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Reactor Containment Bldg Integrated Leak Test,Summary Tech Rept.Describes Summer 1978 Periodic Type B & C Tests at Subj Facil.Measured Leakage of All Sys Well within Tech Spec
	ML20023A391
Person / Time
Site:	Indian Point
Issue date:	11/02/1978
From:	; POWER AUTHORITY OF THE STATE OF NEW YORK (NEW YORK
To:	;
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ML100271754	List: ML100271753; ML20023A391;
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POWER AUT110RITY OF THE STATE OF NEW YORK l INDIAN POINT NUCLEAR POWER PIANT

, UNIT NO. 3 i

REACTOR CONTAINMENT BUILDING INTEGRATED LEAK RATE TEST

SUMMARY

TECHNICAL REPORT l

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PREPARED FOR POWER AUTHORITY OF THE STATE OF NEW YORK PREPARED BY l EBASCO SERVICES INCORPORATED PLANT OPERATIONS & BETIERMENT DEPARTMENT SEPTEMBER 6,1978 I

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THIS DOCUMENT IS THE PROPERTY OF EBASCO SERVICES INCORPORATED. ITS l l

(. USE IS EXPRESSLY RESTRICTED BY THE TERMS OF THE CONTRACT BEWEEN EBASCO SERVICES INCORPORATED AND THE POWER AUTHORITY OF THE STATE OF NEW YORK.

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f TABLE OF CONTENTS PAGE I. I NTRO DU CT I O N . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1 II.

SUMMARY

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, III. TEST D IS C US S IO N . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3 l

A. Dascription of Containment ............................ 3 B. Des cription o f Ins trumenta tion . . . . . . . . . . . . . . . . . . . . . . . . 4

1. Temperature Instrumentation ....................... 4

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2. Humidity Instrumentation .......................... 5 l 3. Pres sure Ins trumenta tion . . . . . . . . . . . . . . . . . . . . . . . . . . 5 f 4. Flow Instrumentation .............................. 5

5. Ancillary Ins trumenta tion . . . . . . . . . . . . . . . . . . . . . . . . . 5 C. Description of Computer Program ....................... 5 D. E rr o r A na ly s i s . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . ~6 l

E. Description of Tests .................................. 7 I

IV. RESU LTS AND V ERIF ICATION . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11 V. CON C LUS IO NS . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 13 VI. FIGURES.................................................... 15 VII. APPENDICES A. Computer Generated Report

1. Integrated Leak Rate Test (ILRT)

2. Controlled Leak Rate Test (CLRT) l f

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t 1 I. INTRODUCTION A periodic Type "A" Integrated Leakage Rate Test (ILRT) was performed .

on the containment structure of the Power Authority of the State of New t

York, Indian Point Nuclear Power Plant - Unit No. 3 pressurizea water reactor in July and August of 1978 utilizing the " Absolute Method" of testing. This test was performed at a pressure in excess of the calculated peak containment internal pressure related to the design bases accident (P,) and specified in the Technical Specifications.

This report describes and presents the results of this periodic Type "A" Leakage Rate Test including supplemental test method utilized for verification.

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II.

SUMMARY

Type "B" and "C" tests were pe-formed by Power Authority of the State of New York station personnel and repairs / corrections were made where necessary.

At the start of the Type "A" test, all valves were to be in their normal position for accident conditions. Exceptions to this valve line-up were noted during the test and are documented in the official copy of the Integrated Leak Rate Test periodic test procedure which is on file at

- the Indian Point Station. The calculated total-tLne simple leakage rate was 0.007 %/ day by weight at 58.396 psia (total containment pressure at the end of the test) . A least squares statistical fit of the total time simple leakage rates gave a leakage rate of -0.003%/ day by weight. The supplementary Controlled Leak Rate Test (CLRT) results verified the meas-ur d leakage within the allowable acceptance band.

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III. TEST DISCUSSION d

A. Description of Containment The reactor containment structure completely encloses the entire reactor and reactor coolant system to ensure no leakage of radioactive materials to the environment in the unlikely event of a loss of coolant accident.

The containment vessel is a reinforced concrete vertical right cyl-inder with a hemispherical dome and a generally flat base supported on rock. A welded steel liner with a minimum thickness of 1/4 inch is attached to the inside face of the concrete to ensure a high degree of leak tightness. Small steel channels are welded over all joints in the containment vessel liner forming leak tight air chambers. These chambers are continuously pressurized with air to serve as a leak prevention system.

These channels also serve to identify any liner plate weld leakage.

The containment has side walls measuring 148 feet from the liner on the base to the spring line of the dome and has an inside diameter of 135 feet. The side walls of the cylinder and the dome are 4 1/2 feet and 3 1/2 feet thick, respectively. The inside radius of the dome is equal to the inside radius of the cylinder so that the discontinuity at the spring line due to the change in thickness is on the outer surface. The flat concrete base mat is 9 feet thick with the bottom liner plate located on top of this mat. The bottom liner plate is covered with 3 feet of concrete, the top of which forms the floor of the containmant.

I i All penetrations made in the containment vessel were considered as potential leak sources and as such were designed with double barriers and treated by a leak prevention system. There are approximately 60 electrical penetration cannisters, 80 process piping penetrations, one personnel access airlock, one airlock / equipment hatch and one fuel transfer tube penetration.

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l Each process piping system which penetrates the containment vessel is designed to maintain the leak integrity of the containment vessel through the use of double leak tight barriers. The design of process piping isolation barriers is such that no single active failure I degrades the leak tightness of the containment vessel. An Isolation Valve Seal Water System is provided as a leak prevention system.

The containment vessel, penetrations and isolation valves are aligned to simulate accident conditions for the performance of the Integrated Leak Rate Test. An extra degree of conservatism in testing is provided by not using the Isolation Valve Seal Water or the Channel Weld and Penetration Pressurizing Systems during the Integrated Leak Rate Test.

The :ontainment vessel and all associated isolation valves, pene-trations and support systems have been designed to limit leakage to 0.1%

by weight of the contained air per day at 47 psig. The calculated peak accident pressure is 40.6 psig.

B. Description of Instrumentation A ' state-of-the-art' ILRT instrumentation package was utilized to allow leakage rate determination by the " Absolute Method". The primary measure-ment variables include containment pressure, dewpoint and temperature as a function of time. Ancillary measurements include ambient out-side pressure and temperature. During the supplemental CLRT, containment bleed-off flow is also measured. Instrument readings were output at 15 minute intervals automatically via a data logger and printer.

1. Temperature Ins trumen ta tion Thirty precision Resistance Temperature Detectors (RTD's) were located throughout the containment to allow measurement of the volumetrically weighted average temperature. The location of the temperature detectors in the containment is depicted in Figure 1. The specified accuracy of the RTD's is ! .15 F. The repeatability of the sensor is quoted as t .1 F.

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2. Humidity Instrumentation i I

Ten Lithium-Chloride wetted deweells were located throughout the containment I to allow measurement of the volumetrically weighted average containment vapor pressure. The location of the dewcells in the containment is depicted in Figure 2. The specified accuracy of the dew cells is 1.0 F dewpoint.

The repeatability of the sensor is quoted as .25 F.

3. Pressure Instrumentation

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Two precision quartz bourdon tube pressure indicators were supplied in the instrumentation package for the determination of containment absolute

, pressure. One precision pressure indicator was used as the primary sensor

, while the second indicator was considered as a backup. The equipment manu-fseturer specification accuracy of the precision pressure indicators is 1 002 psia. The repeatability of the instrument is quoted as i .001 psia.

4 Flow Instrumentation One thermal mass flowmeter with a range of 1 to 10 scfm and an accuracy of + 0.1 scfm was used during the Supplemental CLRT. The repeatability of the instrument is quoted as + 0.05 scfm.

5. Ancillarv Instrumentation The ambient outside temperature at the site was measured using a pre-cision RTD with the same specifications as those given in 1. above. The ambient barometric pressure was measured with a strain gauge absolute pressure indicator with an accuracy of 10.017 psia. The repeatability of the instrument is quoted as t 0.017 pain.

C. Description of the Computer Program The Ebasco ILRT computer program is an interactive Fortran IV program written specifically for fast, easy utilization during all phases of the ILRT and CLRT. Data entry and modifications, if necr eaery, are readily accomplished by the data acquisition team. In addition to extensive data verification routines, the program calculates, on demand, point-to-point, total time and mass point leak rates as well as first order linear regressions s

for these leakage rate calculations. Conputation of the 95% regression confidence interval for the leak rate calculations

, i is available on demand. Data rejection based upon the Chauvenet criterion may be utilized in the analysis.

Both a' priori and d posterioriinstrument error contribution to the leak rate are computed using the standard error approach. The a' priori error is based upon nominal pretest conditions whereas n' posteriori error is based upon actual test conditions.

Data evaluations are enhanced by the flexible display of either sensor variables or various computed values in tabular or graphical form on the computer terminal. Data is recorded on magnetic tape to preeent loss

, during the testing. All data is stored on the computer systems in use with retrieval capability to any desired dats base throughout the testing.

Temperature, pressure and humidity data are entered interactively via the computer terminal at 15 minute intervals. Computer verification and checking routines supplement data verification by the data acquisition team. Modifications are promptly made when errors are detected. Prior to issuance of this report, further extensive data verification has been performed.

The computer generated reports based upon verified data substantiate for both the ILRT and .CLRT that a successful test has been completed in accordance with 10 CFR 50, Appendix J.

D. Error Analysis Three types of error analysis are performed using the Ebasco ILRT computer program. These types are s' priori instrument loop error, a' posteriori instrument loop error and a statistical regression confidence inte rval .

The a' priori instrument loop error is based upon the standard error approach in which individual contributions of the various sensors and dis-play equipment are added to provide the worst possible error. Additional conservatism is added by not taking credit f'or any error cancelling terms generated by multiple sensors of the same variable. This error is computed l

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to a 95% confidence. Prior to the test, this a' priori loop error verifies that the instrumentation system is sufficiently sensitive to measure leakage rates in the range desired. The calculated a' priori instrument loop error is 0.052%/ day at a 95% confidence level.

The a' posteriori instrument loop error is also based upon the standard error approach and is computed to a 95% confidence. No simplifying assumptions other than constant containment. free volume are made in the derivative calculations for parameter sensitivity in the standard error formula.

Instrument loop errors are computed from containment conditions once variable 4

bias has been compensated. This leakage error due to instrumentation is i

then reported for both the ILRT and CLRT as the maximum probable instrument loop error. The calculated maximum prob'ble a instrument error is-0.021%/ day at a 95% confidence level.

A statistical regression confidence interval is generated for the first order regression line of the simple total-time leak rates. The significance of this interval is that 95% of all analyzed leakage rates measured fall within this interval when transformed to frequency space. The 95% regress' ion confidence interval for the ILRT is 0.014%/ day.

E. Description of Tests Interpretation of the final analysis of test data show results well wi- .n the specified limits for this containment as delineated in Section V (u. Lusions) of this report.

J The containment was made ready for the Integrated Leak Rate Test with the Containment Structural Integrity inspection performed in accordance with procedure 3PT-A2 " Containment Structural Inspection" on July 26, 1978. The containment was closed for the ILRT on 2030 hour0.0235 days 0.564 hours 0.00336 weeks 7.72415e-4 months s- 7/26/78 with pressurization starting at 2130 hours0.0247 days 0.592 hours 0.00352 weeks 8.10465e-4 months . Pressurization was accomplished using up to nine (9) mobile air compressors with a total capacity of approximately 10000 scfm.

These units were connected to the containment as shown in Figure 3. Four of nine compressors were secured at 0015 hours1.736111e-4 days 0.00417 hours 2.480159e-5 weeks 5.7075e-6 months 7/27/78 to reduce the pressuriz- I ation rate to allow containment entry for inspection purposes. At 0100 hours0.00116 days 0.0278 hours 1.653439e-4 weeks 3.805e-5 months l I

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the containment entry was made with no signs of abnormalities, oil carry-over, smoke or water vapor observed. During the containment entry it was noted that one of the personnel airlock inner bulkhead shaf t seals was leaking. The outer door of the airlock and outer bulkhead was determined leak tight and this became the ILRT houndary. The containment entry was completed at 0200 hours0.00231 days 0.0556 hours 3.306878e-4 weeks 7.61e-5 months with pressurization at a higher rate resumed. ,

Pressurization was secured at 1500 hours0.0174 days 0.417 hours 0.00248 weeks 5.7075e-4 months with 45 psig pressure in the containment vessel. Af ter an appropriate stabilization per'od, the apparent leakage rate was determined to be .147./ day, or about twice allow-able, at 0000 hours0 days 0 hours 0 weeks 0 months 7/28/78 with active leak survey teams attempting to find the excess leakage. At this time, it was noted that two of the ten dewcells began to exhibit noisy signals.

During the next 48 hours5.555556e-4 days 0.0133 hours 7.936508e-5 weeks 1.8264e-5 months , the leak survey teams continued to attempt to identify the excess leakage. Many systems were temporarily blanked-off to look for possible leaks with no apparent decrease in leakage rate. By 0400 hours0.00463 days 0.111 hours 6.613757e-4 weeks 1.522e-4 months 7/30/78, it was identified that the leak was somewhere in the

33 and #34 containment fan cooler service water supply and return lines inside the containment. Isolation of this leakage was started and most of the temporarily blanked systems vera unblanked. Also daring this time period, seven of the ten dewcells in the containment (numbers 1, 2, 3, 4, j 5, 6 & 7) were exhibiting noise on the signal. The five dewcells exhibiting the worse noise were deleted from analysis of the leakage rate. It was also i noted during this time that the primary pressure instrument did not exhibit as good repeatability as the backup sensor. The pressure drop sensed by the two instruments was identical over long periods of time (1-2 hours) but over 15 minute periods, the primary sensor appeared to occasionally stick on one value ,

Isolation of the #33 and #34 containment fan cooler service water supply and return lines was completed on 1630 hours0.0189 days 0.453 hours 0.0027 weeks 6.20215e-4 months , 7/31/78 with the official start of the 24 hour2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months ILRT initiated at that time. Data was accumulated for 24.25 hours2.893519e-4 days 0.00694 hours 4.133598e-5 weeks 9.5125e-6 months and acceptable leakage was measured. The ILRT was completed at 1645 hrs on 8/1/78.

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,- e Chemistry and Health Physics sampled the containment air volume prior to ini-tiation of the Controlled Leak Rate Test (CLRT). The mass flow meter was adjusted to 7 scfm bleedoff flow. This flow is approximately equal to the containment design leakage rate of 0.1%/ day.

The CLRT commenced at 1830 hours0.0212 days 0.508 hours 0.00303 weeks 6.96315e-4 months on 8 /1/78 with stable conditions inside the containment. At the start of the CLRT, the backup pressure indicator was selected for use due to its better repeatability. The CLRT was completed at 0145 hrs on 8/2/78.

Depressurization of the containment commenced at 0255 hrs on 8/2/78.

Atmospheric pressure was reached at 0015 hrs on 8/3/78. An internal '

inspection of the containment was completed at 1000 hours0.0116 days 0.278 hours 0.00165 weeks 3.805e-4 months on 8/3/78. During the inspection it was noted that the motor cooler service water vent and drain valves on #33 and #34 Containment Fan Cooler Units were lef t open during the ILRT. This was the source of leakage in the service water system.

A summary of the Containment ILRT boundary changes and subsequent actions are given below:

a) The No. 31 Reactor Coolant Pump seal injection valve No. 250A was removed prior to the test and the line capped. Subsequent to the ILRT the valve was re-installed and a Type C leak rate test was performed. Zero leakage was detected.

i b) The personnel lock boundary during the ILRT was the outer bulkhead due to a shaft seal leak on the inner bulkhead. Subsequent to i the ILRT, a pre-repair Type B leak test was performed with 0.00893 scfm leakage detected. The mechanical stuffing box on the shaft seal was tightened with zero leakage detected in the post-repair i Type B leak test.

c) The Weld Channel and Penetration Pressurization lines to the air-locks were capped in order to isolate the airlocks from other penetrations in the system. This was necessary since the Pressuriza-tion System was not in service during the ILRT and leakage was sus-pected through the personnel lock inner containment-side door seal.

Capping of the Weld Channel supply lines to the airlocks allowed credit to be taken for the double door seals which would be the sys-i tem boundary during norn.a1 and accident plant conditions. Isolation valves have been installed to allow this system to be aligned in this manner during future ILRTS.

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d) The station air penetration ILRT boundary was moved to turbine hall isolation valves SA-10 due to air leakage detected at the bleedoff point that was attributed to the Contairunent Isolation Valve s . Subsequent to the ILRT, this leakage was determined to

be from the station air system via station aie valve SA-11. No repairs on the Contairunent Isolation Valves SA-24 were made and zero leakage was detected.

e) The #33 and #34 Containment Fan Cooler Service Water supply and return lines were isolated outside of the containment due to a leak inside. This was performed by blar. king off valves SWN 41 and 44 (service water supply and return isolation valves) and relief valve SWN42 (#34 Fan Cooler service water inlet relief) . Sub -

sequent to the ILRT, the motor cooler vent and drain valves were found open, thus explaining the leakage path. Relief valve SWN-42 was repaired and the service water leaders were tested with water in accordance with Technical Specifications with acceptable in-leakage determined.

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I IV. RESULTS AND VERIFICATION The Type A Integrated Leakage Rate Test was conducted for a period of 24.25 hours2.893519e-4 days 0.00694 hours 4.133598e-5 weeks 9.5125e-6 months with a total of 98 samples of data sets taken. The containment pressure at the end of the ILRT was 58.396 psia. Since the backup pressure indicator was used during the CLRT in an attempt to improve repeatability, the backup pressure indicator was used during final ILRT calculations.

Changing from tne primary to the backup pressure indicator did not change the calculated leakage rates but did improve pressure loop error from .0020 psia to .0012 psia. As noted in Section III.e), seven of the ten dewcells exhibited noisy signals subsequent to pressurization. The five worst dew-cells (#1, #2, J3, #6 and #7) were deleted from the analysis as they all exhibited loop errors in excess of four times the quoted loop repeatability.

Deweells #4 and #5 exhibited loop errors approximately four times the quoted loop repeatability while Dewcells #8, #9 and #10 exh'ibited loop errors equal to the quoted loop repeatability. Dewcells #4 and #5 were not deleted as this would leave no humidity sensors active in the upper area of the contain-ment. The Chauvenet Rejection criteria was applied to the 98 samples with samples 2 and 3 showing excessive deviation based upon total time leak rates These samples were rejected from analysis. The results of the computed total time least squares fit of the data revealed a leakage rate of -0.0037./ day by weight, a total time simple leakage rate of 0.007%/ day by weight and a fitted mass point leakage rate of -0.005%/ day by weight.

The maximum probable instrument loop error for the ILRT was 0.021%/ day by weight with the largest contributor to this error caused by the Dewcells.

The 95% statistical regressicn confidence interval for the ILRT was 0.014%/ day by weight. For conservatism, these leakages rates are not corrected from test pressure to peak accident pressure.

Following satisfactory completion of the ILRT, a 7.25 hour2.893519e-4 days 0.00694 hours 4.133598e-5 weeks 9.5125e-6 months CLRT was performed. This test was conducted by superimposing e known leak rate approximately equal to the containment design leakage rate of 0.1%/ day by f weight. The mass flow meter reading was recorded at 15 minute intervals and averaged over the duration of the test to give 7.12 scfm. This is t equivalent to 0.1037./ day by weight leakage for the given conditions of containment pressure and temperature during the test. The Chauvenet Rejection criteria was applied to the 30 samples with samples 2 and 3 showing excessive deviatiou basea upon total tbme leakage rates. The measured total time least squares fit of the data was .103%/ day by weight, a total time simple leakage rate of .097%/ day by weight and a fitted mass 4- point leakage rate of .1307./ day by'veight. Thus, the sbmple total time leakage rate and the least squares fit of the total time leakages give very good agreement with the calculated superimposed leakage. Agreement with the fitted mass point was not as good due to the noisy nature of the first few data sets caused by the deweell sensor problems mentioned above,and since the Chauvenet Rejection criteria was not used on mass point calculations.

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l V. CONCLUSIONS l

The high containment leakage measured initially has been identified due to an improper valve lineup on a closed seismic Class I post-accident system inside the containment. During normal operation these service water vent and drain valves would be closed and the system would be in operation. During accident conditions any anomalies in the Containment Fan Cooler Service Water Supply System would result in service water leakage out of the system since the service water header pressure is higher than post-accident containment pressure.

The Integrated Leakage Rate Test at P, (40.6 psig) provided acceptable results as evidenced by the computer printout and graphs in Appendix A of this report. The measured leak rate is well within the specified limits.

The acceptance criteria for the ILRT is as follows:

a) The maximum allowable operational leak rate shall not exceed 75%

of the Ccatainment Design Leakage Rate of 0.1%/ day by weight at a pressure of not less than 40.6 psig. This is equivalent to 0.075%/ day by weight.

As shown in Section IV, the measured leakage rate for the contain-ment was -0.003%/ day by weight at a test pressure of 43.6 psig. If the maximum probable instrument loop error is added to this value, the leakage rate including instrument error would be 0.018%/ day by weight at a 95% confidence level. If the 95% statistical regression confidence interval is added to the measured leakage rate, the leakage rate would be 0.011%/ day by weight at a 95% confidence

interval. Both of the abov,e values are less than the acceptance criteria of 0.075%/ day by weight.

b) The accuracy of the ILRT shall be verified by a supplemental test which confirms the accuracy of the ILRT by verifying that the difference between the containment leakage rate measured during the supplementa' est and the ILRT is within 25% of the containment design leakage rate of 0.1%/ day by weight. This is equivalent to 0.025%/ day by weight.

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The measured leakage during the CLRT was 0.103%/ day by weight with a superimposed leakage equivalent to 0.1037./ day by weight. The measured net CLRT containment leakage was therefore 0.0%/ day by weight. The measured ILRT leakage rate was -0.0037/ day by weight, thus giving a difference between the CLRT and ILRT measurements of 0.0037./ day by weight. This difference between the CLRT and *.LRT measurements is within the acceptance criteria and the accuracy of the ILRT has been verified.

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POWER AUTHORITY OF THE STATE OF NEW YORK I

INDIAN POINT UNIT NO. 3 ILRT :

RTD LOCATION / VOLUME I

RTD 17 VOLUME 722,850 CU. FT. 7 RTD'S

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RTD'S AT EL. 98'-0" RTD 2125 VOLUME 341,954 CU. FT E L. 81'-6" 5-RTD'S

-AT EL. 71'-0" RDT 26-30 VOLUME 428,715 CU. FT.

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POWER AUTHORITY OF THE STATE OF NEW YORK INDIAN POINT UNIT NO. 3 ILRT DEWCELL LOCATION / VOLUME DEWCELLS 1-4 VOLUME 1,016,284 CU. FT. _ 4 DEWCELLS AT EL. 210'-0" EL.165'-0" POLAR -

CRANE DEWCELLS 5-7 VOLUME 1,014,047 CU. FT.

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POWER AUTHORITY OF THE STATE OF NEW YORK -

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APPENDIX A Computer-Generated Report i

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Ih'IEGRATED LEAK RATE TEST (ILRT) i

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O D F T T . A C E S .T D E M T R A N E EAN E MLI EIE R

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RRA + 0 77P ES 0. 0 . EP 44 PP 0 1 P H L Y EIT 0 TNO L KTTSEN 0 775 20 ANI sT0 E - 0 T3 S EFO U T 0 N4 SIS 1 HCC J EINLAf T E I I 25 L I Rf A +N 09 R E 0 C8 R E0R N N - A ROR O FAE KL 3C aa - 5 F

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OBSERVATION NUMBER -

1 10 19 28 37 46 55 64 7 31,34- ........i........i........i........i........i........i........i........3........2 8 91

........i...... -

COMPUTED LEAK RATES RELATIVE TO LIMITS' XX STATISTICAL TOTAL TIME LERK RATE 28.19- ---

CONTAINMENT DESIGN LERK RATE NRC TECHNICAL SPECIFICATION LIMIT x-u INSTRUt1ENT ERROR LIllIT REDUCTION w i COMPtJTED FIRST ORDEi ETJ9 TION FIT c.D 24 83-w W

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-2 00- i i i i i i i i i i i 0 120 240 360 480 600 720 840 960 1080 1200 1320 1440 TIME IN MINUTES

OBS7VRTION nut ER I 2 o,1400 ........0........9........8........7.,

1 1 3 4 5 64 7 6........5.................3........2........1 8 9 COMPUTED LEAK RATE FIT RELATIVE TO LIMITS CONTAINNENT DESIGN LEAK RRTE 0.1250 - --

N z Rw;Cq, Tw..;

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-0 0100- i i i i i i i i 0 120 i i i 240 360 480 600 720 840 960 1080 1200 1820 1440 TIME IN MINUTES

OBSE'/RTION NUME R 1 10 19 28 37 46 55 64 73 82 91 87 20 '''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''

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OBSE sVRTION NUMbtiR -

1 10 19 28 37 46 55 64 73 82 91 0.730 +1'''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''' '

COMPUTED FIT RELATIVE TO CRITICAL LIMIT XX SIMPLE TOTAL TIME LEAK RATE 0 551- m-= INSTRUMENT ERROR LIMIT REOUCTION v v C9:f UTED ! IF.CT OF.DEF. U;UI.TI'JM II-GREEN 1CTA33N 10 GThTICTICHL REJECTIlN o

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0 120 240 360 480 600 720 849 960 1080 1200 1320 1440 TIME IN MINUTES

OBS..tVRTION NUMudR .

I 10 19 28 37 46 55 64 73 82 91 58 450 ' ''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''' .

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OBSE..VRTION NUMB R ,

1 10 19 28 37 46 55 64 73 82 91 0 4500 ''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''e''''''''''''' .

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VARIADLE TADLE

SUMMARY

SAMPLE DELTA TEMP 1 TEMP 2 TEMP 3 TEMP 4 TEMP 5 TEMP 6 NUMBER HINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 0 86.640 86.970 86.530 86.630 86.280 87.340 2 IS 86.660 86.940 86.500 86.620 86.260 87.380 3 30 86.640 86.960 86.500 86.610 86.260 87.330 4 45 86.610 86.940 86.5GO 86.610 86.280 87.340 5 60 86.640 86.950 86.490 86.610 86.270 87.350 6 75 86.600 86.950 86.510 86.610 86.240 87.330 7 90 86.610 86.940 86.500 86.620 86.260 87.300 8 105 86.620 86.930 86.490 86.590 86.270 87.330 9 120 86.560 86.940 86.510 86.600 86.240 87.310 3

10 135 86.610 86.900 86.510 86.600 86.240 87 310 l

11 150 86.610 86.910 86.490 86.590 86.250 87.310 12 165 86.600 86.940 86.500 86.600 86.230 87.300 13 180 86.610 86.910 86.480 86.600 86.230 87.300 14 195 86.590 86.890 86.480 86.590 86.260 87.300 15 210 86.620 86.900 86.460 86.580 86.220 87.300 16 225 86.600 86.920 86.460 86.580 86.230 87.300 i 17 240 86.560 86.9 0 86.490 86.570 86.220 87.300 18 255 86.590 86.900 86.460 86.600 86.220 87.290 19 270 86.600 86.890 86.460 86.580 86.220 87.280 20 285 86.600 86.910 86.460 86.570 86.220 87.320 i 21 300 86.550 86.860 86.450 86.570 86.220 87.300 1

22 315 86.620 86.880 86.440 86.590 86.220 87.300 23 330 86.550 86.870 86.460 86.570 86.230 87.260 24 345 86.610 86.880 86.460 86.560 86.220 87.290 25 360 86.600 86.890 86.460 86.560 86.220 37.300 26 375 86.580 86.890 86.450 86.600 86.190 87.2s0 27 390 86.560 86.870 86.440 86.570 86.210 37.260 28 405 86.570 86.870 86.470 86.560 86.220 87.270 29 420 86.560 86.900 86.450 86.550 86.200 87.260 30 435 86.570 86.880 86.460 86.540 86.240 87.280 31 450 86.570 86.860 86.450 86.560 86.200 87.260 32 465 86.530 86.880 86.460 86.550 66.200 87.250 ;

33 480 86.540 86.850 86.430 86.530 86.190 87.260 39 495 86.510 86.860 86.420 86.540 86.170 87.250 I' 35 510 86.580 86.860 86.430 86.550 86.180 67.250 1 36 525 86.550 86.860 86.430 86.520 86.170 87.250 l 37 540 86.490 86.850 86.420 86.540 86.190 87.240 l 38 555 86.550 86.850 86.420 86.530 86.180 87.230 39 570 86.510 86.840 86.410 86.510 86.170 87.230 to 585 86.530 86.820 86.400 86.540 86.180 87.220 41 600 86.460 36.830 86.420 86.500 86.150 87.220 42 615 86.520 86.820 86.400 86.500 86.160 87.220 43 630 86.470 86.840 86.400 86.520 86.160 87.220 44 645 86.440 86.790 86.380 86.510 86.140 87.210 45 660 86.480 86.800 86.400 86.510 86.150 87.180 46 675 86.480 86.810 86.400 86.480 86.140 87.200 47 690 86.500 86.800 86 390 86.490 86.150 87.190 48 705 86.460 86.800 86.390 86.480 86.110 87.170 49 720 86.460 86.780 86 370 86.480 86.140 87.190 50 735 86.420 86.790 36.390 86.470 86.130 87.180

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l-VARIABLE TADLE

SUMMARY

SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 TEMP 12

, NUHDER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 0 86.620 87.480 87.030 87.330 87.110 87.460 2 15 86.610 87.470 87.110 87 370 87.110 87.410 I

3 30 86.620 87.450 87.020 87.330 87.100 87.440 4 45 86.600 A7.480 87.000 87.330 87.100 87.430 5 60 86.610 87.500 87.040 87.320 87 090 6 87 380 I 75 86.610 87.460 87.030- 87 330 87.100 87.370 7 90 86.590 87.480 87.030 87 330 87.090 87.400 8 105 86.590 87.430 87.030 87 320 87.110 87.450 8

9 120 86.590 87.460 87.010 87 310 87.060 87 350 to 135 86.600 87.420 87.030 87 320 87.070 87.430 11 150 86.560 87.430 87.020 87.280 87.080 87.400 12 165 86.580 87.430 87.070 87 270 87.060 87 370 13 180 86.570 87.420 87.010 87.290 87.060 87 380 14 195 86.570 87.430 87.000 87.280 87.060 87.410 15 210 85.560 87.470 86.980 87.290 87 050 87 370 16 225 86.570 87.410 87.000 87 280 87.060 240 87 350 17 86.550 87.420 87.040 87 300 87.050 87 390 18 255 86.560 87.410 86.990 87 280 87.060 87.330 ,

19 270 86.540 87.420 86.970 87.290 87.060 87.380 20 285 86.550 87.440 86.970 87 290 87.060 87.350 21 300 86.550 87.410 87.060 87.280 87.060 22 87 350 315 86.550 87.410 86.980 87.260 87.040 87.290 23 330 86.550 87.400 87.050 87.280 87.060 87 370 24 345 86.560 87.410 86.970 87.250 87.050 25 87.380 360 86.540 87.400 86.990 87.300 87.060 87.330 26 375 86.530 87.410 87.010 87 250 87.040 27 87.350 390 86.530 87.410 86.970 87.240 87.030 87 300 28 405 86.520 87.380 86.990 87.290 87.050 420 87 370

- 29 86.520 87.410 86.980 87.250 87.030 87.370 y 30 435 86.520 87.390 86 970 87.250 87.040 87 350 450 86.520

. 31 87.390 87.030 87.270 87.030 87 360 32 465 86.500 87.380 86.960 87.250 87.030 87 300 33 480 86.500 87.400 87.000 87.270 87.020 87 380 34 495 86.500 87.390 86.960 87.200 87.000 87 350 35 510 86.530 87.390 86.980 87.240 87.010 87 320 36 525 86.500 87.380 86.950 87.230 87.000 87 320 37 540- 86.510 87.370 86.980 87.240 87.010 87 310 38 555 86.480 87.350 87.000 87.210 87.010 87.330.

39 570 86.490 87.350 86.940 87.230 87.000 87.320

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VARIABLE TABLE SUHMARY SAMPLE DELTA TEMP 19 TEMP 20 TEMP 21 TEMP 22 TEMP 23 TEMP 24 NdMBER HINS DEC. F DEC. F DEC. F DEG. F DEG. F DEG. F 1 0 87.050 87.560 87.100 87.790 87.740 87.540 2 15 87.120 87.610 87.110 87.760 87.600 87.490 3 30 87.040 87.550 87.080 87.770 87.620 87.540 4 45 87.030 87.600 87.090 87.150 87.570 87.510 ,

5 60 87.130 87.540 87.090 87.730 87.530 87.500 6 75 87.110 87.540 87.090 87.750 87.540 87.500 7 90 87.040 87.560 87.100 87.730 87.550 87.530 ,

8 105 87.040 .87.550 87.060 87.750 87.590 87.500 9 120 87.020 87.560 87.060 87.710 87.590 87.500 10 135 87.020 87.500 87.040 87.750 87.570 87.480 e 11 150 87.030 87.510 87.060 87.740 87.700 87.490 12 165 87.050 87.520 87.060 87.710 87.540 87.470 13 180 87.070 87.550 87.070 87.730 87.530 87.460 g 14 195 87.010 87.530 87.060 87.750 87.600 87.460 l 15 210 87.000 87.530 87.040 87.730 87.550 87.450 l 16 225 37.030 87.510 87.030 87.750 87.530 87.470 , ;

l 17 240 86.990 87.470 87.030 87.720 87.600 87.470 18 255 86.980 87.500 87.040 87.720 87.520 87.430 l 19 270 87 030 87.520 87.040 87.720 87.500 87.450 ,

t 20 285 87.020 87.530 87.030 87.720 87.470 87.450 l 21 300 86.990 87.520 87.040 87.720 87.510 87.480 22 315 87.050 87.520 87.020 87.700 87.520 87.450 23 330 86.980 87.490 87.010 87.700 87.520 87.460 24 345 87.010 87.510 87.020 87.750 87.530 87.450 l 25 360 86.980 87.553 87.030 87.700 87.530 87.450 '

1 26 375 87.000 87.540 87.020 87.710 87.550 87.450 27 390 86.990 87.520 86.980 87.700 87.510 87.450 28 405 86.980 87.520 87.010 87.710 87.490 87.420 29 420 87.020 87.480 87.020 87.720 87.570 87.410 30 435 86.950 87.500 87.010 87.720 87.520 87.410 31 450 86.993 37.480 87.010 87.710 87.540 87.410 32 465 86.950 87.460 87.000 87.710 87.610 87.400 33 480 86.940 87.500 86.990 87.690 87.540 87.440 34 495 86.950 87.480 86.970 87.710 87.610 87.410 35 510 87.000 87.500: 86.980 87.710 87.480 87.400 36 525 86.950 87.470 86.980 87.690 87.530 87.400 37 540 86.950 87.460 86.990 87.690 87.490 87.400 j 38 555 86.990 87.500 86.960 87.670 87.590 ~87.390 39 570 86.940 87.460 86.970 87.710 87.460 87.400 to 585 86.960 87.460 86.970 87.700 87.520 87.390 41 600 86.960 87.420 86.970 '87.720 87.580 87 390 42 615 86.900 87.430 86.960 07.690 87.530 87.380 43 630 86.950 87.450 86.980 67.710 87.510- 87.380 44 645- 86.910 87.450 86.950 87.700 87.640 87.360 45 660 86.900 87.430 86.960 87.700 87.550 87.360 46 675 86.920 87.430 86.930 87.680 87.610 87.320 47 690 86.900 87.420 86.940 87.680 87.630 87.350 48 705 86.910 87.420 86.930 87.640 87.570 87.340 . -

49 720 86.890 87.400 86.940 87.660 87.580 87.340 50 735 86.900 87.410 86.940 87.660 87.540 87.330 -

_3 e

VARIADLE TABLE

SUMMARY

1 SAMPLE DELTA TEMP 19 TEHP 20 TEMP 21 TEMP 22 fEMP 23 TEMP 24 I

NUMBER HINS DEG. F DEG. F DEG. F DEG. F DEC. F DEG. F 51 750 86.880 87 390 86.930 87.680 87.610 87.330

52 765 86.880 87.390 86.940 87.650 87.620 87.310 53 780 86.880 87.390 86.910 87.660 87.590 87 340 54 795 86.870 87 380 86.910 87.660 87.550 87.320 55 810 86.860 87 390 86.910 87.650 87.580 87 320 56 825 86.860 87 390 86 910 87.640 87 540 87 300 57 840 86.830 87 350 66.900 87.640 87.440 87.310 58 855 86.820 87.370 86.890 87.620 87.570 87.270 '

59 870 86.840 87 360 86.880 87.630 87.510 87.280 60 885 86.860 87.350 86.870 87.630 87.600 87.280 4 61 900 86.820 87.340 86.870 87.600 87.590 87.260 62 985 86.820 87.340 86.860 87.620 87.470 87.280 63 930 86.850 87.330 86.870 87.610 87'.500 87.270 ,

64 945 86.810 87.330 86.860 87.590 87.540 87.290 65 960 86.830 87.310 86.860 87.610 87.520 87.270 66 975 86.800 87 320 86.860 87.600 87.520 87.260 ,

67 990 86.810 87.290 86.840 87.630 87 520 87.250 68 1005 86.810 87 300 86.850 87.600 87.490 87.240 69 1020 86.770 87.280 86.840 87.590 87 330 87.240 ,

70 1035 86.790 87.340 86.820 87.590 87.500 87.250 71 1050 86.780 87 300 86.830 87.610 87.370 87.230

72 1065 86.760 87.270 86.820 87.570 87.460 87.210 .

73 1080 86.720 87.270 86.830 37.580 87.480 87.240 74 1095 86.770 87.260 86.810 87.570 87.480 87.210 75 1110 86.760 87.260 86.810 87.570 87.500 87.210 76 1125 86.750 87.260 86.810 87.550 87.460 87.200 77 1140 86.770 87.270 86.810 87.570 87.500 87.200

78 1855 86.750 87.250 86.800 87.560 87.430 87.180 79 1870 86.750 87.280 86.810 87.590 87.540 87.190 80 1185 86.740 87.260 86.790 87.570 87.470 87.190

v. 81 1200 86.760 87.230 86.800 87.550. 87.440 87.210 ,

82 1215 86.720 87.200 86.770 87.570 87.290 87.210 83 1230 86.760 87.240. 86.790 87.520 87.250 87.170 84 1245 86.750 87.220 86.770 87.470 87.450 87.160

85 1260 86.740 87.270 86.780 87.560 87.320 87.160 86 1275 86.710 87.210 86.760 87.550 87.400 87.170 87 1290 86.720 87.200 86.770 87.550 87 350 87.160 ,

88 1305 86.750 87.200 86.740 87.540 87 360 87.150 89 1320 86.700 87.200 86.750 87.530 87 360 87.150 90 ~ 1335 86.680 87.170 86.740 87.500 87.400 87.140 91 1350 86.700 87.180 86.749 87.510 87.440 87.120 92 1365 86.700 87 170 86.720 87.520 87.470 87.130 93 1380 '86.660 87.170 86.710 87.510 87.450 87.120 94 1395 86.670 87.170 86.710 87.480 87.420 87.110 95 1910 86.600 87.170 86.710 87.490 87 350 87.120 96 1425 86.650 87.160 86.720 87.520 87.400 87.100 97 1440 86.640 87.170 86.680 87.510 87.450 87.090 98 1455 86.670 87.170 86.700 87.480 87.430 87 090 END OF TABLE

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VARIAULE TABLL SUMMANT .

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SAMPLE DELTA TEMP 25 TEMP 26 TEMP 27 TEMP 28 TEMP 29 TEMP 30

NDMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F

1 0 87.100 87 320 87.410 87.910 87.370 87.180 2 :15 87.120 87.330 87.410 87,920 87 350 87.190 3 30 87.100 87 310 87.410 87.930 87.380 87.180 ,

8 4 45 87.110 87 320 87.400 87.900 87.360 87.200 5 60 87.110 87 310 87.430 87.830 87.330 87.190 6 75 87 120 87 300 87.430 87.890 87.330 87.150 e, 7 90 87.110 87.290 87.P10 87.850 87.360 87 180 ,

8 105 87.120 87 300 87.430 87.890 87.330 87.170 9 120 87.110 87 300 87.420 87.820 87.330 87.170 e 10 135 87.130 87 300 8 .430 87.850 87 310 87.150 3 11 750 87.100 87.290 87.400 87.920 87.320 87 130 12 165 87.110 87 300 87.400 87.880 87 300 87.140 s

13 180 87.110 87.300 87.390 87.860 87.290 87.160 '

14 195 87 080 87 300 87.410 87.900 87 300 87.130 15 210 87.080 87.29G 87.380 87.820 87.270 87.140 16 225 87.060 87.290 87.400 87.900 87.270 87 140 17 240 87.050 87 300 87.390 87.900 87 280 87.130 18 255 87.080 87.290 87.390 87.910 87.280 87.150 t e 19 270 87.090 87.290 87.380 87.910 87 270 87.130 20 285 87.050 87 300 87.390 87.890 87.260 87.130 21 300 87.070 87.290 87.400 87.920 87.250 87.130 -

- 22 315 87.080 87 290 87.390 87.910 87.260 37.130 23 330 87.080 87.290 87.400 87.900 87.250 87.110 24 345 87.060 87.290 87.360 87.880 87.240 87.120 25 360 87.070 87.290 67.400 87.890 87.240 87.120 26 375 87.060 87 300 87.390 87.910 87.220 87.130 27 390 87.050 87 280 87.370 87.910 87.230 87.130 l 28 405 87.080 87 280 87.370 87.860 87.250 87.140 29 420 87.060 87.290 87.350 87.910 87.243 87.120 30 435 87 070 87.280 87.370 87.840 87.230 87.120 .

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3 VARIABLE TABLE SUMMART e t SAMPLE DELTA IIUM 6 IlUM 7 ItUM 8 IlUM 9 IlUM 10 .

NUMBER HINS FRACTION FRACTION FRACTION FRACTION FRACTION o I O DELETED DELETED 0.621 0.633 0.631 g 2 15 DELETED DELETED 0.689 0.633 0.631 3 30 DELETED DELETED 0.616 0.633 0.631 4 45 DELETED DELETED 0.687 0.632 0.635 g 5 60 DELETED DELETED 0.617 0.634 0.629 6 75 DELETED DELETED 0.620 0.623 0.627 7 90 DELETED DELETED 0.625 0.634 0.634 g 8 105 DELETED DELETED 0.621 0.63S 0.633 9 120 DELETED DELETED 0.621 0.641 0.633 10 135 DELETED DELETED 0.624 0.631 0.632 e il 150 DELETED DELETED 0.623 0.645 0.636 12 165 DELETED DELETED 0.623 0.634 0.633 13 180 DELETED DELETID 0.622 0.635 0.627 ,

14 195 DELETED DELETED 0.619 0.624 0.638 15 210 DELETED DELETED 0.621 0.633 0.628 16 225 DELETED DELETED 0.620 0.633 0.633 3 17 240 DELETED DELETED 0.627 0.64) 0.635 18 255 DELETED DELETED 0.620 0.637 0.644 19 270 DELETED DELETED G.619 0.642 0.632 3 20 285 DELETED DELETED O.617 0.635 0.633 '

21 300 DELETED DELETED 0.621 0.637 0.627 a 22 315 DELETED DELETED O.626 0.632 0.634 .

23 330 DELETED DELETED 0.625 0.631 0.637 24 345 DELETED DELETED 0.621 0.614 0.633 25 360 DELETED DELETED 0.626 0.635 0.632 26 375 DELETED DELETED 0.628 0.635 0.635 27 390 DELETED DELETED 0.626 0.639 0.635

, 28 405 DELETED DELETEP 0.621 0.639 0.628 29 420 DELETED DELETED 0.626 0.635 0.636 30 433 DELETED DELETED 0.623 0.637 0.640 31 450 DELETED DELETED 0.615 0.633 0.631 s 32 465 DELETED DELETED 0.622 0.634 0.643 33 480 DELETED DELETED 0.621 0.637 0.633 34 495 DELETED DELETED 0.619 0.636 0.631 s 35 510 DELETED DELETED 0.621 0.639 0.638 36 525 DELETED DELETED 0.626 0.638 0.629 37 540 DELETED DELETED 0.623 0.643 0.647 38 555 DELETED DELETED 0.625 0.644 0.613 39 570 DELETED DELETED 0.625 0.634 0.635 40 585 DELETED DELETED 0.628 0.643 0.634 41 600 DELETED DELETED 0.624 0.636 0.644 42 615 DELETED DELETED 0.622 0.631 0.632 43 630 DELETED DELETED 0.620 0.638 0.640 44 645 DELETED DELETED 0.625 0.632 0.637 45 660 ' DELETED DELETED 0.622 0.641 0.640 46 675 DELETED DELETED 0.625 0.637 0.639 47 690 DELETED DELETED 0.625 0.619 9.638 48 705 DELETED DELETED 0.628 0.635 0.632 49 720 DELETED DELETED 0.633 :0.650 0.636 50 735 DELETED DELETED 0.627 0.640 0.641

() GP

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O 4 VARIABLE TABLE

SUMMARY

SAMPLE DELTA IluH 6 ItUM 7 ItUM 8 I!UM 9 IlUM 10 NUMBER HINS FRACTION FRACTICN FRACTION FRACTION FRACTION 51 750 DELETED DELETED 0.623 0.635 0.637 52 765 DELETED DELETED 0.625 0.634 0.642 53 780 DELETED DELETED 0.623 0.641 0.635 54 795 DELETED DELETED 0.627 0.640 0.638 55 810 DELETED DELETED 0.621 0.639 0.635 56 825 DELETED DELETED 0.627 0.629 0.632 57 840 DELETED DELETED 0.624 0.637 0.643 58 855 DELETED LELETED 0.619 0.636 0.641 59 870 DELETED DELETED 0.631 0.644 0.638 60 885 DELETED DELETED 0.626 0.641 0.638 61 900 DELETED DELETED 0.626 0.639 0.635 62 915 DELE!LD DELETED 0.627 0.634 0.647 63 930 DELETED DELETED 0.627 0.648 0.639 64 545 DELETED DELETED 0.619 0.645 0.638 65 960 DELETED DELETED 0.626 0.639 0.636 66 975 DELETED DELETED 0.629 0.647 0.640 67 990 DELETED DELETED 0.627 0.635 0.639 68 1005 DELETED DELETED 0.626 0.645 0.636

. 69 1020 DELETED DELETED 0.631 0.639 0.648 70 1035 DELETED DELETED 0.628 0.639 0.636 71 1050 DELETED DELETED 0.630 0.643 0.644 72 1065 DELETED DELETED 0.631 0.648 0.633 73 1080 DELETED DELETED 0.628 0.636 0.637 74 1095 DELETED DELETED 0.630 0.642 0.637 75 1810 DELETED DELETED 0.626 0.644 0.631 76 ll?S DELETED DELETED 0.630 0.635 0.641 77 1840 DELETED DELETED 0.624 0.635 0.639 78 1155 DELETED DELETED 0.629 0.652 0.6)$

79 1870 DELETED DELETED 0.632 0.645 0.641 80 1185 DELETED DELETED 0.632 0.650 0.638 81 1200 DELETED DELETED 0.629 0.643 0.641 82 1215 DELETED DELETED 0 630 0.635 0.638 33 1230 DELETED DELETED 0.629 0.643 0.638 84 1245 DELETED DELETED 0.633 0.649 0.638 85 1260 DELETED DELETED 0.627 0.646 0.630 86 12T5 DELETED DELETED 0.628 0.646 0.639 87 1290 DELETED DELETED 0.635 0.643 0.631 88 1305 JELETED DELETED 0.633 0.651 0.641 89 1320 '~LETED DELETED 0.635 0.643 0.640 90 1335 STED DELETED 0.629 0.642 0.644 91 1350 . .6ETED DELETED 0.631 0.651 0.644 92 1365 1'LETED DELETED 0.634 0.648 0.653 93 1380 D'LETED DELETED 0.630 0.645 0.638 4 94 1395 '.LETED DELETED 0.629 0.642 0.646 95 1410 Ot CTED DELETED 0.630 0.638 0.635 ~

96 1925 DELITED - del.ETED 0.634 0.654 0.635 97 1440 DEL 6TED DELETED 0.626 0.647 0.638

98. 1955 DELETED DFLETED 0.630 0.642 0.641 i

END OF TABLE

END OF REPORT ON CONTAINHENT LEAK RATE TEST TO NRC

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LEAK R ATE COHPUTED USIl1G TOTAL TIHE HETHOD AS NECOttHENDED BY APPENDIX J FOR to CFR 50 (REACTOR CONTAINHENT LEAKAGE TESTING FOR WATER COOLED POWER REACTORS)

TEST PERIOD STARTED AT 1830 HOURS ON AUGUST 1.1978 A LEAST SQUARES FIRST ORDi~ FIT OF LEAK RATE TO TIME SHOULD YIELD A SLOPE OF 0 AND AN INTERCEPT EQUAL TO THE LEAK R ATE AS COHP'..tD AT THE INITI AL START TIME THE EQUATION HAS THE FORM - LsST+R WHERE L - CORRELATED LEAK RATE ;

S - SLOPE OF CORRELATION T - TIME IN HOURS R - INTERCEPT LEAK RATE 1 LEAK RATE : 0.005 HOURS + 0.069 PER CENT HEAN : 0.087 PER CENT I E

I 1

INITI AL CONTAINHENT AIR WEIGHT = 747361 LBS.

FINAL CONTAINHENT AIR WEIGHT . 747143 LBS.

FITTED HASS POINT LEAK RATE IS 0.130 PER CENT PER DAT 1

CONTROLLED LEAK RATE TEST (CLRT)

SUPPLEMENTAL VERIFICATION FOR ILR'

' LEAKAGE OF .075 5 PER DAT AT 58.486 PSIA IS TX 4 Wa -ENT 10 5.20 SCFM.

SUPPLEMENTAL TEST (CLRT) DATA AND PREVIOUS ILRT RLSC &LUS INJECTED LEAKAGE HUST BE WITHIN 255 0F LA ( 1.73 SCFHt ti:F 7ERIFICATION HAXIMUM PROBADLE TEMPERATURE LOOP ERROR IS 0.008 DEGREES F.

HAXIMUM PROBABLE PRESSURE LOOP EREOR IS 0.0012 PSIA.

HAXIMUM PRODABLE HUMIDITT LOOP ERNOR IS 1.353 PERCENT.

as HAIIMUM PROBABt.E INSTRUMENT ERROR IS .0212 PERCEbT PER DAT es WITHIN A COMPUTED CONFIDENCE OF 95.00, PERCENT.

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COMPUTED LERK RATES RELATIVE TO LIMITS XX STATISTICAL TOTAL TIME LEAK RATE 14.11 - ---

CONTAINNENT DESIGN LEAK RATE NRC TECHNICAL SPECIFICATION LIMIT n-x INSTRUMENT ERROR LIMIT REDUCTION

- COMPUTED FIRST CROER EQUATICil FIT l o

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OBSEP"9 TION NUMBf '-

1 3 5 7 9 11 13 15 17 19 21 23 25 27 29 0 1200 '

COMPUTED LEAK RATE FIT RELATIVE TO LIMITS CONTAINMENT DESION LERK RATE 0 1120- --

NRC TECHNICAL SPECIFICATION LIMIT

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COMPUTED FIT RELATIVE TO CRITICAL LIMIT XX SIMPLE TOTAL TIME LEAK RATE 0.2694- m-m INSTRUMENT ERROR LIMIT REOUCTI0tl x m COMPUTED FIRST ORDER ECU;TI0f' F IT OREEf4 OCTA0011 IS ST ATISTICAL REJECTIC'l x

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OBSER TION NUMBE 1 3 6 7 9 11 13 16 17 19 21 23 26 27 29 86.80 ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' '

VOLUMETRICALLY WEIGHTED CONTAINMENT TEMPERATURE 86.77-F-

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OBSmtVATION NUMoER -

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AVERAGE CONTAINMENT PRESSURE 58.390-58.386- ,

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- - . = _ . - _ _

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s 4

VARIABLE TABLE

SUMMARY

SAMPLE DELTA AVG. TEM AVG. PRE VAP. PRE LEAK COM LEAK TRA ERROR (T)

DEG. F PSIA PSIA PER CENT PER CENT PER CENT

NUNDER HINS 0.422 0.069 0.000 0.000 0 86.709 58.391 0.00u 0.000 -

! l 2 15 86.703 58.389 0.415 0.070 58.388 0.413 0.071 0.000 0.000 3 30 86.703 0.050 45 86.703 58.387 0.419 0.072 0.055 4

0.419 0.073 0.283 0.050 5 60 86.687 58.385 15.893 0.050 86.677 58.384 0.430 0.075 6 75 0.076 1.272 0.050 0.417 7 90 86.675 58.383 -1.472 0.050 86.o66 58.383 0.416 0.077 t 8 105 0.424 0.078 0.278 0.050 9 120 86.655 58.379 -0.275 0.050 86.653 58.379 0.419 0.079 to 135 0.418 0.080 -0.569 0.050 150 86.646 58.378 -0.926 0.050 il 86.644 58.376 0.414 0.082 12 165 0.417 0.083 -0.802 0.050 13 180 86.637 58.375 -0.645 0.050 86.634 58.373 0.417 0.084

' 14 195 0.412 0.085 -0.781 0.050 210 86.627 58.373 15 225 86.626 58.372 0.415 0.086 -0.712 0.050 16 0.415 0.087 -0.629 0.050 17 240 86.620 58.371 0.050 255 86.633 58.370 0.419 0.089 -0.480 18 0.419 0.090 -0.354 0.050 19 270 86.616 58.369 0.050 285 86.607 58.367 0.419 0.091 -0.249 20 0.420 0.092 -0.158 0.050 21 -300 86.596 58.366 0.050 86.590 58.365 0.419 0.093 -0.130 22 315 0.418 0.094 -0.061 0.050 23 330 86.586 58.362 -0.033 0.050 345 86.579 58.361 0.417 0.096 24 0.425 0.097 0.046 0.050 25 360 86.575 58.360 0.074 0.050 86.573 58.360 0.420 0.098 26 375 0.428 0.099 0.136 0.050 27 390 86.565 58.358 0.154 0.050 405 86.560 58.357 0.422 0.100 28 0.426 0.101 0.185 0.050 29 420 86.555 58.356 0.181 0.050 435 86.554 58.353 0.417 0.103 30 END OF TABLE i

,Z

1. 4 4

h

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

t 1%RIABLE TABLE SUMHARY SAMPLE DELTA TEMP 1 TEMP 2 TEMP 3 TEHP 4 T*MP 5 TEMP 6 MUMBER MINS DEG. F DEG. F DEG. F DEG. T DEG. F DEG. F 1 0 86.100 86.46L 86.030 86.160 85.790 86.870 2 15 96.100 86.490 85.030 86.250 85.800 86.860 3 30 86.090 86.460 86.040 85.160 85.800 86.850 4 45 86.120 86.460 86.040 86.140 85.790 86.840 5 60 86.070 86.470 86.030 86.140 85 790 86.830 6 75 86.070 86.450 86.030 $6.110 85.760 86.820 7 90 86.P50 86.470 86.010 86.120 85.770 86.820 .

8 105 86.060 86.430 86.000 86.110 85.750 86.820 9 120 86.050 86.450 85 990 86.110 85.740 86.790 to 135 86.030 86.400 85.980 86.110 85.730 86.790 11 150 86.030 86.410 85.990 86.090 85.730 86.790 12 165 86.040 80.420 85.970 86.090 85.720 86.800 13 180 86.040 86.400 85.990 86.070 85.720 E6.780 14 195 86.010 86.400 85.980 86.060 85.730 86.780 15 210 86.000 86.400 85.960 86.080 85.710 86.780 16 225 86.t20 86.390 85.960 86.079 85.700 86.770 17 240 86.040 86.390 85.960 86.060 85.700 86.760 18 255 85.960 86.400 85.960 86.050 85.700 86.770 19 270 86.000 86.360 85.950 86.050 85.710 86.770 20 285 86.000 86.380 85 940 86.020 85.670 86.750 21 300 85.990 86.360 85.940 86.050 85.680 86.730 22 315 85.970 86 350 85.930 86.050 85.660 86.740 23 330 16.000 86.330 85.900 86.020 85.680 86.740 24 345 85.990 86 350 85.980 86.040 85.670 86.720 25 360 85.970 86.350 85.930 86.020 85.660 86.720 26 375 85.960 86.330 85.920 86.020 85.640 86 720 27 390 85.970 86.350 85.920 86.010 85.670 86.700 28 405 85.950 46.320 85.890 86.010 85.650' 86.700 29 420 85 950 86.330 85.910 85.990 85.620 86.690 30 435 85.940 86.320 85.890 86.000 85.620 86.700 END OF TABLE r

/

(* L

=

VARIABLE TABLE

SUMMARY

i SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 TEMP 12 l NUMDER HIh3 DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 0 86.130 86.990 86.630 86.900 86.6a0 87.000 2 15 86.100 86.990 86.610 86.860 86.620 86.990 3 30 86.110 86.990 86.590 86.850 86.630 87.030 4 45 86.120 86.970 86.600 86.860 86.640 86.986 5 60 86.090 86.990 86.580 86.850 86.630 86.970 6 75 86.090 86.950 86.580 86.820 86.610 86.950 7 90 86.080 86.940 86.590 86.820 86.600 8f. 960 8 105 86.070 86.940 86.560 86.810 86.580 86.930 9 120 86.070 86.930 86.570 86.840 86.600 86 910 to 135 86.050 86.910 86.560 86.810 86.590 86.930 11 150 86.040 86.910 86.540 86.790 86.590 86.920 12 165 86.040 86.940 86.540 86.790 86.560 86.880 13 180 86.040 86.910 86.540 86.790 86.590 86.910 14 195 86.050 86.890 86.540 86.780 86.550 86.870 15 210 86.030 86.900 86.540 86.790 86.550 86.900 16 225 86.030 86.910 86.520 86.770 86.550 86.910 17 240 86.040 86 900 86.500 86.780 86.580 86.910 18 255 86.030 86.910 86.510 86.760 86.550 86.890 19 270 86.030 86.900 86.490 86.750 86.530 86.920 20 285 86.010 86.870 86.530 86.760 86.540 86.880 21 300 86.010 86.850 86.500 86.760 86.530 86.870 22 315 85.990 86.870 86.480 86.750 86.520 86.810 23 330 85.970 86.870 86.470 86.730 86.5PO 86.890 24 345 85.980 86.850 86.480 86.760 86.480 86.880 25 360 85.980 86.830 86.470 86.730 86.510 86.820 86.470 86.910 j 26 375 85.990 86.840 86.460 86.720 2' 390 85.970 86.830 86.440 86.710 86.480 86.800 28 405 85.960 86.830 86.460 86.720 86.480 86.820 29 420 85.950 86.790 86.450 86.700 86.480 86.850 30 435 85.950 86.800 86.430 86.690 86.470 86.850 END OF TABLE l

e 9 D

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EOMWWWWWWWWWWWWWeemeWWWemWWWWWCW WW MQ N60000000000CC000000000000000000

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7

~

VARIADLE 7ABLE

SUMMARY

SAMPLE DELTA TEMP "9 TEMP 20 TEMP 21 TEMP 22 TEMP 23 TEMP 24 NUMDER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEC. F l 0 86.580 87.090 86.640 87.430 87.380 87.040 2 15 86.560 87.e50 86.630 87.410 87.310 87.040 3 30 86.560 87.070 86.640 87.420 87 360 87.000 4 45 86.590 87.050 86.610 87.440 87.380 87.020 5 60 86.550 87.070 86.620 87.390 87 330 86.990 6 75 86.580 87.060 86.600 87.420 87.250 86.970 7 90 86.540 87.050 86.610 87.420 87 310 87.000 8 105 86.550 87.030 86.590 87.380 87 300 86.970 9 120 86.500 87.020 86.590 87.390 87.230 86.960 10 135 86.530 87.050 86.600 87.360 87.200 86.950 11 150 86.510 87.010 86.560 87.400 87.270 86.960 12 165 86.530 87.060 86.550 87.390 87.270 86.950 13 180 86.510 86.990 86.560 87.400 87.200 86.950 i 14 195 86.550 87.010 86.540 87.400 87.280 86.940 i 15 210 86.530 87.010 86.540 87.360 87.260 86.940 16 225 86.510 87.020 86.550 87.350 87.160 86.940 s 17 240 86.490 86.980 86.530 87.360 87.200 86.910

, 18 255 86.510 87.010 86.550 87.330 87.160 86.910 19 270 86.470 86.990 86.510 87.350 87.260 86.940 20 285 86.490 87.010 86.520 87.370 87.240 86.900 21 300 86.460 86.980 86.530 87.360 87.100 86.910 22 315 86.500 86.950 86.500 87.340 87.193 86.900 l 23 330 86.450 86.960 86.500 87.290 87.240 d6.900 24 345 86.450 86.930 86.480 87.340 87.070 86.900 25 360 86.470 86.980 86,480 87.320 87.180 86.870 26 375 86.470 -86.980 86.500 87.310 87.170 86.870 27 390 86.450 86.930 86.470 87.310 87.170 86.880 28 405 86.440 86.920 86.460 87.270 87.160 86.860 1

29 420 86.440 86.940 86.470 87.320 87.080 86.830 30 435 86.410 86.930 86.480 87.290 87.250 86.830 END OF TADLE

(

1

\

0 4

/

VARIABLE TADLE

SUMMARY

SAMPLE DELTA TEMP 25 TEMP 26 TEMP 27 TEMP 28 TEMP 29 TEMP 30 NUMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F l 0 86.630 87.010 87.070 87.510 86.940 86.710 2 IS 86.640 86.990 87.080 87.560 86.920 86.720

'3 30 86.620 87.000 87.080 87.560 86.940 86.710 4 45 86.640 86.990 87.070 .87.590 86.920 86.720 5 60 86.610 86.980 87.060 87.580 86.910 86.690 6 75 86.620 86.980 87.070 87.570 86.920 86.700 7 90 86.590 86.980 87 060 87.550 86.920 86.680 8 105 86.620 86.970 87.050 87.550 86.900 86.700 9 120 86.590 86.960 87.050 87.530 86.890 86.670 to 135 86.580 85.960 87.060 87.560 86.900 86.660 11 150 86.560 86.950 87.040 87.520 86.900 86.640 12 165 86.580 86.950 B7.020 87.520 86.890 86.660 13 180 86.570 86.930 87.050 87.530 86.880 86.640 14 195 86.580 86.950 87.050 81.460 86.880 86.640 15 Pio 86.540 86.950 87.030 87.430 86.870- 86.630 16 225 86.570 86.940 87.030 87.490 86.890 86.660 17 240 86.560 86.930 87.050 87.460 86.850 86.630 18 255 86.540 86.940 87.040 87.440 86.850 86.630 19 270 86.520 86.930 87.070 87.500 86.870 86.610 20 . 285 86.550 86.930 87 020 87.490 86.850 86.630 21 300 86.540 86.920 87.010 87.470 86.850 86.610 22 315 86.510 d6.910 87.040 87.480 86.850 86.590 23 330 86.500 86.910 87.010 87.470 86.830 86.580-24 345 86.530 86.910 86.990 87.480 86.820 86.600 25 360 86.530 86.900 87.020 87.430 86.830 86.570 26 375 86.480 86.900 87.020 87.440 86.820 86.580 27 _390 86.500 86.890 87.000 87.440 86.820 86.590 28 405 86.480 86.890 87.050 87.470 86.820 86.560 29 420 86.470 86.880 87.010 87.430 86.820 86.570 30 435 86.500 86.880 97.050 87.460 86.800 86.550 END OF TADI.E

.r 1

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- I .

5 4

+

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C000000000000000000000000000000 MA UR HF 4N597479533827691153095435248612 O844877758564554555757766767677 I666666666666666666666666666666 T

C000000000000000000000000000000 NA UR

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_ A URDDDDDDDDDDDDDDDDDDDDDDDDDDDDDD V HF I 198754319986533210976521008763 988888887777777777666666665555

_ A333333333333333333333333333333 I

SS888888888888888838888888888888 EP555555555555555$55555555555555 R

P A O505050505O5O40505050505050505 TS 134679023S6R 96245780134679023 LN 111I1? 1 2222223333333444 EI

_ DM ER

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,. 4 ;

[ \

VARIABLE TABLE SOHHARY SAMPLE DELTA HUN 6 HUH 7 HUM 8 HUM 9 HUN 10 3

NUNDER HINS FRACTION FRACTION FRACTION FRACTION FRACTION 1 0 DELETED DELETED 0.631 0.648 0.643 2 15 DELETED DELETED 0.635 0.655 0.642 3 30 DELETED DELETED 0.632 0.639 0.638 4 45 DELETED DELETED 0.633 0.646 0.646 5 60 ' DELETED DELETED 0.633 0.646 0.651 6 75 DELETED DELETED 0.628 0.654 0.640 7 90 DELETED DELETED 0.631 0.653 0.640 8 105 DELETED DELETED 0.637 0.643 0.638 9 120 DELETED DELETED 0.638 0.648 0.634 10 135 DELETED DELETED 0.634 0.646 0.643 11 150 DELETED DELETED 0.632 0.650 0.642

12 165 DELETED DELETED 0.631 0.652 0.656 13 180 DELETED DELETED 0.637 0.647 0.646 14 195 DELETED DELETED 0.635 0.653 0.644

, 15 210 DELETED DELETED 0.639 0.661 0.646 16 225 DELETED DELETED 0.629 0.654 0.653 17 240 DELETED DELETED 0.635 0.646 0.645 0.661 0.638 18 255 DELETED DELETED 0.635 19 270 DELETED DELETED 0.634 0.660 0.643 20 285 DELETFn DELETED 0.6 37 0.655 0.647 21 300 DELETED DELETED 0.636 0.658 0.647 22 315 DELETED DELETED 0.637 0.651 0.657 23 330 DELETED DELETED 0.642 0.640 0.647 24 345 DELETED DELETED 0.641 0.640 0.642 25 360 DELETED DELETED 0.637 0.655 0.648 26 375 DELETED DELETED 0.641 0.653 0.641 27 390 DELETED DELETED 0.646 0.658 0.649 28 405 DELETED DELETED 0.633 0.657 0.649 29 420 DELETED DELETED 0.639 0.644 0.650 30 435 DELETED DELETED 0.633 0.650 0.639 END OF TABLE END OF REPORT ON CONTAINHENT LEAK RATE TEST TO NRC 3

i w

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4 E Q eD e 53 e m e3 es eD e3 O e3 eD W e up e el e e m e eD e e m e3 e E3 e e # E3 e m e e e s e e E3 e W e e m e e >

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ML20023A391: Difference between revisions

Latest revision as of 01:50, 21 February 2020

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4 E Q eD e 53 e m e3 es eD e3 O e3 eD W e up e el e e m e eD e e m e3 e E3 e e # E3 e m e e e s e e E3 e W e e m e e >

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