ML20062D874

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Reactor Containment Bldg Integrated Leak Rate Test, for 820514-19
ML20062D874
Person / Time
Site: LaSalle Constellation icon.png
Issue date: 05/19/1982
From:
COMMONWEALTH EDISON CO.
To:
Shared Package
ML20062D872 List:
References
NUDOCS 8208060250
Download: ML20062D874 (61)


Text

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a REACTOR CONTAINHENT BUILDING INTEGRATED LEAK RATE TEST 1

l LASALLE COUNTY NUCLEAR POWER STATION UNIT ONE May 14-19, 1982 8208060250 820728 PDR ADOCK 05000373-P PDR

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TABLE OF CONTENTS PAGE INTRODUCTION.......................................................

1 A.

TEST PREPARATIONS.............................................

2 A.1 Type A Test Procedure....................................

2 A.2 Type A Test Instrumentation..............................

2 A.2.a Temperature A.2.b Pressure i

A.2.c Vapor Pressure A.2.d Flow j

A.3 Type A Test Measurenent 3

A.4 Type A Test Pressurization...............................

3 B.

TEST METHOD...................................................

16 1

B.1 Basic Technique..........................................

16 B.2 S upp l emen ta l Ve r i f i ca t i on Tes t...........................

16 B.3 Linear Regression Analysis....

16 B.4 Ins t rumenta t ion E rror Ana lys is - App l ica tion.............

16 C.

SEQUENCE OF EVENTS............................................

17 C.1 Test Preparation Chronology..............................

17 C.2 Tes t P ressu ri za t ion Chronology...........................

17 C.3 Temperature Stabilization Chronology.....................

17 C.4 24-Hour Phase of Leak Rate Test........................... 18 C.5 Induced Leakage Phase....................................

19 C.6 Depressurization Phase.............

19 C.7 Floor Bypass Phase.......................................

19 TYPE A TEST DATA.............................................. 21 C.1 24-Hour Phase Date.......................................

21 C.2 Induced Phase Date.......................................

21 D.

TEST CALCULATIONS.............................................

22 E.

TYPE A TEST RESULTS AND INTERPRETATION........................

37 i

E.1 24-Hou r Phase Tes t Res ul ts...............................

37 E.2 Induced Phase Test Results...............................

37 E.3 Leak Rate Compensation for Non-Vented Pene tra tions and Change i n Drywel l Sump Level............

37 APPENDIX A TYPE B AND C TESTS.................................

39 APPENDIX B AS FOUND LEAK RATES................................

46 1

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APPENDlX C HYDROSTATIC TEST...................................

47 APPENDIX D CALCULATIONS.......................................

50 APPENDIX E TYPE "A",

"B", AND "C" TESTING SCHEDULE............

57 d

TABLE ONE I ns t rumen t.Speci fi ca t i on...........................

4 TABLE TWO Sensor Physical Locations..........................

5 TABLE THREE 48 psig Type A Test - 24 Hour Phase 22 TABLE.FOUR 48 psig Type A Test - Induced Leak Rate Phase 32 s

1 TABLE A-1 Type B and Type C Test Results.....................

40 TABLE C-1 Hyd ros t a t i c Te s t Re s u l t s...........................

48 FIGURE ONE Idealized View of Drywell and Suppression Pool......

6 FIGURE TWO Sensor Locations per Subvolume 7-14 4

FIGURE THREE Measuremen t Sys tem Schematic Arrangement...........

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INTRODUCTION This report presents details of the Integrated Primary Containment Leak Rate Test (IPCLRT) successfully performed on May 14 through 19, 1982, at LaSalle County i

Nuclear Power Station, Unit One. The test was performed in accordance with 10CFR50, Appendix J and the LaSalle County Unit One Technical Specifications.

t I

The total primary containnent integrated leak rate, adjusted to include penetrations not tested during the IPCLRT, was found to be 0.3919 wt%/ day at a test pressure of 40 psig, which was within the 0.476 wt%/ day acceptance criterion. The associated upper 95% confidence limit was 0.3933 wt%/ day.

Excluding non-testable penetrations, the supplemental Induced phase leakage test resul t was 0.8179 wt%/ day. This value should compare with the sum of the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> phase result (0 3737 wt%/ day) and the induced leak rate of 5.3 scfm (0.527 wt%/ day).

The statistical value of 0.8179 wt%/ day lies within the allowable tolerance band of 0.25LA, + 0.159 wt%/ day.

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2 SECTION A - TEST-PREPARATIONS A.1 Type A Test Procedure The IPCLRT was performed in accordance with Procedure LTS 300-4, Revision 3, and Pre-Operational Test PT-PC-101, Revision 25 Temporary Procedure Change Numbers 52-82, 53-82, and 57-82 were made to LTS 300-4 to correct the proce-dure for system valve lineup changes. The range for Pa was also changed to allow for testing the containment at a higher pressure.

These procedures were written to comply with 10CFR50 Appendix J, ANSI N45.4-1972, ANSI /ANS-56.8-1981, and LaSalle County Unit One Technical Specifications.

A.2 Type A Test instrumentation Table One shows the specifications for the Instrumentation used in the IPCLRT.

Table Two lists the physical locations of the temperature and humidity sensors within the primary containment.

Figure One is an idealized view of the drywell and suppression chamber showing the di f ferent subvolumes.

Figure Two shows RTO and dewcell locations per subvolume.

a.

Temperature Sensors were suspended to prevent direct thermal influences from any metal surfaces. Sensors were also kept away from any direct air flows.

Each RTD-bridge network was calibrated to yield an output of 60 mV to 120 mV over the range of 60 F to 120 F.

Calibrations were done by Volumetrics of Inglewood, Cali fornia. Calibration sheets for the RTD's and their signal conditioning boards is included in Table One, b.

Pressure Two precision quartz bourdon tube pressure gauges were utilized.

Each gauge had a local digttal readout in addition to a Binary Coded Decimal output to the process computer.

Primary containment pressure was sensed by the pressure gauges in parallel through a 3/8" tube connected to a test tap on a VQ penetration.

Each precision pressure gauge was calibrated over the range 0. psia to 100 psia in approximately 5 psia increments using a Volumetrics Inc.

VCM 809/1138 calibration standard.

c.

Vapor Pressure Ten Lithium Chloride Dewpoint Temperature Units were installed throughout the Drywell and Suppression Pool. The dewpoint cells were placed in locations where the chance of the dewcell becoming damaged was slight.

A calibration was done on each dewcell network over the range of 45 F to 90 F.

Calibration was done to yield an output of 45 mV to 90 mV over the range of 45 to 90 F.

Calibrations were performed by Volumetrics using dewcell standard, Volumetrics Inc., Serial No. VMC 209/319

3 d.

Flow A rotameter flowmeter, Fischer-Porter, calibrated to within

+1.025% by Volumetrics, was used for flow measurement. Tubing connected the rotameter to a test tap on one of the primary containment penetration lines.

A.3 Type A Test Measurement The IPCLRT was performed utilizing a Interface with the Volumetrics Data Acquisition System (DAS) and Prime Computer.

Information from the RTD's and dewcells is sent to a Dual Multiplexer Scanner in the Drywell.

The Scanner takes the data and sends it through a electrical penetration (E-20) to a System Console. The System Console takes the raw data and converts it into data readable to a computer and the test engineer.

via telephone lines. This information is then sent to the Prime Computer where all needed calculations are performed and a hard copy of the Information is produced. (See figure 3)

A.4 Type A Test Pressurization Two 300 scfm 600 hp electric oil-free air compressors were used to pressurize the primary containment.

The compressors were physically located outside the reactor building.

The compressed air was piped into the reactor building through an existing PCILRT Pressurizing Line.

For case of handling a flexible 4 inch pipe was used outside of the reactor building.

The drywell was pressurized through the "A" containment spray header 16 inch flange with an inboard valve NO 1821-F017A, open during the pressurization process.

INSTRUMENT SPECIFICATIONS 4'

TABLE ONE INSTRUMENT MANUFACTURER MODEL NO.

SERIAL NO.

RANGE ACCURACY

. REPEATABILITY Precision Pressure Volumetrics 2287, 2348 0-100'psiat +0.02% reading 1,0.001% F.S.

Gauges (2)

RTD's (30)

Volumetrics 14629.lLRT 5042-1, 5042-16 60 - 120 F

+0.1 F

-+0.1 F

5042-2, 5042-17 5042-3, 5042-18 5042-4, 5042-19 5042-5, 5042-20 5042-6, 5042-21 5042-7, 5042-22

-5042-8, 5042-23 5042-9, 5042-24 5042-10,5042-25 5042-11,5042 5042-12,5042-27 5042-13,5042-28 5042-14,5042-29 5042-15,5042-30

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Dewcells (10)

Volumetrics 5042-1, 5042-6 45 - 90 F

-+1.0 F

-+0.5 F 5042-2, 5042-7 5042-3, 5042-8 5042-4, 5042-9 1

5042-5, 5042-10 0-600 scfh 2.3% F.S.

Flowmeter (1)

Fischer & Porter RMB-57 l

1

TABLE TWO 5

IPCLRT INSTRUMENT PHYSICAL LOCATIONS RTD NO.

EPN SUBVOLUME INSTRUMENT INSTRUMENT ELEVATION AZIMUTH

  • 822',

1 ITE-CT021 1

0 2

ITE-CT022 1

826, 180 3

ITE-CT025 6

730, 90 4

1TE-CT026 6

730, 270 0 5

ITE-CT019 2

804, 115 6

ITE-CT020 2

804, 295 0 7

ITE-CT017 3

811, 0

8 1TE-CT018 3

815, 180 9

ITE-CT016 3

808, 270 10 1TE-CT015 3
797, 90 11 1TE-CT014 4
791, 90 12 1TE-CT013 4
785, 0

13 1TE-CT027 4

791, 270 14 ITE-CT029 4
785, 180 15 ITE-CT012 5
777, 270 16 ITE-CT011 5
772, 180 17 ITE-CT010 5
767, 90 18 1TE-CT009 5
762, 0

19 1TE-CT008 7

758, 270 20 ITE-CT007 7
754, 180 21 ITE-CT006 7
750, 90 22 ITE-CT005 7
746, 0

23 ITE-CT023 6

743, Oo 24 ITE-CT024 6
743, 180 25 ITE-CT001 8
708, 130 26 ITE-CT003 8
708, 195 27 ITE-CT030 8
708, 78 28 ITE-CT002 8
724, 108 29 ITE-CT028 8
724, 78 30 1TE-CT004 8

724 287 DEWCELL NO.

EPN SUBV0LUME INSTRUMENT INSTRUMENT ELEVATION AZIMUTH

  • 1 IME-CT036 1

826' O

2 1ME-CT035 3

812' 180 3

IME-CT037-3 803' 180 4

1ME-CT034 4

791' O

5 1ME-CT033 5

773' 180 6

IME-CT039 5

763' O

7 IME-CT038 6

746' 270 8

IME-CT032 7

752' oo 9

IME-CT031 8

708' 1950 10 1ME-CT040 8

724' 78

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ITE-CT018, Elev. 815 ft, Rad.14 fc.

IME-CT037 Elev. 803 ft, Rad. 21 f(.

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ITE-CIO27, Elev. 791 f t,

Rad. 16 ft-ITE-CT013, Elev. 785 ft, Rad. 28 ft

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ITE-CT012, Elev. 777 ft, y

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ITE-CT004, Elev 724 ft, Rad. 38-9 in.

ITE CT001, Elev. 708 ft, Rad. 39-8 in.

ITE-C.T028, Elev. 724 f t,

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IME-CT040. Elev. 724 f t, Rad. 22 ft~

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ITE-CT030, Elev. 708 ft j'

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IME-CT031, Elev. 708 ft, Rad. 39 ft 8 in.

ITE-CT003, Elev. 708 ft, Rad. 39 ft 8 in.

Fig. 2.8 - Plan View of Sensor Locations, Subvolu:ne 8

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l CE CE CE RID's Dew-cells Frecision Pressure Gages I

CE CE Conditioning Conditioning A=plifiers Aeolifiers ~

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CE Acurex Autodata Nine Data Logger u

CE EIR-RS-232 Paper Tape Interface

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Prime Process Computer Computer II 1 l

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Storage Printer Plotter Printer i

Fig. 3 - Cc puter centrolled data acquisition and data processing syste:

15

SECTION B - TEST METHOD 16 B.1 Basic Technique The absolute method of leak rate determination was used. The absolute method uses the ideal gas laws with measured containment temperature, dew point and air pressure to determine dry air mass in the containment. The leak rate can then be determined from the rate of mass loss.

B.2 Supplemental Verification Test The supplemental verification test superlmposes a leak of known magnitude on the existing leakage.

The degree of detectability of the combined leak rate provides a basis for resolving any uncertainty associated with tie 24-hour phase of the test.

B.3 Linear Regression Analysis The leak rate is assumed to be constant during the testing period, ideally yielding a straight-line plot with a negative slope. However, sampling techniques and test conditions are not perfect; consequently, the measured values will deviate from the ideal straight-line' situation.

A least squares fit statistical analysis was performed to determine a regression line for mass versus time af ter each set of data was acquired.

The slope of this regression line was designated to be the statistically averaged leak rate. This quantity was compared to the Technical Specifi-cation allowable operational leak rate LT (0.476 wt%/ day).

Associated with the statistically averaged leak rate was the upper 95%

confidence limit leak rate. The calculation of this upper limit was based upon the standard deviations from the regression line and the one-sided Students-T Distribution function. A procedureal requi rement speci fied that the upper 95% confidence limi t leak rate must be less than the Tech-nical Specification allowable operational leak rate LT (0.476 wt%/ day).

B.4 Instrumentation Error Analysis-Application An instrumentation error analysis was performed prior to the test in accordance with ANSI N45.5-1972. The instrumentation system error was calculated in two parts. The first part was to determine system accuracy and the second part was to determine system repeatability. The system error analysis performed prior to the test yielded a total instrument uncertainty of +0.00850 wt%/ day.

During the test one of the dew cells mal functioned (number 3). This dewcell was removed from the test and a new error analysis was performed. The new error analysis yielded a total instrument uncertainty of +0.00992 wt%/ day.

The instrumentation uncertainty is used only to illustrate the system's ca'pability to measure the required parameters that are necessary for calculation of the primary containment leak rate.

The instrumentation uncertainty is always present in the data and is incorporated in the 95%

upper confidence limit in the form of data scatter.

Procedures required that the summation of the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> statistical leak rate and the total instrument uncertainty be less than LT (0.159 wt%/ day).

3 SECTION C - SEQUENCE OF EVENTS 17 C.1 Test Preparation Chronology The pretest preparation phase and containment inspection were completed on May 14, 1982 with no visible structural deterioration being found. Major preliminary steps included:

1.

Completion of all Type B and C tests, component repairs, and retests.

2.

Completion of IPCLRT pretest valve checklist including isolation of drywell and suppression chamber pressure sensors.

3 Blocking of four drywell to suppression chamber vacuum breakers in the open position for pressure equalization between the drywell and suppression chamber volunes.

4.

Venting of the reactor vessel to the primary containment via the manual head vent line and the drywell equipment drain sump.

5 Completion of pretest data gathering system, including computer p rog ram, instrument console, and associated wi ring.

C.2 Test Pressurization Chronology Date Time Event 5/15/82 0156 Primary Containnent pressurization initiated.

0208 Reactor Scram Alarm at 1.25 psig.

0211 Reactor Scrammed.

0440 Second Ai r Compressor started.

0600 Found leakage on input sensing line of instrument 1821-N048A.

0659 Primary containment pressure reached 55.55 psia.

Pressurization was complete.

C.3 Temperature Stabilization Chronology Date Time Event 5/15/82 1135 Water leakage on ICM01M sight glass found.

Repairs initiated.

1448 Test terminated due to instrument and sight glass leaks.

Estimated leakage rate C0 500 SCFM.

Repairs initiated.

1630 Inspection for leakage.

1740 Packing leak on valve 1MC033 found.

Leakage slight, no repairs initiated.

1940 Final check for leakage.

2200 Computer communication line down, data being sent to Chicago computer.

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C.3 Temparature Stxbilization Chronology (Cont'd.)

18 Date Time Event 5/16/82 0100 Drywell Air Temperature changing by 0.1 F/hr.

0220 Vessel level at 290".

0223 Vessel level raised to 310".

0415 Outage for removal of compressor connection to containment hung.

0330-Spool piece and flange being installed, stabilization 0445 complete.

0725 Trip of reactor building breaker removed power from DAS.

0800 Reactor building power brought back.

Data acquisitioner

.DAS reinitiate C.4 24-Hour Phase of Leak Rate Test Date Time Event 5/16/82 1218 Started 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> test phase.

Data sets being taken every 10 minutes.

1345 Channels 2, 4, 5-9 deleted from data acquisi tioner scan.

2200 Leakage remaining high.

Inspection for leaks initiated.

2345 Hydrogen recombiner, Unit 1 Loop seal valve developed a leak (250 SCFM). Test stopped and loop seal refilled.

Test restarted using data set #70.

I 5/17/82 0140 Data Acquisitioner stopped sending data. The unit was r

re i n i t i a ted.

l 0214 Restarted 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> test using data set #84.

0224 Computer accepting data.

0234 Computer stopped accepting data from acquisi tioner.

0300 Hand entering data.

0530 Sump valves 1RE024 and 25 were found placed in Auto.

Valves have opened and pumped 83 gallons from'the drywell equipment sump.

0830 Conouter pointer repaired, computer accepting data.

0835 Backup computer calculations being checked in Chicago Data is wrong.

l 0840 Two data sets found missing.

l.

1135 Hydrogen recombiner loop seal line plugged.

F C.4 24-Hour Phase of Leak Rate Test (Cont'd.)

19 Date

, Tine Event 5/17/82 1412 Drywell and suppression pool volumes were found to be wrong in the computer program. These were corrected and all data was recalculated.

2115 The data acquisitioner shutdown, due to heat.

I t was restarted with no apparent data loss.

2138 1 Data set found missing.

5/18/82 0100 Data acquisitioner output speed increased.

Problem resolved.

1-2 data sets lost.

0145 Channel 42 (Dewcell #2) went bad.

Dewcell removed and data recalculated.

0302 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> test completed.

The 95% upper confidence limit leak rate was 0.3933 %/ day well below the allowable leak rate of 0.476%/ day. The statistically averaged leak rate was 0.4624%/ day.'

C.5 Induced Leakage Phase Date Time Event 5/18/82 0345 Chemistry sampled containment atmosphere.

0530 Induced leak rate 320 SCFH ini tiated (OSSht/ day) /

0630 Stabilization complete.

0810 The data acquisitioner stopped sending an'd printing data.

Problem resolved, no data lost.

1102 induced leak rate test completed. The measured induced leakage rate was 0.8179%/ day. The measured leakage rate minus induced leakage minus statistically averaged leakage rate (24hr) produced a difference of 0.1098%/ day within the limits of 0.159%/ day.

C.6 Depressurization Date Time Event 5/18/82 1939 Depressurization initiated.

5/19/82 0118 Depressurization stopped at 5.4 psig.

0139 vacuum breaker closed.

0232-Suppression Pool depressurized.

C.7 Floor Bypass Tests Date Tine Event 5/19/82 0232 5 psid floor bypass test started.

f C.7 Floor Bypass Tests (Cont'd.)

20 Date Time Event 5/19/82 0335 5 psid Bypass Floor Test completed.

Leakage rate is 7.12 SCFM,'well below the limit of 73 SCFM.

0340 Drywell depressurization restarted.

0416 Drywell depressurization stopped at 1.8 psig.

1.5 psid bypass floor test started.

0521 1.5 psid bypass floor test completed.- Leakage rate 3 32 SCFM, well below the Ilmit of 73 SCFM.

0545 Drywell opened up.

Inspection shows no deviations.

NOTE: The Hydrogen Recombiner Loop Seal Vaive was checked after the test and found to have a dirty seating surface.

c o

SECTION.C - TYPE'A TEST DATA 21 C.1 24 Hour Phase Data Data for the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> phase is illustrated in Table Three. Graphic record of this portion of the test is presented' in graphs 1 through 6.

This data-has been corrected and the' raw data f rom dewcell 3 has been eliminated.

C.2 Induced Phase Data Data for the induced phase is presented in Table Four.

Graphic illustration of the major parameters is presented in graphs 7 through 10.

This data has also been corrected and raw data from dewcell 3 has been eliminated.

F SECTION D - TEST CALCULATIONS 22 Calculations for the test were based on LaSalle County Procedure LTS-300-4.

A reproduction of _ this procedure is found in Appendix D.

The instrument error analyses are also found in Appendix D.

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9.84 10:36 58 97 02 1 02756E+05 1 02920E+05 54 628 0 3776 0 5737 0 3821 0.3RP1 i

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Table Three -- 39.6 PSIG TYPE A TEST - 24 HOUR PHASE Page 25 20.82 21:35 123 97.54 1.02581E*03 1.02917E*05, 54.500

0. 3183

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F SECTION E - TYPE A TEST RESULTS AND INTERPRETATION Page 37 E.1 24 Hour u e Test Results Based upon data collected during the 24 hour phase,.the following results were determined: Actual Leak Rate Acceptance (wt%/ day) Criterion (wt%/ day) . Total time measured leak rate 0.3707 0.476 Statistically averaged leak rate 0 3737 0.476 Upper 95% confidence limit leak rate 0 3751 0.476 E.2 Induced Phase Test Results A leak of 5 33 SCFM (0.554 wt%/ day) was induced on the primary containment for this phase of the test. The following results were determined: Actual Leak Rate Acceptance (wt%/ day) Criterion (wt%/ day) Total time measured leak rate 0.8143 1.0867 0.7687 Statistically averaged leak rate .0.8179 1.0867 0.7687 Upper 95% confidence limit leak rate 0.8542 1.0867 0.7687 E.3 Leak Rate Compensation for Non-Vented Penetrations The Integrated Primary Containment Leak Rate Test was performed with the following penetrations not drained and vented as required by 10CFR50, Appendix J. The As Lef t Leak Rate of each of these penetrations, as determined by Type C testing is listed: Penetration Function ScFh wt%/ day M-16 RBCCW Supply 0.458 0.0008 M-17 RBCCW Return 2.085 0.0036 M-25 PCCW "A" Supply 0.47 0.0008 M-26 PCCW '.'B" Supply 0.93 0.0016 M-27 PCCW "A" Re turn 0.47 0.0008 M-28 PCCW "B" Return 0.94 0.0016 M-30 RWCU Suction 0.0 0.0000 M-36 Recirc Loop Sample 0.0 0.0000 M-96 Drywell Equipment Sump 0.465 0.0008 M-97 Drywell Floor Sump 0.0 0.0000 M-98 Drywell Equipment Sump Cooling 0.0 0.0000 M-22 Inboard MSIV Drain 0.468 0.0008 M-7 RHR Shutdown Cooling Suction 0.0 0.0000 M-15 RCIC Steam Supply 0.469 0.0008 ECCS/RCIC Worst Division 2.803 0.0048 TOTAL 0.0165

( Page 38 This yields.the following adjusted leak rates: Statistically averaged leak rate: 0 3919 wt%/ day Upper 95% confidence.Ilmit leak rate: 0.3933 wt%/ day NOTE: Drywell sump levels were not used in calculating the final leak rate. Sumps were filled during the test by a leakage path from the reactor vessel to the sumps. Since the vessel head was vented to these sumps-volume-In subvolume 6 never changed. 4 A >p r P f-l I I l

f Page 39 ) APPENDlX A TYPE B ANC C TESTS Presented herein are the results of local leak rate tests conducted on all penetrations, double gasketed seals, and isolation valves. All valves with leakage in excess of the Individual valve leakage limite were restored to an acceptable leek-tightness. Total leakage for double gasketed seals and total leakagt for.all other penetrations and isolation valves following repairs satisfied the Technical Specification Limi ts. These results are listed in Table A-1. S 9~ \\ s \\ 4 Y, sX s,. + m i ( 3 1 \\( 1, x.. 4 g ew ~ ~ i N g< l \\ l s } l l 1 s t W. ~" " s - s M l

f TABLE A-1 Page 40 TYPE B AND C TEST RESULTS VALVE (S) OR MEASURED LEAK RATE (SCFH) s PENETRATION TEST VOLUME AS FOUND DATE AS LEFT DATE 1821-F022A Main Steam isolation Valves 0.556 10/27/81 0.556 10/27/81 IB21-F028A IB21-F067A 1E32-F001A 1821-F022B 7 94 10/27/81 7 94 10/27/81 IB21-F0288 IB21-F0678 s 1E32-F001B i 1821-F022C 1 99' 10/27/81 1 99 10/27/81 IB21-F028C IB21-F067C 1821-F001C 1821-F0220 0.794 10/27/81 0 794 10/27/81 1821-F028D IB21-F067D 1E32-F001D IB21-F016 Inboard MSIV Drain Unable to 10/19/81 0.468 1/12/82 1821-F019 Determine IVQO26 Suppression Chamber Vent 2.66 6/2/82 2.66 6/2/82 1VQO27 IVQ043 IVQO29 Drywell Vent 4.14 5/28/82 4.14 5/28/82 IVQO30 1VQ042 IVQO31 Suppression Chamber Purge 3.03 5/28/82 3.03 5/28/82 IVQO32 IVQ040 IVQO34 Drywell Purge 1.42 5/25/82 1.42 5/25/82 IVQO35 IVQO36 IVQ068 1CM027 Suppression Chamber Cont-0.0 2/21/82 0.0 2/21/82 1CM028 inuous Air Monitor ICM029 Drywell Continuous Air 0.0 2/21/82 0.0 2/21/82 1CM030 Monitoring ICM031 PC Air Sample 0.0 2/21/82 0.0 2/21/82 1CM032 1CM033 Sample Return to Sr "ession 0.139 2/21/82 0.139 2/21/82 ICM034 Chamber 1821-F032A Feedwa te r Unable to 12/8/81 1.5 1/19/82 De te rmi ne

I Pag 2 41 VALVE (S) OR MEASURED LEAK RATE (SCFH) PENETRATION TEST VOLUME AS FOUND DATE AS LEFT DATF 1821-F065A Unable to 1/30/82 4.18 5/4/82 Determine 1821-F010A 0.0 12/13/81 0.0 12/13/81 1821-F0328 0.47 12/8/81 0.47 12/8/81 1B21-F065B Unable to 1/30/82 1.77 2/17/81 Determine 1821-F010B 0.0 12/8/81 0.0 12/8/81 IG33-F040 0.0 3/7/82 0.0 3/7/82 11N001A Drywell Pneumatic Suction 0.466 11/22/81 0.466 11/22/81 11N001B IB33-F019 Reci rc Loop Sample 0.0 2/24/82 0.0 2/24/82 1833-F020 1RF012 Drywell Floor Drain Sump 0.0 4/2/82 0.0 4/2/82 1RF013 M-111 Drywell Pressure Hatch Door 0.0 2/18/82 0.0 2/18/82 Seals M-111 Drywell Personnel Hatch 0.0 5/10/82 0.0 5/10/82 M-112 Drywell Equipment Hatch 0.0 5/10/82 0.0 5/10/82 M-113 Suppression Pool Hatch #1 0.0 6/4/82 0.0 6/4/82 H-114 Suppression Pool Hatch #2 0.874 5/14/82 0.874 5/14/82 M-115 CRD Removal Hatch 0.47 2/28/82 0.47 2/28/82 Drywell Head 0.0 5/13/82 0.0 5/13/82 M-42 TIP Flange 0.0 10/22/81 0.0 10/22/81 l M-43 TIP Flange 0.0 10/22/81 0.0 10/22/81 M-44 TIP Flange 0.0 10/22/81 0.0 10/22/81 l M-45 TIP Flange 0.0 10/22/81 0.0 10/22/81 M-46 TIP Flange 0.0 10/22/81 0.0 10/22/81 l 1PC001A Outboard 0-Ring Seal 0.0 10/22/81 0.0 10/22/81 l Inboard 0-Ring Seal 0.84 10/22/81 0.84 10/22/81 Actuator 0-Ring 0.0 10/22/81 0.0 10/22/81 Actuator Seal Unable to 10/22/81 0.47 1/6/82 Determine i IPLOO1B Outboard 0-Ring 0.0 10/26/81 0.0 10/26/81 Inboard 0-Ring Seal 0.0 10/26/81 0.0 10/26/81 Actuator 0-Ring 0.0 10/26/81 0.0 10/26/81 Actuator Seal 0.0 10/26/81 0.0 10/26/81

I Page 42 VALVE (S) OR MEASURED LEAK RATE (SCFH) PENETRATION TEST VOLUME AS FOUND DATE AS LEFT DATE IPC001C Outboard 0-ring seal 0.0 10-22-81 0.0 10-22-81 Inboard 0-ring seal 0.467 10-22-81 0.0467 10-22-81 Actuator 0-ring 0.0 10-22-81 0.0 10-22-81 Actuator Seal 0.0 10-22-81 0.0 10-22-81 IPC0010 Outboard 0-ring seal 0.47 10-22-81 0.47 10-22-81 Inboard 0-ring seal 0.0 10-22-81 0.0 10-22-81 Actuator 0-ring 0.0 10-22-81 0.0 10-22-81 Actuator Seal 0.0 10-22-81 0.0 10-22-81 IVQO30 inner Flange 0-ring 0.0 2-21-82 0.0 2-21-82 IVQO27 inner Flange 0-ring 0.46 3-1-82 0.46 3-1-82 IVQO31 inner Flange 0-ring 0.0 2-21-82 0. 0.' 2-21-82 IVQO34 Inner Flange Gasket 1.89 3-31-82 1.89 3-31-82 IPC003C Inner Flange 0-ring 0.0 10-28-81 0.0 10-28-81 IPC003A Inner Flange 0-ring 0.0 10-28-81 0.0 10-28-81 IPC003D inner Flange 0-ring 0.0 10-28-81 0.0 10-28-81 IPC003B Inner Flange 0-ring 0.0 10-28-81 0.0 10-28-81 IPC002C Inner Flange 0-ring 0.0 10-26-81 0.0 10-26-81 IPC002A Inner Flange 0-ring 0.0 10-28-81 0.0 10-28-81 l 1PC002D Inner Flange 0-ring 0.0 10-28-81 0.0 10-28-81 i IPC002B Inner Flange 0-ring 0.0 10-28-81 0.0 10-28-81 1RE026 Drywell Equipment Unable to 11-20-81 0.0 3-30-82 1RE029 Drain Sump Cooling Determine E-2 Electrical Penetrations 0.414 11-21-82 0.414 11-21-82 E-3 0.0 11-21-81 0.0 11-21-81 E-4 0.0 11-20-81 0.0 11-20-81 E-5 0.466 11-21-81 0.466 11-21-81 E-6 0.0 11-21-81 0.0 11-21-81 E-7 0.0 11-21-81 0.0 11-21-81 E-8 0.0 11-20-81 0.0 11-20-81 E-9 0.0 11-21-81 0.0 11-21-81 E-10 0.0 11-21-81 0.0 11-21-81 ( E-11 0.0 11-20-81 0.0 11-20-81

T Page 43 VALVE (S) OR HEASURED LEAK RATE (SCFH) PENETRATION TEST VOLUME AS FOUND 11/Z0/61,AS LEFT DATE_ DATE E-12 0.0 0.0 11/20/51 E-13 0.0 11/21/81 0.0 11/21/81 E-14 0.0 11/20/81 0.0 11/20/81 E-15 0.0 11/20/81 0.0 11/20/81 E-16 0.0 11/20/81 0.0 11/20/81 E-17 0.0 11/21/81 0.0 11/21/81 E-18 0.0 11/20/81 0.0 11/20/81 E-19 0.0 11/21/81 0.0 11/21/81 E-20 0.0 11/21/81 0.0 11/21/81 E-21 0.0 11/21/81 0.0 11/21/81 E-23 0.0 11/21/81 0.0 11/21/81 E-24 0.0 11/21/81 0.0 11/21/81 E-25 0.0 11/21/81 0.0 11/21/81 1RE024 Drywell Equipment Drain Sump 0.465 4/9/82 0.465 4/9/82 1RE025 IG33-F001 RWCU Suction 6.04 3/8/82 0.0 3/26/82 1G33-F004 IE51-F080 RCIC Turbine Exhaust Vacuum Breaker 4.03 2/5/82 0.0 3/11/82 IE51-F086 IVP063A PCCW A Supply 0.47 1/27/82 0.47 1/27/82 1VP113A l IVP063B PCCW B Supply 0 93 10/21/81 0.93 10/21/81 IVP113B IVP053A PCCW A Return 0.47 1/22/82 0.47 1/22/82 IVP114A IVP053B PCCW B Return 0 94 1/22/82 0.94 1/22/82 IVP114B 11NO31 TIP Index Purge Air Supply 0.0 3/4/82 0.0 3/4/82 11N017 Drywell Pneumatic Discharge to Unable to 2/21/82 0.674 2/21/82 IIN018 Drywell Determine l IHG001A Combustible Gas Control A Suction Unable to 2/11/82 0.0 3/16/82 f IllG002A Determine t

b Page 44 VALVE (S) OR MEASURED LEAK RATE (SCFH) PENETRATION TEST VOLUME AS FOUND DATE AS LEFT DATE 1HG005A Combustible Gas Control A Return 1.26 2/22/82 1.26 2/22/82 1HG006A IHG0018 Cumbustible Gas Control B Suction Unable to 2/11/82 0.69 5/6/82 1HG002B determine 1HG005B Combustible Gas Control A Return Unable to 2/22/82 1.62 5/7/82 1HG006B determine 1E51-F063 Steam to RCIC 0.469 2/11/82 0.469 2/11/82 IE51-F076 1E51-F064 IE51-F008 M-38 Service Air to Drywe11 0.0 4/23/82 0.0 4/23/82 M-37 Clean Condensate to Drywe11 0.0 4/20/82 0.0 4/20/82 1CM017B Drywell Humidity Monitor B Suction 0.0 10/20/81 0.0 10/20/81 1CH018B ICM019A Drywell Humidity Monitor A Discharge 1.413 12/2/81 1.413 12/2/81 1CM020A ICM0198 Drywell Humidity Monitor B Discharge 0.0 10/22/81 0.0 10/22/81 1CM020B ~ 1CM017A Drywell Humidity Monitor A Suction 0.0 10/20/81 0.0 10/20/81 1CM018A 1E12-F023 RHR/RCIC Head Spray 0.467 2/17/82 0.467 2/17/82 IE51-F013 IFC113 Cycled Condensate to Refueling Bellows 0.0 11/2/81 0.0 11/2/81 IFC114 IFC115 Rx Well Drain 0.0 2/21/82 0.0 2/21/82 1FC086 IWR029 RBCCW Supply Unable to 3/13/82 0.458 6/14/82 1WR179 Determine IWR040 RBCCW Return 19.02 3/13/82 1.62 5/6/82 IWR180 IIN074 Drywell Pneumatic Dryer Purge 0.466 11/22/81 0.466 11/22/81 11N075 IE22-F004 HPCS Injection 1.78 1/13/82 1.78 1/13/82 1E12-F008 RHR Shutdown Cooling Suction 13 12 2/2/82 0.0 3/20/82 1E12-F009 1C41-F004A SBLC Injection Line Unable to 2/25/82 1.39 3/20/82 1C41-F004B Determine IC41-F007

I Page 45 VALVE (S) OR MEASURED LEAK RATE (SCFH) PENETRATION TEST VOLUME AS FOUND DATE AS LEFT DATE 1E51-F069 RCIC Vacuum Pump Discharge 0.56 11/2/81 0.56 11/2/81 1E51-F028 1E51-F068 RCIC Turbine Exhaust 1.4 11/2/81 1.4 11/2/81 1E51-F040 1VQ047 Drywell inerting Make Up 0.0 2/21/82 0.0 2/21/82 1Vq048 IVQ050 Suppression Pool inerting 0.47 10/20/81 0.47 10/20/81 IVQ051 Make Up M-46 TIP Ball Valve A 0.464 3/30/82 0.464 3/30/82 M-45 TIP Ball Valve B 0.0 3/30/82 0.0 3/30/82 M-44 TIP Ball Valve C 0.464 3/30/82 0.464 3/30/82 M-43 TIP Ball Valve D 0.464 3/30/82 0.464 3/30/82 M-42 TIP Ball Valve E 0.464 3/30/82 0.464 3/30/82 1E12-F016A RHR A Drywell Spray Unable to 12/23/81 0.468 1/20/82 1E12-F017A Determine 1E12-F016B RHR B Drywell Spray 0.468 12/22/81 0.468 12/22/81 1E12-F017B 1E12-F042A RHR A LPCI Injection 0.469 12/23/81 0.460 12/23/81 IE12-F0428 RHR B LPCI Injection 1.87 12/22/81 1.87 12/22/81 1E12-F053A A RHR Shutdown Cooling Return 0.0 12/23/81 0.0 12/23/81 IE12-F053B B RHR Shutdown Cooling Return 0.47 12/23/81 0.0 12/23/81 IE22-F005 LPCS Injection 0.0 4/1/82 0.0 4/1/82 1E12-F042C RHR C LPCI Injection 0.463 4/2/82 0.463 4/2/82 H-33,53,95,102 Post LOCA Hydrogen Control 13.49 5/13/82 13.49 5/13/82 System Unit 1 Post LOCA Hydrogen Control 7.16 6/11/82 7.16 6/11/82 System Unit 2 1-11,35,36,45 Post LOCA Containment Unable to 2/21/82 13.66 3/31/82 47,50 Monitoring System Determine

b Page 46 APPENDlX B AS FOUND LEAK RATES The as found leak rate for the primary containment isolation valves, excluding the main steam isolation valves and leakages identified during the IPCLRT, was unable to be determined due to excessive leakage in several volumes. The total leak rates prior to initial criticality are summarized as follows: ITEM AS FOUND LEAK RATE AS LEFT LEAK RATE TECH SPEC LIMIT (SCFH) (SCFH) (SCFH) Isolation Valves Unable to Determine 41.871 231.4 Testable Penetrations 15.79 15.79 Double Gasketed Seals Unable to Determine 5.941 Main Steam Isolation Valves (Tested at 25 psig) Steam Line "A" 0.556 0.556 25.0 Steam Line "B" 7 94 7 94 25.0 Steam Line "C" 1 99 1.99 25.0 Steam Line "D" 0.794 0.794 25.0 TOTAL Through Leakage @ 25 psig 11.28 11.28 Complete details of these local leak rate test results are contained in LTS-300-5 and pre-operational test PT-PC-101. Based on the above, the total as found leak rate of the primary containment was greater than the Technical Specification criteria of 0.381 wt%/ day. -An as found leakage rate above 0.381 wt%/ day is expected, due to the fact that LaSalle Unit 1 is now out of the construction phase.

o APPENDIX C Page 47 HYDROSTATIC TEST Presented herein are the results of hydrostatic leak rate tests conducted on isolation valves. All valves with leakage in excess of the leakage limit (lgpm/ valve) were restored to an acceptable leak tightness. These results are listed in Table C-1. A

( 9" TABLE C-1 HYDROSTATIC TEST RESULTS VALVE (S) OR MEASURED LEAK RATE (GPM) PENETRATION TEST VOLUME AS FOUND DATE AS LEFT DATE IE21-F005 LPCS Injection Stop Valve 0.1 4/26/62 0.1 4/26/02 1E21-F006 LPCS Injection Testable Check Valva 0.0 4/26/82 0.0 4/26/82 IE22-F004 HPCS Injection Stop Valve 0.0 3/12/82 0.0 3/12/82 1E22-F005 HPCS Injection Testable Check Valve 4.0 3/7/82 0.0 4/27/82 1E21-F041A LPCI A Injection Testable Check Valve 4.0 5/3/82 0.0 5/27/82 IE21-F042A LPCI A Injection Stop Valve 0.0 4/24/82 0.0 4/24/82 1E21-F041B LPCI B Injection Testable Check Valve 4.0 2/27/82 0.0 6/4/82 IE21-F042B LPCI B Injection Stop Valve 0.0 3/12/82 0.0 3/12/82 1E21-F041C LPCI C Injection Testable Check Valve 4.0 3/7/82 0.0 5/3/82 1E21-F042C LPCI C Injection Stop Valve 4.0 3/7/82 0.0 4/5/82 1E51-F065 RCIC Injection Outboard Testable Check 4.0 3/10/82 0.0 5/15/82 Valve IE51-F066 RCIC Injection inboard Testable Check 0.0 5/15/82 0.0 5/15/82 Valve IE12-F050A A RHR Shutdown Cooling Return Check Valve 0.2 4/21/82 0.2 4/21/82 IE12-F053A A RHR Shutdown Cooling Return Stop Valve 0.3 4/21/82 0.3 4/21/82 1E12-F050B B RHR Shutdown Cooling Return Check Valve 0.0 4/22/82 0.0 4/22/82 1E12-F053B B RHR Shutdown Cooling Return Stop Valve 0.25 3/8/82 0.25 3/8/82 IE12-F008 RHR Shutdown Cooling Suction 4.0 4/2/82 0.3 4/13/82 1E12-F009 0.0 4/2/82 0.0 4/2/82 1E21-F001 1E21-F011 1E21-F012 LPCS isolation Valves 0.18 4/14/82 0.18 4/14/82 1E21-F018 IE21-F031 1E22-F012 1E22-F014 IE22-F015 HPCS Isolation Valves 0.0 4/27/82 0.0 4/27/82 1E22-F023 1E12-F036A 1E51-F019 RCIC isolation Valves 0.0 4/15/82 0.0 4/15/82 1E51-F031 1E12-F036B 1E12-F004B IE12-F088B RHR B isolation Valves 0.033 4/19/82 0.033 4/19/82 1E12-F064B

f Page 49 TABLE C-1 HYDROSTATIC TEST RESULTS VALVE (S) OR MEASURED LEAK RATE (GPM) PENETRATION TEST VOLUME AS FOUND DATE AS LEFT DATE 1E12-F074B RHR B' Isolation Valves 0.0 4/17/82 0.0 4/17/82-1E12-F055B 1E12-F311B IE12-F011B 1E12-F073B RHR B Isolation Valves 0.0 4/17/82 0.0 4/17/82 1E12-F053B IE12-F311B 1E12-F011B IE12-F024B RHR B Isolation Valves 0.0 4/19/82 0.0 4/19/82 IE12-F025B 1E12-F027B 1E12-F005 RHR C isolation Valves 0.5 4/14/82 0.5 4/14/82 IE12-F009C IE12-F064C l 1E12-F088C 1E12-F021 RHR C isolation 0.25 4/16/82 0.25 4/16/82 1E12-F025C 1E51-F080 RCIC lsolation Valves 0.0 4/15/82 0.0 4/15/82 1E51-F086 1E51-F102 1E12-F302 RHR isolation Valves 0.0 4/16/82 0.0 4/16/82 IE12-F004A RHR A Isolation Valves 0.2 4/14/82 0.2 4/14/82 1E12-F088A t 1E12-F064A 1E12-F030 1E12-F011A RHR A isolation Valves 0.0 4/17/82 0.0 4/17/82 IE12-F074A 1E12-F055A 1E12-F311A 1E12-F011A RHR A isolation Valves 0.0 4/17/82 0.0 4/17/82 1E12-F073A 1E12-F055A 1E12-F311A 1E12-F027A RHR A isolation Valves 0.0 4/16/82 0.0 4/16/82 i IE12-F025A 1E12-F024A 1B33-F013A P.eactor Recirc Seal Injection Check 0.0 4/12/82 0.0 4/12/82 Valve IB33-F017A 0.0 4/13/82 0.0 4/13/82 IB33-F0138 0.0 4/13/82 0.0 4/13/82 IB33-F017B 0.4 4/13/82 0.4 4/13/82

f Page 50 e O B APPENDlX D The following are the computations made to determine the instrument error of the instruments used during the IPCLRT. Also included is a reproduction of the computational procedures used during the IPCLRT. Instrumentation Error Analysis (Initial) La = 0.635%/ day .25 La = 0.159%/ day Pa = 54.3 psia T = 541.2 R Dew T = 68.1 F N=2 Pressure - Total Absolute Pressure E = (.0002)(54.3 psia) = 0.0109 psia E = (.00001)(100 psia) = 0.001 psia E +E ep = 1 N i (0.0109 psia)2 + (0.001 psia)2 + 0.00774 psia = ep 2 Water Vapor Pressure N = 10 E = (1.0 F) E = (0.5 F) E +E epr " i N r " 1 (1.0 F)2+ (0.5 F) + 0.354 F = epr ep = Temperature N = 30 E = 0.1 F E = 0.1 F E +E eT = 1 NZ

0. k (0. k eT = 1

= + 0.0258 F = eT 3 t = 24 hours E 2 2 2 eT 2 E + 2 *P" +2 ISG = +- t p p T 2400 0.0774 psia 0.354 F 0.0258 R I "1 24 c'. 3 psia 54 3 psia 541.20R + +2 ISG = + 0.00850%/ day ISG 0.25 La La = 0.159%/ day

Paga 51 APPENDIX D The following are the cornputations made to determine the instrument error of the instruments used during the 1PCLRT. Also included is a reproduction of. the computational procedures used during the 1PCLRT. Instrumentation Error Analysis (Final)' La = 0.635%/ day .25 La = 0.159%/ day Pa = 54.3 psia T = 541.2CR Dew T = 68.1 F N=2 Pressure - Total Absolute Pressure r E = (.0002)(54.3 psia) = 0.0109 psia E = (.00001)(100 psla) = 0.001 psia E E +E ep = + N (0.0109 psla) + (0.001 psia) + 0.00774 psia = ep = ,p,.- 2 Water Vapor Pressure N=9 E = (1.0 F) E = (0.5 F) E +E epr " i N = + (1.0 F) + (0.5 F) + 0 373 F = epr = ep 9 r Temperature N = 30 E = 0.1 F E = 0.1 F eT = + E +E NZ 4 eT = 1 (0.1 F) + (0.1 F) = + 0.0238 F = eT t = 24 hours t ISG = + 2 + 2 'UI +2 0.0774 psia 0.354 F 0.0258 R ,gg,,2400 2 +2 +2 - 24 54.3 psia 54.3 psia 541.20R ISG = + 0.00850%/ day ISG 0.25 La La = 0.159%/ day i

f- .*/ Page 52 6 CALCULATIONS PERFORMED FOR IPCLRT DATA Data coljected from pressure sensors, dew cells and RTD's located in the containment are processed using the following calculations. A. Average Subvolume Temperature and Dewpoint. T.= I(all RTD's in the jth subvolume) 3 Number of RTD's in jth subvolume F D.P., = I(all dew cells in jth subvolume) 3 Number of dew cells in jth subvolume F where T =

  • nerace tr-ner,ture ef the jth subvolume D.P..

= average dewpoint of the jth subvolume J B. Average Primary Containment Temperature and Dewpoint. NVOL (VF ) * (T ) oF T= 4j=1 j j NV0' D.P. = ~ (VT. ) * (D.P..) oT 1 J J J: where T = average containment temperature D.P. = average containment dewpoint VT. = volume fraction of the jth subvolu.me J NVOL = number of subvolumes If T. ir undefined then J T.= T. for 1 < j < (NYCL - 2) j j+4 T = T. f o r j = NVOL - I J'a T,= estimate for j = NVOL J If D.F.. is undefined J D.P.. = D.P..+1 for 1 < j < (NYOL - 2) j J D.P.. = D.P.. l for j = NVOL - 1 J J-D.P..= estimate f o r j = NVOL J

F Pags 53 E. Measured Leak Rate. L (TOTAL) = (W - W.)

  • 2400

%/ DAY BASE 1 m t

  • W i

BASE L (POINT) = (W. - V.)

  • 2400 2-1 1

%/ DAY m 1-1)

  • W.1-1 (t. - t.

2 where k = c ntainment dry air mass at t = 0 BASE time from start of test at ith data set

t. =

i sime from start of cent et (L I)LL 3mie 3rt t f,3 W. = dry air mass at ith data set i W. = dry air mass at (i-1)th data set 1-1 L (TOTAL)= measured leakage f rora the start of test to ith data set m two data sets L (POINT)= measured leakage between the last m T. Statistical Leak hate and Confidence Limit. LINEAP. LEAST SQUAPIS TITTING TIE IPCLRT DATA The method of "Least Squares" is a statistical procedure for finding the of measured data. The criterion best fitting regression line for a set fitting line to a set of data points is that the sum of the for the hest ceviations of the observed points free the line must be a squares of the minimum. When this criterion is met, a unique best fitting line is obtained The value of the leah rate based cn all cf the data points in the ILRT. regrerrion is called tne ststistically average lean rate. based on the the leak rate is constant during the testing Since it is assumed that period, a p2ct of tne measured containment cr/ air mass versus time veuld ideclly yieIc a straight line with a necative sicpe (assuming a non-zere conditions are net Opviourly, sarr.pling techniques and test leak rate). ideal and consequently the measured values will deviate from the perfect straignt line situation. the calculated leah rate is obtained Based on this statistical process, from the equation: W = At + B time t where W = contained dry air mass at

I Pcga 54 ,o e B = calculated dry air mass at time t = 0 A = calculated leak rate t = test duration B h, Ch Dry Air Mass (lbs) 4 Test Duration (hrs) The valuc-. for the Least Squares fit constants A and B are given by: 0) A = {N

  • I(ti) * (W ) - It.
  • IV.} = Z(t. - t) * (W.

i 1 1 1 1 -2 {N

  • I(ti)2 - (It.)2}

I(t. t) 1 1 {I(td} (v }) ~ { (ti} * (w )) B = IV -A*It = i i j o 9 N N

  • I(ti)~ - (It.)*

1 where t = the average time for all data sets U = the average air mass for all data sets The second formulas are used in the process computer program to reduce round-off-error. By definition, leakage out of the containment is considered positive leai:a ge ; therefore, the statistically average leak rate is giver. by: 1 = (-A) ~ (2400) s (weight i/ DAY) b STATISTICAL UNCERTAINTIES In order to calculate the 95% confidence licits of the statistically average leai: rate, the standard deviation cf the least squares slope and the student's TDistribution function are used as follows. 9 o 1 N

  • I(W )' - (IV.)'

g (N-2) N

  • I(t )2 - (It.)2) - A'}

o={

  • (

1 1 n L' hen perioriaing these cale' '.ations on the process computcr. I(W;)~ and (IV,)~ bet c:ue so larr:e t I... t they overil:v. Tt. avoid th!s proble.u 3W i :. r.t: : ;i-j tuu d ic,r W.. SW. is the d::icrei.(c betwes n L a n.i L'

  • 7 1
  • 1 1

Paga 55 v-e The single sided T-Distribution with 2 degrees of freed:m is approximated by the following formula from NBS Handbook 91: T.E. = 1.646698 + 1.455393 + 1.975971 (N-2) (N-2) -Tne upper confidence limit (UCL) is given by UCL r L, + o * (TE)

  • 2400 (weight *4/ DAY)

B 9 O 9 e o W l'uumi i _m___ l

(. ... e Page 56 IPCLRT DEFINITIONS (39.6 PSIG TEST PRESSURE) Maximum Allowable Leakage Rate (LA) ~ L A = 0.635% of containment volume per day 3 (0.00635)(394638 f t /24 hrs = 3 2506 ft /24 hrs = 3 104.4 ft /hr. = 104.4 (39.6 + 14.7) = 385.7 SCFH = 14 7 Maximum Allowable Operational Leakage Rate (L ) 75% of Maximum Allowable Leakage Rate L = t 0.75 (0.635%/ day) = 0.476%/ day = 289 3 SCFH Maximum Allowable Total Type "B" and "C" test (L)j 0.6% of Maximum Allowable L = g (0.60)(0.635%/ day) = 0 381%/ day = 231.4 SCFH = 1 l l --mg it p t qm--- g---yv---w -g--- ,y-- p

,o'o Page 57 APPENDlX E 1YPE "A", "B", AND "C" TESTING SCHEDULE The primary containment leakage rates will be demonstrated at the following test schedule and will be determined in conformance with criteria specified in Appendix J of 10CFR50 using the methods and provisions of ANSI N45.4-1972: a. Three Type A Overall Integrated Containment Leakage Rate tests will be conducted at 40 i 10 month Intervals during shutdown at P, 39.6 psig, a during each 10 year service period. The third test of each set will be conducted during the shutdown for the 10 year plant inservice inspection. b. If any periodic Type A test falls to meet 75 L, the test schedule for a subsequent Type A tests will be reviewed and approved by the Commission. If two consecutive Type A tests fall to meet 75 La, a Type A test will be performed at least every 18 months until two consecutive Type A tests meet 75 L, t which time the above test schedule will be resumed. a c. The accuracy of each Type A test will be verified by a supplemental test which: 1. Confirms the accuracy of the test by verifying that the di f ference between the supplemental data and the Type A test data is within 0.25 L - a 2. Has duration sufficient to establish accurately the change in leakage rate between the Type A test and the supplemental test. 3 Requires the quantity of gas injected into the containment or bled from the containment during the supplemental test to be equivalent to at least 25 percent of the total measured leakage at P, 39.6 psig. a d. Type B and C tests will be conducted with gas at P, 39.6 psig*, at intervals no greater than 24 months except for tesis involving: l l 1. Air locks, 2. Main steam line isolation valves, 7. Valves pressurized with fluid from a seal system, and 4. ECCS and RCIC containment isolation valves in hydrostatically tested lines which penetrate the primary containment. e. Air locks will be tested and demonstrated OPERABLE per Surveillance Require-ment 4.6.1.3 of Technical Specifications. f. Main steam line isolation valves will be leak tested at least once per 18 months. g. ECCS and RCIC containment isolation valves in hydrostatically tested lines which penetrate the primary containment will be leak tested at least once l per 18 months. h. The provisions of Technical Specification 4.0.2 are not applicable to 24 month or 40110 month surveillance Intervals.

  • Unless a hydraulic test is requi red.}}