ML19327A940

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Final Rept, Reactor Containment Bldg Integrated Leakage Rate Test
ML19327A940
Person / Time
Site: Comanche Peak Luminant icon.png
Issue date: 07/31/1989
From:
BECHTEL POWER CORP.
To:
Shared Package
ML19327A939 List:
References
NUDOCS 8910240014
Download: ML19327A940 (83)


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Texas Utilities Company 1

Comanche Peak i

Steam Electric Station Unit 1 l

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L Reactor Containment Building Integrated Leakage Rate Test 1

Final Report.

July 1989-Bechtel Power Corporation l

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TEXAS UTILITIES ELECTRIC COMPANY COMANCHE PEAK STEAM ELECTRIC STATION UNIT I REACTOR CONTAINMENT BUILDING INTEGRATED LEAKAGE RATE TEST FINAL REPORT

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PREPARED BY BECHTEL POWER CORPORATION SAN FRANCISCO, CA JULY 1989 w-r

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TABLE OF CONTENTS SECTION lPAGE T

1.

INTRODUCTION 1

2.

TEST SYNOPSIS 2

3.

TEST RESULTS SUPWARY 4

4.

TEST METHODOLOGY 10 5.

ANALYSIS AND INTERPRETATION 12 6.

REFERENCES 14 APPENDICES A.

DESCRIPTION OF BECHTEL ILRT COMPUTER PROGRAM B.

INSTRUMENT ERROR ANALYSIS l'

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C.

ILRT TEST DATA D.

ILRT & LLRT TEST SUMMARIES E.

LEAKAGE RATE MEASUREMENT SYSTEM DIAGRAM l.

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INTRODUCTION The Prestart Test Program Integrated Leakage Rate Test (ILRT) was conducted on the reactor containment building at the Comanche Peak Steam Electric Station Unit I during the period July 4-7, 1989.

The test was conducted to demonstrate that the' leakage from the reactor containment system at the design loss of coolant accident pressure does not exceed the maximum allowed by the plant Technical Specifications (Reference 6.1).

The ILRT was conducted in accordance with the plant test procedure EGT-701A Revision 1 (Reference 6.2).

The test procedure conformed to the general testing requirements established in 10CFR50 Appendix J (Reference 6.3), ANSI N45.4 - 1972 (Reference 6.4), ANSI /ANS 56.8-1981 (Reference 6.5), and ANSI /ANS 56.8-1987 (Reference 6.6),

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TEST SYNOPSIS Preparation for the Integrated Leakage Rate Test (ILRT) included installation of a temporary pressurization system that included oil free air compressors and refrigerated dryers, instrumenting the containment with temperature, dew point and pressure monitoring sensors, and process system valve lineups.

I Prior to pressurization of the containment for ILRT, prerequisites specified in the test procedure (Reference 6.2) were completed.

Specifically, a survey of the containment exterior and accessible interior was performed per 10CFR50 l

Appendix J (Reference 6.3).

No evidence of structural deterioration was found during the containment inspection. Also, a containment temperature survey was conducted to determine that the ILRT instrumentation will accurately represent containment atmospheric conditions during the test. The containment temperature survey was conducted with containment fans off, a condition that was also maintained during ILRT.

Records of satisfactory completion of the i

test prerequisites is documented and records are maintained in the Official Test Copy of procedure ECT-701A, Revision 1.

Containment pressurization was started at 2033 hours0.0235 days <br />0.565 hours <br />0.00336 weeks <br />7.735565e-4 months <br /> on July 3, and a pressurization rate of approximately 3.6 psi /hr was maintained.

Pressurization system consisted of air compressors with an aggregate capacity of 14,400 scfm, after cooler, and a refrigerated air dryer.

During containment pressurization the containment fan coolers, with cooling water through the cooling coils, were run to control air temperature and prevent stratification.

Pressurization was stopped at 0400 on July 4 to investigate decreasing level indication in the Reactor Coolant Drain Tank.

The reading was determined within expectations and l

pressurization was resumed at 0619 on July 4.

Pressurization was stopped at i

1443 and a blind flange was installed in the pressurization line at 1550 on July 4.

Containment pressure was at the test condition of 49.3 psig.

Containment fans were stopped, cooling water to the cooling coils was isolated, and a temperature stabilization period was started.

Temperature stabilization criteria specified in Reference 6.2 were met four hours after reaching the test pressure. However, the measured leakage at the end of stabilization period was excessive. A survey of all containment penetrations was initiated to determine cause of high leakage rate.

Instrument air isolation valves 1-HV-3487 and 1-01-030 were inadvertently cycled during leak search. Therefore a LLRT penalty is taken for this penetration.

Leak search results indicate that there was no significant leakage through the containment isolation valves before or after being cycled.

Leakage from a containment recirculation sump was found and isolated at the containment spray pumps 1 and 3.

No penalty is taken for this penetration as this system retains water filled. A blind flange was installed to isolate containment purge at valve 1-HV-5538.

A penalty is taken for this penetration. Following restoration of the ILRT valve lineup, the ILRT was started at 1415 hours0.0164 days <br />0.393 hours <br />0.00234 weeks <br />5.384075e-4 months <br /> on July 6.

At the end of 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> after the ILRT start, the leakage rate and 95 percent Vpper Confidence Levels as specified in the Reference 6.2, for Mass Point Analysis were satisfied.

Total Time Analysis, although not required per the procedure, is also reported for information. During the entire ILRT test period the containment pressure remained between 48.3 and 50.0 psig as required. 1

i following the 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> of ILRT, a supplemental verification test was conducted.

At 1420 hours0.0164 days <br />0.394 hours <br />0.00235 weeks <br />5.4031e-4 months <br /> on July 7, a steady leakage of air at a rate equal to 8.96 scfm from the containment was established. After one hour of stabilization the leakage rate was measured for a period of four hours to verify accuracy of i

the ILRT instrumentation and the test methodology. The supplemental verification test validated the test results and ILRT instrumentation. After completion of verification test the containment was depressurized to O psig.

Various items of data needed to support or supplement the ILRT were recorded at regular intervals during the test, as required by the test procedure. All recorded data are included in the Official Test Copy of the procedure (Reference 6.2).

Data required to support ILRT results are included here in App ndix C.

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3.

TEST RESULTS

SUMMARY

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.l A. Plant Information 1

Owner:

Texas Utilities Electric Company NRC Docket No.:

50 - 445 Plant:

Comanche Peak Steam Electric Station Unit 1 Location:

Glen Rose, Texas Containment Type:

Reinforced Concrete NSSS Supplier:

Westinghouse, PWR Date Test Completed:

July 7, 1989 B. Technical Data 1.

Containment Free Air Volume (FSAR) 2,985,000 Cu. Ft.

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Design Pressure 50 psig 3.

Design Temperature 280 'F 4.

Calculated Peak Accident Pressure 48.3 psig L

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Calculated Peak Accident Temperature 270.5 'F 6.

Containment Average Temperature 40-120 'F Limits during ILRT C. Test Results - Type A Test at Peak Accident Pressure 1.

Test Method Absolute 2.

Data Analysis Techniques Mass Point Leakage Per ANSI /ANS 56.8-1981 3.

Test Pressure (actual) 49.0 psig 4.

Maximum Allowable Leakage Rate La 0.100 wt%/ day 5.

75% of La 0.075 wt%/ day l

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ILP.T Test Results (Lm) Leakage Rate wt%/ day From Regression at 95% UCL Mass Point 0.022 0.023 Total Time 0.024 0.026 7.

Verification Test Imposed Leakage Rate Li 5/ day (=La) 8.96 scfm 8.

Verification Test Results (Lvm) Leakage Rate wt%/ day Mass Point 0.115 Total Time 0.129 9.

Verification Test Limits (Lv) Test Limits 5/ day Mass Point Total Time Upper Limit Li+Lm+0.25La) 0.152 0.154 Lower Limit Li+Lm-0.25La) 0.102 0.104 10.

Report Printouts:

The report printouts and data plots for the Type A test and Verification calculations are provided for the mass point analysis in Appendix C. ~

11.

ILRT Adjustments and Other Penalties:

Water Level Changes:

During the Type A test, water levels in the reactor cavity sump, containment sumps 1 and 2, containment CCW drain tank, accumulators 1-4, and pressurizer relief tank were recorded hourly during the test.

Level changes observed during the conduct of the test are listed in table 5-2.

local Leakage Rate Penalties e

The penetrations not in their Post LOCA lineup during the ILRT are listed in Table 5.1 in Section 5.

A minimum pathway-leakage from these penetrations is added to the ILRT results. The analysis of these penalties is presented in Section 5.

Total Penalties Total penalties to be added to ILRT results above for final as left conditions are 0.002 wt%/ day.

12. AS LEFT ILRT Results ( Wt% Day) 95% UCL Penalties As Left Mass Point 0.023 0.002 0.025 Total Time 0.026 0.002 0.028 0.075 Acceptance Limit 0.075 l

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l D. Integrated Leakage Rate Measurement System The following instrumentation system was used for ILRT:

1.

Absolute Pressure Gages Quartz Bourdon Tube with Optical Tracking PI-1 PIT-012 A L

PI-2 PIT-012 B Calibrated Range 0-100 psia Calibration Accuracy 0.01% of reading Sensitivity 0.001% of full scale Resolution 0.001% of full scale Repeatability 0.001% of full scale 1

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Dry Bulb Temperature Sensors 100 Ohm platinum RTD TE-2 through TE-41 Calibrated Range 0 - 300 'F Calibration ~ Accuracy 0.5 'F Sensitivity 0.018 'F Repeatability 0.018 'F 3.

Dew Point Temperature Sensors Chilled Mirror j

l HE-1 through HE-14 Calibrated Range 40-100 'F Calibration Accuracy 2.0 'F Sensitivity 2.0 'F 4.

Flowmeters FM-1 Mass Flow Meter Calibrated Range 0-15 scfm Rotometer Calibrated Range 0-10 scfm Calibration Accuracy 2% of Full scale Sensitivity 1% of full scale Resolution 0.1 scfm 5.

Data Acquisition System Fluke 228CB data logging system with 2281A extender chassis Multiplexing with 16/17 bit A/D converter and digital clock Output Printer / Display /RS232 interface Calibration Range 0-256 ohms / 4-20 mA/ 0-8 Volts Calibration Accuracy 0.017 % + 0.0057 ohm on 0-256 ohm range 0.25 % + 0.004 mA on 4-20 mA range 0.005 % + 0.000007 Y on 0-8 V range 1 min /24 hour Resolution 0.001526 % of range 1 second for clock Repeatability 0.001526 % of range Sampling Rate 2 samples /sec 6.

Table 3-1 provide the associated locations and Volume Fraction for the dry bulb and dew point sensors used during the test.

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i TABLE 3-1 CONTAINMENT TEMPERATURE AND DEWPOINT SENSOR LOCATIONS AND VOLUME FRACTIONS FOR ILRT RTD Elevation Azimuth Distance from Volume Instrument No.

Feet Degrees center Feet Fractions TE-2 814 295 60 0.0111 TE-3 814 0

54 0.0128 TE-4 814 135 52 0.0133 TE-5 814 230 56 0.0171 TE-6 840 45 52 0.0053 TE-7 842 135 52 0.0124 TE-8 842 225 58 0.0157 TE-9 840 220 36 0.0090 TE-10 840 137 40 0.0081 TE-11 838 0

58 0.0097 r

TE-12 840 320 36 0.0090 TE-13 840 45 39 0.0090 TE-14 850 270 20 0.0170 TE-15 865 0

47 0.0056 TE-16 911 45 52 0.0054 TE-17 850 90 32 0.0170 TE-18 880 160 55 0.0164 TE-19 880 270 48 0.0275 TE-20 883 335 54 0.0189 TE-21 883 75 40 0.0252 l

TE-22 880 210 55 0.0164 TE-23 883 105 40 0.0252 l

TE-24 870 315 36 0.0066 l

TE-25 870 225 34 0.0066 TE-26 870 143 43 0.0057 l

L TE-27 870 50 50 0.0066 TE-28 928 225 40 0.0510 TE-29 928 135 40 0.0510

'TE-30 928 315 40 0.0510 TE-31 928 45 40 0.0510 l

TE-32 1010 225 40 0.0419 TE-33 1010 135 40 0.0419 TE-34 1010 45 40 0.0419 TE-35 1010 315 40 0.0419 L

TE-36 973 180 40 0.0549 1

TE-37 1045 0

24 0.0376 TE-38 1045 180 24 0.0376 l

TE-39 973 90 40 0.0549 I

TE-40 973 0

40 0.0549 TE-41 973 270 40 0.0549 7

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TABLE 3-1(CONTINUED)

CONTAINMENT TEMPERATURE AND DEWPOINT SENSOR LOCATIONS AND VOLUME FRACTIONS FOR ILRT Dew Point Elevation Azimuth Distance from Volume Instrument No.

Feet Degrees center Feet Fractions HE-1 820 300 55 0.0271 HE-2 820 120 55 0.0271 HE-3 845 0

55 0.0216 HE-4 845 150 55 0.0216 HE-5 850

'SG 1/4 0.0304 HE-6 850 SG 2/3 0.0304 HE-7 880 90 40 0.0877 HE-8 880 270 40 0.0877 HE-9 928 135 40 0.1020 4

HE-10 928 315 40 0.1020 HE-11 973 270 40 0.1098 HE-12 973 90 40 0.1098 HE-13 1021 45 40 0.1214 HE-14 1021 225 40 0.1214 1

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E. Local Leakage Rate Results:

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Local leakage rate tests on required containment pentrations were l

conducted in accordance with plant procedures. A summary of local leakage rate test results are included in Appendix D.

F.

Information Retained at Plant The following infornsation is available for review at the facility:

1.

A system lineup'at time of test showing required valve positions and r

status of piping systems, 2.

The P&lDs of systens which penetrate the containment.

3.

A listing of all containment penetrations, including the total number l

of like penetrations, penetration size and function.

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A continuous, sequential log of events from initial survey of i

containment to restoration of all tested systems.

5.

The working copy of the Official Test Procedure that includes signature sign-offs of procedural steps.

6.

A listing of all the test changes.

7.

Documentation of instrument calibration and standards used for calibration and their traceability to NIST (National Institute of Standards and Technology formerly NBS) j 8.

Computer printouts of all test data collected through the data j

acquisition system, and manual data collected during the test.

9 Procedures for performing all type B and C testing and LLRT test l

data.

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TEST METHODOLOGY The integrated leakage rate test is performed to verify that the leakage from the containment system at calculated accident pressure does not exceed the specified limit.

The containment is prepared for tie test by closing all access ways and aligning valves in post accident position.

All valves are closed using normal means and without exercising or using excessive force.

The valves not aligr.ed in the >ost accident condition are listed in Section 5 of 6

this report. Measured lea (age through these valves, using minimum pathway analysis, is added to the UCL to account for the non. standard lineup. All items that could be damaged by test pressure are removed from the containment l

or vented.

Pressure sources inside the containment are vented or removed, i

Leakage Rate Measurements j

The test objective is accomplished by pressurizing the containment with clean and relatively dry air. The containment atmospheric parameters are measured using the ILRT instruments described in Section 3.

Containment average drybulb temperature, wetbulb temperature and absolute pressure are i

measured. Using the ideal gas law, containment air mass is calculated at every 15 minute interval.

The loss of containment air mass over a specified seriod determines the leakage from the containment. After a leakage rate has seen 4

determined, the calculational method is verified by a supplemental test during which an additional known leakage is imposed on the containment and a new leakage rate is calculated, j

Leakage Rate Calculational Methods Containment leakage rate is calculated using the mass point method described in Reference 6.6.

The method uses containment pressure, drybulb temperatures l

and dewpoint temperatures recorded every 15 minutes as input data.

The mean absolute temperature of the containment was calculated using method described in Reference 6.5.

The measured dewpoint temperatures are used to calculate the l

water vapor pressure in the containment atmosphere.

Evaporation and condensation of water changes the partial pressure of the vapor phase. This partial pressure is subtracted from the containment absolute pressure so that the internal phase changes are not erroneously accounted for as actual in or out leakage from the containment. The mass of dry air in the containment is calculated using the ideal gas law, with average containment temperature and dry air pressure.

The calculated air mass is plotted against time.

The slope of the l

regression line (best fit line) through the air masses is defined as the mass point leakage rate.

The measured leakage rate at a given time is defined as the calculated change in the air mass since the start of the test divided by the elapsed time since the start of the test.

The mass point method utilizes the variance of data points about the regression line to establish a 95 percent Upper Confidence Limit on the leakage rate.

Reference 6.6 describe the calculation method in detail.

After pressurizing the containment to test pressure the containment atmosphere is required to stabilize for a minimum of four hours. Once the stabilization criteria specified in the test procedure are satisfied the test may be started.

The lea (age rate is calculated for a test period of 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.

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l Following determination of the leakage rate the test results are verified by the supplemental verification test.

The supplemental test consists of imposing 3 known amount of leakage from containment (normally La) and measuring the increased leakage rate. The new calculated leakage rate must equal previously calculated leakage rate plus the imposed flow within the allowable tolerance of 25% of La. The supplemental test has a duration of at least four hours.

l Test data collected during the test and leakage rate analysis are presented j

in the Appendix C.

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ANALYSI' AND INTERPRETATION S

5.

The sumary of test results presented in Section 3 of this report is based on data collected during the test. These results must be corrected for the penetrations in non-standard alignment and adjustments must be made for any water level changes during the test.

Local Leakage Rate Addition A number of mechanical systems that penetrate containment and systems that are assumed to be drained and vented post LOCA were maintained in operation or were not vented during the test. To account for leakage which would have passed through these penetrations in the normal post LOCA configuration, the minimum pathway local leakage is totaled and the total is added to the calculated leakage rate UCL. Table 5.1 lists all such penetrations and the penalties associated with them.

Water Volume Correction During the Type A test, water levels in the reactor cavity sump, containment sumps 1 and 2, containment CCW drain tank, accumulators 1-4, and aressurizer relief tank were recorded hourly during the test. Level changes osserved during the conduct of the test are listed in table 5 2.

The water volume changes is equivalent to a leakage rate of 0.0008 %/ day.

Composite Test Results The composite leakage rate is the sum of the calculated rate, the correction for the water level changes and local leakage rate penalties.

The final results are sumarized as follows:

Mass Point (wt%/ day)

Total Time (wt%/ day)

Calculated 95% UCL Calculated 95 %UCL From Test Data 0.022 0.023 0.024 0.026 Local Leakage Penalty 0.0011 0.0011 0.0011 0.0011 (Table 5.1)

Volume Correction 0.0008 0.0008 0.0008 0.0008 (Table 5.2)

Composite 0.024 0.025 0.026 0.028 Acceptance Limit 0.075 0.075 0.075 0.075

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I TABLE 5.1 j

LOCAL LEAKAGE RATE PENALTIES For Penalty Penalty J

Penetration See Leakage j

Number Service Note ()

(SCCM) i MV-12 Chill Water Supply to Cont. Coolers 1

7 MV 13 Chill Water Supply from Cont. Coolers 1

18 MV 7 ILRT Pressure sensing line 1

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Mill 30 ILRT Pressurization line 1

9 Mill 22 Instrument air line 3

632 MV 2 Containment Purge 2

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TOTAL 2535 EQUIVALENT LEAKAGE 0.0011 %/ day e

In service for test.

Isolated for test.

Isolation valves 1 HV-3487 and 1-01-030 inadvertently stroked.

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i TABLE - 5.2 VOLUME CHANGE DURING ILRT CUBIC FEET Containment Sump 1 0

Containment Sump 2 6

l Reactor Cavity Sump 0

Accumulator Tanks 0

Reactor Coolant Drain Tank 0.5 CCDW Drain Tank 0

Pressurizer Relief Tank 18.5 i

Pressurizer 0

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TOTAL 25.0 EQUIVALENT LEAKAGE 0.0008 %/ day 6,

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6.0 REFERENCES

6.1 Comanche Peak Steam Electric Station Unit No. 1. Draft Technical Specification 6.2 Comanche Peak Steam Electric Station, Procedure Number EGT 701A, Revision 1, Containment Integrated Leakage Rate Test.

6.3 Code of Federal Regulation ~, Title 10. Part 50, Appendix J - Primary Reactor Containment Leakage Testing for Water Cooled Reactors.

6.4 ANSI N45.4 - 1972 Leakage Rate Testing of Containment Structures for Nuclear Reactors.

6.5 ANSl/ANS 56.8 1981, Containment System Leakage Testing Requirements.

6.6 ANSI /ANS 56.8 1987, Containment System Leakage Testing Requirements.

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APPENDIX A j

9 DESCRIPTION OF BECHTEL ILRT COMPUTER PROGRAM i

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AMBE1IX A.

IEBCRIPTICM OF IEEMIE IIRr G3EUHR PRXEUM l

A. F1- -- - and T- --i.T m1* %

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The Bechtal IIRP ocmputar pww.wi is used to detemine the integrated leakage rate of a ruclear primary contaiment structure. 7he program is used to ocagute leakage rata based on igut values of time, free air volume, contaiment atnosphezu total pressure, drybulb tasperature (mean 'Naperature, calculated usirg ANSI /ANS 56.8-1981),

ard dowpoint temperature (water vapor pressuru).

Imakage rata is ocmputed usirg the Absolute Method as defined in ANSI /ANS 56.8-1987, "contaiment System Imakage Testing Requirements" and Bi-cop-1, Rev 1, "'Mstirg Critaria for Integrated Imakage Rata 'Nsting of Primary contaiment Structures for Nuclear Power Plants". 7he program is

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designed to allow the user to evaluate containment leakage rate test results at the jobsite during contalment leakage tasting. Current leakage rate values may be obtained at any time during the tastiry period using one of two ocmputational methods, yieldirg three diffarent report printouts.

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In the first printout, the 7btal Time Report, leakage rata is ocmputed frm initial values of free air volume, containment atnesphere drybulb tanparature and partial pressurv of dry air, the latest values of the same parameters, ard elapsed time. These individually ocetuted leakage ratas are statistically averaged using linear regression by the method of least squares. The 7btal Time r

Method is the ocmputational technique upon which the short duration test criteria of af-cop-1, Rev 1, " Testing Criteria for Integrated Isakage Rata 'Msting of Primary containment Structures for Nuclear Power Plants," are based.

3.

The second printout is the Mass Point Report and is based on the Mass Point Analysis 'Mchnique hibed in ANSI /ANS 56.8-1987, l

"Contaiment Systan Isakage 'hsting Requirements". The mass of dry air in the containment is ocmputed at each data point (time), using i

the Ideal Gas Law, frun current values of mean containment at iW,ere drybulb tamperature (based on ANSI /ANS 56.8-1981) and partial pressure of dry air. Contained mass is "plottad" versus time and a repassion line is fit to the data using the method of least squares. Imakage rata is detamined frun the statistically derived i

slope and intercept of the regression line.

4.

The third printcut, the Trend Report, is a suninary of leakage rata values h==4 on 7btal Time and Mass Point computations presented as a function of nunber of data points and elapsed time (test duration).

The Trend Report provides all leakage rata values required for ocuparison to the acceptance critaria of Bi-70P-1 for conduct of a short duration tast.

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'Ibe program generatas a predictor report based on " Suggested critaria for a Short turatice IIRr", 'Nd Brown and Imis Estenssoro, l

Ps-- ima of the First Wcik is an Cudair 7t hstirn, January 18,1982. 'Ihe " predictor" is an estinata of the upper bound on the i

change in mass point calculated leakage rate which will ooour durirq the next four hours. 'Iha estinata is based on the mass point l

calculated leakage retas and 95% UCLs during the previous four hours.

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'Ihe prwsaie is written in a high level language and designed for use on a miwv,.uyatar with direct data irput fran the data acquisition system, Brief descriptions of pawa ih use, forr.ulae used for leakage l

rate cxmputations, ard program logic are prtwided in the following l

pair a.62s.

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If drybulb and dowpoint tesperature sensors should fail during the test, the data fran the sensor (s) are not used. 'Ihe volume fractions j

for the remaining sensors are roocsputed and rel* into the pawsais for use in ensuing leakage rata ocmputations. 'Ibe program l

must have the capabilities of reassignirq volume fraction ard recalculata values during the test.

B. Beolanation of Fii.maih 1.

'Ibe IIRT ocmputer program is writtan, for use by experienced IIRr personnel, to determine containment integrated leakage ratas hamai cn i

the Absolute Method described in ANSI /ANS 56.8-1987 and EN-70P-1.

2.

Information loaded into the program prior to or at the start of the l

test should include but not limited to :

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Number of containment atmosphere drybulb tanparature sensors, dowpoint temperature (water vapor pressure) sensors ard pressure gages to be used in leakage rate ocmputations for the specific test j

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Volume fractions assigned to each of the abcne sensors t

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Calibraticn data for abcNe sensors d.

' Dest title e.

Mavi== allowable leakage rata at test pressuru 3.

Data received fran the data acquisition system during the test, and used to canputa leakage rates:

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Time and date b.

Cantalment atmosphere drybulb tanparatures o

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If drftulb and dowpoint tamparature sensors abould fail during the test, the data frtan the sensor (s) azu not used. The volume fractions for the rummining sensors are rhW and reloaded into the program for use in ensuing leakage rate ocrputations,

c. Innkega nata rtraulam 1.

Ozq:utations Using the 7btal Time Methods a.

Mansured leakage rata frtan data PV11 = W E1 (1) j 1

PVii=WMi (2) i 2400 (W1-W) i att 1 l

W Solving for W and W1 and substituting equations (1) and (2) i 3

into (3) yielas t

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l 2400 TPV Li (4)

=

i11 f f

ati

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TPV where W,Wi = Weight of contained mass of dry air at times t1

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1 and t, respectively,11sn.

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T,Ti = contairment atzesphere @ tamparature at 1

times t i and t, respectively,

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i P,Pi = Partial pressure of the dry air myx-A. of the 1

containment at:mosphere at times ti and t,

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respectively, psia.

V,Vi = containment free air volume at times ti and 1

t,respectivgly(constantorvariableduring

.1 the test), ft.

t,ti = Time at 1st and ith i

data points respectively, hr.

ati = Elapsed time frVm ti o t, hr.

t i

l R = Specific gas constant for air = 53.35 ft.lbf/1hn. 'R.

l Li = Heasured leakage rate corputed during time interval t to t, kt.%/ day.

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t ATi 1 +

l Tg P

P APg=ViVt AVi= i-i aTi=Ti-T1 I

b.

Calculated leakage reta fras regression analysis:

r l

(5)

L=a+baty i

M i

L = calculated leakage rate, wt.%/ day, as determined fran the f

regressien line.

a = (ILi - b Iat )/N (6) j i

i N(IL at ) - (IL )(Iat )

i i

i i

i b=

(7) l KiI a ti ) - (Ia t )2 2

i N = member of data points.

N I=

I i=1 l

c.

95% uppe.T confidence limit on the calculatui leakage ratet UCL = a

  • b J tg + S-

[

i r

A-4

1 i

Wem UCL = 95% upper confidence limit st.4/ day, at elapsed time a tg.

l for a tg < 24 i - b IL at )/(N-2))1/2 2 - AIL t, ( ( I L1 S-i i

=

/

2 - (IAt )2 p)) y 2 (9,)

(1 + 1 + (atg - at)2 (Iati i j N

1 where t, = 1.95996 + 2.37226 + q(N-2) r N-2 i

Tor s ty h 24 i - b EL at )/(N-2))1/2 2 - AIL S-

= t,

((IL1 i

i

/

2 - (It )2fp)) 1/2 (9b) l (1 + ( a ti - a t)2 (Iati i

N e

i 1.6449(N-2)2 + 3.5283(N-2) + 0.85602 wham t, =

(N-2)2 + 1.2209(N-2) - 1.5162

~

Li = calculated leakage rata ccuputad using equation (5) at total alapsed tire at, t/M.

i 3;, Isti N

2.

Caputation using the Mass Point Methodt j

a.

Contained mass of dry air fra datat l

l l

Wi = 144 P Vii (10)

RTi when l

All symbols as previously defined.

F l

l A-5

I b.

calculated leakage rate frta regression analysis, W = a + b a t I, = -2400 N a

(11)

W re I

i, calculated lenkmqpe rate, wt.%/ day, as dotarmined frta

=

the rugression line.

(IWi - bIat )/N (12) a

=

i N(IW.it ) - (IW )(Eat )

i i

i i

(13) b

=

N(Iati ) - (I at )#

d i

th ati= htal elapsed time at time of i data point, hr.

Number of data points.

N

=

th Wi contained mass of M air at i data point, lla,

=

as a:mputed frua equation (10).

N I

I

=

i=1

% reduon truncation error, the ocmputer program uses the following equivalent fortadation:

AWi b

g

-!at )/N (14) a = W 1 + (I i

W W

1 1

1 JWi AWi l

N (I at)-I Iati i

W W

1 2

(15) b Wi

=

N(Iati ) - (Ist )2 2

i whers is as prwiously defined.

W1 c.

95% upper confidanoa limit.

-2400 UCL =

(b - S )

(16) b a

A-6 l

Wars tXL = 95% y confidence limit, wt.%/ day, sul/2

  • [NIat 2 - (Iat )2)1/2 gg7) i i

1.6449 (N-2)2 + 3.5283 (N-2) + 0.85602 wher t, =

(N-2)2 + 1.2209 (N-2) - 1.5162

" I (Wi - (a + b at ) / ' W i

S

=

N-2 l

I (aW M )2. ( 3(3wiy1) g y.

l

)l N-2

= W i 1 1

i i

I(aW M )(Iat )M/'

W l

( I( a W /W ) a ti-i 1 i

i 1 (18)

E(a ti ) - (I a t )2g 2

i d.

Predictor 100(2(IXL-L)+4(l81+2S))

A la Where t

i l

UCL = 95% typer confidence limit of mass point calculated leakage l

rata at and of test.

l-L

= Mass point calculated leakage rate at and of test.

B

= Value of linear regression analyais slope of mass point calculated leakage rata vs. time for last 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> of test data.

S

= Linear regression analysis standard deviation of slope.

A L

Ia = Allowable leakage rate.

+

l In tems of elapsed time, a t and y point calculated leakage rate Imi calculated at the erd of i time interval.

l A-7

i f

'q g i

~

1 I

ini - B I ati A

M 4 hr 4 hr (19) i M I uni ati-I Iai I ati 4 hr 4 hr 4 hr (20)

B

=

1 2

M I ati

-(I at )2 l

i 4k 4&

j i

I L

I Iai-AI mi - B I uni a ti i

4 hr 4hr 4hr (21)

(M) s

=

g st )2) 2 i - (4 hr (M-2) (M I at I

i 4 hr i

m poh calmisW IW rate MmW ming hta

(

uni

=

ty to t.'as a t.

i 5

4 hr = suunnation over last 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> of test data.

I N

I I

=

N-M+1 number of data points for last 4 hours4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> of test.

M

=

i f

h r

b 9

A-8

D. Pmpram Ingric i

1.

The Bactitel 11RT caguter program logic flow is controlled by a set i

of user options. The user options and a brief description of their associated function are presented below.

OPPICH

(

CDtGND fuCTICH After startirq the program e:ceaution, the user either antare the name of the file containing i

prwiously entered data or initializes a new data t

file.

l t

CATA Enables user to entar row data. When the system requests values of time, volume, tanparature, pressure and vapor pressure, the user enters the appropriate data. After ocupleting the data entry, a mamary is printed out. The user then verifies l

that the data were entered A. d y.

If errors are detected, the user will than be given the I

  1. dty to correct the errors. After the user verifies that the data were entered m. W y, a Corrected Data simmanry Report of time, data, average j

I tempersture, partial pressure of dry air, and water f

vapor preamtre is printed.

l l

TRFND A Trend Report is printed.

l 7UIAL A Tbtal Time Report is printed.

l MMis A Mass Point Report is printad.

['

\\

l TDM Enables user to sign-off tasporarily or pernanently. All data is saved on a file for restarting.

CERR Enables user to correct prwviously entered data, j

LIST A Sunsary Data Report is printed.

f READ Enable the computer to receive the next set of data

+

fran the data Waition system directly.

1 Picr Enables user to plot sumary data, irdividual sensor data or air mass versus time.

i DE2 RTE Enables user to delete a data point.

INSDtr Enables user to reinstate a prwiously deleted data point.

I voIJ7A Enable user to charge volume fractions.

A-9 1

1

t i

l i

OPTION i

CI199dD BEIElf l

l IPED A praiictor report is printed.

j TIME Dmble the usar to specify the time interval for a report or plot.

i VERF Dable the usar to irput imposed leakage rata and l

onlcallated IIJtr leakage rates at start of j

verification test.

E. Qagastar Depart and Ikta Printsatt

) ASS POINT REPCRT i

'Ibe Mass Point *@ presents leakage reta data (wtt/ day) as determined l

by the Mass Point Method. 'Ihe "Omicallated Imakage Rate" is the value detamined fran the rayrussion analysis. 'Ihe "contairnant Air Mass" values are the aneses of dry air in the contalment (1 tun). 'Ibene air masses, detamined fran the Equation of Stata, are used in the regression analysis.

i

'IUIAL TIME RERRP

'Ibe 'mtal Time w.t. presents data lankage rata (wt%/ day) as detamined by the 'mtal Time Method. 'Iha " calculated Imakage Rate" is the value i

l detamined fran the regressicri analysis. '!he " Measured Imakage Rates" are the leakage rate values determined usirsy 'mtal Time calculations.

t

'Ihese values of leakage reta are used in t.'w regression analynis.

i L

l

'mmD Ruont l

'Ihe Trend Report presents leakage rates as determi.W by the Mass Point and 'mtal Time methods in percent of the initial ocritained mass of dry air per day (wt%/ day), versus elapsed time (hours) and runbar of data points.

1 3REDICITR REPORT i

'Ihe predictor w~ds presents a predicted upper bound on the change in calca11ated nasa point leakage ruta over the next four hours.

I SLMSRt Dh'IA REPCRT i

'Ihe Sumary Data report presents the actual data used to calculate leakage rates by the various methods described in the cariputer Program" section of this report. 'Ihe seven colums are TIME, !WrE, TDT, i

PRESSURE, VPRS, VOIDME, ard ADMGS and contain data defined as follcus:

l 1

A-10

1.

TDE:

Time in 244u:ur rotation (hours ard nimtes).

2.

CATE:

Calardar data (month ard day).

i 3.

TEMPS contaimant wei@ tad-average drytulb tanparature in absoluta units, degrees Rankine ('R).

i 4.

MESSURE:

Partial pressure of the dry air wwnt of the i

contairment atmos $ere in absoluta units (psia).

5.

VWts:

Partial pressure of water vapor of the containment atmos @ ere in absoluta units (psia).

6.

VOIINE:

Containment free air volume (cu. ft.).

7.

ADNNES:

Calculated dry air mass (lkun).

I l

F. Staumary of Measured Data and im of Quxected Ikta l

The Sunnary of Mansured Data presents the irdividual ocntalment I

atmosphere drybulb temperatures, dowpoint tanparatures, absoluta total pressure and free air voltme ressured at the time and data.

1.

11NP 1 throu$ TTMP N are the drybulb temperatures, where N = No. of l

Rm's. The values in the ri$t-hard column are tamparatures ('F),

i valltiplied by 100, as read from the data acquisiticus systaan (IAS).

t the values in the left-hand ooltan are the corrected tamperatures l

=:-b ---i in absoluta units (*R).

l

\\

i l

2.

MtES 1 throup MOS N are the total pnsesures, absoluta, were N = No.

l l

of pressure sensors. The ri@t-hand value, in parentheses, is a rameer of counts as read fri:en the t*S.

This count value is convertad L

to a value in psia by the cxmputer via the instnanent's calibration table, counts versus psia. The left-hand ooltam is the absoluta t

total pressure, psia.

[

l 3.

VPRS 1 throu$ VRts N are the dowpoint tamperatures (water vapor presmires), where N

  • No. of dowpoint eensors. The values in the right-hand coltasi are temperatures ('F), m11tiplied by 100 as read l

t fresa the CAS. The values in the left-hard colunn are the water vapor pressures (psia) frtza the steam tables for naturated steam corrompending to the dowpoint (saturation) tamparatures in the cantar ooltam.

The Sumary of Corrected Data presented corrected tampeletare ard l

pressure values and calculated air mass detamined as follows:

1.

TEMPERA 1URE (*R) is the volume wei@ted average containment atsie t sere drytulb tamparature derived frtun TEMP 1 through 11MP N.

l i

t t

A-11 l

I

2.

CCfetD3tD MtESSURE (psia) is the partial pnessure of the dry air ocuponent of the contalment at@, absoluta. '!he volume L

wei@ tad average containment atnosphers water vapor prissure is subtracted frun the volume wei@ tad average total pressure, yieldirn the partial pressure of the dry air.

3.

VAICR MtESSURE (pia) is the volume wei@ tad average contaimant j

atnes@ers water vapor pressurw, absoluta, derived frun VPRS 1 thrtsa$ VMts N.

4.

V011NE (cat. ft.) is the contaimant frue air volume.

j 5.

caNTADMENT AIR MhSS (Itm) is the calculated mass of dry air in the i

contaimant. 'the mass of dry air is calculated using the contaimant l

free air volume and the abwe 'ITMPERA'!URE ard 00RRECIt:D MtESSURE of the dry air.

i i

l

{

l l

l l

l A-12

l p

r APPENDIX 8 INSTRUMENT ERROR ANALYSIS 4

P i

s 5

ISG CALCULATION

( ANSI /ANS 56.8 1981 )

1 CALIBRATION DATA l

SENSOR DISPLAY f 0F SENSORS SENSITIVITY (E)

REPEATABILITY (r) i TEMPERATURE (T) 40 0.0180 deg. F 0.0180 deg. F PRESSURE (P) 2 0.0010 psia 0.0010 psia VAPOR PRESS (Pv) 14 2.0000 deg. F 0.0027 deg. F j

t LENGTHOFTEST(t) 24.00 hrs PRESSURE (P) 63.42 psia TEMPERATURE (T) 541.9 deg. R VAPOR PRESS (Pv) 0.01435 psi /deg. F (at 75 deg. F) t La 0.100 wt%/ day INSTRUMENT MEASUREMENT ERRORS t

t 2 1/2 1/2 eT. [(ET)

+ (rT)

)

/[#ofsensors) eT.

0.00402 deg. F l

eP = ((EP) +(rP) ) /2 /[#ofsensors)/2 1

1 l

2 2

t-i l

eP.

0.00100 psia ePV = ((EPv) + (rPv)

)/2 /(fofsensors)/2 2

2 1 1

ePv.

0.00767 psia INSTRUMENT SELECT!DN GUIDE 2

2 2

1/2 ISG 2400/t( 2(eP/P) + 2(ePv/P)

+ 2(eT/T)

)

0.017 wt%/ day ISG

=

.25La =

0.025wt%/ day

_, ~, - -,._. - -

L APPENDIX C ILRT DATA 4

[

~$

l

[

h 1

i

[

c C

e t

f l

Q 9

e l

e i+ w e%, s..,.,_

.m.--

u r

t N

g 2

,~

,~

,~

n o

, 's, i

.~

S 7

R 0

U Y7 h

O A

H D/E a

L 0

XT L

C 0

A U

E D

5 T

4 7

A 002 a5 5

R a'

L1 0

9 4

2-1 951 8 7. E E

E 9

M 100 I

I T

YOT LD D

UAD E

J N

S LE P

TC A

RU L

L 6

E I

.0 E7 1TA TRE 0

I T

0 NEA UGD 6

A

- K5 A1 KE4 AL1 E

PTE NM E II HOT

'j CP N

T y

ASR MSA b

OAT J

CMS

/

\\'\\

\\

0 0

5 0

5 0

5 0

2 0

7 5

2 0

0 0

0 0

2 1

8 8

8 s

8 "8

d8

8. 4 3

m a-m

'W p

8 l

3Dg d

25" es g

5 8

Ik$

bW e

f 3

O l

l l

l l

l l

l l

8 8

8 8

8 8

R R

R R

R R

8 8

8 8

8 8

8 8

8 8

s 8

8 8

8 8

8 8

.m.

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 MASS POINT LEAKAGE RATE AND VERIFICATION TEST LIMITS START TIME 1530 DATE 707 END TIME 1930 DATE 707

.250

.200 --

UPPER LIMIT

.150 --

RATE

.100 --

/

LOWER LIMIT

.050 --

.000 I

l

.00 1.00 2.00 3.00 4.00 ELAPSED TIME -

4.00 HOURS

- - - - - ~

(.

f 8

l' i

t I

8

- g

/

.g y

[

3 f

be W"

b 8

n EW 3

3 C8

$2 i

I g

~,

R$*

-t

,/

Y c

sus ge

~ ~

8 H

H Eg8

'83 lg-1 :

g 4

s S

8 S

8 8

8 8

o o

8 8

9 o

9 9

R R

8 i

5 S

j 8

B R

m 8

S m

m y

m J

1 i

3 8

g I

?

s r

g l

s

(

3 m

I (g,

M I

.i 4.

r q

3

,,3 P

l M

v.

,b

,.E

?

1>

h t

i N.

4.

t w-

.g l

8

ER I.
R i I.

W H

~'

f s

2 O

/

b

[

y N

M o

s 4

N t

s i

w J

M i

s s

H g

4 t

3 O

(

N 1

  • jy I*r 1

-s 4g 4

8 l

8 8

8 8

o o

8 g

0 o

a o.

~

~

a - -

e 4>

t>

e 1>

1 1,

de d>

p q>

t Sk 4P I

>v.

t IO 4>

I q>

q>

q>

4b ob i

i W

g R 5

'E Mg e

W r

1 a

i M

r b

g l

l da H

O I

b wg.

g t

M M

F ow i

g q

4P.

g g

h db "

1 0

g w

l l

1 1(&

k e

i l

4m l

l m

n>

l

8 7

j 8

m m

N N

w w

(D CD C

ID ED ED w.,

--,,-w-

, - -, > -. - - -,,, -,. ~ -

--,------.g,-

,---n,,.

COMANDE PEAK - UNIT 1 ILRT JULY 1989 PRESStRE PSIA (DRY AIR) l START TIME 1500 DATE 704 END TIME 1930 DATE 707 63.100 1

k l

..I l

)

65.050 --

j i

i 63.000 --

l 4

e i

i l

i l

62.950 --

1

)

i l

62.900 --

i I

62.850

-^^^:-^^^

^-"^;^-4:^^^^--^^^^^^^^

-4
^^--^^--^^^^:-^^

^!"^^^---

-'^- :-^^^^

.00 19.13 38.25 57.38 76.50 i

ELAPSED TIME = 76.50 HOURS

.. ~ _ -.

~,

q s

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 VAPOR PRESSURE PSIA START TIME 1500 DATE 704 Ele TIME 1930 DATE 707 450 t

1 i

.445 --

t l

i

(

.440 -

.I U

J

__V i

j

.435 --

1 i,

1 i

5 f

.430 --

b 1

4 1

I i

.425

^^^^-""-.:- ::- ':^^- -^:: ::-^: :::4:::::^: ::::
4:---

.00 19.13 3e.25 57.38 76.50 ELAPSED TIME - 76.50 HOURS

i i

COMAMCHE PEAM - IMIT 1 ILET JULY 1969

_t I

DRYBULB TEMPERATURE SENSURS Z-41 A AUERAGE

  • F i

START TIME 1500 DATE 794 EMD TIME 1930 EATE 707 98.000 1

l i

t 1

i l.t 4

T 000 --

37-3s l

t w

t t

~

m_

_=

=

l

\\

1

_ 32-35 i

i 39-41 N.000 - -

i i

36 i

AVERAGE t

80.000 --

i 28 j

?

16 i

i I

6-15 & 17-27 j

74.000 --

2, I

2-5 l

f i

m. m 76.59 HDURS i

ELAPSED TIME

=

~

).

}

4 1

i 1

l f,,

ll L

L 9

(L!

Lj i i i

4 ',

p r

E E

i ii

".8 f'

! )

i m

i i

i, i

Y. E

,)

)

u k

55A

-AE 5

l

,e 5

l l W

L 2

(,

E1 h5 A

i, Eig

~

I N.e l

l l

T i

,i l

l s

I y<

a l

l RN f

i 2

'j T

i I i

i EM

{ $

i l

N I

I y

l A

a l

l.

E E

R R

S 9

1 1

1 W

T T-T 1"--

N W-

-V**D-9e v'=r e--=e*T-14"-*w-*e-t-*F-we=='wawWmur_v-es_._ww_w-,m_

m-*---

---m m

,7

. _ _ _ - ~ _,.,. _ _ _ _

11 f

1 i

es b

a.

e p

a.

n m 4

pt e m f

M M

e ne

.j

( )

e n 4

M E

W 4

4 4

9 O

i:

7 e

a e 4

W ges

.p e

us ll g

: g u

L N

N

- - E w

,i..

p.

.gE E

4 i

gg mW e

se W

G Iy e

W W

BS W

1 u

l L

g p

g G H W.

l.

l l

l l

w w

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 TEMPERATURE STABILIZATION 2

'f FROM A STARTING TIME AND DATE OF 1015 706 1989 TIME TEMP ANSI BN-TOP-1 MS-021-5 AVE AT AVE AT DIFF AVE AT AVE dT (HOURS)'

(*R)'

(4 HRS)

(1HR)

(2 HRS)

(2 HRS)

.00 541.179

.25 541.187'

.50.

541.189

.75.

541.197 1.00 541.200 1.25 541.207 1.50 541.212 1.75 541.216 2.00 541.221

.021*

.006*

2.25 541.227

.020*

.010*

2.50 541.230

.021*

.012*

2.75 541.242

.022*

.021*

3.00 541.240

.020*

.019*

3.25 541.242

.017*

.008*

3.50 541.242

.015*

.008*

3.75.

541.250

.017*

.007*

l 4.00 541.254

.019

.014

.005*

.017*

.007*

  • . INDICATES TEMPERATURE STABILIZATION HAS BEEN SATISFIED L

l f

l.

i f

l l

\\

l l

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 l

LEAKAGE RATE (WEIGHT PERCENT / DAY)

MASS POINT ANALYSIS TIME AND DATE AT START OF TEST 1415 706 1989 l

TEST DURATION: 24.00 HOURS TIME TEMP PRESSURE CTMT. AIR MASS LOSS AVERAGE MASS (R)

(PSIA)

MASS (LBM)

(LBM)

LOSS (LBM/HR) 1415 541.254 62.9235 920049.4 1430 541.257 62.9235 920044.9 4.5 18.2 1445 541.260 62.9236 920040.4 4.5 18.0 1500 541.263 62.9238 920039.9

.5 12.6 1515 541.262 62.9245 920050.8

-10.9

-1.4 1530 541.269 62.9251 920047.8 3.0 1.3 1545-541.270 62.9249 920042.4 5.4 4.7 1600 541.273 62.9249 920037.5 4.9 6.8 1615 541.276 62.9251 920035.4 2.0 7.0 L

1630 541.284 62.9256 920028.8 6.7 9.2 l

1645 541.282 62.92G1 920039.8

-11.0 3.8 1700 541.285 62.9259 920033.0 6.8 6.0 1715 541.284 62.9256 920028.4 4.6 7.0 1730 541.289 62.9253 920017.1 11.2 9.9 1745 541.293 62.9257 920015.0 2.1 9.8 1800 541.298 62.9257 920006.6 8.5 11.4 1815 541.300 62.9268 920019.8

-13.2 7.4 1830 541.308 62.9267 920004.6 15.2 10.5 1845 541.310 62.9271 920007.1

-2.5 9.4 1900 541.319 62.9274 919995.7 11.4 11.3 1915 541.322 62.9278 919996.5

.8 10.6 1930 541.327 62.9280 919990.4 6.1 11.2 1945 541.331 62.9281 919984.8 5.6 11.7 2000 541.337 62.9290 919989.9

-5.1 10.3 2015 541.336 62.9295 919997.8

-7.8 8.6 2030 541.345 62.9295 919982.4 15.3 10.7 2045 541.351 62.9302 919982.8

.3 10.3 2100 541.357 62.9306 919978.6 4.2 10.5 2115 541.362 62.9311 919977.0 1.5 10.3 2130 541.368 62.9315 919973.5 3.5 10.5 2145 541.371 62.9321 919975.8

-2.3 9.8 2200 541.382 62.9331 919972.5 3.3 9.9 2215 541.389 62.9336 919966.6 5.9 10.3 2230 541.397 62.9337 919955.9 10.7 11.3 2245 541.399 62.9346 919966.0

-10.1 9.8 2300 541.408 62.9354 919962.9 3.1 9.9 2315 541.419 62.9360 919952.1 10.8 10.8 2330 541.425 62.9367 919952.1

.1 10.5 2345 541.430 62.9370 919948.1 4.0 10.7 0

541.437 62.9380 919951.4

-3.2 10.1 15 541.444 62.9391 919955.1

-3.7 9.4 30 541.452 62.9403 919958.1

-3.1 8.9 45 541.464 62.9410 919948.5 9.6 9.6 100 541.474 62.9420 919947.1 1.5 9.5 115 541.482 62.9424 919939.0 8.1 10.0 130 541.487 62.9432 919941.9

-2.9 S.6 145 541.501 62.9446 919939.2 2.7 9.6

Y.

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 LEAKA!E RATE (WEICHT PERCENT / DAY)

MASS POINT ANALYSIS TIME AND DATE AT START OF TEST 1415 706 1989 TEST DURATION: 24.00 HOURS l

TIME TEMP PRESSURE CTMT. AIR MASS 1455 AVERAGE MASS I

(R)

(PSIA)

MASS (LBM)

(LBM) 14SS (LBM/HR) 200 541.509 62.9450 919930.3 8.9 10.1 215 541.524 62.9459 919919.3 11.1 10.8 230 541.531 62.9469 919921.4

-2.1 10.5 245 541.538 62.9483 919928.7

-7.3 9.7 300 541.550 62.9492 919922.5 6.2 10.0 315 541.562 62.9505 919920.5 2.0 9.9 330 541.570 62.9519 919928.1 7.6 9.2 345 541.579 62.9526 919923.0 5.1 9.4 400 541.591 62.9537 919918.1 4.9 9.5 415 541.598 C2.9551 919926.9

-8.8 8.7 430 541.607 62.9553 919913.7 13.2 9.5 445 541.614 62.9563 919917.8

~4.1 9.1 500 541.630 62.95'5 919907.4 10.3 9.6 515 541.644 62.9587 919902.0 5.5 9.8 530 541.651 62.9594 919900.6 1.4 9.8 545 541.661 62.9597 919887.0 13.6 10.5 1

600 541.671 62.9616 919898.3

-11.3 9.6 615 541.676-62.9621 919896.8 1.6 9.5 630 541.691 62.9633 919888.8 8.0 9.9 645 541.695 62.9636 919887.1 1.6 9.8 700 541.705 62.9646 919883.6 3.6 9.9 1

715 541.715 62.9654 919880.0 3.5 10.0 l

730 541.727 62.9668 919878.9 1.1 9.9 l

745 541.729 62.9680 919892.8

-13.9 8.9 800 541.744 62.9691 919883.8 9.1 9.3 815 541.749 62.9704 919894.6

-10.8 8.6 l

830 541.753 62.9716 919904.9

-10.3 7.9 845 541.762 62.9724 919901.7 3.2 8.0 900 541.775 62.9732 919891.7 10.0 8.4 915 541.778 62.9734 919888.8 2.9 8.5 930 541.790 62.9733 919866.8 21.9 9.5 945 541.793 62.9742 919874.6

-7.8 9.0 1000 541.796 62.9744 919872.4 2.3 9.0 l

1015 541.805 62.9752 919869.6 2.8 9.0 1030 541.809 62.9753 919863.1 6.5 9.2 1045 541.816 62.9761 919864.2

-1.1 9.0 1100 541.819 62.9762 919860.9 3.2 9.1 1115 541.828 62.9771 919858.1 2.8 9.1 1130 541.831 62.9779 919863.7

-5.6 8.7 1145 541.840 62.9791 919866.5

-2.8 8.5 l

1200 541.841 62.9793 919867.4

.8 8.4 1215 541.848 62.9793 919856.6 10.8 8.8 l-1230 541.852 62.9799 919857.7

-1.2 8.6 1245 541.858 62.9802 919852.3 5.5 8.8 1300 541.859 62.9803 919851.0 1.3 8.7 1315 541.865 62.9812 919854.4

-3.4 8.5 l

1330 541.869 62.9821 919862.8

-8.4 8.0 L

1345 541.873 62.9827 919863.5

.8 7.9 1400 541.876 62.9826 919857.6 5.9 8.1 1415 541.880 62.9830 919854.5 3.1 8.1 FREE AIR VOLUME USED (CU. FT.)

=2932051.0 REGRESSION LINE INTERCEPT (LBM)

= 920041.8 SI4PE (LBM/HR)

-8.6

=

MAXIMUM ALI4WABLE LEAKAGE RATE

.100

=

75% OF MAXIMUM ALLOWABLE LEAKAGE RATE

.075

=

THE UPPER 95% CONFIDENCE LIMIT

.023

=

THE CAI4ULATED LEAKAGE RATE

=

.022

4 COMANCHE PEAK - UNIT 1 ILRT JULY 1989 TREND REPORT TIME AND DATE AT START OF TEST: 1415 706 1989 NO.

END TOTAL TIME ANALYSIS MASS POINT ANALYSIS PTS TIME MEAS. CALCULATED UCL CALCULATED UCL 2

1430

.047

.047 99.000

.047 99.000 3

1445

.047

.047 99.000

.047

.049 4

1500

.033

.035

.089

.034

.056 5

1515

'.004

.006

.070

.002

.047 6

1530

.003

.002

.043

.003

.024 7

1545

.012

.001

.046

.002

.021 8

1600

.018

.002

.051

.008

.023 9

1615

.018

.005

.051

.011

.024 10 1630

.024

.009

.055

.017

.027 11 1645

.010

.007

.048

.013

.023

[

12 1700

.016

.008

.046

.014

.021 13 1715

.018

.009

.046

.015

.022 14 1730

.026

.012

.049

.019

.026 15 1745

.026

.015

.050

.021

'028 16 1800

.030

.018

.052

.025

.031 17 1815

.019

.018

.051

.023

.029 18 1830

.027

.019

.051

.025

.031 19 1845

.025

.020

.051

.026

.030 20 1900

.029

.022

.052

.027

.032 21 1915

.028

.023

.052

.028

.032 22 1930

.029

.024

.052

.029

.033 23 1945

.031

.025

.053

.030

.034 24 2000

.027

.026

.052

.030

.033 25 2015

.022

.025

.051

.029

.032 26 2030

.028

.026

.051

.029

.032 27 2045

.027

.026

.051

.029

.032 28 2100

.027

.026

.051

.029

.032 29 2115

.027

.027

.050

.029

.032 30 2130

.027

.027

.050

.029

.032 31 2145

.026

.027

.050

.029

.031 32 2200

.026

.027

.049

.029

.031 33 2215

.027

.027

.049

.029

.031 34 2230

.030

.028

.049

.029

.031 35 2245

.026

.028

.048

.029

.031 36 2300

.026

.028

.048

.029

.030 37 2315

.028

.028

.048

.029

.030 38 2330

.027

.028

.048

.029

.030 39 2345

.028

.028

.048

.029

.030 40 0

.026

.028

.047

.029

.030 41 15

.025

.028

.047

.028

.030 42 30

.023

.028

.046

.028

.029 43 45

.025

.027

.046

.028

.029 44 100

.025

.027

.046

.027

.029 45 115

.026

.027

.045

.027

.029 46 130

.025

.027

.045

.027

.028 47 145

.025

.027

.045

.027

.028 48 200

.026

.027

.045

.027

.028 49 215

.028

.027

.045

.027

.028 50 230

.027

.027

.044

.027

.028

L i

l COMANCHE PEAK - UNIT 1 ILRT JULY 1989 l'

TREND REPORT TIME AND DATE AT START OF TEST: 1415 706 1989 NO.

END TOTAL TIME ANALYSIS MASS POINT ANALYSIS l

PTS TIME MEAS. CALCULATED UCL CALCULATED UCL J

51 245

.025

.027

.044

.027

.028 52 300

.026

.027

.044

.027

.028 53 315

.026

.027

.044

.027

.028 54 330

.024

.027

.043

.027

.028 55 345

.024

.027

.043

.027

.027 56 400

.025

.027

.043

.026

.027 4

57 415

.023

.027

.043

.026

.027 58 430

.025

.027

.042

.026

.027 59 445

.024

.027

.042

.026

.027 60 500

.025

.026

.042

.026

.027 61 515

.026

.026

.042

.026

.027 62 530

.025

.026

.042

.026

.027 63 545

.027

.027

.042

.026

.027 64 600

.025

.027

.041

.026

.027 65 615

.025

.026

.041

.026

.027 66' 630

.026

.026

.041

.026

.027 67 645

.026

.026

.041

.026

.026 l

68 700

.026

.026

.041

.026

.026 69 715

.026

.026

.041

.026

.026 l

70 730

.026

.026

.041

.026

.026 71 745

.023

.026

.040

.026

.026 i

72 800

.024

.026

.040

.026

.026 i

73 815

.022

.026

.040

.025

.026 74 830

.021

.026

.040

.025

.026 75 845

.021

.026

.039

.025

.025 76 900

.022

.025

.039

.024

.025 77 915

.022

.025

.039

.024

.025 78 930

.025

.025

.039

.024

.025 79 945

.023

.025

.039

.024

.025 80 1000

.023

.025

.038

.024

.025 81 1015

.023

.025

.038

.024

.025 E

82 1030

.024

.025

.038

.024

.025 83 1045

.024

.025

.038

.024

.025 84 1100

.024

.025

.038

.024

.025 85 1115

.024

.025

.038

.024

.024 86 1130

.023

.025

.038

.024

.024 87 1145

.022

.025

.037

.024

.024 L

88 1200

.022

.024

.037

.023

.024 L

89 1215

.023

.024

.037

.023

.024 90 1230

.022

.024

.037

.023

.024 91 1245

.023

.024

.037

.023

.024 92 1300

.023

.024

.037

.023

.024 l

93 1315

.022

.024

.036

.023

.024 94 1330

.021

.024

.036

.023

.023 l

95 1345

.021

.024

.036

.023

.023 L

96 1400

.021

.024

.036

.023

.023 L

97 1415

.021

.024

.026

.022

.023 i

1 r

g I

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 LEAKAGE RATE (WEIGHT PERCENT / DAY)

TOTAL TIME ANALYSIS TIME AND DATE AT START OF TEST 1415 706 1989 TEST DURATION: 24.00 HOURS TIME TEMP PRESSURE MEASURED l

(R)

(PSIA)

LEAKAGE RATE 1415 541.254 62.9235 1430 541.257 62.9235

.047 1445 541.260 62.9236

.047 1500 541.263 62.9238

.033 1515 541.262 62.9245

.004 1530 541.269 62.9251

.003 e

1545 541.270 62.9249

.012 1600 541.273 62.9249

.018 1615 541.276 62.9251

.018 1630 541.284 62.9256

.024 L

1645 541.282 62.9261

.010 1700 541.285 62.9259

.016 1715 541.284 62.9256

.018 1730 541.289 62.9253

.026 i

1745 541.293 62.9257

.026 1800 541.298 62.9257

.030 1815 541.300 62.9268-

.019 1830 541.308 62.9267

.027 L

1845 541.310 62.9271

.025 1900 541.319 62.9274

.029 1915 541.322 62.9278

.028 1930 541.327 62.9280

.029 1945 541.331 62.9281

.031 2000 541.337 62.9290

.027 2015 541.336 62.9295

.022 L

2030 541.345 62.9295

.028 l

2045 541.351 62.9302

.027 l

2100 541.357 62.9306

.027 2115 541.362 62.9311

.027 2130 541.368 62.9315

.027 2145 541.371 62.9321

.026 2200 541.382 62.9331

.026 2215 541.389 62.9336

.027 2230 541.397 62.9337

.030 2245 541.399 62.9346

.026 2300 541.408 62.9354

.026 2315 541.419 62.9360

.028 2330 541.425 62.9367

.027 2345 541.430 62.9370

.028 0

541.437 62.9380

.026 15 541.444 62.9391

.025 30 541.452 62.9403

.023 45 541.464 62.9410

.025 100 541.474 62.9420

.025 115 541.482 62.9424

.026 130 541.487 62.9432

.025 145 541.501 62.9446

.025

'f, a

,,, _ _,~--,..,, - - -.,, - - _

,_.,-,,m_-

..-.,,,,,,,,,........-v,-,,,,,--se

,.-.-s,-.

l i

s CONANCHE ~ PEAK - UNIT 1 ILRT JULY 1989 LEAKA2E RATE (WEICHT PERCENT / DAY) 1

-TOTAL TIME ANALYSIS TIME AND DATE AT START OF TEST 1415 706 1989 TEST DURATION: 24.00 HOURS TIME TEMP PRESSURE MEASURED (R)

(PSIA)

LEAKAGE RATE 200 541.509 62.9450

.026 215 541.524 62.9459

.028 230 541.531 62.9469

.027 L

245 541.538 62.9483

.025 300 541.550 62.9492

.026 315 541.562 62.9505

.026 330 541.570 62.9519

.024 345 541.579 62.9526

.024 400 541.591 62.9537

.025 3

415 541.598 62.9551

.023

(

430 541.607 62.9553

.025 445 541.614 62.9563

.024 500 541.630 62.9575

.025 515 541.644 62.9587

.026 530 541.651 62.9594

.025 545 541.661 62.9597

.027 600 541.671 62.9616

.025 615 541.676 62.9621

.025 630 541.691 62.9633

.026 645 541.695 62.9636

.026 l

700 541.705 62.9646

.026 715 541.715 62.9654

.026 730 541.727 62.9668

.026 745 541.729 62.9680

.023 1

800 541.744 62.9691

.024 i

l 815 541.749 62.9704

.022 l

830 541.753 62.9716

.021 1

845 541.762 62.9724

.021 900 541.775 62.9732

.022 915 541.778 62.9734

.022 930 541.790 62.9733

.025 l

945 541.793 62.9742

.023 L

1000 541.796 62.9744

.023 i

1015 541.805 62.9752

.023 l

1030 541.809 62.9753

.024 1045 541.816 62.9761

.024 1100 541.819 62.9762

.024 1115 541.828 62.9771

.024 1130 541.831 62.9779

.023 1145 541.840 62.9791

.022 1200 541.841 62.9793

.022 1215 541.848 62.9793

.023 l

1230 541.852 62.9799

.021 1245 541.858 62.9802

.023 1300 541.859 62.9803

.023 1315 541.865 62.9812

.022 1330 541.869 62.9821

.021 1345 541.873 62.9827

.021 1400 541.876 62.9826

.021 1415 541.880 62.9830

.021 i.

MEAN OF THE MEASURED LEAKAGE RATES

.024

=

MAXIMUM ALI4WABLE LEAKAGE RATE

.100

=

75% OF MAXIMUM ALLOWABLE LEAKAGE RATE

.075

=

THE UPPER 954 CONFIDENCE LIMIT

=

.026 THE CALCULATED LEAKAGE RATE

.024

=

e r

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 LEAKAGE RATE (WEIGHT PERCENT / DAY)

MASS POINT ANALYSIS TIME AND DATE AT START OF TEST: 1530 707 1989 TEST DURATION:

4.00 HOURS TIME TEMP PRESSURE CTMT. AIR MASS LOSS AVERAGE MASS (R)

(PSIA)

MASS (LBM)

(LBM)

LOSS (LBM/HR) 1530 541.898 62.9816 919805.8 1545 541.895 62.9816 919S10.5

-4.8

-19.1 1600 541.894 62.9504 919794.2 16.4 23.2 1615 541.895 62.9807 919796.3

-2.1 12.7 1630 541.901-62.9796 919771.7 24.6 34.1 1645 541.904 62.9792 919760.0 11.7 36.6 1700 541.902 62.9787 919755.3 4.8 33.7 1715 541.907 62.9787 919746.5 8.7 33.8 1730 541.911 62.9778 919727.2 19.4 39.3 1745 541.917 62.9781 919722.2 5.0 37.1 1800 541.915 62.9769 919707.8 14.5 39.2 1815 541.917 62.9770 919705.7 2.1 36.4 1830 541.918 62.9752 919678.4 27.3 42.5 1845 541.922 62.9751 919668.3 10.1 42.3 1900 541.925 62.9750 919662.4 5.9 41.0 1915 541.930 62.9745 919647.0 15.4 42.3 1930 541.927 62.9744 919649.8

-2.7 39.0 FREE AIR VOLUME USED (CU. FT.)

=2932051.0 RECRESSION LINE INTERCEPT (LBM)

= 919817.9

-43.9 l

SLOPE (LBM/MR)

=

l VERIFICATION TEST LEAKAGE RATE UPPER LIMIT =

.152 l -

VERIFICATION TEST LEAKAGE RATE LOWER LIMIT =

.102

(

THE CALCULATED LEAKAGE RATE

.115

=

l

I l

l i

' COMANCHE PEAK - UNIT 1 ILRT JULY 1989 LEAKAGE RATE (WEIGHT PERCENT / DAY)

TOTAL TIME ANALYSIS TIME AND DATE AT START OF TEST: 1530 707 1989 TEST DURATION:

4.00 HOURS TIME TEMP PRESSURE MEASURED (R)

(PSIA)

LEAKAGE RATE 1530 541.898 62.9816 1545 541.895 62.9816

.050 1600 541.894 62.9804

.061 1615 541.895 62.9807

.033 1

1630 541.901 62.9796

.089 1645 541.904

- 62.9792

.095 J

1700 541.902 62.9787

.088 1715 541.907-62.9787

.088 1730 541.911 62.9778

.103 1745 541.917 62.9781

.097 1800 541.915 62.9769

.102 t

1815 541.917 62.9770

.095 1830 541.918 62.9752

.111 1845 541.922 62.9751

.110 1900 541.925 62.9750

.107 1915 541.930 62.9745

.110 1930 541.927 62.9744

.102

=

084 MEAN OF THE MEASURED LEAKAGE RATES VERIFICATION TEST LEAKAGE RATE UPPER LIMIT =

154 VERIFICATION TEST LEAKAGE RATE LOWER LIMIT =

104 129 THE CALCULATED LEAKAGE RATE

=

f r

l T

E w

-+---yv---w, t

e-y y*w--1w-wg-

--wy,-yw<-+-g---v--

w y-v w----e-

' n-g

,~ i t

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 TREND REPORT TIME AND DATE AT START OF TEST: 1530 707 1989

\\

NO.

END TOTAL TIME ANALYSIS MASS POINT ANALYSIS PTS TIME MEAS. CALCULATED UCL CALCULATED UCL 2

1545

.050

.050 99.000

.050 99.000 3

1600

.061

.061 99.000

.061

.605 4

1615

.033

.056

.601

.047

.134 5

1630

.089

.091

.292

.086

.153 6

1645

.095

.109

.245

.102

.147 7

1700

.088

.113

.233

.102

.132 8

1715

.088

.115

.224

.102

.123 9

1730

.103

.121

.219

.108

.125 10 1745

.097

.122

.215

.108

.122 11 1800 102

.124

.212

.110

.121 12 1815

.095

.123

.208

.108

.117 13 1830

.111

.126

.207

.112

.122 14 1845

.110

.129

.206

.115

.123 15 ~1900

.107

.129

.204

.115

.122 16 1915

.110

.130

.203

.117

.123 17 1930

.102

.129

.201

.115

.120 i

l l

1 i

i COMANCHE PEAK - UNIT 1 ILRT JULY 1989

SUMMARY

DATA I

.100 VOLUME =

2932051.

j ALMAX

=

VRATET =

.000 VRATEM =.000 TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 1500 704 542.693 63.1868

.4412 2932051.0 921448.7 1

1515 704 542.306 63.1575

.4393 2932051.0 921680.3 i-1530 704 542.055 63.1243

.4383 2932051.0 921622.2 J

1545 704 541.868 63.0922

.4386 2932051.0 921470.8 1600 704 541.723 63.0785

.4374 2932051.0 921516.9 1615 704 541.604 63.0594'

.4401 2932051.0 921440.6 1630 704 541.495 63.0476

.4385 2932051.0 921455.5 1645 704 541.411 63.0412

.4335 2932051.0 921503.1 1700 704 541.343 63.0363

.4286 2932051.0 921546.4 1715 704 541.288 63.0211

.4333 2932051.0 921418.8 1730 704 541.231 63.0187

.4297 2932051.0 921482.1 1745 704 541.179 63.0095

.4321 2932051.0 921434.3 1800 704 541.134 63.0051

.4275 2932051.0 921447.3 t

1815 704 541.105 63.0033

.4264 2932051.0 921470.1 1930 704 541.068 62.9979

.4263 2932051.0 921454.1 1845 704 541.042 62.9920

.4268 2932051.0 921411.8 1900 704 541.017 62.9884

.4264 2932051.0 921402.3

[

1915 704 540.986 62.9828

.4271 2932051.0 921371.9 l

1930 704 540.952 62.9781

.4278 2932051.0 921362.4 1945 704 540.925 62.9743

.4276 2932051.0 921352.9 2000 704 540.914 62.9711

.4278 2932051.0 921324.5 2015 704 540.902 62.9682

.4282 2932051.0 921302.2 i

2030 704 540.879 62.9650

.4289 2932051.0 921295.5 2045 704 540.864 62.9628

.4282 2932051.0 921287.3 2100 704 540.848 62.9584

.4281 2932051.0 921252.0 2115 704 540.829 62.9574

.4282 2932051.0 921267.9 l

2130 704 540.813 62.9543

.4283 2932051.0 921249.6 2145 704 540.800 62.9517

.4284 2932051.0 921234.1 2200 704 540.791 62.9493

.4283 2932051.0 921216.3 2215 704 540.780 62.9472

.4284 2932051.0 921203.3 2230 704 540.762 62.9449

.4287 2932051.0 921199.6 2245 704 540.752 62.9427

.4290 2932051.0 921184.9 2300 704 540.748 62.9402

.4295 2932051.0 921153.9 2315 704 540.742 62.9385

.4296 2932051.0 921140.4 2330 704 540.736 62.9370

.4297 2932051.0 921128.4 2345 704 540.729 62.9356

.4301 2932051.0 921120.6 0

705 540.725 62.9338

.4294 2932051.0 921101.9 15 705 540.727 62.9330

.4297 2932051.0 921086.8 30 705 540.721 62.9311

.4301 2932051.0 921069.1 45 705 540.719 62.9295

.4302 2932051.0 921047.9 100 705 540.714 62.9289

.4299 2932051.0 921047.7 115 705 540.713 62.9279

.4299 2932051.0 921035.1 130 705 540.714 62.9269

.4299 2932051.0 921018.3 145 705 540.717 62.9258

.4300 2932051.0 920997.3 l

200 705 540.714 62.9244

.4303 2932051.0 920983.1 L

215 705 540.717 62.9235

.4303 2932051.0 920963.5 l

230 705 540.716 62.9225

.4308 2932051.0 920949.8 245 705 540.716 62.9212

.4312 2932051.0 920931.9

t o

COMANCHE PEAK - UNIT 1 ILRT JULY 1989

SUMMARY

DATA ALMAX

=

.100 VOLUME =

2932051.

VRATET =

.000 VRATEM =.000 TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 300 705 540.721 62.9204

.4315 2932051.0 920911.3 315 705 540.722 62.9199

.4314 2932051.0 920902.9 330 705 540.720 62.9188

.4315 2932051.0 920890.8 345 705 540.721 62.9189

.4310 2932051.0 920888.7 400 705 540.724 62.9185

.4308 2932051.0 920878.6 1

415 705 540.729 62.9173

.4315 2932051.0 920852.1 i

430 705 540.730 62.9170

.4304 2932051.0 920846.1 445 705 540.732 62.9165

.4308 2932051.0 920836.1 500 705 540.731 62.9154

.4309 2932051.0 920820.8 515 705 540.731 62.9154

.4315 2932051.0 920820.6 530 705 540.736 62.9150

.4314 2932051.0 920805.4 545 705 540 733 62.9148

.4316 2932051.0 920808.8 l

600 705 540.739 62.9144

.4315 2932051.0 920792.1 615 705 540.734 62.9133

.4316 2932051.0 920785.6 630 705 540.735 62.9123

.4321 2932051.0 920767.7 645 705 540.735 62.9125

.4319 2932051.0 920770.6 700 705 540.744 62.9118

.4321 2932051.0 920747.1 i

715 705 540.737 62.9121

.4318 2932051.0 920761.9 730 705 540.737 62.9110

.4324 2932051.0 920746.3 745 705 540.742 62.9100

.4329 2932051.0 920723.6 800 705 540.744 62.9092

.4328 2932051.0 920707.7 l

815 705 540.748 62.9085

.4329 2932051.0 920690.8 830 705 540.745 62.9086

.4329 2932051.0 920696.9 L

845 705 540.749 62.9077

.4332 2932051.0 920677.4 900 705 540.753 62.9074

.4336 2932051.0 920666.8 j

915 705 540.754 62.9071

.4339 2932051.0 920660.3 l

L 930 705 540.754 62.9070

.4334 2932051.0 920659.5 945 705 540.758 62.9069

.4330 2932051.0 920649.9 1000 705 540.758 62.9060

.4339 2932051.0 920639.1 1015 705 540.758 62.9061

.4333 2932051.0 920639.6 1030 705 540.761 62.9056

.4334 2932051.0 920625.5 1045 705 540.772 62.9050

.4335 2932051.0 920599.3 1100 705 540.770 62.9052

.4333 2932051.0 920605.6 1115 705 540.768 62.9044

.4335 2932051.0 920597.4 1130 705 540.773 62.9043

.4337 2932051.0 920586.5 1145 705 540.772 62.9036

.4339 2932051.0 920577.4 1200 705 540.769 62.9030

.4340 2932051.0 920575.3 1215 705 540.775 62.9026

.4343 2932051.0 920559.3 1230 705 540.777 62.9020

.4345 2932051.0 920545.9 1245 705 540.776 62.9017

.4343 2932051.0 920542.9 l

1300 705 540.780 62.9018

.4342 2932051.0 920539.3 1315 705 540.784 62.9017

.4342 2932051.0 920530.4 1330 705 540.786 62.9005

.4345 2932051.0 920510.0 1345 705 540.784 62.9007

.4342 2932051.0 920516.8 1400 705 540.781 62.8996

.4344 2932051.0 920504.3 1415 705 540.783 62.8995

.4345 2932051.0 920499.9 1430 705 540.779 62.8980

.4346 2932051.0 920497.9 1445 705 540.773 62.8983

.4347 2932051.0 920500.1 o

~ _ _

l l

i COMANCHE PEAK - UNIT 1 ILRT JULY 1989

SUMMARY

DATA

=

.100 VOLUME =

2932051.

j ALMAX VRATET =

.000 VRATEM =.000 i

' TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS I

1500 705 540.768 62.8978

.4352 2932051.0 920499.4 1515 705 540.772 62.8968

.4352 2932051.0 920479.4 1530 705 540.770 62.8967

.4353 2932051.0 920481.1 1545 705 540.770 62.8963

.4352 2932051.0 920474.9 1600 705 540.773 62.8952

.4353 2932051.0 920454.0 1615 705 540.772 62.8950

.4355 2932051.0 920452.9 i

1630 705 540.776 62.8947

.4353 2932051.0 920441.7

'1645 705 540.771 62.8949

.4351 2932051.0 920452.7

?

1700 705 540.768 62.8941

.4355 2932051.0 920445.5 j

1715 705 540.778 62.8937

.4358 2932051.0 920423.1 1730 705 540.781 62.8928

.4357 2932051.0 920405.8 1745 705 540,779 62.8931

.4355 2932051.0 920412.5 1800 705 540.782 62.8919

.4356 2932051.0 920391.2 l

1815 705 540.778 62.8919

.4356 2932051.0 920397.8 1830 705 540.780 62.8917

.4358 2932051.0 920391.0 1845 705 540.783 62.8916

.4360 2932051.0 920383.8 L

1900 705 540.787 62.8915

.4360 7932051.0 920375.9 l

1915 705 540.793 62.8906

.4360 2932051.0 920352.8 1930 705 540.793 62.8905

.4361 2932051.0 920351.3 l

1945 705 540.797 62.8904

.4361 2932051.0 920343.1 2000 705 540.796 62.8905

.4361 2932051.0 920344.9 l

2015 705 540.801 62.8902

.4364 2932051.0 920333.3 e

l 2030 705 540.806 62.8900

.4366 2932051.0 920321.8 2045 705 540.807 62.8897

.4369 2932051.0 920314.4 2100 705 540.809 62.8899

.4366 2932051.0 920314.9 2115 705 540.814 62.8897

.4369 2932051.0 920303.7 2130 705 540.818 62.8903

.4367 2932051.0 920305.6 e

2145 705 540.823 62.8901

.4369 2932051.0 920294.8 2200 705 540.831 62.8911

.4365 2932051.0 920295.0 2215 705 540.833 62.8909

.4366 2932051.0 920290.0 2230 705 540.837 62.8906

.4370 2932051.0 920277.9 2245 705 540.841 62.8904

.4371 2932051.0 920268.9 2300 705 540.843 62.8907

.4368 2932051.0 920270.0 l

2315 705 540.852 62.8910

.4370 2932051.0 920258.9 2330 705 540.855 62.8920

.4365 2932051.0 920266.9 t

2345 705 540.863 62.8923

.4367 2932051.0 920259.0 0

706 540.867 62.8937

.4374 2932051.0 920256.3 i

15 706 540.875 62.8936

.4369 2932051.0 920257.2 l

30 706 540.879 62.8932

.4374 2932051.0 920242.9 45 706 540.888 62.8935

.4370 2932051.0 920233.9 100 706 540.892 62.8954

.4366 2932051.0 920255.1 115 706 540.899 62.8960

.4365 2932051.0 920250.6 130 706 540.910 62.8961

.4368 29320b1.0 920234.0 145 706 540.918 62.8964

.4371 2932051.0 920223.8 200 706 540.928 62.8971

.4369 2932051.0 920217.9 215 706 540.936 62.8980

.4370 2932051.0 920217.8 230 706 540.946 62.8990

.4370 2932051.0 920215.3 245 706 540.956 62.8997

.4368 2932051.0 920208.4

COMANCHE PEAK - UNIT 1 ILRT JULY 1989 l

SUMMARY

DATA ALMAX

.100 VOLUME =

2932051.

=

VRATET =

.126 VRATEM =.124 r

TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 300 706 540.963 62.9003

.4371 2932051.0 920205.6 315 706 540.968 62.9010

.4369 2932051.0 920207.4 330 706 540.974 62.9012

.4372 2932051.0 920200.2 345 706 540.982 62.9024

.4371 2932051.0 920203.6 400 706 540.990 62.9030

.4369 2932051.0 920198.3 415 706 541.005 62.9034

.4370 2932051.0 920179.3 430 706 541.006 62.9042

.4372 2932051.0 920189.4 445 706 541.019 62.9058

.4371 2932051.0 920190.7 500 706 541.027 62.9062

.4372 2932051.0 920182.6 515 706 541.036 62.9072

.4372 2932051.0 920182.5 530 706 541.045 62.9074

.4370 2932051.0 920169.6 545 706 541.050 62.9085

.4369 2932051.0 920176.8 600 706 541.059 62.9094

.4370 2932051.0 920175.2 615 706 541.068 62.9099

.4374 2932051.0 920167.7' 630 706 541.076 62.9110

.4373 2932051.0 920169.5 645 706 541.085 62.9108

.4380 2932051.0 920152.1 700 706 541.091 62.9121

.4377 2932051.0 920160.3 715 706 541.100 62,9124

.4379 2932051.0 920149.8 730 706

.541.105 62.9127

.4376 2932051.0 920145.1 I

745 706 541.110 62.9140

.4373 2932051.0 920155.1 800 706 541.119 62.9143

.4376 2932051.0 920144.9 815 706 541.128 62.9149

.4374 3932051.0 920139.1 830 706 541.131 62.9148

.4381 2932051.0 920131.4 845 706 541.141 52.9155

.4378 2932051.0 920126.0 900 706 541.145 62.9160

.4378 2932051.0 920125.4 915 706 541.152 62.9160

.4383 2932051.0 920113,5 i

930 706 541.162 62.9154

.4384 2932051.0 920087.7

(

945 706 541.168 62.9173

.4380 2932051.0 920106.3 1000 706 541.173 62.9175

.4383 2932051.0 920099.8 i

1015 706 541.179 62.9185

.4383 2932051.0 920103.3 l

1030 706 541.187 62.9187

.4386 2932051.0 920093.4 1045 706 541.189 62.9191

.4382 2932051.0 920095.8 1100 706 541.197 62.9192

.4381 2932051.0 920083.8 1115 706 541.200 62.9200

.4383 2932051.0 920090.8 i

l' 1130 706 541.207 62.9207

.4386 2932051.0 920089.1 1145 706 541.212 62.9202

.4390 2932051.0 920073.9 1200 706 541.216 62.9205

.4388 2932051.0 920070.9 1215 706 541.221 62.9205

.4387 2932051.0 920063.5 1230 706 541.227 62.9216

.4386 2932051.0 920067.7 l

1245 706 541.230 62.9225

.4387 2932051.0 920076.1 1300 706 541.242 62.9228

.4384 2932051.0 920060.4 u

1315 706 541.240 62.9232

.4381 2932051.0 920068.3 1330 706 541.242 62.9236

.4381 2932051.0 920072.8 1

1345 706 541.242 62.9240

.4382 2932051.0 920077.9 i

1400 706 541.250 62.9235

.4387 2932051.0 920056.3 l

1415 7C6 541.254 62.9235

.4388 2932051.0 920049.4 l.

L

e COMANCHE PEAK - UNIT 1 ILRT JULY 1989

SUMMARY

DATA

=

.100 VOLUME =

2932051.

5 ALMAX VRATET =

.126 VRATEM =.124 TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 1415 706 541.254 62.9235

.4388 1932051.0 920049.4 1430 706 541.257 62.9235

.4387 2932051.0 920044.9 i

1445 706 541.260 62.9236

.4386 2932051.0 920040.4 1500 706 541.263 62.9238

.4384 2932051.0 920039.9 1515 706 541.262 62.9245

.4382 2932051.0 920050.8 1530 706 541.269 62.9251

.4381 2932051.0 920047.8 1545 706 541.270 62.9249

.4383 2932051.0 920042.4 1600 706 541.273 62.9249

.4384 2932051.0 920037.5 1615 706 541.276 62.9251

.4381 2932051.0 920035.4 1630 706 541.284 62.9256

.4381 2932051.0 920028.8 1645 706 541.282 62.9261

.4382 2932051.0 920039.8 t

1700 706 541.285 62.9259

.4383 2932051.0 920033.0 L

1715 706 541.284 62.9256

.4387 2932051.0 920028.4 1730 706 541.289 62.9253

.4389 2932051.0 920017.1 1745 706 541.293 62.9257

.4385 2932051.0 920015.0 1800 706 541.298 62.9257

.4386 2932051.0 920006.6 l

1815 706 541.300 62.9268

.4384 2932051.0 920019.8 l

1830 706 541.30S 62.9267

.4385 2932051.0 920004.6 1845 706 541.310 62.9271

.4381 2932051.0 920007.1 1900 706 541.319 62.9274

.4384 2932051.0 919995.7 1915 706 541.322 62.9278

.4384 2932051.0 919996.5 g

1930 706 541.327 62.9280

.4387 2932051.0 919990.4 1945 706 541.331 62.9281

.4386 2932051.0 919984.8 2000 706 541.337 62.9290

.4387 2932051.0 919989.9 2015 706 541.336 62.9295

.4387 2932051.0 919997.8 2030 706 541.345 62.9295

.4387 2932051.0 919982.4 2045 706 541.351 62.9302

.4385 2932051.0 919982.8 2100 706 541.357 62.9306

.4386 2932051.0 919978.6 2115 706 541.362 62.9311

.4385 2932051.0 919977.0 2130 706 541.368 62.9315

.4387 2932051.0 019973.5 2145 706 541.371 62.9321

.4386 2932051.0 919975.8 2200 706 541.382 62.9331

.4385 2932051.0 919972.5 2215 706 541.389 62.9336

.4386 2932051.0 919966.6 2230 706 541.397 62.9337

.4384 2932051.0 919955.9 2245 706 541.399 62.9346

.4385 2932051.0 919966.0 2300 706 541.408 62.9354

.4387 2932051.0 919962.9 2315 706 541.419 62.9360

.4391 2932051.0 919952.1 2330 706 541.425 62.9367

.4389 2932051.0 919952.1 2345 706 541.430 62.9370

.4391 2932051.0 919948.1 0

707 541.437 62.9380

.4391 2932051.0 919951.4 i

15 707 541.444 62.9391

.4390 2932051.0 919955.1 30 707 541.452 62.9403

.4388 2932051.0 919958.1 45 707 541.464 62.9410

.4391 2932051.0 919948.5 100 707 541.474 62.9420

.4391 2932051.0 919947.1 115 707 541.482 62.9424

.4392 2932051.0 919939.0 130 707 541.487 62.9432

.4394 2932051.0 919941.9 145 707 541.501 62.9446

.4394 2932051.0 919939.2 200 707 541.509 62.9450

.4396 2932051.0 919930.3

. =-

l COMANCHE PEAX - UNIT 1 ILRT JULY 1989

SUMMARY

DATA ALMAX

.100 VOLUME =

2932051.

=

VRATET =

.126 VRATEM =.124 TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 215 707 541.524 62.9459

.4396 2932051.0 919919.3 1

230 707 541.531 62.9469

.4396 2932051.0 919921.4 245 707 541.538 62.9483

.4398 2932051.0 919928.7 300 707 541.550 62.949?

.4398 2932051.0 919922.5 315 707 541.562 62.9505

.4395 2932051.0 919920.5 330 707 541.570 62.9519

.4396 2932051.0 919928.1 345 707 541.579 62.9526

.4394 2932051.0 919923.0 l'

400 707 541.591 62.9537

.4392 2932051.0 919918.1 415 707 541.598 62.9551

.4389 2932051.0 919926.9 430 707 541.607 62.9553

.4397 2932051.0 919913.7 445 707 541.614 62.9563

.4397 2932051.0 919917.8 500 707 541.630 62.9575

.4394 2932051.0 919907.4 515 707 541.644 62.9587

.4392 2932031.0 919902.0 530 707 541.651 62.9594

.4395 2932051.0 919900.6 545 707 541.661 62.9597

.4397 2932051.0 919887.0 s

600 707 541.671 62.9616

. 4393 2932051.0 919898.3 615 707 541.676 62.9621

.4393 2932051.0 919896.8 l

630 707 541.691 62.9633

.4396 2932051.0 919888.8 645 707 541.695 62.9636

.4397 2932051.0 919887.1 700 707 541.705 62.9646

.4398 2932051.0 919883.6 715 707 541.715 62.9654

.4399 2932051.0 919880.0 730 707 541.727 62.9668

.4395 2932051.0 919878.9 745 707 541.729 62.9680

.4394 2932051.0 919892.8 600 707 541.744 62.9691

.4392 2932051.0 919883.8 0%5 707 541.749 62.9704

.4389 2932051.0 919894.6 830 707 541.753 62.9716

.4387 2932051.0 919904.9 845 707 541.762 62.9724

.4389 2932051.0 919901.7 000 707 541.775 62.9732

.4391 2932051.0 919891.7 9: 5 707 541.778 62.9734

.4394 2932051.0 919888.8 930 707 541.790 62.9733

.4400 2932051.0 919866.8 94b 707 541.793 62.9742

.4396 2S32051.0 919874.6 1000 707 541.796 62.9744

.4399 2922051.0 919872.4 1015 7L7 541.805 62.9752

.4401 2932051.0 919869.6 1030 707 541.809 62.9753

.4400 2932051.0 919863.1 1045 707 541.816 62.9761

.4402 2932051.0 919864.2 1100 707 541.819 62.9762

.4400 2932051.0 919860.9 1115 707 541.828 62.9771

.4402 2932052.0 919858.1 1130 707 541.831 62.9779

.4404 2932051,0 919863.7 1145 707 E41.840 62.9791

.4402 2932051.0 919866.5 1200 707 541.841 62.9793

.4400 2932051.0 919867.4 1215 707 541.848 62.9793

.4400 2932051.0 919856.6 1230 707 E41.852 62.9799

.4398 2932051.0 919857.7 1245 707 541.858 62.9802

.4401 2932051.0 919852.3 1300 707 541.059 62.9803

.4400 2932051.0 919851.0 1315 707 541.865 62.9812

.4400 2932051.0 919854.4 1330 707 541.869 62.9821

.4396 2932051.0 919862.8 1345 707 541.073 62.9827

.4396 2932051.0 919663.5 1400 707 541.876 62.9826

.4396 2932051.0 919857.6 1415 707 541.880 62.9830

.4398 2932051.0 919864.5

E 1

i COMANCHE PEAK - UNIT 1 ILRT JULY 1989

)

SUMMARY

DATA i

ALMAX

=

.100 VOLUME =

2932051.

VRATET =

.126 VRATEM =.124

)

TIME DATE TEMP PRESSURE VPRS VOLUME AIRMASS 1430 707 541.885 62.9831

.4401 2932051.0 919849.7 1445 707 541.887 62.9831

.4401 2932051.0 919844.3 1500 707 541.895 62.9831

.4401 2932051.0 919831.6 1515 707 541.897 62.9824

.4403 2932051.0 919818.8 j

1530 707 541.898 62.9816

.4406 2932051.0 919805.8 1545 707 541.895 62.9816

.4406 2932051.0 919810.5 1600 707 541.894 62.9804

.4408 2932051.0 919794.2 i

1615 707 541.895 62.9807

.4406 2932051.0 919796.3 1630 707 541.901 62.9796

.4406 2932051.0 919771.7 1645 707 541.904 62.9792

.4405 2932051.0 919760.0 1700 707 541.902 62.9787

.4406 2932051.0 919755.3 1715 707 541.907 62.9787

.4406 2932051.0 919746.5 1730 707 541.911 62.9778

.4405 2932051.0 919727.2 1745 707 541.917 62.9781

.4401 2932051.0 919722.2 1800 707 541.915 62.9769

.4403 2932051.0 919707.8 1815 707 541.917 62.9770

.4403 2932051.0 919705.7 1830 707 541.918 62.9752

.4405 2932051.0 919678.4 1845 707 541.922 62.9751

.4407 2932051.0 919668.3 1900 707 541.925 62.9750

.4403 2932051.0 919662.4 1915 707 541.930 62.9745

.4403 2932051.0 919647.0 1930 707 541.927 62.9744

.4404 2932051.0 919649.8 t

y-

, 5g, 3,.y t s.

. g. e,..u.3 7,

-. %4 4,

3,..3 sr. g,;.. _.. y;, g g 7,;;pggyf,.y

,y a

4

/

4 APPENDIX 0 ILRT & LLRT TEST SUP#tARIES S

5 e

I

Pcss 1 of 7 cy 4

3 1

TEST

SUMMARY

I FOR EGT-701A, ILEV. 1 CONTAINMENT INTEGRATED LEAKAGE RATE TEST SYSTEM FUNCTIONAL TEST STE: TIM L. ROBBINS 1

1.0 OBJECTIVES ECT-701A " Containment Integrated Leakat.e Rate Test" was performed to quantify leakage through all potential leak paths including containment welds, valves, fittings and components which penetrate containment in C

accordance with 10CFR50, Appendix J.

i l.

for Water Cooled Power Reactors."

" Reactor Containment Leakage Testing l

This surveillance test was approved and performed as a System Functional Test.(SFT), part of the Unit 1 Prestart Test Program, fulfilling require-(

monts of Regulatory Guide 1.68. Rev. 2 Appendix A part i and CPSES Tech-l_

nical' Specification 3/4.6.1.2.

This test fulfills commitments made in L

l FSAR Section 6.2 and Table 14.2 2, sheet 59.

i.

2.0 STATEMENT OF CRITERIA AND RESULTS ACHIEVED The following acceptance criteria applied with test results stated:

criteria 4.1 -

For the "As IAft" condition, the 954 upper confidence limit (UCL) of the measured leakage rate (Im), plus all penalty local leakage rate additions, shall be less than 75% of the maximum allowable leakage rate (La) at a containment pressure of 48.3 (+1.7, -0.0) psig (Pa) where:

I l

1 l

La - 0.1 % of the containment air mass at pressure Pa per 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> 1

(i.e. - the 954 UCL (+ "As 14ft" penalty additions) <.075 t/ day)

The Mass Point Analysis Method of ANSI /ANS 56.8 1987, " Containment System Leakage Testing Requirements" is used to determina the leakage race.

i L

Result -

l The 954 UCL

.023 t/ day + "As Left" penalty additions of.00114/ day

+ water level volume correction of.00086/ day *

.0254/ day at a pressure of 49.002 psig.

  • See "3.0 Performance Summary" for discussion of water level changes.

l l.

l l

l l

i Pogo 2 of 7 4

7, i

i criteria 4.2 -

I The results of the verification test using the superimposed leakage method shall prove that the composite containment leakage rate (Lc) differs from the superimposed leakage rate (Lo) plus the measured containment leakage rate (La) by less than or equal to 0.25 La.

(Lo + La - 0.25 L.) $ Lc $ (Lo + La + 0.25 La)

)

where: 0.75 La 5 Lo $ 1.25L.

Lc - composite containment leakage rate (t/ day) as measured by the contain-ment ambient monitoring system during the verification test.

Result -

Lc was determined to be 0.1154/ day.

Lo was.1054/ day (approximately equal to La)

Lo + La - 0.25 L. - 0.102 Lo + Lu + 0.25 L. - 0.152 Criteria:

Lo + La - 0.25 La 5 Lc 5 Lo + Lu + 0.25 La 0.102 $ 0.115 $ 0.152

^

Criteria:

0.75 $ Lo $ 1.25 Lo 1

0.075 $.105 5 0.125 1

i criteria 4.3 -

l No apparent changes in appearance or other abnormal degradation is observed during inspection of the exposed accessible interior and exterior surfaces of the containment building including the liner plate.

This inspection is performed prior to pressurization and following depressurization.

Result -

Inspections of the exposed accessible interior and exterior surfaces of the containment building were performed prior to pressurization and following depressurization. No deterioration, significant anomalies, nor apparent changes in appearance were found.

..__._,_.,_m._

_~._ _

_. ~. _

Pogo 3 of 7 r

3.0 PERMRMAllCE SUlttARY Performance of testing per ECT 701A commenced July 3, 1989 at 2033 hours0.0235 days <br />0.565 hours <br />0.00336 weeks <br />7.735565e-4 months <br /> by starting pressurisation of containment using 14, 400 SC m of compressor capacity. The pressurisation rate was maintained less than 5.0 psi / hour in accordance with ECT 701A. At 0400 hrs (7/4) pressurization was halted due to a concern on Reactor Coolant Drain Tank (RCDT) level anomalias and tank venting.

TDR 8251 was written and after evaluation it was determined the RCDT level was behaving within expectations.' At 0619 hours0.00716 days <br />0.172 hours <br />0.00102 weeks <br />2.355295e-4 months <br /> pressuriza-tion was resumed. At 1443 hours0.0167 days <br />0.401 hours <br />0.00239 weeks <br />5.490615e-4 months <br /> pressurization was completed after obtain-ing test pressure.

At 1500 hours0.0174 days <br />0.417 hours <br />0.00248 weeks <br />5.7075e-4 months <br /> (7/4) the Temperature Stabilization sequence was entered. At 2145 hours0.0248 days <br />0.596 hours <br />0.00355 weeks <br />8.161725e-4 months <br /> preliminary calculations revealed that leakage was greater than allowable and leakage survey teams were sent out to find possible sources.

Some leakage was found by the teams and the source locations recorded in the test log.

In the process of trouble shooting leak sources, instrument i

air valves 1 HV 3487 and 101-030 (penetration MIII 22) and 48" HVAC contain-sent isolation valve =1 HV 5538 (MV 02) were stroked (see TDR 8252 and 8256).

Since the valves were stroked, these penetrations are included as pensity leakage additions.

Containment Spray Pumps 01 and 03 suction, discharge and eductor isolation manual valves were closed due to leakage through pump seals and casing gaskets (see TDR 7999).

Containment Spray Pumps 02 and 04 suction valves were closed but later reopened prior to the ILRT sequence start. Blind flanges were installed on H2 Purge and Exhaust Valves'1 HV-5540 (MIII-19) and 1 HV 5542 (MIII 18) but later removed prior to ILJtT start. N2 blankets were instituted on 48" Containment Purge and Exhaust penetrations MV 01 and MV 02 but were rencved prior to IIJtT start. At 2220 hours0.0257 days <br />0.617 hours <br />0.00367 weeks <br />8.4471e-4 months <br /> (7/5) a blind flange was installed on 1 HV 5538 (MV-02) and left in l

place throughout the 11JtT.

At 0230 hours0.00266 days <br />0.0639 hours <br />3.80291e-4 weeks <br />8.7515e-5 months <br /> on 7/6 the Temperature Stabilization sequence was declared complete, the IIAT sequence begun, and NRC personnel informed. At 1000 hrs. (7/6) mainsteam vent valves 1MS 382,-385,-388, and.392 were found closed.

Per ECT 701A these valves are allowed to be closed and opened to do leak checking of the steam generators. TDR 8254 was written and after evaluation it was decided to open the valves and restart the IIJtT sequence for conservatise sake.

At 1415 hrs. (7/6) the 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> IIJtT was restarted and NRC notified of the new start time. At 1415 hrs. (7/7) the IIJtT sequence was completed with a final 954 Upper Confidence Limit (UCL) of.0234/ day determined without penalty leakage inclusion.

I

t Pago 4 of 7 d

At 1430 hrs. (7/7), after creating a superimposed leakage of approximately 8.9 SC M, a one hour stabilisation sequence was begun prior to entering the Verification test.

At 1530 hrs. (7/7) the Verification Test was started.

At 1930 hrs. the Verification Test was completed with a final Composite Leakege Le determined to be 115t/ day and average superimposed leakage of 105t/ day (8.96 SCFM).

Following the Verification Test, preparations were made to start depressurising and leakage troubleshooting was performed on i

Containment Spray System Train A (Pumps 01 & 03). At 2200 hrs (7/7) depres-l surisation was begun. Containment was entered with.2 psig pressure remain-ing to prepare for personnel entry and begin restoration activities.

At approximately 2200 hrs. (7/8) depressurisation ended with containment at O psig.

Clearances on systems / components were released, IIJtT instruments removed, containment inspections performed, and other restoration activities continued.

During the restoration process penalty leakages were determined for s

Instrument Air penetration MIII-22 and Containment Purge Exhaust penetra-tion MV-02.

"As Found" L1JtTs were performed, the CIVs stroked, and then "As IAf t" LIJtTs done. Since the "As Found" leakages were within their allowable L1JtT range, no corrective actions were implemented prior to the "As laft".

The penalties ("As IAft" Einimum pathway) with measurement in-accuracy included were 632 SCCN for MIII-22 and 1842 for MV 02, resulting in a total of 2474 SCCN. Combined with the planned penalty leakages of 60.99 SCCN, the total of all penalties if 2534.99 SCCM which translates to.00114/ day.

Also evaluated for impact on the overall leakage rate was water level changes in tank and sumps communicating with Containment atmosphere.

Those that indicated change during the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> I1JtT were as follows:

1 l

Level Chanae Equivalent Cu. Ft.

Containment Sump #2 806' to 806'3" 6

Reactor Coolant Drain Tank 34.9% to 35.9%

0.5 L

i Pressuriser Relief Tank 724 to 734 18.5 Total 25.0 For conservatism sake, since these levels increased during the I!JtT, they are factored into the overall leakage determination. The total of a 25.0 cubic foot level increase over 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> is equivalent to a leakage of

.00084/ day. Therefore, the 954 UCL + "As Left" penalty leakages + water level change correction came to.023t/ day +.00114/ day +.0008t/ day for a total of

.0249t/ day (ie

.0254/ day).

4 i

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1 Pes) 5 of 7 I

l Concerning isolation of Containment Spray System (CT) pumps 01 and 03, following completion of the verification test with containment still at l.

test pressure, pumps 01 and 03 discharge isolation valves were opened. No increase in the pumps pressure was observed. However piping between recir-culation sump valve 1 HV 4782 (penetration MS 3) and pump suction valves was found to be air fi Sed.

When the pump suction valves were opened the i

pump pressure increaset Following completion of depressurization, an "As l

l' Found" 1.1JtT was performed on 1-HV 4782 with the leakage found to be within F

allowable I.IAT range. Then the valve was stroked and an "As left" 1.LJtT i

done.

The "As Found" value was 3040. SCCN and "As 14ft" 953 SCCN.

Since l

the valve was within allowable range no corrective actions were needed. A 4

leakage test of CT Pumps 01 & 03 was performed by pressurizing the pumps to 49 psig.

Pump 01's leakage was determined to be approximately 32,000 SCCM and Pump 03's between 20,000 and 32,000 SCCN.

Evaluating the CT Pump 01 & 03 situation, it was determined recire sump l_

valve 1 HV 4782 was leaking through at 3040 SCCN, allowing air to fill piping displacing water / air through CT Pump 01 & 03 seals and casing gaskets, till the suction piping was predominantly air filled. Concerning l

application of a penalty leakage for the CT Systesi, it was determined to be nonapplicable since the-CT recirc sump (inside Containment) and piping is water filled during and post accident (see FSAR Table 6.2.4-2, item

  1. 127 & Note #9).

Therefore leakage through a possibly inoperable CT Train A would be only of water, not Containment atmosphere.

If Train A was oper.

L ating the water would be recirculating back to Containment.

1 It was found even with penalty leakage inclusion and considering the leak-age isolated through CT Pumps 01 & 03, that the total would not have caused failure of the IIAT.

Further evaluation recommends, for future tests, that manipulations not be performed too early inside the stabilization sequence.

Although the temperature stabilization criteria was met within the first six hours, a large temperature difference between the bottom and top of I

containment remained.

It is felt the test would have passed with no mani-pulations being performed, if a longer stabilization time (i.e. 30 hours3.472222e-4 days <br />0.00833 hours <br />4.960317e-5 weeks <br />1.1415e-5 months <br />),

had been utilized.

Five other TDR's beside those mentioned above and a total of 15 TPC's were l^

generated during the course of the test and its preparation and restoration l

activities. None invalidated the test results nor impacted the test objec-

[

tives.

See page 6 of 7 for individual itemization and status of TPC's and TDR's.

The TPC's will os evaluated for inclusion permanently in ECT 701A and incor-porated either by procedure revision or procedure change notice.

+

+ + -

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j l

l 4.O ATTACMENT8 70 TM SUMARY i

4.1 11AT Report by Bechtel Poaer Corporation j

4.2 Telecopy from Babul Patel (Sechtel) to Tim Robbins (TU Electric)

There were 2 intent change TPC's written, both were implemented prior to starting prerequisite verification steps. TPC 1 provided clarification of acceptance criteria and modified the procedure for use as an Srf in lieu of requirements to be implemented for tech, specs. (i.e., deleted radio.

logical hasards, precautions, and 15 day reporting requirement etc.)

There were 15 non intent TPC's written for changes to test methology, l

calculation type corrections, addition and deletions of valves for test boundary and incorporation of alternate level instrumentation for better i

accuracy.

l There were 8 TDR's written during test performance and two post test TDR's.

of which all are closed.

i TDR.7999 Significant air leakage coming out of containment spray pump.

Upon corrective action completion TSR was closed.

[

TDR.8250. Valve 200 0427 installed at penetration N III.1 in lieu of f

1RC0036.

DR C89 1793 was written as corrective action to I

document no tosporary modification tag being hung on this valve. NCR 89 3722 was written and dispositioned by engineer.

ing to utilira this valve as 1RC0036 replacement.

No fttrther i

testing required. TDR and NCR are closea'.

6 i

TDR 8251. RCDT level indication occilation during pressurisation, upon corrective action completion TDR was closed.

i TDR.8252. Racessive leakage through 1HV 5533 during stabilization period.

Upon Corrective action completion TDR was closed.

TDR 8254. Main Steam Systes Vent valves found out of posit; ion. Upon cor.

rective action completion TDR was closed.

TDR 8255 1CC.1067 relief valve installation verification wao not accom-plished prior to containment pressurization. Upon corrective action completion TDR was closed.

TDR 8256. During temperature stabilisation valve 1C1 041 was found leaking.

Upon corrective action completion TDR was closed.

TDR.8292. Test director changed calculation without TPC approval and terminated data acquisition of Attachment 28. Upon corrective action completion TDR was closed.

_--,,,.--,,,a

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l Pcg3 7 of 7 r

s Tolt.8658. Post Test TDet. Instrumentation restoration signed off without proper verification of action. Upon corrective action comple.

1 rien TDit was closed.

TDIt.9009. Post Test TDR.Documsnt administrative errors made during performance of test. Upon corrective action completion TDR was closed.

R L. %

9-n -ag Startup Test Engineer Date

^^^

L

(

l t

i I

TEST

SUMMARY

i ECT.716A, Rev. 4 TYPE B & C LOCAL LEAK RATE TEST J

(

1.0 OBJECTIVES l

t ECT.716A ' Type B and C Local Leak Rate Test" was perforised to quantify leakage of potential containment leakage paths per 10cm50, Appendia J and as identified in FSAR Table 6.2.4.2.

This, meedure l

aise satisfiesSection XI exercising testing requirements f -

.everal containment isolation check valves.

Successful completion of this test procedure satisfies the requirements of Technical Specifications 4.6.1.1.c, 4.6.1.2d, 4.6.1.2h, 4.6.1.3a, 4.6.1.3b, 4.6.1.3c,

)

4.6.1.7.2, and 4.6.1.7.3 which in part satisfy the requirements of 10cm50, Appendix J, type

'A' and

'C' testing.

t i

2.0 STATEKINT OF CRITERIA AND TEST RESULTS ACHIEVED The performance of this test procedure along with ICT.790A, GCT 7954, and ECT 789A satisfies all acceptance criteria and quantifies the j

actual leakage rates of all Type 'a' and

'C' testable containment leakage paths as required by CPSES Technical Specifications.

Attachment I to the test ausmary is a tabulation of leak rate test data for penetrations / valves tested in accordance with ECT 716A.

! combines the test results free ECT.716A.

ECT 790A, i

ECT 795A, and ECT 789A to show that the following test acceptance criteria have been satisfied:

2.1 "The upper confidence limit (UCL) on the combined leakage rate for all penetrations and valves subject to Type "l* and

'C' tests shall be less than 0.60 la, or 320.0 SC m.'

Using the test data tabulations of ECT 716A, Attachment 9 and

of this Test Summary, the Upper Confidence Limit (UCL) for all penetrations and velves subject to Type "B' and Type

'C' testing was less than.60 14 (320 SC N) with an actual value of 67.77179 SCN.

t NOTE:

Valves 1 8802A, 1 88028, and 1 8835 which were tested

{

in ECT 789A and valves 1 8881, 1 4824 and 1 8823 which were tested in ECT.790A are not included in the above i

tabulation because FSAR Amendment 77 removed the requironent to Type

'C' test there valves.

2.2 avalves in penetrations tested with water shall not exceed the leak rates noted below.'

v lvg Maximum taakare a

1HV.4777 78.9 cc/ min o

1HV.4776 78.9 cc/ min 1CT.145 78.9 ce/ min ICT.142 74.9 cc/ min

,,,,... -. - _ _ =. - ' - * - - - - - - ~

^

l l

l t

Both penetrations leak tested with water were shown to have a

(

total leakage less than the 78.9 cc/ min maximum per valve with a total value of.006684 spo.

Individual leakage for each i

valve is as follows:

Velve Naminum Leskame 1NV.4777 0.0 cc/ min i

1NV.4776 0.0 cc/ min 1C7 145 0.0 cc/ min 1C7 142 25.3 cc/ min i

2.3 'Airlocks, Containment Purge and Exhaust Penetrations, and Pressure Relief Penetrations all have individual leakage criteria in addition to the total allowable containment Type "B" and 'C" Leakage of

.60La."

{

As noted below these penetrations all had leakage values significantly less than the maximum allowed by CPSES Technical i

Specifications.

I t

PENETRATION MAXIMUN AM N ED (SCFH)

AS.LEFT (SCFH)

{

i MIII.18 26.665

(.05La) 2.96448 MIII.19 26.665

(.05La) 6.336 NV 1 26.665

(.0$La) 13.011 i

MV.2 26.665

(.0$La) 4.5556 i

NV-14 31.998

(.06La) 0.523398 i

PERS AL (OVERALL) 26.665

( 05La) 12.7989 i

PERS AL SEALS 5.333

( 01La) 0.0487374 ENER AL (OVERALL) 26.665

(.05La) 5.846488 ENER AL SEALS 5.333

(.01La) 0.216138 i

' 2.4 "Only one door in each containment airlock (personnel and emergency) i can be opened at a time."

\\

t The personnal and emergency personnel airlock interlocks that l

allow only one door to be opened at a time were verified to function properly.

3.0 PERFORMANCE

SUMMARY

ECT-716A commenced Febra ry 8, 1989 and concluded August 1, 1989 provideo a summary of the penetrations, and valves tested.

date tested and leakage data. Attachment 2 describes additional testing performed by other procedures with totals that are used to satisfy plant commitments to 10CFR50 Appendix J. Attachment 3 is the summary sheets from the tests described in Attachment 2.

4 6

I 4

-_..__..-.-,-._g

l I

1 l-There were 26 TPCs written during the performance of ECT 716A, all of which were non. intent chonse in nature. TPCs 019, 020, 021, 022, 023 and 024 were written to allow testing by the water addition method.

TPCs 001, 002, 00), 004, 008, and 025 changed the valve lineups on their i

associated tests to facilitate better isolation, easier lineup, or delete valves outside required test boundary.

TPCs 005, 010, 011, 014, and 015 are in response to DCAs adding valves or changing valve number assignments.

TPCs 009, 012, 013, 017, and 018 change direction of i

testing to forward from reverse to better satisfy the intent of 10CFR50 Appendix J. TPC 016 adds penetrations requiring flanges to procedure. TPC

. 007 facilitates more efficient testing of electrical penetration assemblies.

TPC 006 addresses completion of system piping separating units 1 and 2.

TPC 026 was a temporary change to allow testing from l

SFCDs building while Containment Area was inaccessible due to painting.

ECT 716A should be revised to incorporate all of the TPCs written with i

the exception of TPC 026.

The following TDRs were generated during performance of ECT 716A. All were satisfactorily rotested after rework by the responsible organisation, or revision of test method, as applicable.

TDR PEN VALVE DESCRIPTION 6936 NIII.06 1 8381 CHECK VALVE WOULD NOT HOLD TEST PRESS l

6928 NIII.01 1 8046 CHECK VALVE WOULD NOT HOLD TEST PRESS 6953 NIV 16 151 8968 CHECK VALVE WOULD NOT HOLD TEST PRESS 7119 MIV 16 131 8968 AFTER RETEST OF 8069 WAS DISCOVERED THAT CHECK VALVE BONNET BOLTS WERE NOT TORQUED PRIOR TO RELEASE FOR' TESTING, INVALIDATING TEST RESULTS.

7662 NV.01 1HV 5537 FAILED DUE TO EXCESSIVE 1HV.5536 LEAKAGE SEATS & PACKING 6880 MV 5 1CA 016 CHECK VALVE VOUIS NOT HOLD TEST PRESSURE.

6876 NV.9 1CC.629 CHECK VALVE DOES NOT LIFT IN DIRECTION OF F1hW.

e

1 TDR

' PEN VALVE DESCRIPTION i

6952 NV.9 1HV.4701 SEAT LEAKAGE DOESN'T MEET ACCEPT /)lCE l

CRITERIA. WHEN DISASSENSLED. POUND CRACKED WEDGE.

l 7797 NV.9 10C.629 VALVES FAILED DUE TO EECESSIVE

{

1HV.4701 12AKACE THRU SEATS, t

i 6888 NV.12 1CH.024 CHECK VALVE WOUIb NOT Hola TEST h

PRzSSURE.

6976 MS.02 1 8811A NO ACCURATE DATE COULD SE OSTAINED l

i DUE TO EECESSIVE LEAKACE OF SOUNDARY VALVES WHEN TESTED IN REVERSE l

DIRECTION.

[

6962 MS 02 1 88115 SEE TEST DATA RECORDED WITH VENT CIDSED. OPENED VENT AND RETESTED.

i l

l 6963 MS.02 1 84115 SEE TDR e6976 - 1 8811A.

6988 810' ELECT ONE SPRING CHECK OFF THE PENET.

RATION DOES D T H0th PRESSURE.

PENETRATION 48. REP! ACED CHECK VALVE.

j I

8629 MIV.2(b) 1HV 4166 MINIMUM 1&W RANCE READING MIV.2(c) 1HV 4167 INCORRECTLY RECORDED.

IPS 501 READINGS LESS TMAN 20 SCCM i

1HV.4176 SMALL SE RECORDED AS 20 4

1PS.502 SCCN 6923 832' ELECT IVO SPRING CHECK VALVES LEAK ON N2 SUPPLY MANIPola.

l 8980 TEST RESULTS PACKAGE REVIEW COMMENT DEFICIENCIES

{

Po11owing each test and/or retest, the 'As.14f t" positions of each valve was L

specified on the respective Attachment 11 data sheet by the Shift Supervisor.

All TDR's written against this procedure have been closed.

4.0 ATTACMENTS TO THE

SUMMARY

4.1 Attachment 1, laak Rate Database i

4.2 Attachment 2, Summary of IAakage Totals froE all laakage Test procedures.

4.3 Attachment 3. Test Summary Sheets for ECT.789A, ECT 790A and ECT 795A.

f, thu)L k

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r ATTACHKENT 2 i

Page 1 of 1 Three procedures have been written to perform Appendix J required testing that is not included in ECT.716A. These procedures are ECT 789A ECT.790A, and ECT.795A. ECT.789A is a water test while both othere are air tests. The valves required to be included in the Appendix J total, test results, and the procedures used to perform the tests are as follows:

M

{

PROCEDURE V

LEAKACE RESULTS fJtROR ECT 789A 1 8809A

.8 al/ min NA 1 88098 1.18al/ min NA 1 8840 2.68al/ min NA l

ECT.790A 1 8825 1.727 x 10*' SCm 4.989 x 10'11 1 8890A 7.0634 r. 10 5 SCFM 4.989 x 10*11 1 88905 7.0634 x 10 5 SCFM 4.989 x 10*11 ECT.79.5A 1 8701A 4.1815 x 10 2 SCm 4.989 x 10*7 I

1 8708A 7.0634 x 10*' SCm 4.989 x 10*'

1 87018 4.0932 x 10*2 SCm 4.989 x 10*7 1 87085 5.580 x 10*3 SCm 4.989 x 10*9 When the totals from Attachment 9 Table IV are added to these leakages the i

results are: Air IAakage 1.024236 SC m l

From Above 0.089347 $CFM TOTAL 1.113583 SCm Error Squared 2.532915 E 4 SC m From Above 1.008 E.6 SCm TOTAL 2.542995 E.4 SCM STANDARD DEVIATION 1.594677 E 2 SCm i

Upper Confidence Limit:

60 sin x ( 1.113583

+ 1.594677 E 2) - 67.77179 SC W hr Total (LL)

S.D.

UCL i

Type C Water IAakage:

6.6840 E 3 gal sin From Above 1.2310 E.3 g31 sin TOTAL

.0079150 gal min i

n

--._.,n--,

-,. -. ~. -.. - - -, -., -, - -. - -, -.. - - -. - - - - -, -, - - - - - - - -,. - - -., - - -,-

ATTACMMENT 3 Pcge 1 cf 3-ECT St4 MARY ECT.789A 1.0 OBJECTIVts valves with water in accordanca with 10CP1L50 Appen are 1 8402A, 1 44025, 1 8809A. 1 88098, 1 8835 and 1 8440, Valves tested i

2.0 STATEMENT OF CRITERIA AND RESULTS ACHIEVED Acceptance Criteria for each valve with a minimum listed with the actual test values obtained.

y,6LV.]

ACCEPTANCE CRITERI.6 ACTUAL TEST DATA 1 8802A

{

7.07 ML/ MIN 0

ML/ MIN 1 88025 1.98 ML/ MIN 0

ML/ MIN 1 8809A 1.28 ML/ MIN

.8 ML/ MIN 1 48095 1.28 M1/ MIN 1.18 ML/ MIN i

1 8835

.60 ML/ MIN

<.2 MI/ MIN i

1 8840

[

42.95 ML/ MIN 2.68 ML/ MIN i

All valvo leakages were within acceptable limits.

3.0 PEPr0AMANCE

SUMMARY

Test performance began on 04/17/89 after applicable prerequisites were completed.

Valves 1 8802A, 1 88028 and 1 8835 were tested satisfactory.

On 04/18/89 testing of 1 8809A was attempted but systes pressure was higher than test pressure specified.

i satisfactory test of 18809A.

Wrote TPC #4 and completed l

1 84094 and 1 8840 if higher pressures exist inTPC of remaining valves

?

piping.

On 04/21/89 when & Train of RMR was drained down, tested

+

1 88098, taakage rate exceeded allowable limits.

+

Test of 1 8840 was completed satisfactory. On 04/22/89 Retest #1 was performed for 1 88098 af ter drainage boundary valves were adjusted and results were

. satisfactory.

On 07/02/89 Retest #2 was performed to test 1 88098 and 1 8840 due to a test sage found to be out of calibration.

TDRs 7327, 7337, and 7380, 7744 and 7745 were generated during test performance and are closed.

A recommended permanent change to the procedure would be to allow for higher test pressures due to piping being pressurized.

4.0 ATTACHMENTS TO THE

SUMMARY

None J

_.-....._,,,_._.....m,

ATTACHMENT 3 Page 2 of 3 ECT

SUMMARY

ECT.790A 1.0 ONECTIVE8 This test procedure provides for seat leakage testing of air operated valves with att in accordance with 10Cm50 Appendia J.

Valves tested are 1 8841, 1 8825, 1 8824, 1 8823, 1 8490A and 1 88908.

1 i

i 2.0 ' STATEMENT OF CRITERIA AND RESULTS ACHIEVED Results of all valve tests will be figured into ECT.716A and overall acceptability determined. Results were as follows:

vat.vt vA1.vt uAxAoE g393 (SCFM)

($ CPM) 1 1 8881 7.0634 x 10' 7.06 x 10*0 t

1 8825 1.727 x 10

7.06 x 10 6 1 8824 7.0634 x 10 5 7.06 x 10 6 t

1 8823 7.0634 x 10 5 7.06 x 10*'

1 8890A 7.0634 x 10 5 7.06 x 10*'

1 88908 7.0634 x 10 5 7.06 x 10 6 i

l 3.0 PERFORMANCE

SUMMARY

TPC el was written to delete technical specification requirements. TPC e2 was written to allow test performance with RCs loops at 1006 level with steam generator tubes draining.

Test performance began on 05/22/89.

All valves were tested and results recorded. No TDRs were issued for j

this test. No changes require permanent incorporation.

i t

4.0 ATTACmami TO THE

SUMMARY

)

None i

O l

l i

i ATTACID(ENT 3 Page 3 of 3 i

ECT 795A Sqgl681 1.0 0&JECTIVES:

o ECT.795A " Type 'C' 14 cal 1Aak Rate Test for Penetrations MII.02 and MII.03' was performed to quantify leak rates on RNR Hot legs 1 and 4 containment isolation valves 1 4701A and 1 87015 as well as 1 8708A and 1 87085.

The leak rates are to be added to the totals from ECT 716A to satisfy the requirewets of 10Cm50 Appendix J and Technical Specification 3.6.1.25.

2.0 STATENENT OF CRITERIA AND RESULTS ACHIEV,Eg Each of the four valves tested was reufred to meet an acceptable leakage rate when pressurized to between 48.3 ESIC and 50.0 PSIC.

leakage criteria for 1 8701A and 1 87018 is 3500 SCCN each.The acceptable 1 4704A and 1 87088 For valves The test results are as follows:the acceptable leakage criteria is 350 SCCN each l-Valve Test Pressure Leakane

(

1 8701A 49.1 PSIG 1184 sCCN

(

1 8708A 49.1 PSIC 20.0 SCCN 1 47015 49.5 PS10 1159 SCCN

.1 87088 49.5 PSIG 158 SCCN Note:

1 87015 required ratesting after initial failuse of test.

TDR 7915 was generated to document the test failure and required Start up to perform an EE.10.

The retest results are those noted above.

Because the valve passed the 14ak Rate Test following the EE.10, the determination is that the valve was not seating full depth prior to the EE.10, 3.0 PERFORMANCE SUMMA 11Y I

ECT 795A was started on June 22, 1989 on ni he shift with the testing of

[

S valve 1 87018.

The test failed due to leakage past the seat.

TDR 7915 was written and Start up performed an EE.10 after which the leak rate retest passed.

1 87088 was the second valve tested. This is a pressure relief valve that is tested from the discharge side.

l-A work package to break the inlet and discharge flanges to rotate the valve in place was required due to the number of restraints on the discharge side of the piping.

The leak rate test was satisfactory and work package SWP Z.4992 replaced the valve to complete the work.

3 14op was returned to OPS and A loop testing started on June 24, 1989 with the satisfactory testing of 1 8701A. Valve 18708A was tested on June 25, 1989

,resulta using traveler SWP.Z.4991 to provide support for rotation andwith satisfactory reinstallation of the valve.

During the testing of 1 8708A it was noted that there was no " Quality Related" stamp on the cover sheet to EGT 795A.

l DR P89 1679 was written to document the deficiency.

l 1

l At the completion of testing, the RHR system was returned to OPS control.

l

I2 f,

l 1

APPENDIX E LEAKAGE RATE MEASUREMENT SYSTEM DIAGRAM T

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