 50 0 39 4E+00 0 517E+00 -0 25E+00 0 13E+01 79 47 44.51 0. l l 3 E+ 00 0 435E+00 -0 30 E+00 0 12E+01 17 50 0. l l E+ 0 !
18 00 79 68 44 52 0 329E+00 0 352E+00 - 0 38 E+ 00 79 76 44 53 0 254E+00 0 269E+00 - 0 50 E+ 0 0 0 10E+01 18 50 19 00 79 84 44 52 0 366E+00 0 18 7E+ 00 -0 65E+00 0 10E+01 i F I T I S A SSUM F.D TH AT TH E L EAK RATE IS CONSTANT: THE MEAN f. S 0 39 3E+00 THE STANDARD DEVI ATION IS 0 101E+00 SK EW I S PO SI TI VE 0 187E+00 l e t CAL C UL A T E D L EAK RATE AFTER 3 00 HOURS OF TEST IS LEAK RATE BASED ON POINT-TO-POINT CALCULATIONS TIME T EMP ERA TURE PRESSURE L EAK RATE L EAK RATE 95% CONFIDENCE MEASURED CAL CULATED LIMITS 16 50 79 30 44.49 0 904E+00 0 24tE+00 -0 21 E+ 01 0 2 6 E+ 01 79 43 44 50 -0 117 E+ 00 0 291 E+00 -0 19 E+01 0 25E+01 17 00 44 51 -0 449 E+00 0 341E+00 -0 18 E+ 01 0 2 4E+ 01 17 50 79 47 0 25E+01 18 00 79 68 44 52 0 9 77E+00 0 391 E+ 00 -0 17 E+ 01 18 50 79 76 44 53 -0 436E-01 0 44t E+00 -0 18E+01 0 26E+01 44 52 0 926E+00 0 491 E+00 -0 19 E+ 01 0 29 E+ 01 19.00 79 84
- F. ,
l' .'., I F I T I S A SSUM ED TH A T TH E L EAK RATE I S CONSTANT: THE MEAN IS 0 366E+00 , THE STANDARD DEVIATION IS 0 238E+00 i SK E h I S NEGATI VE
'
Figure 2 0 lbE CAL CUL A I F.D L E Ad wATE AFTER 3 00 HOURS OF TFST le 0 49th+00
-- - _ - _ _ - _ _ - _ _ _ _ _ _ _ - _ _ _ - _ _ _ _ _
e 1 _
+
IF YOU LANT TEST DATA STARTING AT TIME OTHER THAN 16 00 ENTER YES ' N f **
= YES ENTER NEW STARTING TIME IN HOURS CONTINUOUS FROM START OF TEST k #fM = 1700,0620 4 TERMINATE? IF SO ENTER YES =
i <END REPORT' IF S0 ' ENTER Y ES _ INTERIM REPORT? IF SO ENTER YES
* = YES DEMONSTRATION OF PROGRAM OUTSI DE TEMP = 57 LEA TH ER = CL EAR 4
TIME AFTER START OF TEST = 2 000 HR CONTAINMENT AVERAGE TEMPERATURE = 79 837 F CONTAINMENT AVERAGE PRESSURE = 44 524 PSI LEAK RATE BASED ON CONDITIONS AT 17 00 620 TIME TEMP ERATUR E PRESSURE LEAK RATE LEAK RATE 9 5% CONFIDENCE MEASURED CALC UL ATED L IMI TS 17 50 79 47 44 51 -0 449 E+00 -0 263E+00 -0 15E+ 01 0.lOE+01 18 00 79 68 44 52 C . 2 6 4E+ 00 -0 327E-01 - 0 12E+ 01 0 11 E+ 01 18 50 79 76 44 53 0 161 E+00 0 197E+00 -0 92E+00 0 13E+01 19 00 79 84 44.52 0 352E+00 0 427E+00 -0 8 5E+00 0 17E+01 IF IT I S ASSUMED TH AT TH E L EAK RATE I S CONSTANT: THE MEAN IS 0 823E-Ol j\(wn THE STANDARD DEVI ATION IS 0 157E+ 00 f] L Od EL I S NEGATI VE s . .h., 'r.i > . .c ' .qn
- -. - . L t.
.
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Figure 2P
_ _ _ _ _ _ - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - _ _ _ _ L EAK RATE BASED ON POINT-TO-POINT CALCULATIONS TIME TEMPERATURE PRESSURE L EAK RATE LEAK RATE 95% CONFIDENCE MEASURED CALCULATED LIMITS 17 50 79 47 44 51 -0 449 E+ 00 -0. l l 3E+ 00 -0 37E+01 0 35E+01 18 00 79 68 44 52 0 977E+00 0 197E+00 -0 30 E+ 01 0 34E+01 18.50 79 76 44 53 -0 436E-01 0 508E+00 -0 27E+01 0 37E+01 19 00 79 84 44 52 0 926E+00 0 818 E+ 00 -0 28 E+01 0 44E+ 01 IF I T I S ASSUMED THAT THE LEAK RATE IS CONSTANT: THE MEAN IS 0 353E+00 THE SiTNDARD DEVI ATION IS 0 308E+00 SK EW IS NEGATIVE
!HE CAL C UL A T E D '_ L A A RATE AF1ER P.00 HollRS OF TEST 15 0.blRt+00 IF YOU WANT TEST DATA STARTING AT TIME OTHFR in JI 17 00 ENTER YES
= TERMINATE? IF SO ENTER YES = YES PROGRAM STOP AT 2590
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J
. TABLE OF CONTENTS ,
Section g
'
4 FINAL TEST REPORTS,
SUMMARY
DATA AND CURVES 4-1 , 4.1 29.5 PSIG ILRT 4-1 4.2 29.5 PSIG VERIFICATION TEST 4-1 4.3 59 PSIG ILRT 4-1 4.4 59 PSIG VERIFICATION TEST 4-1 4-1 _ _ . _ . . . _ . _ . . ,_ .--. . - -
_,_ - _
. - . ,
.
4 FINAL TEST REPORTS,
SUMMARY
-DATA AND CURVES
- 4.1 29.5 PSIG ILRT The curve of Leak Rate versus Time is found on Figure 7. Supporting summary data is found on Figures 1 through 6. Individual data sets are given by Figures 8 through 49.
4.2 29.5 PSIG VERIFICATION TEST The curve of Leak Rate versus Time is given on Figure 54. Supporting summary data is given on Figures 49 through 53. Individual data sets are given by Figures 55 through 75. 4.3 59 PSIG ILRT The curve of Leak Rate versus Time is given on Figure 62. Supporting summary data is given on Figures 76 through 81. Individual data sets are given by Figures 82 through 123. 4.4 59 PSIG VERIFICATION TEST The curve of Leak Rate versus Time is given on Figure 129. Supporting summary dsta is given on Figures 123 through 128. 'ndividual data sets are given by Figures 130 through 150.
- Start times and test dates are given on each of the rollowing figures.
.
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= .1170,0 7.10, 79. n 37 (.9 h , 43 79 4? P 4, I
= 91.N 0 7 30, 7 9. ti16 N19, n3 79 40P /,1
= 2,%O.P730,79 796u94,43 793; ton,I
'
= Pf!! S,0 7 30, 79 79H 69h, 43 7921 :' t ,1
= PP 30,0 7 30,7'* . 74 8195, 43 79117 3, t
= 2245,0730,79,/00599,43 791173,1 2300,0~/ 30,79 7 69 499, 43 79117 3,1
= 2315,0730,79 773499,43.790156,1
= 2330,0730,79.7'/3098,43 790156,1 2345,0730,79.779696,43 789139,1
= P /:00,0730,79 7 72 496, 43 789139,1
= 0015,0731,79 760096,43 769139,1
= 0030,0731,74.761197,43 789139,1
= 00 45,0 7 31,79. 7 6819H, 43 789139,1
= 0100,0 7 31,79 7 62296,43 7h9139,1
= 0115,0731,79 75HS96,43 7b91 9,1
= O l 30,0 7 31, 79. ~< 66 69E , 43 76 9139,1
- 0145,0731,79 76'/697,43 769139,1
= 0200,0731,79 762799,43 789139,1
= O215,0731,7Y.75SO9P,43 7b9139,1
= O230,0731,79 75SI96, 43 7h9139,1 ,
= ODeb,0 7 31,79 7 5 4395, 43 759139,1
= 0300,0731,79 7 5369h,43 789139,1
= 031b,0731,79 767995,43 790156,1
= 0 330,0'i 31, 79 7 6 479 9, a3 79 015 6,1
= 0345,0731,79 776298,43 790156,1
= 0A00',0731,79 76589F,43 79117J,I
= 0415,0731,79 771098,43 791173,1
= 0430,0731,79 767497,43 791173,1
= 0445,0731 79 791n19,t3 792191,1
= 0500,0731,79 779096,43.~/v2191,1
= 0515,0731,79 787198,43 792191,1
= 0S30,0731,79 798398,/:3 79320%,1
= 0 545,0 7 31,79. '/H9 498, 43 79 422 ^,1
= 0600,0731,79 797797,43 794224,1
= 0615,0731,79 803497,43 794224,1
= 0630,0731,79 804699, 43 795241,1
= 0 6 45,0 7 31, 79.b l 3 49;,, 43 7V S2 41,1
= 0 700,0 ~/ 31, 79. 81729b, /.3 7 9 62 S8,1 a 0 715,0 7 31, 79.L*P.2 596, 43 79 62 ab e l
'
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ilMI A F 'l i i: L'I AF T OF '! P " T = 10. 000 HI? C .W'l A l 'h i .'! T A V F ! A t:E TI'; *;- f' A TUF:E = 79.HCP F CNN'lAIEUNT AVM: A6F >>%- :' '41 = 43 796 PSIA
'l l : E N I eASiD ON 101ol TINF CAL CI.L A T I ON $
HOURS DA li, MFAN OF CALCUL A TED OF TEST EN T: IFi CALC. LN L FAK RATE O.75 4 -0 2 43 E+ 00 -0.994F-Ol 1 00 5 -0.IbkEi00 0.IOSF-OI 1 25 6 - 0 . I S') E + 0 0 0 13E E-01 1 50 7 -0. I 4h E+ 00 0 211E-03
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R.50 11 - 0. -151 E - O I O.514'-01 3 75 IP -0. G 66E-O l O.497E-Ol 3-00 13 -0.x30F-01 O.4ESF.-01 3 25 14 -0 77 3h-01 O.499F-Ol 3 50 15 -0 72'/E-Ol O.487E-Ol 3 7L 16 -0 69 4F -01 O.464E-01
. 00 17 -0 656F-Ol O . 4/> S E- O l
'4 25 18 -0 622F-OI O.465E-Ol 4.SO 19 -0. 59 4F-O 1 0.4S3F-O1 4 75 20 - O . b~t 3 E- 01 O.429E-01 5 00 21 -0 553F.-01 0 40 7E-Ol
$.25 22 -0 535F.-O I O.3S?F-01 5 50 23 -0 515' h- 01 0 368E-Ol 5 75 24 -0 50')F-Ol O.354F-Ol
(. 00 25 -0 48HF-Ol O.33hE-Ol 6 25 26 -0. 472E-O ! O'.336E-OI 6 50 27 - 0 46 ^_ E- 01 0 31Ar-Ol 6 75 28 -0 453E-Ol O.296E-Ol 7.00 29 -0 443E-Ol O . 2 '/ 8 E- 01 - 7 25 30 -0 4331:-01 0 271E-01 7.SU 31 -0 42SF-O ! O.?bSE-01 s.7S 32 -0. 416F-O l O .2 47E- O I h.00 33 -0.407E-O!
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S
- UMMAFY OF MEASUPED DATA AT TIME 2130 730 EMP 1= 76.360 IEMP d = 78.680 TEMP 3= 78.380 TEMP 4 = 78.210 TEMP 5= 77.800 TEMP 6= 78.070 TEMP 7= 77.730 TEMP 8= 77.950 TEMP 9= 77,990 TEMP 10 = 77.990 TEMP 11 = 77,590 TEMP 12 = 75.790 TEMP 13 = 77.320 TEMP 14 = 7e,110 TEMP 15 = 77,170 TEMP 16 = 78.360 TEMP 17 = 78.270 TEMP 18 = 79.080 TEMP 19 = 83.600 TEMP 20 = 77.660 TEMP 21 = 7e,770 TEMP 22 = 79.660 TEMP 23 = 82,940 TEMP 24 = 85.300 TPPI 1 =
44.153
- PF 1 = 0.359 VFPS 2= 0.359 DIFF. PFE!S. = 1.000
.
-c IF '.U ENTEF iE:
.
rl' FFESS. COPPECTED DATA
SUMMARY
l i t
. = 2130 DATE = 730 T~"; = 79.837698 -
- .. r 43.794224 j IFF = 1.itiiiO l
1 RIG. 8
,
.. -
*
.
i
,
SUMMAPY OF MEASUPED DATA RT TIME 2145 730
..EMP 1 =- 76.390
. TEMP 2= 78.750
, TEMP 3'= 78.380 TEMP 4 = 78.190
- TEMP 5= 77.810 l TEMP 6= 78.030 TEMP 7_= '77.690
~
TEMP 8= 77.950 TEMP 9= 77.970 TEMP 10. ==- 77.990 4 TEMP 11 77.590 - > TEMP 12 = 75.850 TEMP 13 = 77.310 TEMP 14 = 78.110 TEMP 15 = 77.164 TEMP 16 = 78.320 TEMP 17!= 78>250 TEMP 18 = 79.050 TEMP 19 = 83.560 TEMP 20 = 77.660 TEMP 21 = 78.750 TEMP 22 = 79.600 TEMP 23 = 82.890 TEMP 24 = 85.280 TPPS 1 = 44.153
.PFS 1 x 0.359 VFPS 2= 0.359
- DIFF. FFESS. = 0.
.
=
CHArfGE AfW DATA IF SD ENTER YES i
.
TEMP. AfiD PRESS. COPFECTED DATA
SUMMARY
T8ME = .2145 DATE = 730-TEMP = 79.816499 FRES = ~ 43.79422yJn<n,.s ,, ll 1.6 M i .- ';l:0 67 ESS. DIFF = ~ ",,0 ;358630
.
9W[
. '
.u FIG.19-
. _. .. . . . - .
_ - - - _ _ __-_ _ _ _ _ - .
. , -
4 IUMMPPY OF MEASURED DATA AT TIME 2200 730 d '
.EMP 1 = 76.410 TEMP 2= 78.570 TEMP 3= 78.360 !
TEMP 4= 78.220 TEMr 5= 77,750 TEMP 6= 78.040 TEMP 7= 77.690 TEMP 8= 77,940 TEMP 9= 77.960 TEMP 10 = 77.990
. TEMP 11 = 77,530 j TEMP 12 = 75,340 TEMP 13 = 77,310 TEMP 14 = 78,100 TEMP 15 = 77.160 i
TEMP 16 = 78.320 TEMP 17 = 78.220 TEMP 18 = 79.010 TEMP 19 = 83.540 , TEMD 20 = 77.660 1 TEMP 21 = 78.720 TEMP 22 = 79.550 1 I TEMP 23 = Pr.870 I TEMP 24 = 8;.260 TPPS 1 = 44.152 v'P PS 1 = 0.359 VFPS 2= 0,359 DIFF. PFESS. = 1.000 , i I
-
CHANGE ANY DATA IF 30 ENTER YES l 1
-
TEMP. AND'PPESS. CORRECTED DATA
SUMMARY
- TIME = 2200
-DATE =' 730
- TEMP.= 79.796099 PEES.= 43.792208 reE55.:DIFF = 1.358830 FIG. 10
,
,
_
.
. .
-
SUMMARY
OF MEASUPED DATA AT TIME 2215 730 TEMP 1 = 76.430 TEMP 2= 78.690 TEMP 3= 78.370 TEMP 4= 78,210 TEMP 5= 7T.750 TEMP 6= '78.060
-
TEMP 7'= 77.690 TEMP 8= 77,940 TEMP 9, = . 77,980 TEMP 10 = 78.000 - TEMP 11 = 77.640 TEMP 12 = 75.850 TEMP 13 = 77.320 TEMP 14 = 78.100 TEMP 15 = 77,150 TEMP 16 = 78.300 TEMP 17 = 78,230 TEMF 18 = 79.000 TEMP 19 = 83,510 TEMP 20 = 77.690 TEMP 21 = 78,710 TEMP 22 = 79.600 TEMP 23 = 82.850 TEMP 24 = 85,230 PPS 1 = 44.151 VPPS 1 = 0.359 VPRS 2= 0.359 DIFF. PPESS. = 1.000
.
CHAriGE Atty DATA IF SD EriTER YES
=
TEMP. At4D PFESS. COPFECTED DATA
SUMMARY
TIME = 2215 _ DATE = 730 i TEMP = '79.798698 i E! = 43.792191 ,
- j. PPESS..DIFF = 1.358830.
l t 2:G. ll
,_ -
,
.
' ':f! MARY OF MEASURED DATA AT TIME 2230 730 .
t
' i
. . . t l.
t TEMP 1 = 76.450 TEito 2= 78.640 TEMP 3= 78.410 TEMP 4 = 78.210 TEMP 5= 77.750 TEMP 6= 78.060 TEMP 7= 77.700 TEMP 8= 77.950 TEMP 9= 77.970 TEMP 10 = 78.010 TEMP 11 = 77.630 TEMP 12 = 75.890 TEMP 13 = 77.310 TEMP 14 = 78.080 TEMP 15 = 77.160 TEMP 16 = 78.290 TEP'P 17 = 78.230 TEMP 18 = 79.000 TEMP 19 = 83.500 TEMP 20 = 77.680 TEMP 21 = 78.670 , TEM
- 22 = 79.600 1 TEMP 23 = 82.840 TEMP 24 = 85.240
. TFFS 1 = 44.150 i 1 PFT
'
1 = 0.359
/ DOS 2= 0.359 LIFF. FFESS. = 1.000 CH6hGE ANY DATA IF SO ENTER YES
=
, TEMP. AND PPESS. CORRECTED DATA
SUMMARY
__ T:n ;;;a 6v5 = 2250
-
Yg, k- DnT 7::a
-
Do rs = 73o
'
T ~m.
~ ^. .~ -- '.'.'..'.'.'
-
r?"n : 77, 7?? / f f i'/TES = f 3. 7f/ /13 h
- F C S . O A R = /, 3 f f g 3 0
, FIG. 12
_.
.
.
.
=
'.UMMARY OF MEASUPED DATA AT TIME 2245 730 .EMP 1 = 76.460 TEMP 2= 78.590 TEMP 3= 78.380 TEMP 4'= 78.200 TEMP 5= 77,740 TEMP 6= 78.060 TEMP 7= 77.710 TEMP Gu 77,930 TEMP 9 = ,77,990 TEMP 10 = 78.010 .
TEMP 11 = 77.610 TEMP .12 = 75.850 TEMP 13 = 77.320 TEMP 14 = 78.110 TEMP 15 = 77.160 TEMP 16 = 78.280 TEMP 17 = 78.210 TEMP 18 = 78.990
= 3.460 TEMP 20 = 77.690 TEMP 21 = 78.670 TEMP 22 = 79.580 TEMP 23 = 82.800 TEMP 24 = 85,210 TPPC 1 = 44,150 /PPO 1 = 0.359 '/P PI -
2= 0.359 DIFF. PPE05. = 1.000 CHAriGE AfiY DATA IF 50 ENTER YES = -TEMP. AffD PPESS. COPPECTED DATA
SUMMARY
7,AF - 2245" I I"'E = 22I5 b/rF : ~3b ' LCT - 736 7&M/2 = 7# Yf# 3 ? Y
~ 77 _ ;: , m:- =9
. fst&& s' f3. 71// 73 sit ?ss C irp,' =. J..?C88 30 FIO. 13
_ _ _ _ _ _ _ _ _ _ _ _ _ _ ..
$
.
- .. S'.c: Y CF MEAIUPED DATA AT TIME 2300 rou
, . , , . .
,. 1 . - = , . .. 4 y. .o
- .. =
-
4 :c.- -
,5
. . e. 0 0 T E '1: 3= Te,400
-
T a -
.,.c _E,4__
,
Mc . . .o
-- . m,31 0 2
1n IEM h 3['Sh
,'[ o 1" C' P.* O 4
E= .=. -
. . . <. 1 0 TIric e= 77.920 TEMo '= 77.970 TEMc 10 = 78.010 TEMP 11 =
77.650 TEMS 12 = 75.850 TEMP 1: = m oon TEMP 14 = 7[3l{{f TEMP 15 = 77.150 TEM' 16 = 78,270 TEMF 17 = 78,200 TEMF 16 = 7?,980 7EMP 19 = 83,450 TEMP 20 = 77.680 TEMP El = 78.710 {{MF i=MF 22 = 79.510 23= ?2.790 T ElP d4 = 85,190
- CI 1 =
44.15)
'
F C _~ 1 = 0.359 CP: - 2= 0,359
'
7--- - r- F E :. e. .. = 1.000 t
-
- cA GE ArW DATA IF IC ENTEP YEI 1
1 TE"F. At+D FFE!! . CCFFECTED DATA
SUMMARY
TIME = 2300
- :
~ - = . .: n.
T z..= = ,. m ,,
'= = "='" l
=. -- . . m . 1,, = 1 . . .sv
.
o., ,,, P00R ORlGINAL l l
~y+
.' i s . A+
l
.I
- .-
.- l
,
.
_
SUMMARY
[N MEASURED DATA AT TIME 2315 730
.EMP 1 = 76.480 TENP 2= 78:580 TEMP 3= 78.390 -
TEMP 4 = 78.230 TEMP 5= 77,700 TEMP 6= .78.040 TEMP '7.= '77.710
-
TEMP TEMP s= 77.930 9= 77,980 TEMP 10 =' 78.010 TEMP 11 = 77.620 ~~ TEMP 12 = 75.930 TEMP 13 = 77.340 TEMP 14 = 78.150 TEMP 15 = 77.150 TEMP 16 = 78.250 TEMP 17 = 78.200 TEMP 18 = 73,980 TEMP 19 = 83,440 TEMP 20 = 77.700 TEMP 21 = 78.710 TEMP 22 = 79.560 TEMP 23 = 82,770 TEMP 24 = 85.190 TPPS 1 = 44,149
/PPS 1 = 0.359 VPPS 2= 0.359 DIFF. PPESS. = 1.000 CHANGE ANY DATA IF SO ENTER YES
=
,
TEMP. AND PPESS. CDRRECTED DATA
SUMMARY
T8ME = 2315 DATE = T30, s ' e .i TEMP = 79.773499 FPES = 43.790156 , rFESS. DIFF = 1.35883 1 r m; ... e,m, . o. a r %,- %.O..
., -4
{q{. . { EY 5Y ' FIG. 15 1
.
~
*
=
- UNMACY CF MEASUFED DATA AT TIME 2330 730 TEMC TcMP 1 = 76.500 2= 78.740 TEMR 3= 79.420 TEMP 4 =
TEMP 78.230 5= 77.710 TEMP 6= 78.070 TEMP 7= 77,730 TEMP 8= 77.950 TEMP 9= TEMP 78.010 10 = 78.010 TEMP 11 = TEMP 77.640 12 = 75.930
- TEMP 13 = 77,350 TEMP 14 = 73,140 TEMP 15 =
TEMP 77.170 16 = 78.270 TEMF 17 = TEMP 78.200 18 = 7s,979 TEMP 19 = 33,410 TEMP 20 = 77,710 TEMF 21 TEMF
=
78.700 22 = 79,53o TEf1P 23 = TEMP e2.760 24 = 85.160 TFF: 1 = 44,149 VF o$ 1 = 0,359 VFP 2= o,359 LIFF. FFEST. = 1.000 1 1 1
-1 1
=
- HFr4GE Ftt'r DATA IF CD EtiTEP YES 1
4 i l t TEMF , Arid PEE!! . COPPECTED DATA SUMMAPY l T I f1E = 2330-IATE = T30 TEMF = 79.773098
~CEO = 43.790156 j p { jij,tf "i
-
* -
.
. ,
. , , ; s .; ,,,
4E!!. DIFF = 1.153:_:i$ U
?IG. 16
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-
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.
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it , /. = 'st.090
'i > :i t ' i = 7 7 . 't i. s) 11 .i ,. - "s'i.9 %
I t <t 9 : 'IS.000 i s v, 1 :# .: '/ t . . 40
'l F ' . t 11 ,
'/ 't . 6 3 G l t . .! 1* = *o u . '* H '
1F 13 = '/ 'i. 150 ie - 1 /: : */ P. 1 (,o it # IL = 7 ", . 1 s o l' ! . , . I t, -
's ' . *-
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s,
< F- I v. : *i: . -l 'l O
'! ' : i l '. = J.a.
'li
'
/
~ 7 . 'i l t ,
il , . 'l -
*i h . 'I 'i t -
e - 's ,* . E . . e 1
'
- .- < ;? . 't ;lC
'l - . p <. - s i. . i t,o ip 1 -: 44 1/-
- t. ; c: 1 : n . 3 h',
t l- , = U . J '/ 1: 5, F. , . f c. r . = 1. r.r. ;
.
- ( .Y i A l f. I !- ,
I- : 1 'J Y i-
'l i
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-
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+ -
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.
F1G. 17
- 8' ~~~
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.
.
_
.
SUMMAP'r CF MEA!UPED DATA AT TIME 2400 730 EMP 1 = 76.560 TEMP 2= 78.610 TEMF 3= 78.420 TEMP 4 = TG.260 TEMP 5= 77.700 TEMP 6= 78.070
- =- .%. c. . _ ~
,..<o0 TEMP 8= 77.950 TE*? 9= 77.990 TE:qP 10 = 78.040 TEMP 11 = 77.670 TEMP 12 = 76.000 TEMP 13 = 77.370 TE."P 14 = 78.180 TEMP 15 = 77.170 TEMP 16 = ??.260 TEMP 17 = 78.180 T E *!P 18 = 78..;80 TEMP 19 = S3.390 TEMP 20 = 77.740 TEMP 21 = 78.760 7EMP 22 = 79.540 TE:1P 23 = 82.730 TEMP 24 =
85.150
.
TPCI 1 = 44.148
' C' : 1 = 0.359
.::- o ..
- J wo
. .
.au.
LIFF. FFE55. = 1.000 CHAriGE ArW DATA IF 20 Er1TER YES
=
TEMP. PriD PFEH. COPFECTED DATA
SUMMARY
T it'E = 1400 I'~E = 7.20 T. r . e.c = .s . . e w: 2 .s p . e
>p c..
6
= , ,. ..g.
N ( o., g p q q E:::. D!cF = 1.15?830 11 l l'n FIG. 13 i- ,
, . ..
. -
'
'
.
SUMMARY
OF MEASUPED DATA AT TIME 15 731
.EMP 1 = 76.600 TEMP 2= 78.690 TEMP- 3= ~73,440 t
TEMP 4 = 78.260 TEMP 5= 77.670 TEMP 6= 78.090 TEMP 7* 77.750 TEMP 8= 77,950 TEMP 9= 77,990-TEMP 10 = ' 78. 060 TEMP 11 = 77.650 ' TEMP 12 = 75,930 - TEMP 13 = 77.370 TEMP 14 = 78.190 TEMP 15 = 77.180 ' TEMP- 16 = 78.260 TEMP '17 = 78,190 TEMP 18 = 78.950
- TEMP 19 = 83.350
, TEMP 20 = 77.760 4 TEMP 21 = ,78,730
- TEMP 22 = 79.490 j TEMP 23 = 82.700 TEMP 24 = 35.130
.
, TPPS 1 = 44,148
/PP! 1= 0.359 VFRS 2= 0.359 '
DIFF.'FFESS. = 1.000 4
;
4 CHANGE ArW DATA IF SD ENTER YES
- i t
; i
' TEMP..AND PFESS. CDRFECTED DATA SUMMAPY d TIME = 2415. .
- DATE =. -731:
TEMP,=' 79.760098 FCEI = 43.789139- . , '
-reESS.DIFFl$*lcIlCQq?f30P'3(%(( I i
, ,'una;T i g; ) d -,
.
~ -{';
s < !
- s . . ,
'
i [
-
FIY. 19
-. ;
.
-
S c -
._ __ _ _ - - _ . _ _ - . - -. _ _ _ _
,
.
' ' . . " G F '. OF t#EA!UFED DATA AT TIME 30 731 TEMP 1 = 6.590
'EMC 2= 79.750 TEMF 3= 7?,410 TEMP 4= 78.260 TEMF 5= 77.690 TEf1P 6 = 78.g,e0 2-epo ,, ,
, - e, ...O ten: 2= 77.940 TE r1 9=
TEMF 78.000 10 = 78.060 TEMP 11 = 77.660 TEf1P 12 = 76.000 TEMP 13 = 77,390 TEnP 14 = 78.200 TEMP 15 = 77.200 TEMP 16 = 78.270
'Ef'F 17 = 78,160 TEMF 18 = 73,970 TEMP 19 = 83.360 TEMP 20 =
TEMP 77.760' 21 = 78.750
'
'
TEMP 22 = 79.500 TEMP 23 = 82.680 T E '1R 24 = e5.110
, . _ .
*-
I = 44.143 ; 1
.
x'F C - 1 = 0,359 1 "F I 2= 0.359
- :Cr. FFEIC. = 1.000 C 4 r ".:E ArW DATF IF 10 ErlTEP YES
=
.
! TEtic . Ar4D cPE 5. CCPFECTED DATA COMMAPY
- TrE = 2.t 3 0
....
ah, t =
. , , . ,
,;i ye , . + n , , v . . .+ '. - W ^'- 4
-
'C r* C = 7?.7tI197
~ E? = Ab.?5$15?
F' G C '. * .
.
**Cp
.& .
- 4 .
'
. C.:5. .*, ..*- l.~p 71 % '
.u
__
*
.
'
=
SUMMARY
OF MEASURED DATA AT TIME 45 731 EMP 1 = 76.610
.EMP 2= 78.730 TEMP 3= 78.430 TEMP 4= 78.290 TEMP 5= 77.700
,
TEMP 6= 78.090 ' TEMP 7= 77.760 TEMP I,' 8.= 77.940 TEMP 9= 78,040 TEMP 10 = 78.060 TEMP 11 r 77.690 TEMP 12 = 76.000 '
. TEMP 13 = 77.420 '
TEMP 14 = 78.210 TEMP 15 = 77.190 $ TEMP 16 = 78.250 2 TEMP 17 = 78.190 TEMP 18 = 78.960 - TEMP 19 = 83.840 ~
'i TEMP 20 = 77.780 TEMP 21 =
78.770
- TEMP 22 = 79.540 TEMP 23 = 82.680 TEMP 24 = 85.100
, . TPFS 1 = 44.148
- l 'PP S 1 = 0.359
/PPS 2= 0.359 DfFF. PRESS. = 1.000
,
=
CHANGE ANY DATA IF-50 ENTER YES
!
1
.
TEMP. AND PPESS. CDPRECTED DATA
SUMMARY
T8ME = 2445 DATE = 731 TEMP = 7b?6819.8 FPEI=f',.IIUj!dj(
,'j43.789139. (1!$.rN,k NdJ1b, III. DIFF1= 1.358830 FIG. 21
-
, _ -. _
,
.
.
-.
-.
~4;ct?A.:V CF PEA 2UPED DATA AT TIME 100 731
. TEMS li= 6.650 TEN;' 2= 78.710 TEMF ?= 79.470
, TEMP '4 =-
78.270'
- TEMP 5= 77.700 TEN" 6= 78.100 TENF 7 =. 77,790 TEMP S= 77.960 TEMP 9= 78.030 TEMP 10 = 78.090 TEMP 11 =
77.670
- TEMP 12 = 76.070 TEMP 13 = 77.420 TEMP 14 = 78.230 TEMP 15 = 77.200 TEMP 16 = -78.270 TEMP 17 = 78.190
' EMF 18 = 78.960
,
'EMP !
TEi F 19 = 83.330 ! 20 = 77.780
- l i 'EMP 21 =
78.740 l l 7EMP 22 = 79.460 TEMC 23 = 82.660
'EMP 24 =
85.090
**! 1 =
44.148 l I ' '; C :
"
1 = 0.359 1 i-
'
< *;2 a= 0.359
, 5:.07 PCEIC. = 1.000 1 1
' I
;@r GE Art'y DATA IF SD EffTER YES
=
5
- TEPF, .At#D FFE00. CCFFECTED DATA-SUMMAPY.
4 A TIME = i=00
- ....T c. .= - .- o i
.-
. .
.
-
.:hc = . ; ,:::..::
, .. _mm .
E'." = 4 '. . ~::,5.
. 1 .5.'.
. ecE!! LIFF r '1.358830
-
-]!V,.
iu
,
T V .* a b is , -.h')' e i
. . . _ _ . _ _ _ _ . _ _ _ _ _ _ _ _ _ _ _ _ - .
-
.
b.
"UMMAPY OF~ MEASURED DATA AT TIME -115 .731- .EMP2 1 = .76.660 TEMP 2 =- 78.700 TEMP- 3=- - 78.500-TEMP 4 = 78.300 '
TEMP' 5=- 77.710 TEMP' 6= 78.090 TEMP 7 =- 77.790 TEMP S= 77.970 TEMP 9= 78.020 TEMP 10 = '78.090 TEMP ~ 11 = 77.700 ' TEMP 12 = 76.060 TEMP 13 = 77.440 TEMP 14 = 78.230 TEMP 15 = 77.220 TEMP 16 = 78.280 TEMP 17 = 78.170 TEMP 18 = 78.950 TEMP 19 = 83.290 TEMP 20 = 77.810 TEMP 21 = 78.750 TEMP 22 = 79.510 TEMP 23 = 82.620
. TEMP 24 = 85.070 TPPS 1 = 44.148 ,PPS 1 = 0.359 VPPS 2= 0.359 DIFF. PFESS. =. 1.000 CMANGE ANY DATA IF SD ENTEP YES =
TEMP. AND.PPE50. COPFECTED DATA IUMMPPY TZME = 2515 DATE = 731' TEMP = 79;758598~ PPE!-= 43.769139 . 210._DIFF = 1.358830
,
'- t/f N O 7- ;'"a-n ,frg.ya,9;$ i-
. -
una - IIG. 23-8
,
. =
cl.f1MAPY OF MEA!UPED DATA AT TIME 130 731
.EMP 1 = 76.660 TEf1P 2= 78.650 TEfP 3= 78.490 TEf1P 4 = 78.300 TEMP 5= 77.720 TEMP 6= 78.120 TEMP 7= 77.790 TEMP S= 77.970 TEMP 9= 78.050 TEMP 10 = 78.110 TEMP 11 = 77.730 TEMP 12 = T6.110 TEMP 13 = 77.440 TEMP 14 = 78.250 TEMP 15 = 77.240 TEMP 16 = 78.280 TEMP 17 = 78.210 TEMP 18 = 78.970 TEMP 19 = 83.300 TEMP 20 = 77.820 TEMP 21 = 78.760 TEMP 22 = 79.490 TEMP 23 = 82.620 TEMP 24 = 85.070 TPPS 1 = 44.148
/PP5 1 =
0.359 ; VPPS 2= 0.359 I l DIFF. FRESS. = 1.000 CHAf tC-E ANY DATA IF 50 EtiTER YES
=
TEMP. AfiD PPESS. COPPECTED DATA
SUMMARY
TIME = .i330 DATE = 731 Y TEftP = 79.766698 ' FRE: = 43.789139
, 22;. DIFF = 1.358820 TL S. 24
, . . _ _ _ _ _ _ - _ _ -
,
1 . o . CUMMARY OF MEASURED DATA AT TIME- 145 731
'EMP 1 = 76.680 EMP 2= 78.770 TEMP 3=- 78.530 TEMP 4-= 78.320 TEMP 5=- 77.710 TEMP 6= 78.120 TEMP 7= 77.830 TEMP 8= 77.970 '
TEMP 9= 78.050 TEMP 10 = 78.120 TEMP 11 = 77.720
! TEMP 12 = 76.110 TEMP 13 = 77.410 TEMP 14 = 78.240
' TEMP 15 = 77.230 TEMP -16 = 78.280 TEMP 17 = 78.190 TEMP 18 = 78.970 TEMP 19 = 83.290 TEMP 20 = 77.830 TEMP 21 = 78.760 TEMP 22 = 79.500 TEMP 23 = 82.610 l TEMP 24 = 85.050 l TFPS 1 = 44.148
' 'P PI 1 = 0.159 PPS 2= 0.359 DIFF. PRESS. = 1.000
- CHAriGE ANY_ DATA IF 20 EriTER YES
.
I TEMP. AND PFESS. CDPFECTED DATA
SUMMARY
TZME = .2545
.DATE = 731 TEhMk f/ 'f79"367 A37,y '
d j] ' ' ' bli j f
'r y : ? ; - FFE f =E fd3.789139.lijlQ_j ""ESS. DIFF = 1.358830 I
FIO. 25
.
- - _ _ _ _ _ _ . _ _ _ _ - _ _ _ _ _ _ _ _ _
'
,
-
a
$Uf1MFPY OF MEASURED DATA AT TIME 200 731
.EMP 1 = 76.720 TEMP 2= 78.730 TEMP 3= 78.520 TEMP .4 = 78.330 TEMP 5= 77.710 TEMP 6= 78.120 TEMP 7= 77.810 TEMP S= 77.990 TEMP 9= 78.050 TEMP 10 = 78.120 TEMP 11 = 77.760 i TEMP 12 = 76.130
, ' TEMP 13 = 77.460 TEMP 14 = 78.260 TEMP 15 = 77.250 TEMP 16 = 78.280 TEMP 17 = .78.190 TEMP 18 = 78.970 TEMP 19 = 83.260 TEMP 20 = 77.840 TEMP 21 = 78.740 TEMP 22 = 79.480 TEMP 23 = 82.590 TEMP 24 = 85.020 , TPP! 1 = 44.148
,
-
.PPS 1 = 0.359 VPPS 2= 0.359 DIFF. PPESS. = 1.000 l
!
CHANGE ANY DATA IF-50 ENTER YES
=
i l
)
l TEMP. AfiD PFESS. CORRECTED DATA
SUMMARY
TINE = 2600 DATE = 731 4
- TEMP - =. 79.762799 !
,
FREI = 43.789139
. 200. DIFF = 1.358830 TIG. 26 i
_ . _ _ _ .
.
.
=
IUMMARY OF MEASURED DATA AT TIME 215 731
#EMP 1 = 76.740 TEMP 2= 78.780 TEMP 3= 78.500 TEMP 4 = 78.320 TEMP 5= 77.710 TEMP 6= 78.130 TEMP 7= 77.820 i
TEMP 8 =- 77.980 TEMP 9= 78.070 TEMP 10 = 78.130 TEMP 11 = 77.770 TEMP 12 = 76.150 TEMP 13 = 77.450 TEMP 14 = 78.280 TEMP 15.= 77.250 TEMP 16 = 78.290 TEMP 17 = 78.180 TEMP 18 =' 78.940 TEMP 19 = 83.250 TEMP 20 = 77.840 TEMP 21 =- 78.780 TEMP 22 = 79.460 TEMP 23 =- 82.560
-TEMP 24 = 85.010 TPFS 1 = 44.148 IFF 5 1= 0.359 VPPI 2= 0.359 LIFF. FFE!3. = 1.000
.
CHANGE AfiY DATA IF 50-ENTER YES
=
,
l
, TEMF '. Arid PRESS. CORRECTED DATA SUMMAPY TZME = 2615 DATE = Til TENP = 79.755898
- FCES =- 43.789139 FeEis. DIFF = 1.358830
.
. FIG. 27
.
.
.
,,
-
- UMMAPY OF MEASUPED DATA AT TIME 230 731
*EMP- 1 = 76.720 IMP' 2= 78.720 TEMP 3= -78.530 TEMP 4 = 78.340 TEMP 3= 77.690 TEMP 6= 78.120 ,
-TEMP 7= 77.840 TEMP S= 77.990
-TEMP 9= 78.050 TEMP 10 = 78.150 TEMP 11 = 77.750 TEMP 12 = 76.160 TEMP 13 = 77.460 TEMP 14 = 78.270 TEMP 15 = 77.250 TEMP 16 = 78.290 TEMP 17 = 78.210 TEMP 18 = 78.950 TEMP 19 = 83.220 TEMP 20 = 77.880 TEMP 21 =-
78.760 TEMP 22 = 79.490 TEMP 23 = 82.550 TEMP 24 = 84.990 TFPI 1 = 44.148
' 'P P ! 1 = 0.359
,
PFS 2= 0.359 DIFF. PPESS. = 1.000 CHAriGE 6 tty DATA IF 50 EtiTER YES '
=
i TEMP. ArtD PRESS. CORFECTED DATA
SUMMARY
'
TIME = 2630 l DATE-= 731 TEMP = 79.755198 PPE! = 43.789139
!
raESC. DIFF_= 1.358830 FIG.'28 i .
-
-
.. .-
. . . . . . . .
. _ - - _.
- +
t ,
* >
1
.
=
4
'UMMPPY OF MEASUPED DATA AT TIME 245 731 iEMP 1 = 76.770
, TEMP 2= 78.660 4 ' TEMP 3= 78.530 TEMP 4'= 78.350 TEMP 5= 77.730 TEMP 6= 78.140 TEMP 7= 77.860 , TEMP 8= 77.990 j TEMP 9= 78.060 TEMP 10 = 78.170 TEMP 11 = 77.750 TEMP 12 = 76.160 l TEMP 13 = 77.470 3 TEMP 14 = 78.280
'
TEMP' 15 = 77.270 TEMP 16 = 78.290 TEMP 17 = 78.190 i TEMP 18 = 78.960 ! i TEMP 19 = 83.210
. TEMP 20 = 77.880 , TEMP 21 = 78.770 TEMP 22 = 79.450
> TEMP 23 = 82.550 TEMP 24 = 84.980 i
- TPPS 1 =
44.148 'l VFPS 1 = 0.359 i VPPS 2= 0.359 't i DIFF. PPESS. = 1.000 !
-
,
-
.
! I _ CHANGE ANY DATA IF SD ENTEP 'vES _ f
i l r TEMP. Arib PFESS . COPPECTED DATA IUMMAPY
.
- T!ME = 2645 i
i . DATE =. 731
.
[ -TEMP = 7'.9.754398 i. ' FREE.= 41.769139~ he.EIT DIFF = 1.358830 l i- ! L FIG. 29 <
-
z.
.
IUMMARY OF. MEASURED DATA AT TIME 300 731
*EMP 1 = 76.780 IMP 2-= 78.810
- , TEMP 3= 78.550 4- TEMP 4= 78.370 TEMP- 5= 77.710 TEMP 6= 78.140 TEMP 7= 77.870 TEMP- 8= 78.000 TEMP 9= 78.080 TEMP 10 = 78.170 TEMP 11 = 77.810
-TEMP 12 = 76.180 TEMP 13 = 77.520
! TEMP 14 = 78.320
!
TEMP 15 = 77.280 TEMP 16 = 77.310 TEMP 17 = 78.210 TEMP 18 = 78.950 TEMP 19 = 83.220 TEMP 20 = 77.880 TEMP. 21 = 78.780 TEMP 22 = 79.450 TEMP 23 = 82.530 TEMP 24 = 84.990 TPP5 1 = 44.148 "PP! 1 = 0.359 PRO 2=
~
0.359 DIFF. PPESS. =
,
1.000
.
=
CHAf4GE ANY DATA IF SD ENTER YES TEMP. AND PPESS. CORRECTED. DATA
SUMMARY
TIME = 2700- ! DATE = 7'31 TEMP'= .79.753698 FFEE = 43.769139 CCEII. DIFF~= 1.358830
-TIG. 30' l
. - . .
-
_ - _ _ _ _ _ _ _ _ _ _ _ _
=
- UMMAFY OF MEASUPED DATA AT TIME 315 731 E!1P 1 = 76.740 2MP 2= 78.850 TEMP 3= 78.570 TEMP 4 = 78.380 TEMP 5= 77.730 TEMP 6= 78.170 TEMP 7= 77.900 TEMP 8= 78.020 TEMP 9= 78.100 TEMP 10 = 78.200 TEMP 11 =
.-8.820 - $ gg g, g TEMP bpN TEMP 12 = 76.200 )
TEMP 13 = 77.500 TEMP 14 = 78.310 TEMP 15 = 77.280 TEMP 16 = 78.310 TEMP 17 = 78.210 TEMP 18 = 78.970 TEMP 19 = 83.200 TEMP 20 = 77.930 TEMF 21 = 78.810 ' TEMP 22 = 79.450 TEMP 23 = 82.520 TEMP 24 = 84.970 TPPS 1 = 44.149
'F F : 1 =
0.359 FPS 2= 0.359 LIFF. PFE55. = 1.000 .
=
CHAR 4GE AriY LATA IF SC EriTEP YES TEt1P . ArtD PFESS. COFFECTED DATA SUMMAFY T Ir1E = 2715 ' LATE = 731 TEMP = J' '-' :"- _
-
% 7t}e]G]qqq ghj FFE: = 43.790156
" E!:. LIFF = 1.158820 TI ' . 31
._ '
.
. -
o
-3UMMARY'DF MEASURED' DATA AT TIME 330 731 (EMF. 1= -76.760 TEMP 2-= 78.810 TEMP 3= 78.570
~
TEMP 4= -78.400 TEMP 5= 77.730 TEMP 6= 78.170 TEMP 7= 77.880 TEMP S= 78.020 TEMP 9= 78.090 TEMP 10 = 78.200 TEMP 11 = 77.840 TEMP 12 = 76.250 TEMP 13 = 77.500 TEMP 14'= 78.310 TEMP 15 = 77.310 TEMP 16 = 78.300 TEMP 17 = 78.220 TEMP 18 = 78.970 TEMP 19 = 83.190 TEMP 20 = 77.930 TEMP 21 = 78.800 TEMP 22 = 79.420 TEMP 23 = 82.510 TEMP 24 = 84.960 TPPS 1 = 44.149 VPPI 1 = 0.359 VPPS 2= 0.359 LIFF. PPESS. = 1.000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PPESS. CORRECTED DATA
SUMMARY
- TIME = 2730 DATE = T31 - TEMP = 79.764799 . FFEI = 43.790156 ! P - E I': . DIFF = 1.358830 l l FIG. 32 ;
;
I
-
.
=
-
;UMMAPY OF MEASUFED DATA AT TIME 345 731 TEMo 1 = 76.840 TEMP 2= 78.820 TEMP 3= 78.600 TEMP 4 = 78.410 TEMP 5= 77.760 TEMP 6= 78.180 TEMP 7=
TEf1P 8=
-'I_;c:- p .3{
TEf1P 78.030 9= 78.110 TEMP 10 = 78.230 TEMP 11 = P6.5;O 7},,$$ TEMP 12 = 76.300 TEf1P 13 = 77.520 TEMP 14 = 78.360 TEf1P 15 = 77.320 TEMP 16 = 78.310 TEMP 17 = 78.230 TEf1F 18 = 78,999 TEMP 19 = 83.180 TEMP 20 = 77.940 TEMP 21 = 78.790 TEf1P 22 = 79.460 TEf1P 23 = 82.490 TEMP 24 = 84.930 T:FI 1 = 44.149 '
./P P I 1 = 0.259 VFPI 2= 0.359 LIFF. FFEII. = 1.000 CHAf tGE AfiY DATA IF IO Ef1TEP 'vEi -
T Ef4P . AfiL FFEIS. COPFECTED DATA LUMMAPY T I f1E = 2745 EATE = 721
'
TEttF = ^' . . % 2 .s.- S - - + *
- 02Sb b FCE: = 43.790156 wE::. LIFF = 1.458620 FIG. 33
[
, . . . _ _ _ . . _ . _ _ - - .
-
. _.
=
~
i IUMMAPY OF MEASUPED DATA AT TIME 400 731
.
EMP 1-= 76.820 rEMP 2= 78.730 TEMP 3= 78.590 TEMP '4=' 78.430
. TEMP 5= 77.750 TEMP 6= 78.190 TEMP TEMP 7= Z .:: -
S =' ?S'.080 7 f
- 8l) ff/r TEMP 9= 78.120 TEMP 10 = 78.E20 TEMP. 11 = 77.860 TEMP 12 = 76.280 TEMP 13 = 77.550 TEMP 14 = 78.380 TEMP 15 = 77.310 TEMP 16 = 78.330 TEMP 17 = 78.220 TEMP 18 = 78.960 TEMP 19 = 83.160 ffS
'
, TEMP TEMP 20 21
=
=
~** can 78.790
.)
- TEMP 22 = 79.440 TEMP 23 = 82.490 TEMP 24 = 84.940 TPPS 1 = 44.150
" ' PP5 1 = 0.359 l
/PPS 2= 0.359 .
DIFF. PPESS. = 1.000
'
i
<
l _ CHAffGE ANY DATA IF IO- ENTEP YES l TEMP. AND PRESS. COFFECTED DATA SUMMAPY 1 TIME = 2800 DATE = 7:Il-TEMF = ~ . ; : :- : 79. 758878
'43.791173
.
, FFE': = ' E . DIFF = 1.158830
- FIG. 34 l
L
- . . ~
.'a _
.
.
.,- .
IUf1 MARY.0F'MEASUPED DATA AT TIME 415 731 , ~ EMP 1 =- 76.880 TEMP 2= 78.820-TEMP- 3= 78.590 1 TEMP 4= 78.430 TEMP TEMP 5= ' 77.750 6= '78.210 TEMP 7= 77.920 i~ TEMP 8= 78.040 TEMP 9= 78.130
,
TEMP 10 = 78.240 i TEMP 11 = 77.910' TEMP 12 = 76.260 TEMP 13 = .77.560 TEMP 14 = 78.400 t TEMP 15 =' 77.330 1 TEMP 16 = 78.330 , TEMP 17 = 78.230 ' TEMP 18 = 78.960 TEMP 19 =- 83.140 TEMP 20 = 77.980 ' TEMP 21 = 78.800 ' TEMF 22 = 79.450 TEMP 23 = 82.460
'
TEMP 24 = 84.910 TPRS 1 = 44.150-
~
PFI 1 = 0.359 VPPS 2= 0.359 j DIFF. PPESS. = 1.000 s
,
i CHANGE ANY DATA IF SD ENTER YES' i
- TEMP.. Ar4D FPE55. COPPECTED DATA
SUMMARY
4
- $
TIME = 2815 LATE '= 731
-
. TEMP = 79.771098
&
.
FPEI = .43.791173
.III. DIFF'= 1.358830
~
FIG. 35'
. - _ _ _ _ _ _ _ _ _ - _ _ _ - _ - - - _ _ _ _ _ _ , _ = _ . __
. .- , - , , - . .. .. .-
+ b+ -
.
CUMMAPY.0F MEASUPED' DATA 1AT. TIME 430 731
,
TEMP- 1 = 76.890 EMP' 2= -78.790-
.EMP 3= 78.640 TEMP .4 = 78.450
- TEMP - 5=- 77.750 TEMP 6= 78.210
< 4 ' TEMP 7 =. 77.940' TEMP 8= '78.040 TEMP' 9 =- 78.160 TEMP 78.250
- >
10 =
- TEMP -11 = 77.890 TEMP 12 = 76.320 TEMP 18 '= 77.550 TEMP 14 = 78.390 !
i' TEMP 15 = 77.340 ' TEMP 16 = 78.340 4 TEMP 17 = 78.230 l TEMP 18 = 78.560 TEMP 19 = 83.140 TEMP 20 = 77.980 , TEMP 21 = 78.020 ' TEMP 22 = 79.440 l
- TEMP
23 = 82.470 i TEMP 24 = 84.900 , 3
,
t TPPO 1 = 44.150 I 2 ' s VPPS 1 = 0.359 PCS 2= 0.359 i DIFF. FFESS. = 1.000
1 i i i
! ; -.. CHAh6E AfiY DATA IF 20 EttTER.YEi ; : ;
i-1 i 4 l i TEMP. AfiD'PFESS. COFFECTED DATA CUMMAPY TIME =. 2830~ 1 l DATE = -731-TEMP = 79.747497'
.
'-PF E; .= 43.791173 ' .
7-
;- FCE00. DIFF =- 1.356630-l-
4 b t - ?!1. 36- . 1
--_--_._!-u.. -- - . - -
._
- -
,.
'
CUMMAPY-DF.MEASUPED-DATA AT-TIME 445' 731 EMP- -1 = ~76.'930 EMP 2= 78.900 TEMP 3= 78.650 TEMP 4= 78.460 TEMP 5= 77.770 TEMP 6= 78.220 TEMP 7= 78.940 TEMP S= 78.060 TEMP 9= 78.150 TEMP 10 = 78.260 TEMP 11 = 77.920 TEMP 12 = 76.330 TEMP 13 = 77,580 TEMP 14 = 78,410 TEMP 15 = 77.350 TEMP 16 = 78.360 TEMP 17 = 78,240 TEMP 18 = 78,990 TEMP 19 = 83.120 TEMP 20 = 77.990 TEMP 21 = 78.790 TEMP 22 = 79.440 TEMP 23 = 82.460 TEMP 24 = S4,890 TPP2 1 = 44,151
'F P P 1 = 0.359 RCT 2= 0.359 DIFF. FRESS. = 1.000 CHAriGE ANY DATA IF IO ENTEP YEI
=
>
.
! 1_ r TEMF . AND FFE55. CCFFECTED DATA 'SUMMAFY
.
TIME =- 254S i DATE = 731 ,. TEMP = 79.791899
~
t
- EEC =' 43.792191 l -
.
.
l "EI . DIFF = 1. 356830 l IFIC. 37- ,
-
__
._. ._
-
_ . _ - -
. -4
.
SUMMAPY OF MEA!UPED DATA'AT_ TIME 500. 731-TEMP' 17=. 76.830
- EMP- -2= 78.860 (EMP' 3= 78.630 TEMP 4= .78.450-TEMP 5= 77.770~
TEMP- 6= _78.220 - TEMP.- 7= 77.950 TEMP 8=. 78.060 TEMP 9= 78.160 TEMP _10 = 78.260 TEMP 11 = .77.950 TEMP 12 = 76.360 TEMP 13 = 77.600 TEMP 14 = 78.410 TEMP 15 = 77.370 TEMP 16-= 78.360 TEMP- 17~= 78.260-TEMP-~18 = 78.980 TEMP 19 = 83.120- - TEMP 20 = 78.000 TEMP 21 = 78.850 TEMP 22 = 79.440 TEMP 23 = 82.440 TEMP 24 = 84.890 TPPS 1 = 44.151
' 'P PS
-
1 = 0.359 PPS 2= 0.359 DIFF. PPESS. = 1.000
= CHANGE AfiY DATA .IF 20 ENTER YE!
TEMP . _ Arid PPE!!.- CDPFECTED DATA IUMMARY TIME ~= 2900
~DATE = 731
' TEMP =- 79.779099-PRE! = E4$2.7921911 -
~
.
- PCEII. DIFFl=. I I .35SN 30
._I.-38
'
<
3.. _.
, . . - ,-.. . . . .- -
*
.
-
= .
. IUr'riAPY OF MEASUPED DATA AT TIME. 515 731.
.EMP 1.= 76.930 TEMP 2.= 78.900-TEMP 3 =~ 78.640 TEt1P 4= 78.470-TEMP 5= 77.800 TEMP 6= 78.240 TEMP 7= 77.990
~ TEMP 8= 78.070' s
TEMP 9= 78.180 TEMP 10'= 78.290 TEMP 11 = 77.940 TEMP 12 = 76.360 TEMP 13 = 77.590 TEMP 14 = 78.450 TEMP 15 = 77.380 ' TEMP 16 = 78.370 TEMP 17 = 78.270 $ TEMP 18 = T8.980 TEMP 19 = 83.100 - TEMP 20 = 78.020
!
TEMP 21 = 78.830 TEMP 22 = 79.450 i TEMP 23 = 82.430 j TEMP 24 = 84.880 { TP C.$ 1 = 4'.151-4
.PP2 1 = 0.359 VFFI 2= 0.359 i ;
DIFF. PPESS. = 1.000 l . 4
=
CFAriGE AtiY DATA IF CG EtiTER YE! $ .. 1 4
$
i
TEMP. At<D PFEIS. COPPECTED DATA SUr1MAPY I T I t1E , = 2915 DATE'= 731-
*
,
; TEMP = 79.767198 SEE .
= S3'.192191 t-
.
. EiP. DIFF~= 1.356830
! , t i i . l- TIG . -- 39 L l L.
., ._ . ,
4
*
- =
-
IUMMARY:OF MEASUPED DATA AT-TIME- 530- 731-Er1P 1 = 176.960 EMP- 2 =~-78.970
. TEMP. 3=- 78.640
<
-TEMP 4= 78.500 TEMP 5= .77.820 TEMP 6= 78.260
- TEMP' 7'= 78.000 TEMP- 8= 78.100-TEMP 9= 78.180 , TEMP TEMP 10 =- 78.310 11 = 77.960 . TEMP 12 = 76.420
,
TEMP 13 = 77.620 - TEMP 14 = 78.480
- TEMP ~15 = -77.380 TEMP 16 = 78.380 TEMP 17 = 78.280 ,
TEMP 18 = 79.000 TEMP 19 = 83.100 TEMP 20 = 78.050 TEMP 21 = 78.850 TEMP 22 = 79.450 TEMP 23 = 82.420 4 TEMP 24 = 84.860 4 - .! TPPI 1 = 44.152 l ,
'
' 'PPI 1 = 0.359 PPO 2= 0.359 i
DIFF. PPESS. = 1.000 i i CHAftGE ANY DATA IF 50 Et4TER YE!
- ,
!
*
! T EMP .~ Af4D PFESS. COPPECTED DATA SUMNAPY
-
I
!
TIrtE = - 2930.
-DATE =
'
j 731 i
- TEr1F = - 79.798398 FPEI.=. 43.793208
~ E."J.i . 'DIFF = 1.358830
, b i '
' ?IG.I40 e
1 8 _ _ _ - _ _ _ . _ _ _ ._
.
o .
!UMMARY OF NEASUPED DATA ~AT TIME 545 731 '
.'EMP 1' = 76.910 EMP 2= 78.T60 TEMP 3= 78.670 TEMP 4= 78.500 TEMP. 5= '77.780
-TEMP. 6= 78.260 TEMP 7= 77.940 TEMP 8= 78.100 TEMP 9 =. 78.190 TEMP 10 = 78.310 TEMP '11 = 77.950 TEMP 12 = 76.450 TEMP 13 = 77.640
>
' TEMP' 14 = 78.450 TEMP 15 = 77.890-TEMP- 16 = 78.400 TEMP 17 = 78.290 TEMP 18 = 78.990 TEMP 19 = 83.070 TEMP 20 = 78.030 TEMP :I: = 78.840 TEMP 22 = 79.450 TEMP 23 = 82.420 TEMP 24 = 84.870 TPPI 1 = 44.153
' 'P P S 1 = 0.359 FPS 2= 0.359 LIFF. FFESS. = 1.000 CHANGE Ah'r DATA IF.IG ENTEP YES =
TEMF. AND PFESS. CORFECTED DATA IUMMAFY TIME = 2945
. DATE := '731 TEND =- 79.789495~
FEEI = 4?.794224 ^
*
- E!!. DIFF = 1.359830 FIG. 41' 4
-
- y M
.
.
o
- UMMAPY OF MEASUPED DATA AT TIME 600 731 TEr1P 1 = 77.000 TEMP 2= 78.910 TEMP 3= 78.700 TEMP 4 = 78.530 TEMP 5= 77.810 TEMP 6= 78.280 TEMP 7= 78.010 TEMP 8= 78.110 TEMP 9= 78.200 TEMP 10 = 78.330 TEMP 11 = 77.960 TEMP 12 = 76.440 TEMP 13 = 77.640 TEMP 14 = 78.500 TEMP 15 = 77.410 TEMP 16 = 78.400 TEMP 17 = 78.320 TEMP 18 = 78.990 TEMP TEMP 19 = '83.060 20 = 78.070 EMP 21 = 78.840 TEMP 22 = 79.440 TEMP 23 = 82.400 TEMP 24 = 84.830
'PPS 1 = 44.153 VPP ' 1 = 0.359
'.!P P S
.
2= 0.359 LIFF. PPE!!. = 1.000 CHAR 4GE ArW DATA IF 20 EttTEP YE5
=
TE*1P . Arid PFESS. COPPECTED DATA SUMMAPY TIME = 1000 DATE = 7?! TEMP = 79.797797 ace: = 43.794224 A*E :. DIFF = 1.156930 FIG. 42
.
9 % - i __ _ _ _ _ _ . - -
*
.
.
s
SUMMARY
OF MEASURED DATA AT TIME 615 731 TEMP 1 = 77 050 TEMP 2= 78 950 i TEMP 3= 78 690 TEMP 4= 78 530 TEMP 5= 77.840 TEMP 6= 78 300 TEMP 7= 78.030 TEMP 8 = 78 130 TEMP 9= 78 220 TEMP 10 = 78 350 TEMP 11 = 77 960 TEMP 12 = 76.450-TEMP 13 = 77 660 TEMP 14 = 78 510 TEMP 15 = 77 430 TEMP 16 = 78 420
- TEMP 17 = 78 310 TEMP 18 = 79 010 TEMP 19 = 83 070 TEMP 20 = 78 070 TEMP 21 = 78 830 TEMP 22 = 79 430 TEMP 23 = 82 373 TEMP 24 = 84 820 TPRS I = 44 153
- VPRS I = 0.359 VPRS 2= 0 359 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SC ENTER YES
,
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
- TIME = 3015
^ 'DATE = .731
' TEMP = 79 803497 i PRES = 43 7042R4 r l ! PRESS. DIFF = 1 358830 FIG. 43' L
-
g .
. - - -
.
* .
*
=
'
SUMMARY
OF' MEASURED DATA AT TIME 630 731 TEMP 1 = 77 060 TEMP 2'= 78 990 TEMP 3 =- 78 730 TEMP 4= 78 570 TEMP 5= 77 830 TEMP 6 = 78 300 j TEMP 7 = 78 040 TEMP 8 = 78 120 TEMP 9= 78.220-TEMP 10 = 78 350 TEMP 11 = 77 970 TEMP 12 = 76 440 > TEMP 13 = 77.680 TEMP 14 = 78 490 TEMP 15 = 77.430 TEMP 16 = 78 400 TEMP 17 = 78 300 TEMP 18 = 79 000 TEMF 19 = 83 060 TEMP 20 = 78 090 TEMP 21 = 78 860 TEMP 22 = 79 440 TEMP 23 = 82 380 TEMP 24 = 84 800 TPRS 1 = 44 154 VPRS 1 = 0.359 VPRS 2= G.359 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
.. TEMP. AND PRESS. CORRECTED DATA'
SUMMARY
TIME = 3030 DATE = 731
-TEMPc= 79 804699 PRES = 43 795241.
PRESS. DIFF =' l.358830-FIG. 44
-
U .
.
SUMMARY
OF MEASURED DATA AT TIME 645 731 TEMP 1 = 77 060 TEMP 2= 78 900 TEMP 3= 78.700 TEMP 4= 78 560 TEMP 5= 77.850 TEMP 6= 78 310 TEMP 7 = 78 070 TEMP 8= 78.I30 TEMP 9= 78 250 TEMP 10 = 78 360 TEMP 11 = 78 050 TEMP 12 = 76.460 TEMP 13 = 77.710 TEMP 14 = 78 530 TEMP 15 = 77 470 TEMP 16 = 78 430 TEMP 17 = 78 360 TEMP 18 = 79 000 TEMP 19 = 83 040 TEMP 20 = 78 090 TEMP 21 = 78 850 TEMP 22 = 79 470 TEMP 23 = 82 370 TEMP 24 = 84 820 TPRS 1 = 44 154 VPRS 1 = 0 359 VPRS 2= 0.359 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SD ENTER YES
=
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
-TIME = 3045 DATE = 731 TEMP = 79 813498 PRES = 43 795241 PRESS . DIFF = _l.358830 FIG. 4
.5
. . . ..
.
'I ,
*
=
SUMMARY
CF MEASURED DATA AT TIME .700 731 TEMP l.= 77 070 TEMP 2= 78 880 TEMP 3= 78.720 TEMP 4 = 78 570 TEMP 5= 77 840 TEMP ~6 = 78 320 TEMP 7 = 78.060 TEMP R = 7F.140 TEMP 9 = 78 250 TEMP 10 = 78.390 [ TEMP 11 = 78 030 ' TEMP 12 = 76.480 TEMP, 13 = 77.710 TEMP 14 = 78 570 TEMP 15 = 77.460 TEMP 16 = 78 430 TEMP 17 = 78.350 TEMP 18 = 79 030 TEMP 19 = 83.030 TEMP 20 = 78 120 TEMP 21 = 78 860 TEMP 22 = 79 470 TEyP 23 = 82.370 , , TEMP 24 = 84 800 TPRS I = 44 155 VPRS I = 0 359 VPRS 2= 0 359 DIFF. PRESS. = 1 000 CPANGE ANY DATA IF SO ENTER YES
= l 4
. TEMP. AND PRESS. CCRRECTED' DATA
SUMMARY
TIME = 3100 DATE = 731 ,
,
'
TEMP = 179.F17298- [ PRES = 43 796258 l
!
PRESS..DIFF'= l'.358F30 ' i
-
' fl. G . 4 6 ' . . .
-
-
.
0
*
SUMMARY
OF MEASURED DATA AT TIME 715 731 TEMP 1 = 77 090 TEMP 2= 78 920 TEMP 3= 78 790 TEMP 4 = 78.580 TEAP 5= 77 880 TEMP 6= 78 330 TEMP 7 = 78 110 TEMP 8= 78 150 TEMP 9= 78 280 TEMP 10 = 78 410 TEMP 11 = 78 070 TEMP 12 = 76.520 TEMP 13 = 77 710 TEMP 14 = 78 550 TEMP 15 - 77.500 TEMP 16 = 78 450 TEMP 17 = 78 360 TEMP 18 = 79 010 TEMP 19 = 83 030 . TEMP 20 = '8-140 TEMP 21 = .a.890 TEMP 22 = 79 450 TEMP 23 = 82 360 TEMP 24 = 84.780 TPRS I = 44 155 VPRS I = 0 359 VPRS 2= 0 359 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
_ TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3115
.DATE = 731 TEMP =. 79 822598
'FRES = ' 43 796258
'
,
PRESS. DIFF =- 1 358830 FIG. 47 L
_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ . __ _ - _ _ _ _ _
.
* .
. .,
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*
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st.,,.c> FIG. 46 j
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.
.
OCONEE'29 5 PSIG ILRT.VERIF 1100,0731,79'.866698,43 793802,1
- 1115,0731,79 875298,43 792573,1 1130,0731,79 879698,43 792785,1 1145,0731,79 878598,43 791556,1 1200,0731,79 881498,43 791556,1 1215,0731,79 890697,43 788036,1 1230,0731,79 898298,43 788036,1 1245,0731,79 895499,43 790539,1 1300,0731,79 906199,43 790539,1 1315,0731,79 906098,43 789522,1 1330,0731,79 912898, 43 788278,1 1345,0731,79 926497,43 788278 1 1400,0731,79 923298,43 788278,1 1415,0731,79 931897,43 788278,1 1430,0731,79 939999,43 787019,1 1445,0731,79 948699,43 788278,1 1500,0731,79 947998,43 787261,1 1515,0731,79 953598, 43 786244,1 1530,0731,79 966298,43 786002,1 1545,0731,79 973199,43 786002,1 1600,0731,79 980797,43 786002,1 9999,,,,,
,
.
FIG. 49 i
'
- R, e y. 2
'
t 1
,
._ _ _ _ _ _ _ _ . - _ _ _ _ _ _ '.
. OCONEE 29 5 PSIG ILRT VERIF TIME, DATE START OF TEST 11 00 731
.
, TIME AFTER START CF TEST = 5 000 HR CONTAINMENT AVERAGE TEMPERATURE = 79 981 F CONTAINMENT AVERAGE PRESSURE = 43 786 PSIA TRENDS BASED ON TOTAL TIME CALCULATIONS HOURS DATA MEAN OF CALCULATED OF TEST EN TRI ES CALC. LR L EAK RATE O.75 4 0 29 5E+00 0 201 E+00 1 00 5 0 268E+00 0 164E+00 1 25 6 0 282E+00 0 241E+00 1 50 7 0 28 6E+00 0 264E+00 1 75 8 0 270E+00 0 218 E+00 2.00 9 0 259E+00 0 191E+00 2 25 10 0 2 50E+00 0 176E+00 2 50 11 0 2 45E+00 0 173E+00 2 75 12 0 242E+00 0 173E+00 3 00 13 0 237E+00 0 167E+00 , 3 25 14 0 233E+00 0 162E+00 3 50 15 0 231E+00 0 163E+00 3 75 16 0 227E+00 0 158E+00 4 00 17 0 22 4E+00 0 156 E+ 00 4 25 18 0 222E+00 0 156E+00 4 50 19 0 220E+00 0 157E+ 00 4.75 20 0 219 E+00 0 157E+ 00 5 00 21 0 217E+00 0 157E+00'
. .
a THE CALCULATED LEAK RATE I'S 0.'157E+00' THE MAXIMUM ALLO L.ABLE LEAK RATE IS 0 177E+00 THE LAST I DATA POINTS ESTABLISH A N5GATIVE SLOPE
. -
. .
.
FIG. 50 Rev. 2
.
v
.
OCONEE 29 5 PSIG ILRT VERIF .
.
ABSOLUTE CALCULATIONS
.
TIME, DATE START OF TEST 11 00 731 TIME AFTER START OF TEST = 5 000 HR CONTAINMENT AVERAGE TEMPERATURE = 79 981 F CONTAINMENT AVERAGE PRESSURE = 43 78 6 PSI A LEAK RATE BASED ON TOTAL TIME CALCULATIONS TIME TEMPERATURE PRESSURE LEAK RATE L EAK RATE 95% CONFI DENCE (PSIA) MEASURED CAL CUL ATED LIMITS 11 25 79 88 43 79 0 423E+00 0 277E+ 00 0 15E+00 0 40 E+ 00 11 50 79 88 43 79 0 227E+00 0 271E+00 0 15E+00 0 39E+ 00 11 75 79 88 43 79 0 235E+00 0 265E+00 0 14E+00 0 39E+00 12 00 79 88 43 79 0 189E+00 0 258E+00 0 14E+ 00 0 38E+00 12 25 79 89 43 79 0 338E+00 0 252E+ 00 0 13E+00 0 37E+00 12 50 79 90 43 79 0 304E+00 0 246E+00 0 13E+00 0 36E+ 00
- 12 75 79 90 43 79 0 175E+00 0 239E+00 0 12E+00 0 36E+00 13 00 79 91 43 79 0 177E+00 0 233E+00 0 12E+00 0 35E+00 13 25 79 91 43 79 0 182E+00 0 227E+00 0. l l E+ 00 0 34E+00 13 50 79 91 ' 43 79 0 203E+00 0 220E+00 0 10E+00 , 0 34E+ 00 j 13 75 79 93 43 79 &.207E+00 0 214E+00 0 98E-Ol 0 33E+00 - ,
'
14 00 79 92 43 79 0 185E+00 0 208E+00 0 91 E-01 0 32E+00 14 25 79 93 43 79 0 182E+00 0 201E+00 0 8 5E-01 0 32F+00 l
)
14 50 79 94 43 79 0 199E+00 0 195E+00 0 78 E-01 0 31 E+00 14 75 79 95 43 79 0 178E+00 0 189E+00 0 71E-OI 0 31 E+ 00 , 15 00 79. 95 43 79 0 180E+00 0 182E+00 0 64E-01 0 30E+00 FIG. 51 Rev.2
-
l
. .- - -______
<
. .
~ 15 25 79 95 43 79 0 188E+00 0 176E+00 0 56E-01 0 30E+00 15 50 79 97 43 79 0 193E+00 0 170E+00 0 49E-01 0 29E+00 15 75 79 97 43 79 0 190E+00 0 163E+00 0 41 E-01 0 29E+00 16 00 79 98 43 79 0 187E+00 0 157E+00 0 34E-01 0 28E+00 IF IT IS ASSUMED THAT THE LEAK RATE IS CONSTANTt-THE MEAN IS 0 217E+00 THE STANDARD DEVI ATION IS 0 645E-01 SK EW IS POSITIVE THE CALCULATED LEAK RATE AFTER 5 00 HOURS OF TEST IS 0 157E+00
.
M EASURED 1- EAK RATE COMPUTED FROM MEASURED VALUES TEMPERATURE AND PRESSURE CALCULATED LEAK RATE COMPUTED FROM LINEAR LEAST SOUARE FIT OF MEASURED LEAK RATES
/
.
* -
.
.>.- .,
..
,
.
.
*
'.
.
.
.
FIG. 52
. Rev.2
.
% .
L EAK RATE BASED ON POINT-TO-POINT CALCULATIONS ,
.
TIME TEMPERATURE PRESSURE LEAK RATE LEAK RATE 9 5% CONFI DENCE (PSIA) MEASURED CAL CUL A T ED LIMITS 11 25 79 88 43 79 0 423E+00 0 218 E+ 00 -0 46E+00 0 89E+00 . 11 50 79 88 43 79 0 317E-01 0 214E+ 00 -0 45E+00 0 88E+00 11 75 79 88 43 79 0 250E+00 0 211 E+ 00 -0 45E+00 0 87E+00 12 00 79 88 43 79 0 517E-01 0 208E+00 -0 45E+00 0 8 6E+00 , 12 25 79 89 43 79 0 936E+00 0 205E+00 -0 44E+ 00 0 85E+00 12 50 79 90 43 79 0 135E+00 0 202E+00 -0 44E+00 0 8 5E+00 12 75 79 90 43 79 -0 398E+00 0 198E+00 -0 4 4E+0Q u. 8 4E+ 00 13 00 79 91 43 79 0 191 E+ 00 0 195E+00 -0 4 4E+00 0 83E+00 13 25 79 91 43 79 0 221E+00 0 192E+00 -0 44E+ 00 0 83E+00 13 50 79 91 43 79 0 39 4E+00 0 189 E+ 00 -0 45E+00 0 82E+00 ' 13 75 79 93 43 79 0 2 42E+00 0 186E+00 -0 45E+ 00 0 82E+00 14 00 79 92 43 79 -0 567E-01 0 182E+00 -0 45E+00 0 62E+00 14 25 79 93 43 79 0 153E+ 00 0 179E+00 -0 46E+00 0 82E+00 14 50 79 94 43 79 0 420E+00 0 176E+00 -0 46E+ 00 0 82E+00 14.75 79 95 43 79 -0 121 E+ 00 0 173E+00 -0 47E+00 0 82E+00 15 00 79 95 43 79 0 211 E+00 0 169 E+ 00 -0 48E+ 00 0 82E+00 15 25 79 95 43 79 0 323E+00 0 166E+00 -0 49 E+00 0 82E+00 15 50 79 97 43 79 0 279E+00 0 163E+00 -0 50E+ 00 0 82E+ 00 9 15 75 79 97 43 79 0 123E+00 0 160E+00 -0 51 E+ 00 0 83E+ 00 16 00 79 98 43 79 0 135E+ 00 0 157 E+ 00 -0 52E+00 0 83E+00 IF I T I S A SSUM ED TH A T TH E L EAK RATE IS CCNSTANTt
'
THE MEAN IS 0 18 7 E+ 00 THE STANDARD DEVIATION IS 0 288E+00 SK Eb IS NEGATIVE . , THE CALCULATED LEAK RATE AFTER 5 00 HOURS OF. TEST IS 0 157E+00
.
FIG. 53'
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1
SUMMARY
OF MEASURED DATA AT TIME 1100 731 TEMP 1 = 77.300 TEMP 2= 79 090 TEMP 3= 78 900 , TEMP 4 = 78 770 TEMP 5= 78 020 TEMP 6= 78 500 TEMP 7 = 78 260 TEMP 8= 78 270 TEMP 9= 78 430 TEMP 10 = 78 590 TEMP 11 = 78 240 - TEMP 12 = 76 790 TEMP 13 = 77.920 TEMP 14 = 78 790 TEMP 15 = 77.650 TEMP 16 = 78 570 TEMP 17 = 78 470 TEMP 18 = 79 080 TEMP 19 = 82 850 TEMP 20 = 78 340 TEMP 21 = 78 900 TEMP 22 = 79.500 - TEMP 23 = 82 190 TEMP 24 = 84 600 TPRS 1 = 44 155 VPRS 1 = 0 361 VPRS 2 0 361 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1100 DATE - = 731 TEMP = 79 866698 PRES'= 43 793802 FIG. 55 PRESS. ' DIFF = 1 361287
..
-
.
. .
SUMMARY
OF MEASURED DATA AT TIME 1115 731 TEMP 1 = 77.370. TEMP ~ 2= - 79 090 TEMP '3=- 78 970 TEMP- 4 = 78 790 TEMP 5~= 78 020 TEMP 6 = 78 500-TEMP. 7 = 78 280 TEMP 8= 78 280 ' TEMP 9= 78 450 TEMP '10 = 78 600 TEMP 11 = 78 290 TEMP 12 = 76 800 TEMP 13 = 77 950 TEMP 14 = 78.750' TEMP 15 = 77.670 TEMP 16 = 78.590 TEMP 17 = 78 500 TEMP 18 = 79 100 TEMP 19 = F2 860 TEMP 20 = 7M.340 TENP 21 = 78 950 TEMP 22 = 79 490 TEMP 23 = 82 170 TEMP 24 = 84.580 TPRS 1 = 44 155 VPRS I = 0 363 VPRS 2= 0 362 DIFF. PRESS. = 1.000 CHANGE ANY DATA IF S0. ENTER YES
=
.
'
. TEMP. AND_-PRESS.;CCRRECTED DATA
SUMMARY
-
. TIME =' 1115 "DATE = 731
.
TENP;= 79 975298
'
. PPESt= 43.792573'
~
PRESS. DIFF = =l'.'362516 iFIG. . 56
~
C
.
.
^
=
SUMMARY
OF MEASURED DATA AT TIME 1130 731 TEMP 1 = 77.350 TEMP 2= 79 140 TEMP 3= 78 960 TEMP 4= 78 800 TEMP 5= 78 040 TEMP 6= 78.520 TEMP 7 = 78 300 TEMP 8= 78 290 TEMP 9= 73 440 TEMP 10 = 78.620 TEMP 11 = 78 300 TEMP 12 = 76 820 TEMP 13 = 77 950 TEMP 14 = 78 810 TEMP 15 = 77.690 TEMP 16 = 78.580 TEMP 17 = 78 530 TEMP 18 = 79 100 TEMP 19 = 82.840 TEMP 20 = 78 360 TEMP 21 = 78 950 TEMP 22 = 79 500 TEMP 23 = 82 170 TEMP 24 = 84.560 TPRS 1 = 44 154 VPRS 1 = 0 361 VPRS 2= 0.361 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES = TEMP. AND PRESS. CORRECTED DATA'
SUMMARY
TIME = 1130 DATE = 731 - TEMP = 79 879698 PRES = 43.792785 PRESS. DIFF = 1 361287 FIG. 57
- -
*
.
.
G
'
SUMMARY
OF MEASURED DATA AT TIME 1145 731 4 TEMP 1 = 77.380 TEMP 2= 79.080 TEMP 3= 78 970 TEMP 4= 78 810 TEMP 5= 78 030 TEMP 6= 78.530 TEMP 7 = 78 300 TEMP 8 = 78 290 TEMP 9= 78 450 TEMP 10 = 78 630 TEMP 11 = 78 290 TEMP 12 = 76 840 TEMP 13 = 77 960 TEMP 14 = 78 830 TEMP 15 = 77.700 TEMP 16 = 78.580 TEMP 17 = 78 510 TEMP 18 = 79 110 TEMP 19 = 82 840 TEMP 20 = 78 390 TEMP 21 = 78 940 TEMP 22 = 79.500 TEMP 23 = 82 150 TEMP 24 = 84.540 TPRS I = 44 154 VPRS 1 = 0 363 VPRS 2= 0 362 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1145 DATE = 731
'
TEMP = .79 878598 PRES = 43 791556 PRESS.-DIFF = 1 362516 TIG. SS l
*
-
.
D
~
SUMMARY
OF MEASURED DATA AT TIME 1200 731 !
'
TEMP 1 = 77 370 TEMP 2= 79 060 TEMP 3= 78 960 TEMP 4 = 78 810 TEMP 5= 78 060 TEMP 6= 78 540 TEMP 7= 78 340 TEMP 8= 78 300 TEMP 9= 78 470 TEMP 10 = 78.650 TEMP 11 = 78 330 TEMP 12 = 76 850 TEMP 13 = 77 990 TEMP 14 = 78 820 TEMP 15 = 77 710 TEMP 16 = 78.590 TEMP 17 = 78 510 TEMP 18 = 79 120 TEMP 19 = 82 820 TEMP 20 = 78 390 TEMP 21 = 78 930 TEMP 22 = 79 500 TEMP 23 = 82 160 TEMP 24 = 84.520-TPRS I = 44 154 VPRS I = 0 363 VPRS 2= 0 362 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1200 DATE = 731 TEMP = 79 881498 PRES = 43 791556 PRESS. DIFF =- 't.362516 FIG. 59
. _ . '
. s
SUMMARY
OF MEASURED DATA AT TIME 1215 731 TEMP 1 = 77.420 TEMP 2= 79 140 TEMP 3 = 79 020 TEMP- 4 = 78 840 TEMP S= 78 080 TEMP 6= 78 560 ' TEMP 7= 78 3E0 TEMP 8= 78 310 TEMP 9 = 78 470 TEMP 10.= 78.660 TEMP 11 = 78 330 TEMP 12 = 76 850 TEMP 13 = 78 010 TEMP 14 = 78,g90 TEMP 15 = 77.720 TEMP 16 = 78 600 TEMP 17 ". 78 540 TEMP 18 = 79 120 TEMP 19 = 82 810 TEMP 20 = 78 410 TEMP 21 = 78 950 TEMP 22 = 79.500 TEMP 23 = 82 160 TEMP 24 = 84.500 TPRS I = 44 153 VPRS 1 = 0 365 VPRS 2= 0 365 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
l
;
l TEMP. AND PRESS. CORRECTED DATA
SUMMARY
,
TIME = 1215 OATE = 731 l TEMP = 79 890697 PRES = 43 788036 PRESS. DIFF = 1 365019 FIG '60
.
. - -
'
,
S
SUMMARY
OF MEASURED DATA AT TIME 1230 731 TEMP 1 = 77.450 TEMP 2= 79 120 TEMP 3= 79 030 TEMP 4 = 78 860 TEMP 5= 78 090 TEMP 6= 78.570 TEMP 7 = 78 330 TEMP 8= 78 320 TEMP 9= 78 490 TEMP 10 = 78.660 TEMP 11 = 78 350 TEMP 12 = 76 900 . TEMP 13 = 78 010 TEMP 14 = 78 880 TEMP 15 = 77.740
'EMP 16 = 78 630 TEMP 17 = 78.S40 TEMP 18 = 79 130 TEMP 19 = 82 820 TEMP 20 = 78 440 TEMP 21 = 78 970 TEMP 22 = 79.510 TEMP 23 = 82~.150 TEMP 24 = 84.490 TPRS I = 44 153 VPRS 1 = 0 365 VPRS 2= 0 365 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
= TEMP. AND PRESS. CORRECTED DATA'
SUMMARY
TIME = 1230 DATE = 731 TEMP = 79 898298-PRES = 43,788036 PRESS.-DIFF = 1 365019 FI3. 61
.
E a
SUMMARY
OF MEASURED DATA AT TIME 1245 731 TEMP 1 = 77.440 TEMP 2= 79 190 TEMP 3= 79 010 TEMP 4= 78 870 TEMP 5= 78 070 TEMP 6= 78 570 TEMP 7 = 78 360 TEMP 8= 78 330 TEMP 9= 78 510 TEMP 10 = 78 690 TEMP 11 = 78 370 TEMP 12 = 76.900 TEMP 13 = 78 000 TEMP 14 = 78 860 TEMP 15 = 77.760 ' TEMP 16 = 78.610 TEMP 17 = 78 530 TEMP 18 = 79 150 TEMP 19 = 82 800 TEMP 20 = 78 440 TEMP 21 = 78 940 TEMP 22 = 79 490 TEMP 23 = 82 130 TEMP 24 = 84.460 TPRS 1 = 44.iS3 I VPRS 1 = 0 363 VPRS 2= 0 362 DIFF. PRESS. = 1 000 l CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME =' 1245 DATE = 731
.
TEMP = 79 895499 PRES =- 43 790539 PRESS. DIFF = 1 362516 FIG. 62
- a
SUMMARY
OF MEASURED DATA AT TIME 1300 731 TEMP 1 = 77.500 TEMP 2= 79 210 TEMP 3= 79 030 TEMP 4 = 78 870 TEMP 5= 78 100 TEMP 6= 78.590 TEMP 7= 78 360 TEMP 8= 78 360 TEMP 9= 78 520 TEMP 10 = 78 700 TEMP 11 = 78 400 TEMP 12 = '76 920 TEMP 13 = 78 020 TEMP 14 = 78 890 TEMP 15 = 77 780 TEMP 16 = 78.640 TEMP 37 = 78,350 TEMP 18 = 79 150 TEMP 19 = 82 790 TEMP 20 = 78 450 TEMP 21 = 78 950 TEMP 22 = 79 500 TEMP 23 $ 82 130 TEMP 24 = 84.460 TPRS I = 44 153 VPRS 1 = 0 363 VPRS 2= 0 362 DIFF. PRESS. = 1 000
,
CHANGE ANY DATA IF SO ENTER YES = TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1300 DATE = 731 TEMP = 79 906199 PRES = 43.790539 PRESS. DIFF = 1 362516 FIC, 63
.
'
.
. o
SUMMARY
OF MEASURED DATA AT TIME 1315 731
.
TEMP 1 = 77 460 TEMP 2= 79 150 TEMP 3= 79 050 TEMP 4 = 78 900 TEMP 5= 78 100 TEMP 6 = 78.620 TEMP 7 = 78 380 TEMP 8= 78 360 TEMP 9= 78 520 TEMP 10 = 78 700 TEMP 11 = 78 370 TEMP 12 = 76 960 TEMP 13 = 78 060 TEMP 14 = 78 920 TEMP 15 = 77.790 i TEMP 16 = 78 640 TEMP 17 = 78 560 TEMP 18 = 79 150 TEMP 19 = 82 780 TEMP 20 = 78 460 TEMP 21 = 78 970 TEMP 22 = 79 520 TEMP 23 = 82 110 TEMP 24 = 84.440
<
TPRS 1 = 44 152 VPRS 1 = 0 363 VPRS 2= 0 362 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
= .
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
-.
TIME = 1315 DATE = 731
.
TEMP : . 79 906098 PRES = 43 7R9522 l-PRESS.'DIFF = 1 362516 . FIG. 64 .
.
*
.
" .
SUMMARY
OF MEASURED DATA AT-TIME 1330 731 > TEMP 1 = 77 490 TEMP 2 =- 79 160 TEMP 3= 79.050 TEMP 4= 78 920 TEMP 5= 78 110 TEMP 6= 78 610 TEMP 7 = 78 400 TEMP 3= 78 350 TEMP 9= 78 540 TEMP 10 = 78 720 TEMP 11 = 78 430 TEMP 12 = 76 970 TEMP 13 = 78 060 TEMP 14 = 78 920 TEMP 15 = 77.790 TEMP 16 = 78 640 TEMP 17 = 78.570 TEMP 18 = 79 160
. TEMP 19 = 82 780
' TEMP 20 = 78 480 TEMP 21 = 78 970 TEMP 22 = 79 540 TEMP 23 = 82 110 TEMP 24 = 84.420 TPRS I = 44 152 VPRS I = 0 364 VPRS 2= 0 364 DIFF. PRUSS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
.
TIME = 1330 DATE = 731
.
TEMP c 79 912898 PRES = 43.788278 PRESS. DIFF = 1 363760
- l. FIG. 65
.
8
SUMMARY
OF MEASURED DATA AT TIME 1345 731 '
.
TEMP 1 = 77'.510 1EMP 2= 79 260 TEMP 3= 79 090 TEMP 4 = 78 920 TEMP' 5= 78 130 TEMP 6= 78 620 TEMP 7= 78 410 TEMP 8 = 78 370 TEMP 9 = 78 550 TEMP 10 = 78 730 TEMP 11 = 78 440 TEMP 12 = 76 950 TEMP 13 = 78 080 TEMP 14 = 78 950 TEMP 15 = 77 800 TEMP 16 = 78 660 TEMP 17 = 78 610 TEMP 18 = 79 180 TEMP 19 = 82 770 TEMP 20 = 78 490 TEMP 21 = 79 000 TEMP 22 = 79 550 TEMP 23 = 82 120 TEMP 24 = 84 430 TPRS I = 44 152 VPRS 1 = 0 364 VPRS 2= 0 364 DIFF. PRESS. = 1 000
.
CHANGE ANY DATA IF SO ENTER YES
=
.
e TEMP. AND PRESS. CORRECTED DATA SUMM A RY TIME = 1345 DATE = 731 TEMP = 79,.926497 , PRES = 43.'788278 PRESS. DIFF = 1 363760 ' FIG. 66 Rev.2.
.
-..g -
_
*
.
u
SUMMARY
OF MEASURED DATA AT TIME 1400 73) TEMP 1 = 77.490 TEMP 2= 79 220 TEMP 3= 79 090 TEMP 4 = 78 920 TEMP 5= 78 140 TEMP 6= 78 630 TEMP' 7= 78 430 TEMP 8= ',~
.
78 380 TEMP 9= 78 570 TEMP 10 = 78 740 TEMP !! = 78 420 TEMP 12 = 76 960 TEMP 13 = 78 090 TEMP 14 = 78 950 TEMP 15 = 77 820 TEMP 16 = 78 640 TEMP 17 = 78.620 TEMP 18 = 79 190 TEMP 19 = 82.760 TEMP 20 = 78 510 TEMP 21 =' 78 980 TEMP 22 = 79 540 TEMP 23 = 82 100 TEMP 24 = 84.400 TPRS 1 = 44 152 VPRS 1 = 0 364 VPRS 2= 0 364 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1400 DATE = 731 TEMP = 79 923298 , PRES = 43.788278
-PRESS. .DIFF = 1 363760 FIG. 67
__ - _ _ _ _ _ - _ _ _ _
.
'
* - .
'
SUMMARY
OF MEASURED DATA AT TIME 1015 731 TEMP 1 = 77 550 TEMP 2= 79 350 TEMP 3= 79 130 TEMP 4 = 78 930 TEMP 5= 78 150 TEMP 6= 78 640 TEMP 7 = 78 440 ' TEMP 8= 78 380 TEMP 9 = 78 570 TEMP 10 = 78 750 ,
'
TEMP 11 = 78 460 , TEMP 12 = 77 010 TEMP 13 = 78 120 TEMP 14 = 78 980 TEMP 15 = 77 820 TEMP 16 = 78 660 TEMP 17 = 78 640 TEMP 18 = 79 190 TEMP 19 = 82 750 TEMP 20 = 78 510 TEMP 21 = 78 970 TEMP 22 = 79 550 TEMP 23 = 82 090 , TEMP 24= 84 390 TPRS I = 44 152 VPRS 1 = 0 364 VPRS 2= 0 364
- DIFF. PRESS. = 1 000
'
.
- CHANGE ANY DATA IF SO ENTER YES
= .,
*
. .
.
1 TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1415 DATE = 731 TEMP = 79 931897 PRES = 43 788278.' ( PRESS. DIFF = 1 363760' FIG. 68
-Rev.2 )
K
.
.
,
-
.
r
*
SUMMARY
OF MEASURED DATA AT TIME 1430 731 TEMP ~1 = 77.590 TEMP 2= 79 250 TEMP 3= 79 150 TEMP 4 = 78 960 TEMP $= 78 160 TEMP 6= 78 680 TEMP 7= 78 450 TEMP 8= 78 400 TEMP 9 = 78 590 TEMP 10 = 78 780 TEMP 11 = 78 500 TEMP 12 = 77.060
- TEMP 13 = 78 140 1 TEMP 14 = 78 980 1 TEMP 15 = 77.840 TEMP 16 = 78 680 TEMP 17 = 78 620 TEMP 18 = 79 210 TEMP 19 = 82 740 TEMP 20 = 78 520 TEMP 21 = 79 000 TEMP 22 = 79.560 TEMP 23 = 82.070
' TEMP 24 = 84 390 TPRS 1 = 44 152 VPRS 1 = 0 365 VPRS 2= 0 365 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND-PRESS. CORRECTED DATA
SUMMARY
TIME = 1430 DA TE = 731 TEMP = 79 939999 PR E S = 43 787019 PRESS. DIFF = .l.365019 FIG. (9
T
<
.
.
=
SUMMARY
OF MEASURED DATA AT TIME 1445 731 TEMP 1 = 77.620 TEMP 2= 79 280 TEMP 3= 79 140 TEMP 4 = 78 960 TEMP 5= 78 170 TEMP 6= 78 680 TEMP 7= 78 460 TEMP 8= 78 410 TEMP 9= 78 600 TEMP 10 = 78.780 TEMP 11 = 78 490 TEMP 12 = 77 010 TEMP 13 = 78 130 TEMP 14 = 79 000 TEMP 15 = 77 860 TEMP 16 = 78 680 TEMP 17 = 78 660 TEMP 18 = 79 220 - TEMP 19 = 82 760 TEMP 20 = 78 560 TEMP 21 = 79 020 TEMP 22 = 79.550 TEMP 23 = 82 090 TEMP 24 = 84 380 T T'RS 1 = 44 152 ( VPRS I = 0 364 VPRS 2= 0 364 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
c a TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1445 DATE = 731 TEMP = 79 948699 PRES = 43 788278 PRESS. DIFF = 1 363760 FIC. 70- _ - _ _ - _ _ _ _ - _ _ _ _
.
-
8 .
SUMMARY
OF MEASURED DATA AT TIME 1500 731 TEMP 1 = 77.590 TEMP 2= 79 310 TEMP 3= 79 110 TEMP 4 = 78 980 TEMP 5= 78 180 TEMP 6= 78 690 TEMP 7 = 78 480 TEMP 8= 78 410 TEMP 9= 78.610 TEMP 10 = 78 790 TEMP 11 = 78 510 TEMP 12 = 77.030 TEMP 13 = 78 140 TEMP 14 = 79 010 TEMP 15 = 77.880 TEMP 16 = 78 680 TEMP 17 = 78 660 TEMP 18 = 79 230 TEMP 19 = 82 740 TEMP 20 = 78 560 TEMP 21 = 79 000 TEMP 22 = 79 570 TEMP 23 = 82 070 TEMP 24 = 84 350 TPRS 1 = 44 151 VPRS 1 = 0 364 VPRS 2= 0 364 DIFF. PRESS. = 1 000 ! CHANGE ANY DATA IF SO ENTER YES
=
e TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1500 DATE = 731 TEMP = 79 947998
' . PRES = 43 787261 i PRESS. DIFF = 1 363760 l l l FIG. 71 l !
. - -
__ _ - _ _ _ _ -
. a
'
.
SUMMARY
OF. MEASURED DATA AT TIME 1515 731 TEMP 1 = 77 620 TEMP 2= 79 250 TEMP 3= 79 150 TEMP 4 = 78 990 TEMP S= 78 190 TEMP 6= 78 710 TEMP -7 = 78 500 , TEMP 8= 78 440 TEMP 9= 78.620 TEMP 10 = 78 810 TEMP- 11 = 78 530 TEMP 12 = 77.040 TEMP 13 = 78 180 TEMP 14 = 79 010 TEMP 15 = 77 880 TEMP 16 = 78 700 TEMP 17 = 78 660 TEMP 18 = 79.240 TEMP 19 = 82 730 TEMP 20 = 78 580 TEMP 21 = 79 000 TEMP 22 = 79 550 _ TEMP 23 = 82.060 TEMP 24 = 84 370 TPRS 1 = 44 150 VPRS 1 =- 0 364 VPRS 2= 0 364 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1515 DATE = 731 TEMP'= 79 953598 PRES = 43.786244 PRESS. DIFF = 1 363760 FIG. 72
=-- - _
_ _ _
.
.
= .
SUMMARY
OF MEASURED DATA AT TIME 1530 73p TEMP 1 = 77.660 TEMP 2= 79 260 TEMP 3= 79 170 TEMP 4 = 79 010 TEMP 5= 78 200 TEMP 6= 78 730 TEMP 7 = 78 490 TEMP 8= 78.430 TEMP 9 = 78 630
'
TEMP 10 = 78 820 TEMP 11 = 78 570 TEMP 12 = 77 110 TEMP 13 = 78 180 TEMP 14 = 79 050 TEMP 15 = 77 900 TEMP 16 = 78 720 TEMP 17 = 78.680 TEMP 18 = 79 240 TEMP 19 = 82.730 TEMP 20 = 78 600 TEMP 21 = 79 000 TEMP 22 = 79 580 TEMP 23 = 82 080 TEMP 24 = 84 360 7 pas 1 = 44 151 VPRS 1 = 0 365 VPRS 2= 0 365 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
, TEMP. AND PRESS. CORRECTED DA;A
SUMMARY
TIME = - [[30 l DATE = g 93/ TEMP = 79 966298 f , PRES = 43.786002 i PRESS. DIFF = 1 365019 FIG. 73 !
.
.
,
,
,
a s
SUMMARY
OF MEASURED DATA AT TIME 1545 731
.
'
TEMP 1 = 77 650 . TEMP 2= 79 320 TEMP 3= 79 170 TEMP 4 = 79 030 TEMP 5= 78 230
-TEMP ~6 = -78.730 TEMP 7 = 78.510 TEMP 8= 78 440 TEMP 9= 78.650 TEMP- 10 = 78 840 TEMP !! = 78 540 TEMP 12'= 77 130 TEMP 13 = 78.200 TEMP .14 = 79 080 TEMP 15 = 77 910 I
TEMP 16 = 78 740 TEMP 17 = 18.700 TEMP 18 = 79 250 TEMP 19 = 82.720 TEMP 20 = 78 610 TEMP 21 = 79 000 {' TEMP 22 = 79.590 ' TEMP 23 = 82.080 TEMP 24 = 84 340 TPRS 1 = 44 151 VPRS 1 = 0 365 VPRS 2= 0 365 DIFF. PRESS. = 1 000
,
CHANGE ANY DATA IF SO ENTER YES
=
i
't TEMP. AND PRESS. CORRECTED DATA
SUMMARY
- TIME = 1545 DATE = 731 TEMP = 79 973199 PRES = 43 7R6002
- PRESS. DIFF = 't.365019 4
?I G . .~ 7 4~
. . , . -
.
o .
*
SUMMARY
OF MEASURED DATA AT TIME.'600 731 . TEMP 1 = 77.740 TEMP 2= 79 320 TEMP 3= 79 190 TEMP 4 = 79 030 TEMP 5= 78 230 TEMP 6= 78 740 TEMP 7 = 78 550 TEMP 8= 78 450 TEMP 9= 78 660 TEMP 10 = 78 860
' TEMP 11 = 78 580 TEMP 12 = 77 160 TEMP 13 = 78 220 TEMP 14 = 79 060 TEdP 15 = 77 940 TEMP 16 = 78 750 TEMP 17 = 78 680 TEMP 18 = 79 260 TEMP 19 = 82 710
, TEMP 20 = 78 620 TEMP 21 = 79 020 TEMP 22 = 79.600 TEMP 23 = 82 070 TEMP 24 = 84 350 TPRS 1 = 44 151 VPRS 1 = 0 365 VPRS 2= 0 365 DIFF. PRESS.'= 1 000
.
CHANGE ANY DATA IF SO ENTER YES
=
. TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1600 DATE = 731
.
TEMP = 79 980797 , PRES = 43.786002 PRESS. DIFF = 1 365019 FLG. 75
.
.
ENTER TIME, DATE, T EM P, PRESS, PRESS DIFF
' HEN FINISHED ENTER 9999,,,,,
..
= 0215,0802,85.341498,73 375829,1
= 0230,0802,85 275797,73 368152,1
= 0245,0802,85 192797,73 360031,1
= 0300,0802,85 133397,73 352926,1
= 0315,0802,85 091396,73 344807,1
= 0330,0802,85 035598,73 337702,1
= 0345,0802,84 982897,73 330597,1
= 0400,0802,84 925997,73 323492,1
= 0415,0602,84 872097,73 316387,1
= 0430,0802,84 827998,73 310297,1
= 0445,0802,84 177897,73 303191,1
= 0500,0802,84.733497,73 297102,1
= 0515,0802,84 689298,73 291012,1
= 0530,0802,84 648697,73 285936,1
= 0545,0802,84 601697,73 278831,1
= 0600,0802,84 573298,73 273756,1
= 0615,0802,84 531898,73 268682,1
= 0630,0802,84 493797,73 263607,1
= 0645,0802,84 457897,73 258532,1
= 0700,0802,84 421897,73 254471,1
= 0715,0802,84 388097,73 249397,1
= 0730,0802,84 358997,73 244322,1
= 0745,0802,84 319696,73 241277,1
= 0600,0802,84 284297,73 233156,1
= 0815,0802,84 259697,73 230112,1
= 0830,0802,84 222198,73 225037,1
= 0845,0802,84 200197,73 221992,1
= 0900,0802,84 172897,73 219916,1
= 0915,0802,E 4 144998,73 2128 57,1
= 0930,0802,84 121097,73 209811,1
= 0945,0802,84 091698,73 205751,1
= 1000,0802,64 061399,73 201693,1
= 1015,0802,84 037398,73 198647,1
= 1030,0802,84 014598,73 194586,1
= 1045,0802,83 958198,73 191542,1
= 1100,0802,83 965898,73 188497,1
= 1115,0802,83 944398,73 185452,1
= 1130,0cn2,8 3 9 29298,7 3 18 2 40 7,1
= 1145,0802,83 904198,73 178347,1
= 1200,0802,63 851598,73 175303,1 j
= 1215,0802,83 855699,73 172256,1 l
= 9999,,,,,
.
.
FIG. 76 .; Rev. 1 i j
_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - _ _ _ _ _ _ OCONEE 59 PSIG ILRT . TIMES DATE START OF TEST 2 25 802 TIME AFTER START OF TEST = 10 000 HR CONTAINMENT AVERAGE TEMPERATURE = 83 856 F CONTAINMENT AVERAGE PRESSURE = 73 172 PSIA TRENDS BASED ON TOTAL TIME CALCULATIONS
,
HOURS DATA MEAN OF CALCUL A TED OF TEST ENTRIES CALC. LR L EAK RATE 0 75 4 -0 217E+00 -0 253E+ 00 1 00 5 -0 185E+00 -0 147E+ 00 1 25 6 -0 164E+00 -0 969E-01 1 50 7 -0 148 E+00 -0 651E-01 1 75 8 -0 136E+00 -0 48 5E-01 2 00 9 -0 127E+00 -0 369E-01
'
2 25 10 -0 119E+00 -O.268E-01 2 50 11 -0 111 E+ 00 -0 172 E-01 2 75 12 -0 104E+00 -0 9 43E-02 3 00 13 -0 983E-01 -0 293E-02 3 23 14 -0 934E-01 0 107E-02 3 50 15 -0 885E-01 0 620E-02 3 75 16 -0 8 34E-01 0 129 E-01 4 00 17 -0 791E-01 0 171E-01 4 25 18 -0 753E-01 0 203E-01 4 50 19 -0 718E-Ol 0 231E-01 4 75 20 -0 689E-01 0 243E-01 5 00 21 -0 661E-01 0 259E-01 5 25 22 -0 632E-01 0 28 4E-O l 5 50 23 -0 612E-01 0 281E-01 5.75 24 -0 58 4E-01 0 309E-01 6 00 25 -0 560E-01 0 330E-01 6 25 26 -0 537E-01 0 346E-01 6 50 27 -0 516E-01 0 360E-01 6 75 28 -0 500E-01 0 360E-Ol 7 00 29 -0 479E-01 0 380E-01 7 25 30 -0 460E-01 0 396E-01 l 7.50 31 -0 442E-Ol 0 409E-01 1 7 75 32 -0 425E-01 0 419E-01 8 00 33 -0 410 E-01 0 427E-Ol f 8 25 34 -0 394E-01 0 437E-01 l 8 50 35 -0 380E-01 0 443E-01 8 75 36 -0 367E-01 0 447E-O l 9 00 37 -0 355E-01 0 451E-01 9 25 38 -0 342E-01 0 458E-01 9 50 39 -0 329E-01 0 465E-01 9 75 40 -0 317E-01 0 47tE-OI 10 00 41 -0 307E-L1 0 474E-01 ! l
.
THE CALCULATED LEAK RATE IS 0 474E-01 FIG. 77 THE MAXIMUM ALLOWABLE LEAK RATE IS 0 250E+00 Rev. 1 TH E ' L A ST 0 DATA POINTS ESTABLISH A NEGATIVE SLOPE
- OCONEE 59 PSIG ILRT ABSOLUTE CALCULAT10NS TIME, DATE START OF TEST 2 25 802 TIME AFTER START OF TEST = 10 000 HR CONTAINMENT AVERAGE TEMPERATURE = 83 856 F CONTAINMENT AVERAGE PRESSURE = 73 172 PSIA LEAK RATE BASED ON TCTAL TIME CALCUL ATIONS
. TIME TEMPERATURE PRESSURE LEAK RATE L EAK RATE 95% CONFI DENCE (PSIA) MEASURED CALCULATED LIMITS 2 50 85 28 73 37 -0 153E+00 -0 109E+00 -0 20E+00 -0 21E-01
.
2 75 85 19 73 36 -0 27 6E+00 -0 105E+00 -0 19 E+00 -0 17 E-01
'
3 00 85.I3 73 35 -0 223E+00 -0 101 E+ 00 -0 19 E+00 -0 14E-01 3 25 85 09 73 34 -0 868E-01 -0 967E-01 -0 18E+00 -0 10E-01 3 50 85 04 73 34 -0 802E-0*_ -0 927E-Ol -0 18E+00 -0 62F-02 3 75 84 98 73 33 -0 666E-01 -0 887E-01 -0 17E+00 -0 2 5E-02 4 00 84 93 73 32 -0 675E-01 -0 847E-Ol -0 17 E+ 00 0 13E-02 4 25 84 87 73 32 -0 616E-01 -0 807E-01 --0 17E+00 0 51F-02 4 50 84 83 73 31 -0 525E-01 -0 767E-01 -0 16E+00 0 90F-02 4.75 84 78 73 30 -0 426E-01 -0 727E-01 -0 16E+00 0 13E-01
.
5 00 84 73 73 30 +u.374E-01 -0 687E-01 -0 15E+00 0 17E-01 5 25 84.69 73 29 -0 327E-01 -0 647E-01 -0 15E+00 0 21E-01 5 50 84 65 73 29 -0 342E-Ol -0 607E-01 -0 15E+00 0 24F-01 5 75 84 60 73 28 -0 2 45E-01 -0 567E-01 -0 14E+ 00 0 2?F-01 6 00 84 57 73 27 -0 119E-01 -0.527E-01 -0 14E+00 0 3PF 6 25 84 53 73 27 -0 153E-Ol -0 48 7 E-01 -0 13E+ 00 0 3^F-01
.
FIG. 78 Rev. l
.
,
6 50 84 49 73 26 -0 148 E-01 -0 447 E-01 -0 13E+00 0 40E-01
.
6 75 84.46 73 26 -0 122E-01 -0 407E-01 -0 13E+00 0 44E-01
- 7 00 8 4. 42 73 25 -0 170E-Ol -0 367E-01 -0 12E+00 0. 48 E-01 7 25 84 39 73 25 -0 127E-01 -0 327E-01 -0 12E+00 0 52E-01 7.50 84 36 73 24 -0 490 E-02 -0 287E-01 -0 11E+00 0 56E-01 f
7 75 84 32 73 24 -0 181E-01 -0 247E-Ol -0. l l E+00 0 60E-01 8 00 84 28 73 23 0 184E-02 -0 207E-01 -0 11E+00 0.64E-01 8 25 84 26 73 23 0 303E-03 -0 166E-01 -0 10E+00 0 68 E-01 8 50 84 22 73 23 0 423E-03 -0 126E-01 -0 97E-01 0 72E-01 8 75 84 20 73 22 0 822E-03 -0 864E-02 -0 94E-01 0 76E-01
-
9 00 84 17 73 22 -0 698E-02 -0 463E-02 -0 90E-01 0 80E-01 9 25 84 14 73 21 0 874E-02 -0 627E-03 -0 86E-01 0 8 4E-01 9 50 84 12 73 21 0 765E-02 0 338E-02 -0 82E-Ol 0 89E-Ol' i l 9 75 84 09 73 21 0 785E-02 0 738E-02 -0 78E-01 0 93E-01 10 00 84 06 73 20 0 750E-02 0. l l 4E-01 -0 74E-01 0 97E-01 10 25 84 04 73 20 0 650E-v2 0 154E-01 -0 70E-01 0 10 E+ 00 10 50 84 01 73 19 0 102E-01 0 194E-01 -0 66E-01 0 11E+00 10 75 83 99 73 19 0 798E-02 0 234E-01 -0 63E-01 0 1 ! E+00 - 11 00 83 97 73 19 0 791E-02 0 274E-01 -0 59E-01 0 11E+00
11 25 83 94 73 19 0 823E-02 0 314E-01 -0 55E-01 0 12E+00 11 50 83 93 73 18 0.ll6E-01 J.354E-01 -0 51E-01 0 12E+00 11 75 83 90 , 73 18 0 136E-01 0 394E-01 -0 48 E-01 0 13E+00 12 00 83 88 73 18 0 134E-01 0 434E-01 -0 44E-Ol 0 13E+00 l 12 25 83 86 73 17 0.ll5E-01 0 474E-01 -0 40E-Ol 0 13E+00 IF I T I S A SSUMED TH A T TH E L EAK RATE IS CONSTANT: . THE MEAN I f. -0 30 7 E-01 THE STANDARD DEVI ATION IS 0 621E-01 SKEL IS NEGATIVE THE CALCULATED LEAK RATE AFTER 10 00 HOURS OF TEST IS 0 474E-01 FIG. 79 R.e v. 1
- _ _ _ - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _
.
'
L EAK RATF BASED ON POINT-TC-POINT CALCULATICNS >
.
TIME TEMPERATURE PRESSURE LEAK RATE LEAK RATE 95% CCNFI DFNCF (PSIA) MEASURED CAL C UL ATED LIMITS 2 50 85 28 73 37 - 0 .15 3 E+ 0 0 -0 368E-01 -0 37E+00 0 29E+00 2 75 85 19 73 36 -0 400E+ 00 -0 344E-01 -0 36E+00 0 30r+00 3 00 85 13 73 35 -0 117E+00 -0 319E-Ol -0 36E+00 0 30E+00 3 25 65 09 73 34 0 323E+00 -0 294E-O! -0 36E+00 0 3CI+ 00 3 50 85 04 73 34 -0 534E-01 -0 2 69 E-01 -0 35E+00 0 30E+00 3 75 84 98 73 33 0 129E-02 -0 244E-01 -0 35F+00 0 30F+00 4 00 84 93 73 32 -0 728E-01 -0 219 E-01 -0 35E+00 0 30E+00 4 25 84 87 73 32 ~-0 200E-01 -0 19 4E-01 -0 34E+00 0 30E+00 4 50 84 83 73 31 0 200E-01 -0 170E-01 -0 34E+00 0 31 E+ 00 4 75 84 78 73 30 0 472E-01 -0 145E-01 -0 3 4E+00 0 31 E+00 , 5 00 84 73 73 30 0 144E-01 -0 120E-01 -0 33E+00 0 31 E+ 00 5 25 8 4.69. 73 29 0 183E-Ol -0 950E-02 -0 33E+00 0 31 E+00 5 50 84 65 73 29 -0 511E-01 -0 701E-02 -0 33E+ 00 0 31 F+00 5 75 84 60 73 28 0 102E+00 -0 453E-02 3 33E+00 0 32F+ 00 6 00 84 57 73 27 0 164E+dC -0 20 4E-02 -0 32 E+ 00 0 32E+00 6 25 84 53 73 27 -0 655E-01 0 446E-03 -0 32E+ 00 0 32E+00 6.50 84 49 73 26 -0 705E-02 0 29 3E-02 -0 32E+00 0 32E+00 6 75 84 46 73 26 0 318E-01 0 542E-02 -0 31E+00 0 33E+00 7 00 84 42 73 25 -0 103E+00 0 790E-02 -0 31E+00 0 33E+00 7 25 84 39 73 25 0.686E-01 0 10 4E-01 -0 31E+00 0 33E+00 7 50 84 36 73 24 0 152E+00 0 129 E-01 -0 31E+00 0 33F+00
'
7 75 84 32 73 24 -0 294E+00 0 154E-01 -O.30E+00 0 33E+00 8 00 84 28 73 23 0 440E+00 0 178E-Ol -0 30E+00 0 3aE+00 8 25 84 26 73 23 -0 350E-01 0 203E-01 -0 30E+00 0 34F+00 FIG. 80
.
R.e v. 1
. . _ _ -_________
~
i ' 8 50 8'4 22 73 23 0 34tE-02 0 228E-01 -0 30E+00 0 34E+00 , 8 75 84 20 73 22 0.lllE-01 0 253E-01 -0 30E+00 0 35E+00 9 00 84 17 73 22 -0 210E+00 0 278E-01 -0 29E+00 0 35E+00 9 25 84 14 73 21 0 433E+00 0 303E-01 -0 29E+00 0 35E+00 9 50 84 12 73 21 -0 225E-01 0 328E-01 -0 29E+00 0 35E+00 9 75 84 09 73 21 0 135E-01 0 352E-01 -0 29 E+00 0 36E+00 10 00 84 06 73 20 -0 271E-02 0 377E-01 -0 28E+00 0 36E+00 '
~
10 25 84 04 73 20 -0 243E-01 0 402E-Ol -0 28 E+00 0 36F+00 10 50 84 01 73 19 0 130E+00 0 427E-01 -0 28E+00 0 37E+00 10 75 83 99 73 19 -0 668E-01 0 452E-01 -0 28E+00 0 37E+00 11 00 83 97 73 19 0 577E-02 0 477E-01 -0 28E+00. 0 37 E+00 11 25 83 94 73 19 0 197E-01 0 502E-Ol -0 28 E+ 00 0 38E+00 11 50 83 93 73 18 0 133E+00 0 527E-01 -0 27E+00 0 38E+ 00 11 75 83 90 73 18 0 89 4E-01 0 55tE-01 -0 27E+00 0 38E+00 12 00 83 88 73 18 0 542E-02 0 576E-01 -0 27E+ 00 0 39E+00
'
12 25 83 86 73 17 -0 629E-01 0 601E-01 -0 27E+00 0 39E+00 IF I T I S A SSUM ED THAT TH E L EAK RATE I S CONSTANT: THE MEAN IS 0.ll6E-01 THE STANDhR9 DEVI ATION IS 0 157E+00 SKEl; IS POSITIVE THE CALCULATED LEAK RATE AFTER 10 00 HOURS OF TEST IS 0 601E-01 MEASURED LEAK RATE COMPUTED FROM MEASURED VALUES TEMPERATURE AND PRESSURE CALCULATED LEAK RATE COMPUTED.FROM LINEAR LEAST SOUARE FIT OF MEASURED LEAK RATES
'
! l FIG. 81 l R.ev. 1 l l
.
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SUMMARY
OF MEASURED DATA AT TIME 200 802 TEMP 1 = 81 390 TEMP 2= 82 310 TEMP 3= 84 860 TEMP 4= 85 560 TEMP 5= 85 330 TEMP 6= 85.480 TEMP 7 = 85.440 TEMP 8= 85 150 TEMP 9= 85.580 TEMP 10 = 85.490 TEMP 11 = 82 260 TEMP 12 = 81 050 TEMP 13 = 81 670 TEMP 14 = 84.520 TEMP 15 = 84 990 TEMP 16 = 85 200 TEMP 17 = 85 230
. TEMP 18 = 85.470 TEMP 19 = 86 840 TEMP 20 = 85.460 TEMP 21 = 86 220
, TEMP 22 = 85.520 TEMP 23 = 86 450 TEMP 24 = 87.340 TPRS 1 = 73 826 VPRS 1 = 0. VPRS 2= 0 441 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SC ENTER YES
=
r TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 2600 DATE = 802
- TEMP - 85.422198 PRES = 73.384963 PRESS. DIFF = 1.441061 TI ' . 83
.
.
* ,
.
'
=.
SUMMARY
OF MEASURED DATA AT TIME 215 802
. TEMP 1 = 81 300
" " TEMP 2 = 82 200 TEMP 3= 84.780 TEMP 4 = 85.470 TEMP 5 = 85.220 TEMP 6 = 85.380 TEMP 7 = 85.390 TEMP 8= 85.070 TEMP 9 = 85.490 TEMP 10 = 85.430 TEMP 11 = 82 160 TEMP 12 = 80.960 TEMP 13 = 81 620 TEMP 14 = 84.440 TEMP 15 = 84 900 TEMP 16 = 85 120 TEMP 17 = 85.160 TEMP 18 = 85.380 TEMP 19 = 86.760
'
TEMP 20 = 85.380 TEMP 21 = 86 220 TEMP 22 = 85.430 TEMP 23 = 86.370 ] TEMP 24 = 87 290 TPRS 1 = 73 817 VPRS 1 = 0. VPRS 2 = 0 441 f f DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
!
l l
!
TEMP. AND PRESS. CORRECTED DA1A
SUMMARY
j TIME = 2615 DATE = 802 - , TEMc = FS.341498 j PRES = 73 375829 PRES 3. DIFF =
'
1 441061 l I
- ~. 9 's ~
l
. - --.
. .
. .. .. _ _ _ . _ _ _ _ _ _ _
,
.
- .
= .
SUMMARY
OF MEASURED DATA AT TIME 230 802- - TEMP- 1= 81 230 TEMP 2'= 82 110 TEMP 3=~ 84 720
-TEMP .
4= 85 370 TEMP 5= 85 170 TEMP 6= 85 310 TEMP 7= 85 340 " TEMP 8= 85 020 TEMP 9 = 85 420 ' TEMP 10 = 85 350 TEMP 11 = 82 060 TEMP 12 = 80 900 TEMP -13 = 81 550 TEMP 14 = 84 380 TEMP 15 = 84 640 ' TEMP 16 = 85 060 i TEMP 17 = 85 100 TEMP 18 = 85 310 i TEMP 19 = 86 680 l TEMP 20 = 85 340
- TEMP 21 = 86 120 TEMP 22 = 85.370 TEMP 23 = 86 310 TEMP 24= 87 260
- I' TPRS 1 = 73 808 i
I VPRS 1 = 0. i VPRS 2= 0 440
- DI FF. PRESS. = 1 000 m .
!
i CHANGE ANY DATA IF SO EN TER . Y ES
=
1 1 I TEMP. AND PRESS. CORRECTED-DATA
SUMMARY
TIME = 230 DATE = 802
, : TEMP = 85 275797 4
PRES s' 73 368152 .
'
~ PRESS. DIFF = 1 439602 ,
'
FIG. 85 Rev. 1 _ _ _. -
-. - __. _
- __
. . .
9
='
SUMMARY
'0F MEASURED DATA AT TIME E 45 802 TEMP 1 = 81 130 TEMP 2= 82 020 TEMP 3= 84.640 TEMP 4 = 85.290 TEMP 5= 85 070 TEMP 6 = 85 230 TEMP 7 = 85 280 TEMP 8 = 84 940 TEMP 9= 85.330 TEMP 10 = 85.270 TEMP 11 = 81 970 TEMP 12 = 80 790 TEMP 13 = 81 490 TEMP 14 = 84 310 TEMP 15 = 84.750 TEMP 16'= 84 990 TEMP 17 = 85.000 TEMP 18 = 85.220 , TEMP 19 = 86.610 TEMP 20 = 85 230 TEMP 21 = 86 000 TEMP 22 = 85.300 TEMP 23 = 86.E20 TEMP 24 = 87 190 TPRS 1 = 73 800 VPRS I = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF S0. ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 2645
~
DATE = 802 TEMP = 85 192797 PRES = 73.360031' i l FRESS. DIFF =- 1 439602' i l PI L S6
-
.
. . .
1 =
'
.
.l
SUMMARY
OF MEASURED DATA AT . TIME 300 802 ' J TEMP 1 = 81 080 TEMP. 2= 81 980 T EMP 3= 84 600 TEMP 4=- 85 220 TEMP -5 = 85 010
, TEMP 6= 85 190 TEMP 7= 85 240
' TEMP 8= 84 900 TEMP 9 = 85 290 .i TEMP 10 = 85 250 TEMP 11 = 81 930 TEMP 12 = 80 740 TEMP 13 = 81 470 TEMP 14 = 84 260 . - TEMP 15 = 84 700 ! TEMP 16 = 84 940 - TEMP 17 = S4 960 - ! TEMP 18 = 85 180 . l TEMP 19 = 86 570 ,' i TEMP 20 = 85 200 TEMP 21 = 85.960
'
TEMP 22 = 85 250 TEMP 23 = 86 020 ! TEMP 24 = 87 160 TPRS 1 = 73 793 - " VPRS 1 = 0. . VPRS 2= 0 440
.
i DIFF. PRESS. = 1 000 ,
-
i ' CHANGE ANY DATA IF SD ENTER YES
- i
-
1 I
.
.
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 300 l -DATE : . 802
.
TEMP = 65 133397 PRES = 73 352926 PRESS. DIFF =- 1 439602. FIG. 87-R.e v. 1
.-. . ._, -
-
.
.
.
.,
=
SUMMARY
OF MEASURED DATA AT TIME 315 802 TEMP 1 = 81 040 TEMP 2= 81 910 TEMP 3= 84.530 TEMP 4 = 85.210 TEMP 5= 84 950 TEMP 6 = 85 130 TEMP 7 = 85.190 TEMP 8= 84 860 TEMP 9 = 85.210 TEMP 10 = 85 190 TEMP 11 = 81 830 TEMP 12 = 80.670 TEMP 13 = 81 410 TEMP 14 = 84 210 TEMP 15 = 84.640 TEMP 16 = 84 890 TEMP 17 = 84 930 TEMP 18 = 85 120 TEMP 19 = 86.490 TEMP 20 = 85.140 TEMP 21 = 85 930 TEMP 22 = 85.190 TEMP 23 - 86 090 TEMP 24 = 87.120 ', TPRS I = 73 784 e VPRS 1 = 0. ! VPRS 2= 0 440 DIFF. PRESS. = 1 000 I l 1 l CHANGE ANY DATA IF SO ENTER YES !
=
TEMP. AND PRESS.-CORRECTED DATA
SUMMARY
TIME = 2715 DATE = 802 TEMP = 85 091396 PRES = 73 344807 PRESS. DIFF = 1 439602
'
FIG, 88
_ _ _ _ - _
.
'
'
.. - . . . . . .
*
=
SUMMARY
OF MEASURED DATA AT TIME 330 802 - TEMP 1= 80 980 TEMP 2= 81 840 TEMP 3= 84 470 TEMP 4= 85 120 TEMP 5= 84 880 TEMP 6= 85.090 TEMP -7= 85 150 TEMP 8 = 84 790 TEMP 9 = 85 170 TEMP 10 = 85 120 TEMP 11 = 81 800 TEMP 12 = 80 610 TEMP 13 = 81 340 TEMP 14 = 84 150 TEMP 15 = 84 590 TEMP 16 = 84 840 TEMP 17 = 84 870 . TEMP 18 = 65 060 TEMP 19 = 86 430 TEMP 20 = 85 090 TEMP 21 = 85 870 TEMP 22 = 85 150 TEMP 23 = 86 050 t TEMP 24 = 87 070 - 1
'
TPRS 1 = 73 777
VPRS 1 = 0. VPRS 2= 0 440
.
' DIFF. PRESS. = 1 000 ,
,
i l CHANGE ANY DATA IF SO EbTERYES ' . . l TEMP. AND PRESS. "Pr.RECTED DATA
SUMMARY
TIME =- 330 l DATE = 802 . TEMP = -85 035598' PRES = 73 337702 PRESS. DIFF'=' l.439602 I . FIG. 89 l
- Rev. 1 l
, ._ . .- . .
_ - - _ _ _ _ _ _ _ - _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _
.
.
.
*
-
SUMMARY
CF MEASURED DATA AT TIME 345 802 TEMP 1 = 80 920 TEMP 2= 81 770 TEMP 3= 84.410 TEMP 4 = 85 110 TEMF 5= 84 820 TEMP 6= 85 050 TEMP 7 = 85 110 TEMP .8= 84 750 TEMP 9= 85 110 TEMP 10 = 85 060 TEMP 11 = 81 760 TEMP 12 = 80 550 TEMP 13 = 81 290 TEMP 14 = 84 090 TEMP 15 = 84.530 TEMP 16 = 84 800 TEMP 17 = 84 820 TEMP 18 = 85.010 TEMP 19 = 86 380 TEMP 20 = 85.020 TEMP 21 = 85 820 TEMP 22 = 85 080 TEMP 23 = 85 980 TEMP 24 = 87 030 TPRS 1 = 73 770 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 2745 DATE = 802 TEMP = 84 982897 l l PRES = 73 330597 l l PRESS. DIFF = 1 439602
l I 72:. 90
.
4 a .
SUMMARY
OF MEASURED DATA AT TIME 400 802 TEMP 1 = 80 840 TEMP 2= 81 700 T EMP 3= B4 370 TEMP 4= 85 060 TEMP 5= 84 760 TEMP - 6= 84 990 ' TEMP 7= 85 060 TEMP 8= 84.710 TEMP 9= 85 040 TEMP 10 = 85 010 TEMP 11 = 81 710 TEMP 12 = 80 480 TEMP 13 = 81 220 TEMP 14 = 84 030 TEMP 15 = 84 470 TEMP 16 = 84 740 , TEMP 17 = 84 750 TEMP 18 = 84 950 TEMP 19 = 86 320 TEMP 20 = 84 970 TEMP 21 = 85 760 TEMP 22 = 85 020 - TEMP 23 = 85 930 -
'
TEMP 24= 86 980 TPRS 1 = 73 763 VPRS 1 = 0 VPRS 2= 0 440 DI FF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
i
*
. TEMP. AND PRESS. CORRECTED DATA
SUMMARY
-
TIME = 400 DATE =- 802 , TEMP = 84 925997
-PRES = 73 323492 PRESS. DI FF = - 1 439602 FIG. 91
- R ev. 1-
. .
- - - . . _ _ _ _ _ _ - _ - _ _ _ _ _ _
.
.
=
SUMMARY
OF MEASURED DATA'AT TIME 415 802 TEMP 1 = 80 820 TEMP -2 = 81 660 TEMP 3= 84.320 TEMP 4 = 84 990 TEMP -5= 84.680 TEMP 6= 84 940 TEMP 7 = 85.000 TEMP 8= 84.650
- .
'
TEMP 9= 84 990 TEMP 10 = 84 950 TEMP 11 = 81 620 TEMP 12 = 80 430 TEMP 13 = 81 180 TEMP 14 = 83 980 TEMP 15 = 84 420 TEMP 16 = 84.690 TEMP 17 = 84 720 TEMP 18 = 84 910 , TEMP 19 = 86 260 t TEMP 20 = 84 920 TEMP 21 = 85.690 TEMP 22 = 84 970 TEMP 23 = 85 850 TEMP 24 = 86 950 TPRS 1 = 7.'s.756 i VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 i
<
CHANGE ANY DATA IF SO ENTER YES
=
, TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 2R15
- DATE = 802
. TEMP = R4 872097 PRES =- 73 316387
.
PRESS. DIFF = 1 439602 TI ?. . 92:
. -
7
.
-
.
E
SUMMARY
OF MEASURED DATA AT TIME 430 802 TEMP I = 80.790 TEMP 2= 81.620 TEMP 3= 84 260 TEMP 4= 84 950 TEMP 5= 84 620 TEMP 6= 84 870 TEMP 7= 84 950 TEMP 8= 84 610 TEMP 9= 84 950 TEMP 10 = 84 920 TEMP !! = 81 610 TEMP 12 = 80 360 TEMP 13 = 81 110 TEMP 14 = 83 940 TEMP 15 = 84 390 TEMP 16 = 84.660 TEMP 17 = 84.650 TEMP 18 = 84 850 TEMP 19 = 86 210 TEMP 20 = 84 880 TEMP 21 = 85.600 TEMP 22 = 84 930 TEMP 23 = 85 820 TEMP 24 = 86 920 TPRS 1 = 73 750 VPRS 1 = 0. VPRS 2= 0.440 DIFF. PRESS. = 1 000 i CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 2830 DATE = 802 TEMP = 84 827998 ! PRES = 73.310297 ( PRESS. DIFF = .l.439602 , FIG. 93. L
___ _
-
.
=
SUMMARY
OF MEASURED DATA AT TIME 445 802 TEMP 1 = 80 720 TEMP 2= 81 560 TEMP 3= 84 230 TEMP 4 = 84 890 TEMP 5= 84.570 TEMP 6= 84 840 TEMP 7 = 84 910 TEMP 8= 84.560 TEMP 9= 84 890 TEMP 10 = 84 860 TEMP 11 = 81 560 TEMP 12 = 80 330 TEMP 13 = 81 080 TEMP 14 = 83 880 TEMP 15 = 84 310 TEMP 16 = 84.590 TEMP 17 = 84.610 TEMP 18 = 84 810 TEMP 19 = 86 160 TEMP 20 = S4 820 TEMP 21 = 85.570 TEMP 22 = 84 880 ' TEMP 23 = 85.770 TEMP 24 = 86 870 TPRS 1 = 73 743 VPRS I = 0. VPRS 2= 0.A40 DIFF. PRESS. = 1 000 i CHANGE ANY DATA IF SO ENTER YES y
= '
l I l TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 2845 DATE = 802 TEMP = 84 777897 PRES = 73 303191 PRESS. DIFF = 1 439602 FIG.-94
;
- _ .
-
.
-
a
SUMMARY
9F MEASURED DATA AT TIME 500 802
>
TEMP 1 = 80 690 TEMP 2= 81 520 TEMP 3= 84 190 , TEMP 4 = 84 840 TEMP 5= 84.520 TEMP 6= 84 810 TEMP 7 = 84 870 TEMP 8= 84.510 TEMP 9= 84 850 TEMP 10 = 84 810 t TEMP 11 = 81 490 TEMP 12 = 80 280 TEMP 13 = 81 040 TEMP 14 = 83 850
'
TEMP 15 = 84 280 TEMP 16 = 84.570 TEMP 17 = 84.560 TEMP 18 = 84.760 TEMP 19 = 86 100 TEMP 20 = 84.780 TEMP 21 = 85.580 TEMP 22 = 84 840 TEMP 23 = 85.720 TEMP 24 = 86 850 TPR' I = 73 737 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
- TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 2900 DATE = 802 TEMP = 84 733497 PRES = 73 297102 PR ES S . DIFF = 1 439602 i l i l rIO. 95 l ,-
_ _ _ -
,
=
=
SUMMARY
OF. MEASURED DATA AT TIME 515 802 TEMP 1 = 80 630 TEMP 2= 81 470 TEMP 3= '84 160 TEMP 4= 84 830 TEMP 5= 84.480 TEMP 6= 84 760 TEMP 7 = 84 830 TEMP 8= 84.480 - TEMP 9 = 84.790 TEMP 10 = 84 780 TEMP 11 = 81 470 TEMP 12 = 80.220 TEMP 13 = 80 980 TEMP 14 = 83 820 TEMP 15 = 84 240 TEMP 16 = 84.540 TEMP 17 = 84 520 TEMP 18 = 84 720 TEMP 19 = 96 040 TEMP 20 = 84.760 TEMP 21 = 85.560 TEMP 22 = 84.790 TEMP 23 = 85.670 TEMP 24 = 86 790 TPRS 1 = 73 731 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
. TIME = 2915. DATE = 802 TEMP = 84.689298 PRES = 73 291012 PRESS. DIFF = 1 439602
.
TIG. 96
.
- .
-
.
.
'
=
SUMMARY
OF MEASUMED DATA AT TIME 530 802 TEMP 1 = 80.590 TEMP 2= 81 420 TEMP 3= 846110 TEMP 4= 84 740 TEMP 5= 84.440 TEMP 6= 84.720 TEMP 7 = 84.790 TEMP 8 : 84.450 T E*',P 9= 84.760 TEMP 10 = 84.730 TEMP 11 = 81 420 TEMP 12 = 80 160 TEMP 13 = 80 920 TEMP 14 = 83 760 1 TEMP 15 = 84 210 , TEMP 16 = 84.500 TEMP 17 = 84.490 TEMP 16 = 84.680 TEMP 19 = 86 010 TEMP 20 = 84.710 TEMP 21 = 85.500 TEMP 22 = 84 760 TEMP 23 = 85.620 TEMP 24 = 86.770 TPRS 1 = 73 726 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
., TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 2930 DATE = 802 TEMP = 84.648697 PRES = 73.285936 PRESS. DIFF = 1 439602 FIO. 97-
!
. =
SUMMARY
OF MEASURED DATA AT TIME 545 802 TEMP 1 = 80.550 ' TEMP 2= 81 390 TEMP 33 84 070 TEMP 4 = 84.710 TEMP 5= 84 380 TEMP 6= 84.680 TEMP 7 = 84 760 TEMP 8= 84.420 TEMP 9= 84.700 TEMP 10 = 84.680 TEMP 11 = 81 400 TEMP 12 = 80 120 TEMP 13 = 80 890 TEMP 14 = 83 720 TEMP 15 = 84 140 TEMP 16 = 84.450 TEMP 17 = 84.450 TEMP 18 = 84.640 TEMP 19 = 85 950 TEMP 20 = 84.660 TEMP 21 = 85.440 TEMP 22 = 84.700 TEMP 23 = 85.560 , TEMP 24 = 86.730 TPRS 1 = 73.718 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 , CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 2945 -
.
DATE = 802 TEMP = 84 601697 PR E S = 73 278831 PRESS. DIFF = 1 439602 FIG. 98
.- .
_ ._ _ _ _ _ _
.
.
- u
SUMMARY
0F MEASURED DATA AT TIME 600 802 TEMP 1 = 80 540 TEMP 2= 81 360 TEMP 3= 84 040 TEMP 4= 84 670 TEMP 5= 84 340 TEMP 6e 84 650 TEMP 7= 84 700 TEMP 8'= 84 380 TEMP 9= 84 680 TEMP 10 = 84 660 TEMP 11 = 81 330 TEMP 12 = 80 110 T EMP 13 = 80 860 TEMP 14 = 83 700 TEMP 15 = 84 120 TEMP 16 = 84 430 TEMP 17 = 84.420 TEMP 18 = 84 610 TEMP 19 s 85 940 TEMP 20
- C 4 640 TEMP 21 = 85 440 TEMP 22 = 84 660 TEMP 23 = 85 530 TEMP 24 = 86.700 TPRS 1 = 73 713 VPRS' I = 0 VPRS 2= 0 440 DIFF. PRESS. = 1 000
.
CHANGE ANY DATA IF SD ENTER YES
=
TEMP..AND. PRESS. CCRRECTED DATA
SUMMARY
. TIME = 600 DATE = 602-
-
TEMP = 84 573298
' PRES = 73 273756' -
PRESS. DIFF.=- 1 439602' . FIG ',199 Rev. - 1
-
-
.
.
=
SUMMARY
OF MEASURED DATA AT TIME 615 802 TEMP 1 = 80 500 TEMP 2= 81 310 TEMP 3= 84 010 TEMP 4= 84.620 TEMP S= 84 290 TEMP 6= 84.610 TEMP 7 = 84.690 TEMP 8= 84 350 TEMP 9= 84 650 TEMP 10 = 84.630 TEMP 11 = 81 350 TEMP 12 = 80 060 TEMP 13 = 80 810 TEMP 14 = 83 650 i TEMP 15 = 84 070 TEMP 16 = 84.380 3 TEMP 17 = 84.370 TEMP 18 = 84.560 TEMP 19 = 85 880 TEMP 20 = 84.580 TEMP 21 = 85 350 TEMP 22 = 84.640 TEMP 23 = 85.490 TEMP 24 = 86.650 TPRS 1 = 73.708
,
VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000
.
CHANGE ANY DATA IF SO ENTER YES
=
l TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
l I TIME = 3015 DATE = F02
-TEMP = 84.531898 PRES = 73 268682
PRESS. DIFF = 1 439602 FIT 100
.. . _.
.
.
s
SUMMARY
OF MEASURED DATA AT TIME 630 802 l TEMP 1 = 80.470 j TEMP 2= 81 290 i TEMP 3= 83 990 TEMP 4 = B4.580 TEMP 5= 84 260 i TEMP 6= 84.590
; TEMP 7 = 84.640 TEMP 8= 84 310 '
TEMP 9= 84 600 TEMP 10 = 84.590 TEMP 11 = 81 310
, TEMP 12 = 80 040 2
TEMP 13 = 80.780 l TEMP 14 = 83.620 TEMP 15 = 84 030 i TEMP 16 = 84 370 TEMP 17 = 84 340 TEMP 18 = 84.530 TEMP 19 = 85.830 TEMP 20 = 84.550 TEMP 21 = 85.360 TEMP 22 = 84.590 TEMP 23 = 85.440 TEMP 24 = 86.620 TPRS 1 = 73 703 , VPRS 1 = 0. VPRS 2= 0.440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
' TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 3030 DATE = 802 TEM P = 84.493797 PRES = 73 263607 PRESS. DIFF = 1.439602 FIG. 101
- . _ - .
,
-,-
.
4
SUMMARY
OF MEASURED DATA AT TIME 645 802 TEMP 1 = 80 430 TEMP 2= 81 260 TEMP 3= 83 960 TEMP 4 = 84.560 TEMP 5= 84 220 TEMP 6= 84.540 TEMP 7 = 84 610 ' TEMP R = 84 280 TEMP 9 = 84.560 TEMP 10 = 84.550 TEMP 11 = 81 260 TEMP 12 = 80 000 ' TEMP 13 = 80.750 TEMP 14 = 83.590 1 TEMP 15 = 84 000 TEMP 16 = 84.330 TEMP 17 = 84 300 TEMP 18 = 84.490 TEMP 19 = 85 790 TEMP 20 = 84.510 TEMP 21 = 85 300 TEMP 22 = 84.560 TEMP 23 = 85.410 TEMP 24 = 86.580 TPRS 1 = 73 698
~
VPRS 1 = 0 VPRS 2= 0.440 OIFF. PRESS. = 1 000 I CHANGE ANY DATA- IF SC ENTER YES
= ,
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
. TIME = 3045 DATE = '802 TEMP = 84.'457897 PRES = 73 258532 PRESS. DIFF = 1 439602= TIG. 102
- _
_ . . - _
. . _
.
.
-
.
=
j
SUMMARY
OF MEASURED DATA AT TIME 700 802 ! , TEMP 1 = 80 390 TEMP 2= 81 210
- TEMP 3= 83 940 TEMP 4= 84.520 TEMP 5= 84 180 TEMP 6= 84.500 TEMP 7 = 84.570
- TEMP 8= 84 240
! TEMP 9= 84.540 4 TEMP 10 = 84.520 . l TEMP 11 = 81 230 ' TEMP 12 = 79 980 TEMP 13 = 80 730 i TEMP 14 = 83.550 - TEMP 15 = 83 950
- TEMF 16 = 84 300 TEMP 17 = 84 270 i' TEMP 18 = 84.450 TEMP 19 = 85.750
! TEMP 20 = 84.500 TEMP 21 = 85.340 TEMP 22 = 84.520 TEMP 23 = 85.370 TEMP 24 = 86.540 TPRS 1 = 73.694 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 l CHANGE ANY DATA IF SO ENTER YES
=
.: TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3100 DATE = 802 TEMP = R4.421897 PR ES = 73 254471 PRESS. -DIFF =. 1 439602-TIG. 103 i:
.
.
=
SUMMARY
OF MEASURED DATA AT TIME 715 802 TEMP 1 = 80 380 TEMP 2= 81 190 TEMP 3 = 83 890 TEMP 4 = 84.490 TEMP S= 84 160 TEMP 6= 84.460 TEMP 7= 84.*30 TEMP 8= be.LiO TEMP 9= 84.490 TEMP 10 = 84.480 TEMP 11 = 81 220 TEMP 12 = 79 930 TEMP 13 = 80 670 TEMP 14 = 83.530 TEMP 15 = 83 940 TEMP 16 = 84.270 TEMP 17 = 84 240 TEMP 18 = 84.420 TEMP 19 = 85.720 TEMP 20 = 84 470 TEMP 21 = 85 270 TEMP 22 = 84.480 TEMP 23 = 85 320 TEMP 24 = 86.520 ' TPRS 1 = 73.689 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3115 DATE = 802 , 1 TEMP = 64 388097
'
PRES = 73 249397 PR E S S . DIFF. = 1 439602 TIC.1104
.
.
.
-
s
SUMMARY
OF MEASURED DATA AT TIME 730 802 TEMP 1 = 80 350 TEMP 2= 81 160 TEMP 3= 83 860 TEMP 4 = 84.490 TEMP 5= 84 110
'
TEMP 6= 84.440 TEMP 7 = 84.510 TEMP 8= S4.180 TEMP 9= 84.460 TEMP 10 = 84.470 TEMP 11 = 81 150 TEMP 12 = 79 890 TEMP 13 = 80.640 TEMP 14 = 83.510 TEMP 15 = 83 890 4 TEMP 16 = 84 240 TEMP 17 = 84.210 TEMP 18 = 84 380 TEMP 19 = 85.690 TEMP 20 = 84.430 TEMP 21 = 85.210 TEMP 22 = 84.460 TEMP 23 = 85.290
- TEMP 24 = 86 490 TPRS 1 = 73.684 VPRS 1 = 0.
VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
- TIME = 3130 DATE = 802 TEMP = 84 358997-PRES = 73 244322
.
PRESS. DIFF = 1.439602 ,
""'h
']
r!G. 105 ,
.
.
=
SUMMARY
OF MEASURED DATA AT TIME 745 802 TEMP 1 = 80 320 TEMP 2= Rt.120 TEMP 3= 83 830 TEMP 4 = 84.430 TEMP 5= 84 090 TEMP 6 = 84.400 TEMP 7 = 84.470 TEMP 8= 84 150 TEMP 9 = 84.430 TEMP 10 = 84.410 TEMP 11 = 81 110 TEMP 12 = 79 840 TEMP 13 = 80 600 TEMP 14 = 83 480 TEMP 15 = 83 860 TEMP 16 = 84 220 TEMP 17 = 84 180 TEMP 18 = 84 360 TEMP 19 = 85.640 TEMP 20 = 84.410 TEMP 21 = 85.200 TEMP 22 = 84.410 TEMP 23 = 85 250 TEMP 24 = 86 440 I TPRS 1 = 73 681 l ] VPRS 1 = 0.
'
VPRS 2= 0 440 DIFF. PRESS. = 1 000 i CuANGE ANY DATA IF SO ENTER YES d : TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 3145 ,- DATE = 802 TEMP = 94 319696 PRES = 73 241277' PRESS.LDIFF
~
= -l.439602'
?!S. 106
..
.
.
=
SUMMARY
OF MEASURED DATA AT TIME 800 802 TEMP 1 = 80 270 TEMP 2= 81 100 TEMP 3= 83 800 TEMP 4 = 84.400 TEMP 5= 84 040 TEMP 6= 84 380 TEMP 7 = 84.450 TEMP 8 = 84 120 TEMP 9 = 84.400 TEMP 10 = 84 360 TEMP 11 = 81 120 TEMP 12 = 79 760 TEMP 13 = 80 590 TEMP 14 = 83 430 TEMP 15 = 83 830 TEMP 16 = 84 180
'
TEMP 17 = 84 140 TEMP 18 = 84 310 TEMP 19 = 85.610 TEMP 20 = 84 350 TEMP 21 = 85 190 TEMP 22 = 84 380 TEMP 23 = 85 210 TEMP 24 = 86 410
'
TPRS I =- 73 673 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000
.
l CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3200 . DATE = 802 l - , TEMP = R4 284297 PRES = 73.233156 PnESS. DIFF = 1 439602 FIG. ; l l _ _
.
4
.
=
SUMMARY
CF MEASURED DATA AT TIME 815 802 TEMP 1 = 80 270 TEMP 2= 81 080' TEMP 3= 83 800 TEMP 4 = 84 360 TEMP 5= R4 000 TEMP 6= 84 350 TEMP 7 = 84.400 TEMP 8 = 84 110 TEMP 9- - 84.360 TEMP 10 =' '4.350 TEMP 11 = 81 090 TEMP 12 = 79.780 . TEMP 13 = 80.560 TEMP 14 = 83 410 TEMP 15 = 83.800 TEMP 16 = 84 140 TEMP 17 = 84 110 TEMP 18 = 84 290 TEMP 19 = 85 580 TEMP 20 = 84 320 TEMP 21 = 85 140 TE.vP 22 = 84 350 TEMP 23 = 85 180 TEMP 24 = 86 390 T5rS 1 = 73 670
\) P R 'i 1 = 0.
VPFS 2= 0 440
'. I FF . PRESS. = 1 000 CFANGE ANY OATA IF SC ENTER YES
=
TEMP. AND PRESS. .CCRRECTED DATA-
SUMMARY
TIME = .15
.
DATE = 802 TEMP = 84 259697 PRES . = 73 230112-PRESS. DIFF =- 1 439602 FIG, 108
.
4 a
SUMMARY
OF MEASURED DATA AT TIME 830 802 TEMP 1 = 80 230 TEMP 2= 81 050 TEMP 3= 83.780 TEMP 4= 84 320 TEMP 5= 83 970 TEMP 6= 84 310 TEMP 7= 84 390 TEMP 8= 84 070 TEMP 9= 84 330 ' TEMP 10 = 84 330 TEMP 11 = 81 060 TEMP 12 = 79 740 TEMP 13 = 80.530 TEMP 14 = 83 360 TEMP 15 = 83 760 TEMP 16 = 84 140 TEMP 17 = 84 080 TEMP 18 = 84 260 TEMP 19 = 85.520 TEMP 20 = 84 310 TEMP 21 = 85 110 TEMP 22 = 84.320 ! TEMP 23 = 85 130 TEMP 24 = 86.350 TPRS 1 = 73 665 VPRS I = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
l i ! I j TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3230 DATE = 802 . TEMP = 84 222198 PRES = 73 225037 PRESS. DIFF = 1 439602 ZI3. 109
-
. __ - . _ _
.
' .
.
E
SUMMARY
CF MEASURED DATA AT TIME 845 802 TEMP 1 = 80.200 TEMP 2= 81 030 TEMP 3= 83 740 TEMP 4= 84 310 TEMP 5= 83 920 TEMP 6 = 84 290 TEMP 7 = 84 350 , TEMP 8= 84 040 TEMP 9= 84 320 TEMP 10 = 84 290 TEMP 11 = 81 020 TEMP 12 = 79 710 TEMP 13 = 80.530 TEMP 14 = 83 340 TEMP 15 = 83 730 TEMP 16 = 84 110 TEMP 17 = 84.060 TEMP 18 = R4 240 TEMP 19 = 85.500 TEMP 20 = 84 290 TEMP 21 = 85.050 TEMP 22 = 84.300 TEMP 23 = 85 110 TEMP 24 = 86 350
.
TPRS I = 73.662
VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CrRRECTED DATA
SUMMARY
TIME = 3245 DATE = 802 . TEMP = 84 200197 PRES = 73 221992 PRESS. DIFF = 1 439602 TI~. 110
. _ _ - _ - - _ . _ _ _ - - _ _ _ _ _ _ _ _
..
.
.
- D
SUMMARY
OF MEASURED DATA AT TIME 900 802
.
TEMP 1 = 80 180 TEMP 2= 81 020 TEMP 3= 83.710 TEMP 4= 84.320 TEMP 5= 83 840 TEMP 6= 84 250 TEMP 7 = 84 340 TEMP 8 = 84 020 TEMP 9= 84 220 TEMP 10 = 84 260 TEMP 11 = 81 050 TEMP 12 = 79 680 TEMP 13 = - 80 470 TEMP 14 = 83 320 TEMP 15 = 83.720 TEMP 16 = 84 080 TEMP 17 = 84 030 TEMP 18 = 84 220 TEMP 19 = 85.460 TEMP 20 = 84 250 TEMP 21 = 85 080 TEMP 22 = 84 280 TEMP 23 = 85 090 TEMP 24 = 86 320 TPRS 1 = 73.657 VPRS I = 0. VPRS 2= 0.440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SD ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 3300 DATE = 802 TEMP = 84 172897 PRES = 73 216916
. PRESS. DIFF = 1 439602 TIG. 111
-
. _ _ _ _
. - _ _ ,
,
,
=
SUMMARY
OF MEASURED DATA AT TIME 915 802 U=0S 1 = 80 160 TEMP 2= 80 970 TEMP 3= 83.710 TEMP 4 = 84 280 TEMP 5= 83 890 TEMP 6 = 84 240 TEMP 7 = 84 300 TEMP 8 =- 84 000 TEMP 9= 84 250 TEMP 10 = 84.270 TEMP 11 = PO.980 TEMP 12 = 79 680 TEMP 13 = 80 470 TEMP 14 = 83.300 TEMP 15 = 83.680 TEMP 16 = 84 050 TEMP 17 = 84.010 TEMP 18 = 84 170 TEMP 19 = 85.440 TEMP 20 = 84 240 TEMP 21 = 85 020 TEMP 22 = 84 240 TEMP 23 = 85 030 TEMP 24 = 86.270 TPRS I = 73 652 VPRS I = 0. VPRS 2 = 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SC ENTER YES
=
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3315 DATE = 802
.
TEMP-= S4.I44999 4
'FRES =' 73.212857
. PRESS. DIFF = 1 439602 FIO. 112
. _ . .
.
o .
SUMMARY
CF MEASURED DATA AT TIME 930 802 i TEMP I = 80 130 TEMP 2= 80 970 TEMP 3= '83 680 TEMP 4 = 84 240 TEMP 5= 83 850 TEMP 6= 84 220 ,
~ TEMP 7 = 84 280 TEMP 8 = 83 980 TEMP 9= 84 230 TEMP 10 = 84 240 TEMP 11 = 80 990 TEMP 12 = 79 640 TEMP 13 = 80 450 TEMP 14 = 83 270 TEMP 15 = 83 650 TEMP 16 = 84 030 TEMP 17 = 83 990 t
TEMP 18 = 84 150 TEMP 19 = 85.410 TEMP 20 = 84 200 TEMP 21 = 85 030 TEMP 22 = 84 200 TEMP 23 = RS.020 ] TEMP 24 = 86 250 i TPRS I = 73.649 i VPRS I = 0. VPRS 2= 0.AA0 DIFF. PRESS. = 1 000 l
,
CHANGE ANY DATA IF SC ENTER YES
=
J TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3330 %N DATE = 802
.
TEMP =- 84 121097 PRES = 73 209811 PR ES S . DIFF = 't.439602 4 FI3. 113
'
. , . , . . -. - -
.
-
.
. a
SUMMARY
OF MEASURED DATA AT TIME 945 802 TEMP 1 = 80 110 TEMP 2= 80 930 TEMP 3 = 83.660 TEMP 4 = 84 190 TEMP 5= 83 830
-TEMP 6= 84 180 TEMP 7 = 84 250 TEMP 8 = 83 950
, TEMP 9= 84 220 l TEMP 10 = 84 200 TEMP 11 =- 80 930 TEMP 12 = 79 600 TEMP 13 = 80 440 TEMP 14 = 83 240 TEMP 15 = 83 620 TEMP 16 = 84 030 TEMP 17 = 83 960 TEMP 18 = F4 120 TEMP 19 = 85.390 TEMP 20 = 84 160 TEMP 21 = 85.020 TEMP 22 = 84 170 TEMP 23 = 84 990 TEMP 24 = 86 220 ' TPRS 1 = 73 645 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
4
. TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
. TIME = 3345 -
DATE =- 802
,
TEMP = F4.09169R' PRES = 73 205751
-
PRESS. DIFF = 1 439602-FIC. , - 114 -
.-
-
.
-
.
- -
SUMMARY
CF MEASURED DATA AT TIME 1000 802 TEMP 1 = 80 090 TEMP 2= 80 910 TEMP 3= 83 650 ' TEMP 4= S4-150 TEMP 5= 83 790 TEMP 6= 84 160 TEMP 7= 84 220 TEMP 8 = 83 930 TEMP 9= 84 170 TEMP 10 = 84 180 TEMP 11 = 80 940 TEMP 12 = 79.580 TEMP 13 = 80 400
'
TEMP 14 = 83 240 TEMP 15 = 83.600 TEMP 16 = 83.990 TEMP 17 = 83.940 TEMP 18 = 84 090 - TEMP 19 = 85 330 TEMP 20 = 84 150 TEMP 21 = 84 950 TEMP 22 = 84 140 TEMP 23 = 84 950 TEMP 24 = 86 210 TPRS 1 = 73.641 VPRS I = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 J 1 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3400 DATE = 802
-
#.
TEM' 94 061399 PRES
- 73 201693
' PRESS . DIFF = 1 439602 TIG. 115 4
w
_ - ,-
.
.
'
SUMMARY
OF MEASURED DATA AT TIME 1015 802 TEMP 1 = 80 060 TEMP 2= 80 890 TEMP 3= F3.620 TEMP 4'= 84 170 TEMP. 5= 83 750 TEMP 6= 84 120 TEMP 7 = 84.200 TEMP 8= 83 890 TEMP' 9= 84 160 TEMP 10 = 84 150 TEMP 11 = 80 930 TEMP 12 = 79 550 TEMP 13 = 80 360 TEMP 14 = 83 200 TEMP 15 = 83.560 TEMP 16 = 83 970 TEMP 17 = 83 910 TEMP 18 = g4 070 TEMP 19 = 85.320 TEMP 20 = 84 110 TEMP 21 = 84 950 TEMP 22 = 84 120 TEMP 23 = 84.920 TEMP 24 = 86 179 TPRS I = 73.638 VPRS I = 0 VPRS 2= 0.AA0 DIFF. PP.ESS. = 1 000 CFANGE ANY DATA IF SO ENTER YES-
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME =- 3415 DATE = ~802 - TEMP _= F4 037398 PRES'=- 73 198647~ PRESS. 'DIFF = 1 439602. FIG. 116 _ _ _
. _ -___
#
o
SUMMARY
07 MEASURED DATA AT TIME 1030 802 , TEMP 1 = 80 050 TEMP 2= 80 870 TEMP 3= 83.600 TEMP 4 = 84 130 TEMP S= 83 740 TEMP 6= 84 090 TEMP 7 = 84 190 TEMP 8= 83 880 TEMP 9= 84 130 TEMP 10 = 84 140 TEMP 11 = 80 920 TEMP 12 = 79 550 TEMP 13 = 80 360 TEMP 14 = 83 170 TEMP 15 = 83.540 TEMP 16 = 83 960 TEMP 17 = 83 870 TEMP 18 = 84 040 TEMP 19 = 85.290 TEMP 20 = 84 110 TEMP 21 = 84 900 TEMP 22 = 84 090 TEMP 23 = 84 910 TEMP 24 = 86 140 TPRS I = 73.634 VPRS 1 = 0. VPRS 2= 0.440 DIFF. PRESS. = 1 000 CHANGE ANY OATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
l TIME = 3430 DATE = 802 TEMP = 84 014598 PRES = 73 194586 ! l PRESS. DIFF = 1 439602 , ! - FIG. 117
! _ -
-. -- .
8
SUMMARY
OF MEASURED DATA-AT TIME 1045 802 TEMP 1 = 80.020 TEMP 2= 80 840 TEMP 3= 83.590 TEMP 4 = 84 110 TEMP - 5= 83.690 TEMP 6 = 84 060 TEMP 7 = 84 170 TEMP 8= 83 870 TEMP 9= 84 100 TEMP 10 = 84 100 TEMP 11 = 80 890 TEMP 12 = 79 520 TEMP 13 = 80 350 ' TEMP 14 = 83 150 TEMP 15 = 83 520 TEMP 16 = 83 910 TEMP 17 = 83 870 TEMP 18 = 84 020 TEMP .' = 85.250 TEMP 20 = 84 090 TEMP 21 = 84 830 TEMP 22 = 84 070 TEMP- 23 = R4 870 TEMP 24 = 86 120 1 TPRS 1 = 73 631 VPRS 1 = 0. VPRS 9= 0.440
DIFF. PRESS.'= 1.000 I CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3445 DATE = 802
.
TEMP = R3 988198 PRES =' 73 1915A2 ' PRESS. DIFF = 1 439602 FIG. 118'
. - _ _ . . .
SUMMARY
OF MEASURED DATA AT TIME 1100 802 - TEMP 1 = 80 010 TEMP 2= 80 820 TEMP 3= 83.570 TEMP 4= 84 080 TEMP 5= 83 680 TEMP 6= 84 050 TEMP 7 = 84 140 TEMP 8= 83 850 TEMP 9= 84 100 TEMP 10 = 84 080 TEMP 11 = 80 850 TEMi 12 = 79.510 TEMP 13 = 80 340 TEMP 14 = 83 140 TEMP 15 = 83.500 TEMP 16 = 83.910 TEMP 17 = 83 830 TEMP 18 = 84 000 TEMP 19 = 85 240 TEMP 20 = 84 070 TEMP 21 = 84 820 TEMP 22 = 84.050 TEMP 23 = 84 820 TEMP 24 = 86.090 TPRS I = 73 628 VPRS I = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF S ENTER YES
=
,
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 3500 DATE = 802 , TEMP'= 83 965898 ' PRES = 73.188497 i PRESS. DIFF = 1 439602 l ! l -- wes FI r. . 119
.
=
SUMMARY
OF MEASURED DATA AT TIME 1115 802 TEMP 1 = 79 990 TEMP 2= 80 810 TEMP 3= 83.540 TEMP 4= 84.070 TEMP 5= 83.660
':MP 6= 84 010 TEMP 7 = 84 120 TE.vP R = 83 840 TEMP 9= 84 070 TEMP 10 = 84 050 TEMP 11 = 30 850 TEMP 12 = 79 470 TEMP 13 = 80 310 TEMP 14 = 83 100 TEMP 15 = R3 480 TEMP 16 = 83 890 TEMP 17 = 83.810 TEMP 18 = 83 970 TEMP 19 = 85.220 TEMP 20 = P4.050 TEMP 21 = 84 800' TEMP 22 = 84 020 TEMP 23 = R4 810 TEMP 24 - 86.070 TPRS I = 73 625 VPRS 1=' O.
VPRS 2= 0.440 DIFF. PRESS. = 1 000
.
CMANGE ANY DATA IF SC ENTER YES
=
TEMP. AND PRESS'. .CCRRECTED DATA
SUMMARY
TIME = 3515 DATE = 802 . TEMP =- 83 94439F PR ES = 73 145452 PRESS. DIFF = 1 439602-TIC. 120
.-
.
4
SUMMARY
OF MEASURED DATA AT TIME 1130 802 TEMP 1 = 79 980 TEMP 2= 80.790 TEMP. 3= 83.530 TEMP 4= 84 070 TEMP 5= 83 630 TEMP 6= 83 990 TEMP 7= 84 120 TEMP 8= 83 810 TEMP 9= 84 060 TEMP 10 = 84 040 TEMP 11 = 80 800 TEMP 12 = 79 460 TEMP 13 = 80.290 TEMP 14 = 83 070 TEMP 15 = 83.460 TEMP 16 = 83 880 TEMP 17 = 83.790 TEMP 18 = 83 960 TEMP 19 = 85 190 TEMP 20 = 84 030 TEMP 21 = 84 810 TEMP 22 = 84 000 TEMP 23 = 84 810 TEMP 24 = 86 070 TPRS 1 = 73.622 VPRS 1 = 0. VPRS 2= 0.440 DIFF. PRESS. = 1 000
.
CHANGE ANY DATA IF SD ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 3530 DATE = R02 . TEMP = 83 929298 PRES = 73 182407 PRESS. DIFF = 1 439602 TIG. 121
.-
._-_. . . _ _ _ _ _ _ _ _ _ _ _ _
_ _.
SUMMARY
CF MEASUPED DATA AT TIME 1145 802 TEMP 1 = 79 960 TEMP 2= 80.780. TEMP 3= 83.510 TEMP 4= 84 040 TEMP 5= 83.620 TEMP 6= 83 980 TEMP 7 = 84 100 TEMP 8 = 83.800 TEMP 9 = 84 040 TEMP 10 = 84 020 TEMP 11 = 80 800 TEMP 12 = 79 450 TEMP 13 = 80 270 TEMP 14 = 83 050 TEMP 15 = 83 440 TEMP 16 = 83 840 TEMP 17 = 83 780 TEMP 18 = -83 940 , TEMP 19 = 85 150 TEMP 20 = 84.030 TEMP 21 = 84.780 TEMP 22 = 83 970 TEMP 23 = 84.760 TEMP 24 = 86 040 TPRS 1 = 73 618 VPRS 1 = 0. VPRS 2= 0 440 DIFF. PRESS. = 1 000 CuA?!GE ANY DATA IF e ENTER YES
-
l
)
;
TE'P. AND PRESS. CORRECTED DATA
SUMMARY
i TIME = .3545
.
DATE = ROR TEMP = 'F3.904198~
-
PRES = 73 178347 PRESS. DIFF = 1 439602
'7 % 122
_1
.
SUMMARY
OF MEASURED DATA AT TIME 1200 802 TEMP 1 = 79 930 TEMP 2= 80 760 TEMP 3= 33 480 TEMP 4= 84 000 TEMP 5= 83.590 TEMP 6= 83 950 TEMP- 7= 84 060 TEMP 8= 83.780 TEMP 9= 84 020 TEMP 10 = 84 000 TEMP 11 = 80 760 TEMP 12 = 79 430 TEMP 13 = 80.440 TEMP 14 = 83 040 TEMP 15 = 83 410 TEMP 16 = 83 830 TEMP 17 = 83 750 TEMP 18 = 83 910 TEMP 19 = 85 130 TEMP 20 = 83 990 TEMP 21 = 84 780 TEMP 22 = 83.950 TEMP 23 = 84 750 TEMP 24 = 86 000 TPRS 1 = 73 615 VPRS I = 0 VPRS 2= 0 440 DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SD ENTER YES
=
TEMP. AND PRESS. CORRETED DATA
SUMMARY
TIME = 3600 DATE = 802 -TEMP = R3 881898 PRES = 73 175303 PRESS. DIFF.= 1 439602 FIC. 123
. . . -
SUMMARY
0F MEASURED DATA AT TIME 1215 802 s
.
TEMP 1= 79 920 ' TEMP 2= 80 740 TEMP 3= 83 460 TEMP 4= 83 970 TEMP 5= -83 570 TEMP 6= 83 910 TEMP 7= 84 030 TEMP 8= 83 760 TEMP 9= 83 980 TEMP 10 = 83 980 TEMP 11 = B0 750 TEMP 12 = 79 400 TEMP 13 = 80 250- ' TEMP 14 = 83 010 TEMP 15 = 83 390 TEMP 16 = 83 810 TEMP 17 = 83 730 TEMP 18 = 83 890 TENP 19 = 85 110 TEMP 20 = 83 950 1 TEMP 21 = 84 720 TEMP 22 = 83 910 TEMP 23 = 84 730 TEMP 24 = 85 980 TPRS 1 = 73 612 VPRS 1 = 0 VPRS 2= 0 440 DI FF. PRESS. = 1 000
.
CHANGE ANY DATA IF SO ENTER YES
=
4
\
-
'
\
l i TEMP. AND PRESS. CORRECTED DATA
SUMMARY
i i TIME = 1215 A DATE = 802 TEMP = 83 855699 + l PRES = 73 172256 PRESS.- DI FF = 1 439602 FIG, 123A Rev.
'
1
__
. .
OCONEE 1 59 PSIG VERIF ENTER TIME, DATE, TEMP, PRESS, PRESS DIFF WHEN FINISHED ENTER 9999,,,,,
= 1415,0802,83 688598,73 146621,1
= 1430,0802,R3.678597,73 142561,1
= 1445,0802,83.662497,73 138501,1
= 1500,0802,83 645398,73 133427,1
= 1515,0802, R3.626899,7 3 130381,1
= 1530,0802,83 611897,73 127336,1
= 1545,0802,83.590598,73 123276,1
= 1600,0802,83.578398,73 120677,1
= 1615,0802,83 564097,73 117632,1
= 1630,0802,83 540298,73 11357d,1
= 1645,0802,83.527198,73 109512,1
= 1700,0802,83.521998,73 106467,1
= 1715,0802,R3 510398,73 103868,1
= 1730,0802,83.525997,73 100824,1 I = 1745,0802,83 491998,73 096764,1
= 1800,0802,83 466998,73 092704,1
= 1815,0802,83.449498,73 088644,1
'
= IR30,0R02,83 441897,73.085599,1
= 1845,0802,R3 424597,73.OR1539,1
= 1900,0R02,83.417099,73 078494,1
= 1930,0R02,83 398098,73 072822,1
= 9999,,,,,
I l I
!
l l FIG. 124
f
.
.
OCONEE 1 59PSIG VERIF TIME, DATE START OF TEST 14 25 802 TIME AFTER START OF TEST = 5.250 HR CCNTAINMENT AVERAGE TEMPERATURE = 83 398 F CCNTAINMENT AVERAGE PRESSURE = 73 073 PSIA TRENDS BASED ON TOTAL TIME CALCULATIONS HOURS DATA MEAN OF CALCULATED OF TEST ENTRIES CALC. LR LEAK RATE 0 75 4 0 327E+00 0 310E+00
- 1. C.3 5 0 310E+00 0 270E+00
. 25 6 0.295E+00 0 239E+00 1 50 7 0 283E+00 0 216E+00 1.75 8 0 272E+00 0 198E+00 2 00 9 0.264E+00 0 185E+00 2 25 10 0 255E+00 0 173E+00 2 50 11 0 250E+00 0 170E+00 2 75 12 0 247E+00 0 171E+00 3 00 13 0 243E+00 0 170E+00 3 25 14 0 243E+00 0 180E+00 3.50 15 0.241E+00 0 182E+00 3 75 16 0 239E+00 0 182E+00 4 00 17 0 238E+00 0 183E+00 4 25 18 0 236E+00 0 184E+00 4.50 19 0 235E+00 0 186E+00 4.75 20 0 234E+00 0 188E+00 5 25 21 0 234E+00 0 186E+00
! THE CALCULATED LEAK RATE IS 0.iR6E+00 l THE MAXIMUM ALLOWABLE LEAK RATE IS 0 250E+00 l THE LAST 1 DATA PGINTS ESTABLISH A NEGATIVE SLOPE i l FIG. 125
_ __, _ - - - _ - - _ _ _ _ _ - - _ - - - - _ - _ - - - .
.
CCONEE 1 59PSIG VERIF ABSCLUTE CALCULATIONS TIME, DATE START CF TEST 14 25 802 TIME AFTER START OF TEST = 5.250 HR CCNTAINMENT AVERAGE TEMPERATURE = 83 398 F CENTAINMENT AVERAGE PRESSURE = 73 073 PSIA LEAX RATE 9ASED CN TOTAL TIME CALCULATIONS TIME TEMPERATURE PRESSURE LEAX RATE LEAX RATE 95% CONFIDENCE (PSIA) MEASURED CALCULATED v LIiIls 14.50 83.6R 73 14 0.356E+00 0 277E+00 0 20E+00 0.36E+00 14.75 93.66 73 14 0 302E+00 0 273E+00 0 19E+00 0 35E+00 15.00 R3 65 73 13 0.323E+00 0 26RE+00 0 19E+00 0 35E+00 15 25 83 63 73 13 0.260E+00 0 264E+00 0 19E+00 0 34E+00 15 50 F3.61 73 13 0 235E+00 0 259E+00 0.lRE+00 0 34E+00 15.75 83 59 73 12 0 222E+00 0 254E+00 0 18E+00 0 33E+00 16.00 F3.5R 73 12 0.208E+00 0 250E+00 0 17E+00 0 33E+00 16 25 R3 56 73 12 0 201E+00 0 245E+0t. 0 17E+00 0 32E+00 16.50 33 54 73 11 0 191E+00 0 241E+00 0 16E+00 0 32E+00
- 16.75 93.S3 73 11 0 202E+00 0 236E+00 0 16E+00 0.31E+00 17 00 R3 52 73.11 0 212E+00 0 231E+00 0 16E+00 0 31E+00
'
1 17 25 83 51 73 10 0 205E+00 0 227E+00 'C.15E+00 0 30E+00 17.50 #3.53 73 10 0 241E+00 0 222E+00 0 15E+00 0 30E+00 17 75 F3.49 73 10 0 219E+00 0 218E+00 0 14E+00 0 29E+00'
' FI G . 126 L.mm. _
.
.
i 18 00 83 47 73.09 0.211E+00 0 213E+00 0 14E+00 0 29E+00 , 18 25 83 45 73 09 0 212E+00 0 209E+00 0 13E+00 0.29E+00 18 50 83.44 73 09 0 215E+00 0 204E+00 0 13E+00 0 28E+00 18 75 83 43 73 08 0 219E+00 0 199E+00 0 12E+00 0 28E+00 19 00 83 42 73.08 0 218E+00 0 195E+00 0 12E+00 0 27E+00 19 50 83 40 73 07 0 217E+00 0 186E+00 0 10E+00 0 27E+00 IF IT IS ASSUMED THAT THE LEAR RATE IS CONSTANT: THE MEAN IS 0 234E+00 ^ THE STANDARD DEVI ATI CN IS 0 440E-Ol SKEW IS POSITIVE THE CALCULATED LEAK RATE AFTER 5.25 HOURS OF TEST IS 0 186E+00 MEASURED LEAK RATE COMPUTED FR00 MEASURED VALUES TEMPERATURE AND PRESSURE CALCULATED LEAK RATE COMPUTED FRCM LINEAR , LEAST SOUARE FIT OF MEASURED LEAR RATES
,
e FIG. 127
. LEAK RATE BASED EN POINT-TO-POINT CALCULATIONS TIME TEMPERATURE PRESSURE LEAK RATE LEAK RATE 95% CCNFIDENCE (PSIA) MEASURED CALCULATED LIMITS 14.50 83 68 73 14 0 356E+00 . 0 221E+00 -0 13E+00 0.5RE+00 14.75 83.66 73 14 0.248E+00 0 221E+00 -0 13E+00 0.57E+00 15 00 83 65 73 13 0 364E+00 0 220E+00 -0 13E+00 0 57E+00 15 25 83.63 73 13 0.730E-01 0 220E+00 -0 12E+00 0 56E+00 15.50 83 61 73 13 0 135E+00 0 220E+00 -0 12E+00 0.56E+00 15 75 83.59 71 12 0 157E+00 0 219E+00 -0 12E+00 0.56E+00 16.00 F3.58 73 12 0.126E+00 0 219E+00 -0 12E+00 0.56E+00 16 25 83.56 73 12 0 147E+00 0 219E+00 -0 12E+00 0.55E+00 . 16.50 R3.54 73 11 0 112E+00 0 218E+00 -0 12E=00 0 55E+00 16.75 F3.53 73 11 0 301E+00 0 218E+00 -0 12E+00 0 55E+00 17.00 83.52 73 11 0.308E+00 0 218E+00 -0 12E+00 0.55E+00 17 25 R3 51 73 10 0 136E+00 0 217G+00 -0 12E+00 0.55E+00 17 50 R3 53 73 10 0 676E+00 0 217E+00 -0 12E+00 0.55E+00 17.75 83 49 73 10 -0.675E-01 0 216E+00 -0 12E+00 0.55E+00 1 18 00 83 47 73.09 0 914E-01 0 216E+00 -0 12E+00 0.56E+00 ' 1R.25 83 45 73 09 0.224E+00 0 216E+00 -0 13E+00 0 56E+00 1P.50 83 44 73 09 0 266E+00 0 215E+00 -0 13E+00 0.56E+00 18 75 83 43 73.08 0 298E+00 0 215E+00 -0 13E+00 0.56E+n0 19 00 83 42 73 08 0 197E+00 0 215E+00 -0 14E+00 0 57E+00 19.50 83.40 73 07 0 205E+00 0 214E+00 -0 15E+00 0.57E+00
.
IF IT IS ASSUMED TuAT TWE LEAR RATE IS CCNSTANT: TuE MEAN IS 0 21PE+00 TuE STANDARD DEVIATION IS 0 151E+00 SWEW IS POSITIVE THE-CALCULATED LEAM RATE AFTER 5 25 HCURS CF TEST IS 0 214E+no FIS, 12R
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,_
SUMMARY
-OF MEASURED DATA AT TIME.1415 802 TEMP 1 = 79.790 TEMP 2= 80.620 TEMP 3= 83 320 TEMP 4 = 83 840 TEMP 5= 83 400 TEMP 6= 83 77C TEMP 7= 33.890 TEMP 8= 83 610 TEMP 9 = 83 820 TEMP 10 = 83 830 TEMP 11 = 80 660 TEMP 12 = 79 310 TEMP 13 = 80 080 TEMP 14 = 82 860 TEMP 15 = 83 230 TEMP 16 = 83.650 TEMP 17 = 83 570 TEMP 18 = 83.720 TEMP 19 = 84 900 TEMP 20 = 83 820 TEMP 21 = 84.570 TEMP 22 = 83 750 TEMP 23 = 84.490 TEMP 24 = 85 810 TPRS 1 = 73.579 VPRS 1 = 0 433 VPRS 2= 0. DIFF. PRESS. = 1 000 CuANGE ANY DATA IF SC ENTER YES
=
.
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1415 DATE = F02 l iEXP = l F3.688598 l PRES = 73 146621 l PRESS. DIFF = 1 432758-
'T 3. 130-
-
1
--
.
.
= -
I
SUMMARY
OF MEASURED DATA AT TIME 1430 802 . TEMP 1 = 79 780 TEMP 2= 80 610 TEMP 3= 83 320 TEMP 4= 83 820 i TEMP 5= 83 370 i TEMP 6= 83.750 TEMP 7= 83 870 TEMP 8= 83.610 TEMP 9 = 83 820 TEMP 10 = 83 820 TEMF 11 = 80 650 TEMP 12 = 79.300 TEMP 13 = 80 050 TEMP 14 = 82 830 TEMP 15 = 83 230 TEMP 16 = 83.630 TEMP 17 = 83.550 TEMP 18 = 83 720 TEMP 19 = 84.900 TEMP 20 = 83 830 TEMP 21 = 84.560 TEMP 22 = 83 740 TEMP 23 = 84.480 TEMP 24 = 85.780 TPRS 1 = 73.575 VPRS 1 = 0 433 VPRS 2= 0. DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
.
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 1430 DATE = 802 TEMP = 83 678597 PRES = 73 142561
.
PRESS. DIFF = 1 432758 FIG. 131
.
=
SUMMARY
OF MEASURED DATA AT TIME 1445 802 , TEMP 1 = 79 750 TEMP 2= 80 600
. TEMP 3= 83 310 TEMP -4 = 83 820 TEMP 5= 83 360 TEMP 6= 83 750 1EMP 7 = 83 880 TEMP 8= 83.580 TEMP 9= 83 800 TEMP 10 = 83 810 TEMP 11 = 80.660 TEMP 12 = 79 290 TEMP 13 = 80 040 TEMP 14 = 82 820 '
TEMP 15.=' 83 200 TEMP 16 = 83.610 TEMP 17 = 83.540 TEMP 18 = 83 690 TEMP 19 = 84 880 TEMP 20 = 83.790 TEMP 21 = 84.580 TEMP 22 = 83 710 TEMP 23 = 84.480 TEMP 24 = R5 760 i , TPRS 1 = 73 571 l i VPRS 1 = 0.433 l VPRS 2= 0.
! ,
DIFF. PRESS. = 1 000
- j CHANGE ANY DATA IF SC ENTER YES 1 =
TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
TIME = 1445 DATE = 802 TCMP' = 83 662497 PREE = 73 138501 PRES:1 DIFF = 1 432758 < FIG. 132
.
s
SUMMARY
OF MEASURED DATA AT TIME 1500 802 TEMP 1 = 79 750 TEMP 2= 80.600 TEMP 3= 83 290 TEMP 4 = 83 750 TEMP 5= 83 360 TEMP 6= 83 720 TEMP 7= 83.840 TEMP 8= 83.570 TEMP 9= 83 790 TEMP 10 = 83.780 TEMP 11 = 80 620 TEMP 12 = 79 280 TEMP 13 = 80.030 TEMP 14 = 82 820 TEMP 15 = 83 200 TEMP 16 = 83 600 TEMP 17 = 83 530 TEMP 18 = 83.680 TEMP 19 = 84 850 TEMP 20 = 83 770 TEMP 21 = 84.570 TEMP 22 = 83 690 TEMP 23 = 84.470 TEMP 24 = 85.760 TPRS 1 = 73.566 VPRS 1 = 0 433 VPRS 2= 0. DIFF. PRESS. = 1 000
,
CHANGE ANY DATA IF SO ENTER YES = TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1500 DATE = 802 TEMP = 83.645398 PRES = 73 133427 PRESS. DIFF = 1 432758 FIO. 133
. . =
SUMMARY
OF MEASURED DATA AT TIME 1515 802 TEMP 1 = 79 730 TEMP 2= 80.590 TEMP 3= 83 270
. TEMP 4= 83.770 TEMP 5= 83 330 TEMP 6= 83 690 TEMP 7 = 83 830 TEMP 8= 83.560 TEMP 9= 83.770 TEMP 10 = 83 760 TEMP 11 = 80 610 TEMP. 12 = 79 260 TEMP 13 = 80 030 TEMP 14 = 82 810 TEMP 15 = 83 180 TEMP 16 = 83.580 TEMP 17 = 83.530 TEMP 18 = 83.660 TEMP 19 = 84 830 TEMP 20 = 83 770 TEMP 21 = 84.510 TEMP 22 = 83.670 TEMP 23 = 84.440
' TEMP 24 = 85.720 TPRS 1 = 73.563 i VPRS 1 = 0 433 VPRS 2= 0. DIFF. PRESS. = 1 000 i CHANGE ANY DATA IF SC ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA.
SUMMARY
TIME = ISIS DATE = F02-TEMP = R3 626899 PRES =-_73 1303F1 PRESS.~DIFF = 1 432758 FIG. 134
-
,
.
'
SUMMARY
OF MEASURED DATA AT TIME 1530 802 TEMP 1 = 79 730 TEMP 2= 80.570 TEMP 3= 83.250 TEMP 4 = 83 770 TEMP 5= 83 320 TEMP 6= 83 680 TEMP 7 = 83 830 TEMP 8= 83.550 TEMP 9= 83 750 TEMP 10 = 83 750 TEMP 11 = 80.590 TEMP la 8 38:8f8 TEMP 14 = 82 760 TEMP 15 = 83 170 TEMP 16 = 83.570 TEMP 17 63 480 TEMP 18 = 83 660 TEMP 19 = 84 810 TEMP 20 = 83 740 TEMP 21 = 84.520 TEMP 22 = 83 660 TEMP 23.= 84.410 TEMP 24 = 85.720 TPRS 1 = 73 560 VPRS I = 0 433 VPRS 2= 0. , DIFF. PRESS. = 1 000 . CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME =- 1530 DATE = F02 TEMP = 83 611897 PRES = 73 127336 PRESS. DIFF = 1 432758 FIO. 135
- . _ _ - - - __ _ _ _ _ _ _ _ _ _ - - _ _ - - _ _ _ _ _ _
.
.
- i
SUMMARY
OF MEASURED DATA AT TIME 1545 802 i TEMP 1 = 79.710 TEMP 2= 80.560 TEMP 3= 83 240 TEMP 4 = 83 750 TEMP 5= R3 300 TEMP 6 = 83 670 '
-TEMP 7 = 83 800 TEMP 8= B3.530 TEMP 9 = 83 720 TEMP 10 = 83.720 TEMP 11 = 80 590 TEMP 12 = 79 230 TEMP 13 = 80 010 , TEMP 14 = 82 760 TEMP 15 = 83.150 TEMP 16 = 83.560 TEMP 17 = 83 470 TEMP 18 = 83 640 TEMP- 19 = 84.780
. TEMP 20 = 83.730 t TEMP 21 = 84.470 TEMP 22 = 83.640 TEMP 23 = 84 390 TEMP 24 = 85.680 TPRS I = 73.556 VPRS I = 0 433 VPRS 2 = 0. 4 DIFF. PRESS. = 1 000 CFANGE ANY DATA IF SO ENTER YES
=
i TEMP. ANO PRESS. CCRRECTED DATA
SUMMARY
TIME = 1545 1-
>
DATE = 802 ! TEM P =- 83 590598 PRES = 73.123276 PRESS. DIFF = 1 432758'
'JI G . 136
_
. = '
SUMMARY
OF MEASURED DATA AT TIME 1600 802 TEMP 1 = 79.690 TEMP 2= 80 560 TEMP 3= 83 230 TEMP 4 = 83.740 TEMP 5= 83 290 4 TEMP 6 = 83 650 TEMP 7 = 83 800 TEMP 8= 83 520 TEMP 9= 83 710 TEMP 10 = 83.710 TEMP 11 = 80 580 TEMP 12 = 79 220 TEMP 13 = 79 990 TEMP 14 = 82 740 TEMP 15 = 83 140
TEMP 16 = 83 550 TEMP 17 = 83 470 TEMP 18 = B3 610 TEMP 19 = 84.770 TEMP 20 = 83 730 TEMP 21 = 84.460 TEMP 22 = 83 630 TEMD 23 = 84 370 TEMP 24 = 85.680 TPRS I = 73.552 VPRS 1 = 0 431 VPRS 2= 0. DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1600 DATE = 802
- TEMP = 83 578398
l PRES = 73 120677 PRESS. DIFF = 1 431296 I f l FIO. 137
_ _ _ _ _ _ _ _ _ . - _ _ - _ _ _ - _
.
.
=.
SUMMARY
OF MEASURED DATA AT' TIME 1615 802 _ TEMP l'= '79 700 TEMP 2 = 80 540 _ TEMP 3= 83 230 TEMP- 4 = 8?-740 TEMP 5= 83 250. TEMP 6 =' 83.640 TEMP 7 = 83.790
TEMP 8 = 83.510 , TEMP 9 = 83 700.(, TEMP 10 = 83.700 - TEMP 11 = 80 580 TEMP' 12 = 79 210 TEMP 13 = 79 980 TEMP 14 = 82.730 TEMP. 15 = 83 130 TEMP 16 = 83.520 TEMP 17 = 83 450 TEMP 18 = 83 600 TEMP 19 = 84.740 TEMP 20 = 83 710 TEMP 21 = 84.480 TEMP 22 = 83 610 TEMP 23 = 84 360 TEMP 24 = 85.650 TPRS 1 = 73.549 VPRS 1 = 0 431 VPRS 2= 0. DIFF. PRESS. = 1 000 , CFANGE ANY DATA If SC ENTER YES
=
l 1 TEMP.-AND PRESS.-CCRRECTED~ DATA
SUMMARY
, ' TIME = 1615 l l
DATE = .902 '
TEMP = R3.564097 :
)
PRES = 73 117632 )
'
-PRESS. DIFF = 1 431296-
?!i. 138
_-w,wg
.
.
.
=
SUMMARY
OF MEASURED DATA AT TIME 1630 802 TEMP 1 = 79.670 TEMP 2= 80.530
,
TEMP 3= 83 210 TEMP 4= 83 710 TEMP 5= 83 250 TEMP 6= 83.640 TEMP 7= 83.760 TEMP 8= 83.500 TEMP 9= 83 700 TEMP 10 = 83 690 TEMP 11 = 80 580 TEMP 12 = 79 220
;
TEMP 13 = 79 970 TEMP 14 = 82 700 TEMP 15 = 83 100 TEMP 16 = 83.510 YEMP 17 = 83 460 TEMP 18 = 83.580 TEMP 19 = 84.710 TEMP 20 = 83.700 TEMP 21 = 84 470 l TEMP 22 = 83 500 + TEMP 23 = 84 330 TEMP 24 = 85 650 TPRS 1 = 73.545 VPRS 1 = 0 431 VPRS 2= 0. DIFF. PRESS. = 1 000
,
CHANGE ANY DATA IF SO ENTER YES
=
l TEMP. AND PRESS. CCRRECTED DATA-
SUMMARY
TIME = 1630 l DA TE =
- l 802 TEMP = 83 540298
, PRES = 73 113572
- l l PRESS. DIFF = 1 431296 FIG. 139
. . . . . ._ _ _ -_ - - _ - _ _ - - - _ _ _ _ - _ .
I
=
SUMMARY
OF MEASURED DATA AT TIME 1645 802 i
< TEMP 1 = 79 670 TEMP 2= 80 520 i TEMP 3= 83 180 TEMP 4 = 83 660
,
. TEMP 5= 83 250 j TEMP 6 = 83 640 TEMP. 7 = 83 760 .
TEMP R = 83 480 TEMP 9= 83.670 } TEMP 10'= 83.670 TEMP 11 = 80.580 i TEMP 12 = 79 200 !' TEMP 13 = 79 950 Li TEMP 14 = 82 700 l TEMP 15 = 83 090 TEMP .16 = 83.500 l TEMP 17 = 83 430 ' TEMP 18 = S3.590 TEMP 19 = 84.670 TEMP .20 = 83 680 TEMP :21 = 84.450 TEMP 22 = 83.530 TEMP 23 = 84 330 TEMP 24 = 85 620 3 iPRS 1 = 73 541 , 3 VPRS I = 0.431 , VPRS 2= 0. 4 DIFF. PRESS. = 1 000 i i i i CHANGE ANY DATA IF SO ENTER YES i = i
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
1- } TIME = 1645 -; ' DaTE =- 902 - TEVP ' = R3.527198
.P3ES = 73 109512 PRESS. DIFF = 1 431296
-FIG. 140'
.. ._ _ ._ - __ _
.
O
SUMMARY
OF MEASURED DATA AT TIME 1700- 802
^
TEMP 1 = 79 660 TEMP 2= 80.520 TEMP 3= 83 170 TEMP 4 = 83.580 TEMP S= 83 240 TEMP 6= 83.610 TEMP 7 = 83 740 TEMP 8= 83.480 TEMP 9= 83 680 TEMP 10 = 83 680 TEMP 11 = 80 570 TEMP 12 = 79 200 TEMP 13 = 79 950 TEMP 14 = 82.670 TEMP 15 = 83 090 TEMP 16 = 83 490 TEMP 17 = 83 410 TEMP 18 = 83.560 TEMP 19 = 84.700 TEMP 20 = 83 690 TEMP 21 = 84.440 TEMP 22 = 83.580 TEMP 23 = 84 310 TEMP 24 = 85.600 TPRS 1 = 73.538 a VPRS is = 0 431 VPRS 2= 0. DIFF. PRESS. = 1 000 I CHANGE ANY DATA IF SO ENTER YES
=
. TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1700 DATE =. 802 TEMP = 83.521998 PRES = 73 106467 i I
- i. PRESS. DIFF = 1 431296 1
,
FIG. 141
. _ - . . .__ _.. _ _ _
=
SUMMARY
OF MEASURED' DATA AT TIME 1715 802 TEMP 1 = 79 540 TEMP 2 = 80.520 TEMP- 3= 83.170 ' TEMP 4 = 83.670
'
TEMP 5= 83.220 i TEMP 6' = 83.600 TEMP 7 = 83 720 TEMP 8= 83 470 TEMP 9 = 83.660 ' TEMP 10 = 83.660 TEMP 11 = 80 550 TEMP - 12 = 79 200 TEMP 13 = 79 930 TEMP 14 = 82 680 TEMP 15 = 83 070 TEMP 16 = 83.470 TEMP 17 = S3 420 TEMP 18 = S3.550 TEMP 19 = 84.680 1 TEMP 20 = 83 660 ' TEMP 21 =- 84.440 ! TEMP 22 = 83.550 ' TEMP 23 = 84 290 TEMP 24 = 85.600
., TPRS 1 = 73.534 A VPRS 1 = 0 430 VPRS 2= 0. DIFF. PRESS. = 1 000
- .
CuANGE ANY DATA IF SO ENTER YES
=
1
.
l
.
'
. TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
- TIME = 1715
'
; DATE = F02.
,
- TEUP.=' 93 510398-
j PRES = 73 103868
- PRESS. DIFF =, 1 429R35
. .
JIG. 142
& Trw- , 3 y ..__,.m9 7 yi g. 1_p7- % 4 .m
.p- y,%,. 9
.
'
SUMMARY
OF MEASURED DATA AT TIME 1730 802 4 - TEMP 1 = 79.630 TEMP 2= 80 500 TEMP 3= 83 160 i TEMP 4 = 83 650 i TEMP 5= 83 200 TEMP 6= 83 590 TEMP 7 = 83 730 TEMP 8= 83 440
' TEMP 9= 83 640
' TEMP 10 = 83 640 TEMP 11 = 80.560 TEMP 12 = 79 170 ' TEMP 13 = 79 940 TEMP 14 = 82 650 TEMP 15 = 83 060 TEMP 16 = R4.460 TEMP 17 = 83.390 TEMP IR = 83.540 TEMP 19 = 84.660 TEMP 20 = 83 650 TEMP 21 = 84 420 TEMP 22 : R3.530 TEMP 23 = R4 270 TEMP 24 = R5.880 TPRS I = 73.531 VPRS I = 0.430 VPRS 2= 0. DIFF. PRESS. = 1 000 4 0 CWANGE ANY DATA IF SO ENTER YES i =
1 TEMP. AND PRESS. CCRRECTED DATA
SUMMARY
, TIME = 1730' OATE'= R02
.
TEMP = 83.525997 . PRES = 73 100824
. .
PRESS. DIFF = 1 429R35 FI:.. 143
, --
.
=
SUMMARY
OF MEASURED DATA AT TIME 1745 802
. TEMP 1 = 79 630 TEMP 2= 80 490 TEMP. 3 = 83 140 TEMP 4 = 83.650 TEMP 5= 83.200 TEMP 6= 83.580' TEMP 7 = 83 700 TEMP 8= 83 440 TEMP 9 = 83 640 TEMP 10 = 83.620 TEMP 11 = 80.520 TEMP 12 = 79 170 TEMP 13 = 79 930-TEMP 14 = 82 650 TEMP 15 = 83.060 TEMP -16 = 83 450 TEMP 17 = 83 380 TEMP 18 = 83.530 TEMP 19 = 84.640 TEMP 20 = 83 650 TEMP 21 = 84.390 TEMP 22 = 83.530 TEVP 23 = 84 250 TEMP 24 = 85 670 TPRS 1 = 73 527 VPRS I = 0.430 VPRS 2= 0.
DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=- '
TEMP. AND. PRESS. CCPRECTED' DATA
SUMMARY
. TIME = 1745
'
DaTE.= 1402 TF.MP = M3.49199F'
. PRES = 73 096764
. PRESS. DIFF = '
-
' li429 53 5'-
FIG. 144'
, = .*
SUMMARY
OF MEASURED DATA AT TIME 1800 802 TEMP 1 = 79 630 TEMP 2= 80 480 4 TEMP 3= 83 140 TEMP 4= 83 660 TEMP 5= 83 180 TEMP 6= 83.550 TEMP 7= 83.690 TEMP 8= 83.440 TEMP 9= 83.610 TEMP 10 = 83.600 TEMP 11 = 80.540 TEMP 12 = 79 150 TEMP 13 = 79 950 TEMP 14 = 82 630 TEMP 15 = 83 050 TEMP 16 = 83 440 TEMP 17 = 83 370 TEMP 18 = 83 500 TEMP 19 = 84.600
; TEMP 20 = 83 620 TEMP 21 = 84 380 TEMP 22 = 83 500 TEMP 23 = 84 240 TEMP 24 = 85.540 TPRS 1 = 73 523 VPRS I = 0.430 VPRS 2= 0.
DIFF. PRESS. = 1 000
.
.
CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
. TIME = 1800 2 i DATE = 802 TEMP = 83 466998 PRES = 73 092704 PRESS. DIFF = 1 429835 t FIC. 145 l
-
i.
'
..
SUMMARY
OF MEASURED DATA'AT TIME 1815 802 TEMP 1 = 79.620 TEMP 2= 80 480 - TEMP 3 = 83 120 TEMP 4 = 83 640 TEMP' 5= 83 170 TEMP 6 = 83 550 TEMP 7 = 83 650 TEMP 8= 83.410 TEMP 9= 83 600 TEMP 10 = 83 600 TEMP 11 = 80 500 TEMP 12 = 79 160 TEMP 13 = 79 930 TEMP 14 = R2 610 TEMP 15 = 83 020 TEMP 16 = 83.410 TEMP 17 = 93 340 TEMP 18 = 83.500 TEMP 19 = 84.590 TEMP 20 = 83 610 TEMP 21 = 84 370 TEMP 22 = 83 490 TEMP 23 = 84 200 TEMP 24 = 85.510 TPRS 1 = 73.518 VPRS 1 = 0 430 VPRS 2= 0. DIFF. PPESS. = 1 000. CWANGE ANY DATA IF SC ENTER YES
=~
TEMP. AND PRESS.' CORRECTED DATA
SUMMARY
TIME = 1815 DATE = 802- . TEv P = :E3.449498. 1 1
-P3EE = 73 0FR644- l l
PRESS..DIFF = 1 429835 l l
E10. 166
.;
3 3
SUMMARY
OF MEASURED DATA AT TIME 1830 802 TEMP 1 = 79.600 TEMP 2= 80 470 TEMP 3= 83 120 TEMP 4= 83 620 TEMP 5= 83 140 TEMP 6= 83.540 TEMP 7~?X TEMP 8= 83 400 TEMP 9= 83.600 TEMP 10 = 83 590
'
TEMP 11 = 80 500 TEMP 12 = 79 170 TEMP 13 = 79 910 TEMP 14 = 82.590 TEMP 15 = 83 020 TEMP 16 = 83 400 TEMP 17 = 83 350 TEMP 18 = 83 480 TEMP 19 = 84.580 TEMP 20 = 83.630 , TEMP 21 = 84 370 TEMP 22 = 83 470 TEMP 23 = 84 220 TEMP 24 = 85.490 TPRS 1 = 73.515 VPRS I = 0.430 VPRS 2 = 0. DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES ' = TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1830
.
DATE = 802 TEMP = 83 441897 PRES = 73 085599-PRESS. DIFF = 1 429835 ' FIG, 147
.
.
.
=
.
SUMMARY
OF MEASURED DATA AT TIME 1845 802 TEMP 1 = 79 600 TEMP 2= 80.460 TEMP 3= 83 100 TEMP 4 = 83 600 TEMP 5= 83 140 TEMP 6= 83.530 TEMP 7 = 83 650 TEMP 8= 83 400 TEMP 9 = 83 590 TEMP 10 = 83 590 TEMP 11 = 80.500 TEMP 12 = 79 150 TEMP 13 = 79 920 TEMP 14 = 82.580 TEMP 15 = 82 990 TEMP 16 = 83 400 TEMP 17 = 83 330 TEMP 18 = 83 470 TEMP 19 = 84.550 TEMP 20 = 83.590 TEMP 21 = 84 380 TEMP 22 = 83 460 TEMP 23 = 84 190 TEMP 24 = 85.490 TPRS 1 = 73 511 VPRS 1 = 0 430 VPRS 2= 0. DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SC ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 184S
-DATE = 902 TEMP = F3.428597.
PRES = 73.OR1539 PRESS. DIFF =' l.429R35 FIG.'14S
,
.
..
3 .-
SUMMARY
OF MEASURED DATA AT TIME 1900 802 TEMP 1 = 79 600 TEMP 2= 80 460 TEMP 3= 83.080 TEMP 4 = 83.590 TEMP 5= 83 120 TEMP 6= 83 520 TEMP 7= 83 660 TEMP 8= 83 390
- TEMP 9= 83.570 i
TEMP 10 = 83 570 TEMP 11 = 80.500 TEMP 12 = 79 150 TEMP 13 = 79 910 TEMP 14 = 82 570 TEMP 15 = 82 990 TEMP 16 = 83 390 TEMP 17 = 83 300 TEMP 18 = 83 470 TEMP 19 = 84 550 TEMP 20 = 83.580 TEMP 21 = 84 370 TEMP 22 = 83 440 TEMP 23 = 84 160 TEMP 24 = 85.490 TPRS 1 = 73.508 VPRS 1 = 0 430 VPRS 2= 0. DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
TEMP. AND PRESS. CORRECTED DATA
SUMMARY
TIME = 1900 " DATE = 802 TEMP = 83 417099 PRES = 73 078494 PRESS.'DIFF = 1.429835 FIG. 149
___-____ _ _ _ _ _ _ _ - _ _ _ _ _ _ _______
, '
s e ,
SUMMARY
OF MEASURED DATA AT TIME 1930 802 TEMP 1 = 79 610 TEMP 2= 80 450 TEMP 3= 83.070 TEMP 4= 83.570 TEMP 5= 83 110 TEMP 6= 83.500
. TEMP 7= 83 620 TEMP 8= 83 380 TEMP 9= 83.550 TEMP 10 = 83.530 TEMP 11 = 80.520 TEMP 12 = .79 120 TEMP 13 = 79 890 TEMP 14 = 82 550 TEMP 15 = 82 970 TEMP 16 = 83 370 TEMP 17 = 83 300 TEMP 18 = 83.440
, TEMP 19 = 84 520 TEMP 20 = 83.580 TEMP 21 = 84 320 TEMP 22 = 83.420 TEMP 23 = 84 150 TEMP 24 = 85.460 TPRS 1 = 73.501 VPRS 1 = 0 428 l VPRS 2= 0. I DIFF. PRESS. = 1 000 CHANGE ANY DATA IF SO ENTER YES
=
l TEMP. AND PRESS. CORRECTED' DATA
SUMMARY
TIME = 1930 DATE = 802
,
TEMP = 83.398098
' PRES = 73.072822 PRESS. DIFF = 1 428403 ,
FIG. 150'
G
#
TABLE OF CONTENTS Section Page 5 LOCAL LEAK TESTS 5-1 5.1 IDCAL LEAK TEST
SUMMARY
5-1 5.2 PERSONNEL AND EMERGENCY LOCK LEAK RATE TEST PROCEDURE 5-5 5.3 RB ISOLATION HYDROSTATIC TEST PROCEDURE 5-12
.
5.4 RB ISOLATION PNEUMATIC LEAK TEST PROCEDURE 5-13 5.5 ELECIRICAL PENETRATION LEAK TEST PROCEDURE 5-14
h
.
i l l ! ' 5-1 l i !
_ _ -. _. _ ,
.
>
.
1 . '
.
i , i 1 !. ' LIST OF TABLES i l Table No. Title g i j 5-1 Iocal Leak Test. Summary 5-2 ! r I ! 5-2 Results of Electrical Penetration Leak Rate Tests 5-6 i (
'
, 1 . .
- 1 1 '
.
4 , ,
'
.
! i
!
i
1 l I 1 ! 2 l 1 i
) ,
l i2 'l
!
l
! ..L 1
1 1
- t t
.
i
?
i
*
. 4 4
.5-11
, -
, _ , -. ._ . . , . . .. . _ . _ _ __
.. . . . _ __ _ - - _ _ _ _ . _ . .__
,
.
5 -LOCAL LEAK TESTS 5.1 LOCAL LEAK TEST
SUMMARY
' Local leak tasting of Reactor Building penetrations occupied approximately 10 months prior to the Inegrated Leak Rate Test of the Reactor Building. Final analysis of all penetration leakage rates shows that the total pene-7 l tration leakage rate is approximately .23% of the allowable leaktge rate l 1. of 0.125%/24 hours. (Table 5-1) Two penetrations, the Quench Tank Return Line (Penetration 38) and the Emergency Lock were not satisfactorily tested prior to the Integrated Leak Rate Test. Both penetrations had mechanical difficulties which prevented '
,
local testing. During the Leak Rate Test,the Emergency Lock was forced 7* closed and the Quench Tank Return Line was isolated with a manual valve. When the mechanical problems were corrected both penetrations were locally tested. The results of these tests is given in Table 5-1. The leakage rate measured from these two penetrations was subsequently added to the measured leakage rate from the Integrated Leak Rate Test.
- The results of the Integrated Leak Rate Test discussion in Section 1 of this report includes these additions.
I J
!
l ! 4 l l l
!
> 5-1 i Rev. 1 April'21, 1972 i
- , _ . _ . , . ..
__
. .
TABLE 5-1 LOCAL LEAK TEST
SUMMARY
A. Hydrostatic Tests Penetration Des cription Leak Rate l No. (lb/hr H 2O) l 7, 5 Reactor Building Normal Sump Drain .00188 ' 6 Reactor Coolant Letdown Line .000 7 Reactor Coolant Pump Seal Outlet Line .000 9 Normal Makeup to Reactor Coolant System .00586 10 Reactor Coolant Pump Seal Inlet Line - Loop A .00505 g 23 Reactor Coolant Pump Seal Inlet I Line - Loop B .00748 l 1, l 29 Quench Tank Drain Line .00661 l1,. 1 38 Quench Tank Return Line ** .0660 l 1.
..
52 High Pressure Injection Line .0000 l Total = 0.09288 lb/hr l 1. water
*The above total represents the amount of water leakage through the isolation valves on each penetration. To compare this quantity with the allowable leakage rate through the reactor building a conversion factor of lb l 2.73 50i water has been devised. This conversion is based on the l 1.
- 1. b hr air Manufacturers Standardization Society of the Valve and Fittings Industry SP61 dated 1961 "Hydrotesting of Steel Valves" which equates 10cc/hr/ inch of diameter water leakage to 0.1 Scf/hr/in of diameter air leakage.
l Using the above conversion factor the equivalent air leakage'is .034 lb/hr. l 1, 5-2 Rev. 1 April 21, 1972
. . _ - _ _ _ _ _ _ _ _ _ _ - _ _ _ _ _ _ _ _ _ _ _ _
.
.
B. Pneumatic Tests Penetration Description Laak Rate No. (lb/hr) 1 19 RB Purge Inlet 0.0191 20 RB Purge Outlet 0.0174 60 RB Sample from RB 0.0001 61 RB Sample to RB 0.0004 18 Quench Tank Vent 0.0014 11 E Fuel Transf Tube Cover 0.0000 12 W Fuel Transf Tube Cover 0.0001 Total = 0.0385 C. Electrical Penetrations
.
Total * = .0005 lb /hr D. Others Description Leak Rate (1b/hr air) Personnel Lock Negative
'
l Emergency Lock *
- 0.0088 l Equipment Hatch 0.0003 l Total = 0.0091 1 1,
- Individual leak rates given in Table 5-2 l **Locilly tested after the Integrated Leak Rate Test lJ.
E. -Allowable Leak Rate - l From Technical Specification 4.4.1 "The total leakage from all penetrations i 1. and isolation valves shall not exceed 0.125% of the reactor building atmosphere per 24_ hours". 5-3 Rev. 1. April 21,1972 <__._
.
. .
For average reactor building conditions of 80*F and 59 psig, 0.125%/24hr of the reactor building atmosphere represents approximately 35 lb/hr. Allowable Leak Rate = 35 lb/hr F. Total Measured Leak Rate Total Measured Leak Rate l (from A-D aSove) = .0821 lb/hr l 1, l
.
i 5-4 ! Rev. 1 A$ril 21 01972
. __ - - - _ _ _ _________ - .
Pcge 1 of 6 . TABLE 5-2 RESULTS OF ELECIRICAL PENETRATION LEAK RATE TESTS Unit 1 Date Jaly 28. 1971 l WEST PENETRATION ROOM Penetration Serial No. Type Results Imak Rate (#/hr) Test Date A-1 13 J P Neg. 7/28/71 , A-4 9 F P 4.02 X 10-7
, 6/2/71 A-5 30 F P 9.4 X 10-7 4/21/71 A-6 26 F P 4.9 X 10-7 4/21/71 A-8 29 F P 4.9 X 10~7 4/21/71 A-9 28 F P 4.9 X 10 -7 4/21 /71 A-12 3 G P 1.14 X 10~7 4/22/71 A-13 16 J P Neg. 7/28/71 B-1 19 E P Neg. 4/2 0 / 71 B-2 1 E P 3.06 X 10-5 4/20/71 B-3 8 E P 3.27 X 10-8 6/1/71 B-4 23 E P 9.4 X 10-7 '4/21/71 B-5 30 E P 1.43 X 10 -6 4/19/71 B-6 25 E P 1.06 X 10-7 4/19/71 B-7 24 E P 1.06 X 10-7 4/19/71 B-8 18 E P 7.85 X 10 -7 4/15/71 B-9 6 E P 7.85 X 10 -7 4/15/71 B-10 16 E P 7.85 X 10
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4/15/71 B-11 26 E P 5.37 X 10-6 4714j71 B-12 32 E P 5.42 X 10 -6 4/14/71 5-5 .
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Paga 2 of 6 - < PJnetration Serial No. Type Results Imak Rate (#/hr) Test Date . C-1 20 D P Neg. 5/28/71 , C-2 16 B P 3.27 X 10-8 6/1/71 C-3 1 C P 3.27 I 10-8 6/1/71 C-4 2 C P Neg. 6/1/71 C-5 7 C P 5.80 X 10 -0 6/1/71 C-6 -0 23 C P 5.71 X 10 6/1/71
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4 C-7 4 C P Neg. 6/1/71 i C-8 8 C P Neg. 6/1/71 C-9 30 C P Neg. 6/1/71 C-10 33 C P Neg. 6/1/71 C-11 31 C P Neg. 6/1/71 C-12 3 C P 4.02 X 10-8 6/2/71 C-13 6 C P 9.02 X 10-7 6/1/71 D-3 9 C P 1.35 X 10-7 4/13/71 D-4 5 D P 1.35 X 10-7 4/13/71
D-5 29 D P 1.35 X 10 -7 4/13/71 ) D-6 2 D P 1.89 X 10 -7 4/13/71
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D-7 1 D P 1.89 X 10 4/13/71 D-8 24 D P 1.89 X 10-7 4/13/71 , D-10 1 Cg P Neg. 6/2/71' D-11 5 C P 1.90 X 10-9 4/14/71
- D-12 21 D P 1.90 X 10-9 4/14/71 D-13 8 B P 1.90 X 10 -9 -
4/14/71 MV-1 1 A P Neg. 6/9/71
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MV-2 7 A P Neg. 6/8/71 5-6 e ,m -
-T+- o m -
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Prg3 3 of 6 s Penetration Results Leak Rate (#/hr) Test Date Blind Fanges A-2 P Neg. 6/9/71 A-3 P Neg. 6/10/71 1 A7 P Neg. 6/9/71 B-13 P 1.00 X 10-6 7/25/71 D-1 P Neg." 6/10/71 D-2 P 6.97 X 10-7 6/9/71 D-9 P Neg. 6/9/71 . e 4 l ' 5-7 I . _ . --,
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Pcge 4 ef 6
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RESUTli'S OF ELECTRICAL PENETRATION LEAK RATE TESTS , Unit 1 Date July 27. 1971 EAST PENETRATION ROOM i .
- w atration Serial No. Type Results Leak Race (#/hr) Test Date A-7 27 F P 2.6 X 10-7 7/29/70 A-8 23 F P 5.9 X 10-8 7/29/70 ;
- i A-9 11 F P 5.27 X 10 -0 7/29/70
'0
_ 7 c P 8.3 X 10-7' 8/11/70
- A-ll 9 G P 1.69 X 10 -5 3/11/70 A-12
' 6 J P Neg. 7/29/71 . A-13 10 J P Neg. 7/29/71 B-8 7 E P Neg. 6/4/71 B-9 6 E P Neg. 6 /3/71 B-10 1 F P Neg. 6/10/71 l B-11 2 E P Neg. 6/3/71 , 3 12 1 E P 4.77 I 10-0 5/12/70 j i
- C-2 4 E P 1.21 X 10-7 4/26/71 C-4 4 J P Neg. 7/27/71
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, C-8 6 C P 2.91 X 10 7/29/70 C-9 11 C P 1.30 X 10 -0 7/29/70
--10 15 B P 5.00 X 10-6 11/5/70 C-12 7 -0 D P 2.67_X 10 7/29/70 l
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Pcge 5 of 6 l
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Penetration Serial No. h Results TAak Rate (#/hr) Test Date
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D-1 2 H P 1.21 X 10-7 4/26/71 D-2 4 H P Neg. 6/3/71 D-3 5 H P Neg. 4/26/71 D-4 3 H P 1.21 X 10-7 4/'6/71
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D-7 7 B P 1.62 X 10-6 7/28/71 D-8 12 C P 4.31 X 10-6 7/28/70 D-9 10 D P 1.79 X 10'$ 11/4/70 D-10 12 D P 1.58 X 10-6 117477o 0 D-11 13 D P 1.62 X 10 7/28/70 ; D-12 11 D P 5.00 X 10 -0 7/28/70 D-13 8 D P 8 03 X 10-6 7/28/70 E-1 8 H P Neg. 4/26/71 E-2 1 H P 1.02 X 10-6 4/23/71 , E-3 7 H P 1.02 X 10-6 4/23/71 E-4 9 H P Neg.- 6/3/71 F-3 5 E P Neg. 6/3/71 , i i F-5 17 F P 2.16 X 10 -0 4/22/71 F-6 31 F P 1.85 X 10 -0 7/30/70 i F-8 12 B P Neg. 4/22/71 l i F-9 4 B P 7.87 X 10-5 11/4/70 1.47 X 10 -5
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F-10 5 B P tyf4779 - F-11 9 B P Neg. 4/23/71 1 I MV-1 6 A P - 1.67 X 10-6 6/8/71 l i MV-2 8 A P Neg. 7/26/71 , 5-9 !
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Penetration Results Leak Rate (#/hr) Test Date Blind Flanges B-13 P Negligible 7/25/71 C-1 P Negligible 7/ 25/71 C-3 P 6.02 X 10-5 11/9/70
-5 11/9/70 C-7 P 1.29 X 10 C-11 P 7.83 X 10 -5 11/9/70 E-7 P 5.39 X 10 -0 11/8/70 E-8 P Neg. 11/8/70 E-9 P Neg. 11/8/70 E-10 P 5.28 X 10-6 11/8/70
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F-2 P 2.85 I 10-5 11/8/70 ,
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F-4 P 2.48 X 10-5 11/8/70
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5.2 PERSONNEL AND EMERGENCY TACK LEAK , RATE TEST PROCEDLTE ' Following is a copy of the test procedure used for the conduct of the test. Data sheets are not enclosed as they would add significant.ly to the bulk of the material in this report. They may be seen at Oconee Nuc. f ar Station.
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4 5-11
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TESTPROCEDURERECORDOF* APPROVAL, CHANCES,ANDTESTPERFORMANCEh TEST PROCEDURE NUMBER TP 1 150 8 1 -
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TEST PROCEDURE TITLE Personnel and Emergency Lock. Leak Race Test STATION COORDINATOR .'obert M; Koehler ., SRC REVIEU / y. //,sofs DATE ?/,e / w .
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APPROVED FOR US n DATE ~7 '? 78
/(Oconee Supt'. Signature)
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TEST COMPLETED APPROVAL DATE - (Oconee Supt. Signature) o inor Date Affected Reason for Change Initials inge Section of TP I0' 9 Y A "C C{antf.t a.yfh
- 2. 0 l IW: Also, two %" c'fa,,,j7,e Aco./d 4s ate) to (cren tAe iriner door- eyaahwy valv-e closed for rhe came. reases) - g%
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- I-' E & cl b i$ sonfesses: Idrtet clCCr o{omps -
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Mh C' a. 3 4 c/d e g ,a J o,, z. s is V I L '1 gj y ajofs&ersce.'4botwt "*n +b' a,J e Accus on d< p e,,,g peana,,ay& it
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l Tn c}gpa,ya to;
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!acws & c Crrrcryen y lock.
tL h0 Cut & de* Aessennel4<rc/c. )S S/ ~ N' laxsctser by f-es t cfon.~p is ph-se. Y rnonts/~ css St.ry s izL - p 'T W c.) n' G3 Qa44 to M a c he.V j% H'" W " "~ ' ~ ' Date(s) Conducted Test Coord. iO (Sig.)
/Go4 $ EC09-0 8'****r cmesc #2m
. Shift Supv. (Sir. . )
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FINAL TEST PROCEDURE
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TP 1 150 8 1 PERSONNEL AND EMERG' CY LOCK LEAK RATE TEST OCONEE NUCLEAR STATION 1.0 Purpose 1.1 To verify the integrity of the hatches when pressurized to 115% U c a. u g. design pressure %Tig). 1.2 To determine the leakage rate from the lock volume when pressurized to peak accident pressure sig). 1.3* To determine the leakage rate from the inner and outer electrical "ter door seal volume M'#f penetrations associated with the locks and thAe when pressurized to peak accident pressuregpsig).
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2.0 References 2.1 Dwgs. OM 100-168 and OM 100-169 2.2 " Leak Rate Test Procedure PG-1 for Duke Power Company Units 1, 2 3 (Oconee)," W. J. Woolley Company, October 31, 1969. AW "
+ W'/s/mh iae u
&& ga u g 9 a n ~ r a nc ~ ' M'r u.a. a ie r e re a;Swa 3.0 Time Required
_ji ba"e- per leek 1 m.n hed- ' f y/
,
cb ti Aases f<- Ema<9emy& Peuw nef Ua 14 m>&mq
- 4.0_/her$quWeke,dc c/o & 1 ih f As " ]W None , '
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150/8 Rev. 1 7/14/70
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5.0 Test Equipment . .
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5.1 Barometer , 5.2 Pressure Gauge , 5.3 ASTM T h -~- '2-) ' codd[ '/! Y # 94 - 5.4 Inner Door Clamps 5.5 Test Piping and Air Supply . 5.6 Soap Bubbler Y C% TIDC ' ' C. " C[<tstjo( 6.0 Limitations and Precautions 6.1 Do not pressurize test volumes above 68 psig. 6.2 Use only clean dry air for pressurization.
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7.0 R'equired Plant Status The Reactor Building should be at atmospheric pressure. 8.0 Prerequisite System Conditions 8.1 Test Fittings should be made for each test volume. 8.2 Source of compressed air should be available.
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9.0 Test Method The electrical penetrations and tLe outer door seal volume will be d ,b pressurized to psig and leak tested for 15 minutes each.* The lock
\ volume will be pressurized to 68 psig as a local structural test and l _
then will be leak rate tested at sig. During the leak rate test, , temporary forced closure must be made to the inner lock door to hold ! pressure opposite the design direction. 4 b*f M # shoulcl bA as eD o Po CC E r!t2 M M '** 0* , f L SQun t.t 1stug J A WE c. tes e O P t"- T!"5 S ## # Hj l 10.0 Data Required 10.1 Lock Pressure 150/8 Rev. 1 7/14/70
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10.2 Lock Air Temperature
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10.3 Elapsed Time '
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11.0 Acceptance Criteria The total amount of leakage from each lock should be less than 0.5 lb/hr.
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12.0 Test Procedure 12.1* Pressurize the lock electrical penetrations to sig and hold pressure k for at least 10 minutes. Soap bubble test and observe pressure
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decay. Calculate leakage from Enclosure 13.1. Electrical pene-tration volumes are cubic feet. u 12.2* Close outer door and pressurize 0-ririg seal volume t psig. Soap bubble test and observe pressure decay for at least 10 minutes. Calculate leakage rate from Enclosure 13.1 0-ring . seal volume is . g 1. 4 , 12.3 Close inner door and install inner door clamp [. Insure that
. lock electrical penetration test holes and outer door test holes
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are sealed. Inspect any other likely source of leakage.
" 12.4 Install thermometer in lock volumes insuring that they are readable
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through the door observation ports. i 12.5 Close outer door.
/ 12.6 Pressurize lock volume sig. Bubble check door seals and test connections.
# -C-
-j 12.7 urs
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d'""!$6 12.8 Calculate S bcMRecord e>ner9 enc data 4 w given and onthe on Enclosure 13.2 every hour f r 4keua.o/;m ei a ledkage rate from Enclosure 13.1 Personnel lock volume
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,f i is 1675 cubic feet. Emergency lock volume is 762 cubic feet. -!
- 0ptional at the discretion of the test coordinator, since this is, l,
l. in effect, a " local-local" leak test. _ m &
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ENCI45URE 13.1 - -
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- . EOCK LEAK RATE TEST -
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- Test Date
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End Time
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Cale'ulation Done By
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- PRELIMINARY DATA
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- 1. Pressure gauge reading at start of test - P i= psig.
- 2. Pressure gauge reading hrs. later; = Pi= psig. .
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- 3. Barometer reading at start of tast = Bi= in. Hg.
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- 4. Barometer reading hrs. later = Bi= in. Hg.
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- 5. Atmospheric Pressure at start of test = Patmi ,'
(multiply line 3 by 0.491 psi /in.Hg.) = psia.
- 6. Atmospheric Pressure hrs. later = Patmg -
*
(multiply line 4 by 0.491 psi /in. Hg.) = psia.
- 7. Temperature at start of test = Ti=
- F.
8.' Temperature hrs. ' later = Tg = *F.
- 9. Absolute temperature at start of test - Tai (add line 7 to 459.7') = *R.
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- 10. Absolute te=perature hrs later = Tag (add line 8 to 459.7*) =
- R.
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- 11. Cas constant for air = 53.3 f-lbf/lbm'R
- 12. Volume between valves = Vg it3
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ENCLOTURE 13.1 - Continued' ,
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- 1. Weight of air b'etween valves at start of test .
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1 Tag
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Vg = (Pr + Patsf) Vgx 144 ,
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- 3. " Leakage rate = Wi - Wg . g .' =
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- 4. Leakage rate in cubic feet per hour at 60*F and 14.7 psi. l 1
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LR = W x 53.3 x 520 = W x 13.1
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14.7 x 144 . LR =
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OCONEE NUCLEAR STATION '
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PERSONNEL AND EMETJ:ENCY LOC'
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. LEAK RATE TEST ,
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x1TA SHEET
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Data Recorder
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TIME PRESSURE BAR0!!ETER TEMPERATURE BAROMETER. BAROMETER ** ,
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(psig) (in. Hg) Ti(* F) T2 (*F) TM. (* F) (in. Hg)
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** Temperauture Corrected Pressure Cauge Serial No.
Thermometer Serial No. (T1)
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5.3 RB ISOLATION HYDROSTATIC TEST PROCEDURE Following is a copy of the test procedure used for the conduct of the test. Data sheets are not enclosed as they would add significantly to the bulk of the material in this report. They may be seen at Oconee Nuclear Station. i 4 1 4
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9 J & a 5-12
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WORKING FILE -
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TEST PROCEDURE RECORD OF' APPROVAL, CHARGES, AND TEST PERF0 TEST PROCEDURE NUMBER TP 1 A 150 7 2 TEST PROCEDURE TITLE RB Isolation Hydrostatic Leak Test STATION COCRDINATOR R. M. Koehler '
.m..
SRC REVIEW / z) d.,,un DATE 2/,e / ,,. APPROVED FOR,LSE .a DATE 7 7 7 go'conce' Supt. Si}, nature) '/ '/ TEST COMPLETED APPROVAL DATE - (Oconce Supt. Signature) .nor Date Affected Reason for Change Initials tage Section of TP A,m o _ n
/ 7/28/7/ 2 7,ene) is ,1 q,m t_
AMed % re Elect ctraw.ng dage 2 7/29/7/ 3 . O , ; 1 , 44 C_bein k rt.heAh 7d k- C- g, hwr eg .
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_. lutc(s) Conduct ed Test Coord. k M d __ _ (Sig.) Shift Surv. (si; .)
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Vendor Uitnc Q _ (Si:, . )
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OCONEE NUCLEAR STATION- *
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TP 1 k 150 72 b RB ISOLATION HYDROSTATIC LEAK TEST
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1.0 Purpose
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To verify the sealing capability or the leak race of isolation valvas which when closed by the Engineered Safeguards System entrap water between the valves.
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2 . 0' References 2 ' , PO-144A Component Cooling System :
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2.2 PO-101B High Pressure Injection System ! 2.3 PO-110A Chemical Addition and Sampling System ,
, 2.4 PO-107A Coolant Storage Sys tem (Quench Tank portion)
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2.5 PO-107B Liquid Waste Disposal System (Misc. Waste portion)
. 2.6 FSAR, Section 5. 6. R.1 S
Pressure Trlec h%h
- g,f P6 - 16'll No9h fSU W
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3.0 Time Required Two men, 100 hours. - 4.0, Prereguisite Tes ts
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4.1 TP/1/A/202/3 HP Injection System Electrical Test 4.2. TP/1/A/210/3 CA Sys tem Electrical Test _
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150/7 Rev. 2 Juy 14, 1970 . 0)- _
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4.4 TP/1/B/240/4 CC Sys tem Electrical Tes t NOTE: The above tests are desired prerequisites. If
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the normal source of electrical power to motor operated valves is not available, a temporary
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electrical source is 'accep table. 5.0 Test Equipment 5.1 Hand hydro pump .
, 5. 2 Test p res s ure gauge
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5.3 The rmome te r -
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15 . 4 Calib rated water tank
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6.0 Limitations and Precautions Use only water which meets the specifications of any system in which :Lt is used. 7.0 Required Plant Status A satis f actory water supply mus t be available. 8.0 Prerequisite S y, stem Con ditions 8.1 All power operated valves operable f rom power source and tes ted through full travel.
- 8. 2 All penetrations to be tested are vented to remove j
air as the penetration is fi lle d .
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150/7 Rev. 2 Ju1y 14, 1970
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1 9.0 Test Method l Power operated valves should be closed with power. Manual
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valves and s top check valves should be closed to a tightness
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consis tent with normal operation. The volume b etween the , , isolation valves should be pressurized to 68 psig as a structural check. The pressure should then be reduced to 54 psig and a leak rate test conducted. Thg pressure is to
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be maintained constant at 54 psig with the hydro pump. The leak race will be determined by observing the .ch'ange: r..-
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in water level of the calibrated water tank and elapsed time. ..
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10.0 Data Required 10.1 Calib rated water tank vcluma , 10.2 Elapsed time of test
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10.3 Water temperature . ._
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10.4 Test pressure
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11.0 Acceptance Criteria
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Leakage rate must be less than 2.0 lb/hr.
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12.0 Test Procedure ! ~1:2.1 Ascertain that isolation valves are closed.
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I 12.2 Fill isolation volume _with water and allow 15 min.
. for water temperature to stabilize. "
- 12.3 P res s u riz e the penetration volume to 68 psig an d
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150/7 Rev. 2 July 14,1970 _ . _ . - . _ _
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12.4 Reduce pressure to psi's with drain or vent valve.
,12.5 Record level in calib rated water tank, penetration water l
temperature, pressure, and time. ) 12.6 Maintain 3 psig . pressure in the penetration for approximately hour, using the hand operated hydro
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pump.
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12.7 At the end of the test period, record level in calib rated water tunk, penetration water temperature, and time.
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13.0 Enclosures 13.1 Penetrations To Be Hydra Tested
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13.2 Data Sheet .
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150/7 Rev. 2 July 14, 1970 l
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I 13.1 PENETRATIONS TO BE HYDR 0 STATICALLY TESTED )
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" FEN No. .. PO DWC. INSIDE VALVE OUTSIDE VALVE !
6 101B HP-3 and HP-4 HP-5 7 101B HP-20 HP-21
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9 101B HP-126,HP-127 HP-122.HP-26, HP-120 10 t4P-W6 /d-396 101AC -;i F - A g un-1;;, gp_;g;
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10 HP-/VT //P-28f 1015 C M? 145 HP-206 up_79e
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p?pIts - /%~ HP cP.8 5 23 ' 1013C. .. _ up_933 u,_943 s 23 1018 C, (W ~1,7__? f4/'/ W~ 0$N HF-??n - HP-222 2 52 101B .H P- 15 3 , HP - 15 2 HP-27 - l l
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38 107A CS-13 to CS-1f 38 107A CS-13 C S - 11* 29 107A CS-S CS-6 1 5 107B LWD-1, LWD-2 1
- Check valves should be closed by. reve rs.e wate r flow.
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5.4 RB ISOLATION PNELHATIC LEAK TEST PROCEDURE Following is a copy of the test procedure used for the conduct of the test. Data sheets are not enclosed.as they would add significantly to the bulk of the material in this report. They may be seen at Oconee Nuclear Station. i $ i i
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TEST PROCEDURE RECORD OF' APPROVAL, CHANCES, AND TEST PERFOR2!ANCE - CONTROL COPY TEST PROCEDURE NUdtBER TP 1 A 150 6 2 TEST PROCEDURE TITLE STAT 70N COORDINATOR RB Isolation Pneumatic Le R. McMahon^ h[ ' , SRC REVIEW , f/ / f ,.y f , DATE 5#/ /3 / 7o APPROVED FOR US / b DATE t EY
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TEST CO}1PLETED APPROVAL DATE { (Oconce Supt. Signature) i inor Date Affected ange Change (exact wording) and Initials l Section of TP reason for change & agpvot n!
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Lp *,,a less d?w) '1 P4 p ' 'g o ?- fex kn GY f* W
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1 rhe cmIomp wae Leod'd " - ~y n/19/11 a.t 6 g p,px a.s a.cnfed on tIh* ' 7/29/7/ 24 p.e.it e M ptecedo<e. M e R.m ic 6 9// V/w loa A ea N+k- _ -, kvu.v , Date(s) Conduct cd Test Coord As f,v- (Si g. ) \ 27u 7/ - 3eAk 7/ D M b u b . iu k. d. - (sig.)
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FINAL . TP 1 A 150 6 2
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RB ISOLATION PNEUMATIC LEA,K TEST -
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1.0 Purpose To verify the scaling capability ~ or the leak rate of , isolation valves which, when closed by the Engineered Safeguards System. would trap air or water vapor between
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the isolation valves.
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2.0 References 2 .' l PO-116A Reactor Building. Purge and Penetration Room Ventilation System
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2.2 PO-107A Coolant Storage System (Quench Tank Portion) 2'. 3 PO-104A Spent Fuel Cooling Sy s tem. bC--
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2.4 TS/1/A/150/7 RB Isolation pMsMh Valves _ ch ";t; Test
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30 Time Required .
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- Thirty hours, th ree men. .
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- 4.0 Prerequisite Tes ts -
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- Is ola tibn Valve Portion. . o f b elow listed tests: -
l ( r 4.1 TP/1/B/161/1 RB Purge and Ventilation Valves Elec~
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trical test. ,
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4.2 TP/1/B/230/3 WD Sys tem Electrical Tes t. 5.0 Test Equipment , 5.1 Barometer 5.2 Test Precsure Gauge
~5. 3 Thermometer 5.4 Soap Bubbling Equipment
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6.0 Limitations and Precautions Air for the test should be free of oil and dry enough so that the dev point will not be reached in the volume being tested. 7.0 Required Plant Status - S atis f actory air supply required.
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8.0 Prerequisite Syste'm Conditions 8.1 All power operated valves operable from power source
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8.2 All penetrations to be tested ara vented and drained. . 9.0 Test Method
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Power operated valves should be closed in their normal
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manner with power. Manual valves and s top check valves should be closed to.a tightness consistent with normal operation. The volume b e tw e en the isolation valves should
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be pressurized t o . 6 8 p s i g an d p oi'n 't s' o f p os s ib i c 'le ak a ge
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150/6 Rev.2 August, 13 , ~ 19 70'.
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should be bubble tes ted. The pressure should then be No f' /t CS /7$M of /wQ enMO MOfforcV e. //[&7 /60 ACA reduced to 5 5 p e i;; and.a leak rate test,is to be conducted for a minimum period o.f time according to the following 4 table: .
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Volume (cu. ft.) Duration o f Tes t i ! ! Less than 1/2 3 minutes 1/2 to 1 5 minutes , . 1 to 5 30 minutes
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1 hour
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20 to 40 2 hours . 40 to 50 , 3 hours 50 and up 4 hours
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10.0 Data Required 10.1 Test pressure at beginning and end of. test. 10.2 Barometric pressure and temperature at barometer' l
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at beginning and end of test.
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10.3 Surface temperature o f penetration at beginning and end of test. 10.4 Time elapsed during test.
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1100 Acceptance Criteria
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Leakage rate for each penetration mus t be less chari 0.5 pounds / hour. ^
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12.0 Test Procedure ,
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12.1 Ascertain that isolation valves are closed. , .
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the air supply and bubble test for leakage. .
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/jo/~ /ex .sfas/ ff AfAS 000 00hM0K NM /de M 12.3 Reduce pressure to 5 '- ;;i7, with drain or ven t valve,
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J close valve and bubble test for leaka'ge. 12.4 Record the following items at the b eginning an'd
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12.4.1 Pressure
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12.4.2 Temperature .
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1,2 . 4. 3 Baromet ric Pressure and temperature at b a ro me t e r. 12.4.4 Time .
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. 13.1 Calculation sheet . .
13.2 Volumes b e tw e en penetration isolation valves
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' VOLUMES BETWEEN PENETRATION ISOLATION VALVES -
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i Inside ' Pen. No. PO Dugs. Valves Outside Valves Pipe Volume .
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// 3.00 19 116A PR-6 PR-5 10" A f 20
//3.0l-fV 116A PR-1 PR-2 #
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60 116A PR-7 P R- 8
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.%476 61 ll6A PR-9 PR-10 M
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18 107A GWD-12 CWD-13 E3 i - i Between gaskets of the . 11 104A trans. tube blind flange. 3 *,
.0041 f Between gaskets of the . -
12 104A trans. tube blind flange .0041 f 3 +* ,
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5.5 ~ ELECTRICAL PENETRATION LEAK TEST PROCEDURE . , Following is a copy of the test procedure used for the conduct of the test. Data sheets are not enclosed as they would add significantly to the bulk of , the material in this report. They may be seen at Oconee Nuclear Station. ! i
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TEST PROCEDURE RECORD OF APPROVAL, CHANGES, AND TEST PERFORMANCE
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TEST PROCEDURE NUMBER TP 1 A 150 5 1 TEST' PROCEDURE TITLE Electrical Penetration 0-Ring Seal Laak Tast STATION C03RDINATOR D. R. Wat t enb arae r SRC REVIEW I,/ ,,,tyI;, DATE ' 7//d /70 __
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APPROVED F USE A> gnature) DATE [' [4'
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TEST COMPLETED APPRCVAL - DATE
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*I sys e pa .A.. tim p is r. .s j s.n tos w. H. L c A ny <. ~ ~ L a.-
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FINAL- ' OCONEE NUCLEAR STATION TP 1 A 150 51 ELECTRICAL PENETRATION 0-RING SEAL LEAK TEST
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1.0 Purpose To determine the sealing cap ab ility of os leak r' ate through the doub le 0-ring seal b e tween ele ctrical penetrations and reactor building flanges. 2.0 References l 2.1 FS AR, Section 5.1.4.4 2.2 FSAR, Section 5.6.2.1 - 2.3 OM-337-31, Electrical Penetration - Detail 2.4 OM-337-15, Electrical Penetration - Master E-J 2.5 OM-337-12, Electrical Penetration - Master-B, C-1, l l C-2, and D j l 2.6 OM-337-33, Valve and Gauge Assembly I I 3.0 Time Required
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Two men - 80 hours 4.0 Prerequisite Tests
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Determine leak rate of test fixtures. I 150/5 Rev. 1 July 14, 1970 ,
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5.1 Test pressure gauge, 0-100 psi 5.2 Thermometer or contact pyrometer 5.3 Test valve 5.4 Dry, filtered air supply, 75 psi minimum 5.5 Barometer s
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6.0 Limitations and Precautions Use only dry filtered air. 7.0 Required Plant Status
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None . 8.0 Prerequisite System Conditions - j Seal integrity of SQ charged volume should be confirzad ! by checking gauge, which is permanently mounted on penstration. < 9.0 Test Method l Volume between 0-rings is pressurized to 68 psig initia41y ()as a structural test. Pressure is then reduced to kd 13 and a leak . ate tcs t is performed. Leak rate is determined from observing the pressure decay. 10.0 Data Required
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' 10.1 Temperature of penetration at beginning and end of test. . 150/5 Rev. 1 July 14, 1970
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10.2 Pressure at beginning and end o f tes t. 10.3 Length of test, hours. 10.4 Volume between seals. 10.5 Penetration type. 10.6 Barometric Pressare. 10.7 Ambient Barometer Temperatura 11.0 Acceptance Criteria Maximum allowable leakage is 9 x 10-3 cc/sec or 9.237 x g, 10-5 lbs/hr,=h:2 cc :c;;;d :: 22 ?, l'.7 pai.
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12.0 Test Procedure i 12.1 Attach test assembly and pressurize volume between l l 0-rings to 6 8 psig. 12.2 Bubble check test fittings for leaks. . i
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12.4.2 Temperature on surface of penetration 12.4.3 Pressure as indicated by test gauge 12.4.4 Atmospheric P res s ure 12.5 Bleed o f f air and remove test fixture. NOTE: Temp e rat ure should be taken inside reactor building as near as possible to Olring seal. _ so-150/5 Rev. 1 July 14, 1970
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13.1 Calculation and Data Sheet 1 13.2 Volumes and Minimum Test Times for Types of Penetrations 4 l 2 i 1 .
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ENCLOSURE 13.1 ' V'r 7l i lV 'I PENETRATION VALVE LEAK RATE TEST - CALCULATION AND DATA SHEET / l Thermometer No. Penetration No. 1 Test Gauge No. Test Date Unit No. Beginning Time i Penetration Type End Time . Data Recorder PRELIMINARY DATA -
- 1. Pressure gauge reading at start of test =Pi= psig.
- 2. Pressure gauge reading hrs later = Pg= psig.
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- Barometer reading at s ta rt of test =
Bt= in. Hg. 4..* Barometer reading hrs later = Bg= in. Hg.
. 5. Atmospheric p ressure at start of test = Patmi ,
(multiply line 3 by 0. 491 psi /in. Hg)= - psia.
- 6. Atmospheric pressure h rs later = Patmf (mult ip ly line 4 by 0.491 psi /in. Hg)=
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- 7. Temperature at start of test
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= Ti =
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- 8. Temperature hrs later = T g= OF.
- 9. Absolute tempercture at start of test = Ta t
(add lins 7 to 459.70) = R
- 10. Absolute temperature h rs later = Tag (add line 8 to 459.70 ) =
1 R
- 11. Gas constant fo r air = 53.3 f-lb f/lbmo k.
- 12. Volume between valves =V t ft 3 l
- NOTE: Co rre ct barometer readings for temperature.
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ENCLOSURE 13.1 - Continued CALCULATION
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- 1. Weight of air be tween valves at start of test W g= (Pt + Patmi) 2 2 vt x 144 in 7f R Tag
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Wg= = lbs.
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"f= (Pg + Patmg) m g j2'g2 R Tag .
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- 5. P ene t ra ti on Leakage Rate - in standard cub i c feet per hour
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PLR = TLR - Test Fixture LR = s f t'f h r - a Calculation by
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Supervisor Date
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Type of Penet ration No. Test Volume Test Rig Min. Test Times
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A 4 107 cc 7ece 1 1/2 hr. I I
//., B-J 448G73 70 cc 7 cc 1 hr.
3 Spare (BlindFlangef5@lg 40 cc 7 cc 3/4 hr.
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