ML18024B352

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Reactor Bldg Containment Integrated Leak Rate Test for Facility,Conducted 791121-25
ML18024B352
Person / Time
Site: Browns Ferry Tennessee Valley Authority icon.png
Issue date: 02/21/1980
From:
TENNESSEE VALLEY AUTHORITY
To:
Shared Package
ML18024B351 List:
References
NUDOCS 8002260485
Download: ML18024B352 (113)


Text

TFNNESSEE VALLEY AUTHORITY DIVISION OF POMER PRODUCTION RFACTOR BUILDING CONTAIN'.TNT INTEGRATED LFAK RATE TEST BROGANS FERRY NUCLFAR PLANT UNIT 3 CONDUCTED NOVEtBER 21-25, '1979 DOCKET NUMBER 50-296 Submitted to The United States Nuclear Regulatory Commission Pursuant To Facility Operating License Number DPR-68 8002860

r

1.0 Introduction As prescribed in Browns Ferry Nuclear Plant unit 3 technical specification 4.7.A.2, the leakage of air from the boundary forming the reactor building primary containment is limited to 2 percent of containment air mass per day at the calculated peak accident pressure P

In conformance with Title 10, Code of Federal Regulations, Part 50, Appendix J, Browns Ferry technical specifications require that reactor building integrated leak rate tests be performed as part of the startup and the surveillance programs to demonstrate continuing leak-tight integrity.

An inservice reactor building containment integrated leak rate test

{CILRT) was successfully completed on Hrowns Ferry unit 3 by personnel of the Tennessee Valley Authority on November 25, 1979.

This test was conducted in accordance with a plant approved surveillance instruction, BP SI 4.7.A.2, which is on file at the plant site.

This surveillance instruction implements the requirements of Browns Ferry unit 3 technical specifications and Appendix J to 10 CFR 50.

The American National Standard for Containment Testing, ANSI N45.4-1972 and the proposed American Nuclear Society Standard for Containment

Testing, N-274

, provided guidance for the procedure implemented by the surveillance instruction.

Browns Ferry unit 3 is a boiling-water reactor employing a steel pressure suppression containment and rated 3,293 megawatts thermal.

The Final Safety Analysis Report defines the calculated peak accident pressure P

to be 49.6 psig.

The reactor building containment is divided into two ma]or compartments the drywell, enclosing the reactor and the

'I I

i

forced recirculation system, and a pxessure suppression pool chamber.

These two compartments are connected by blowdown pipes that terminate below the suppression chamber pool level.

Vacuum breakers are provided to ensure that the suppression chamber is never pressurized with respect to the drywell.

For the performance of this CILRT, these vacuum breakers were mechanically locked open to ensure pressure equalization between the drywell and the suppression chamber.

This report outlines the obgectives, principal events, and special equipment used and provides analysis of the test results for the CILRT completed on November 25 on Browns Ferry unit 3'.

2.0 Test Purpose and Results A.

Test Purpose The objective of the inservice CILRT performed on Browns Fexry unit 3 was threefold.

The principal objective was to demonstrate the leak-tight integrity of the reactor building containment for return to power operation.

For Browns Ferry unit 3, the leak-tight integxity is defined by technical specification 4.7.A.2 and the preoperational CILRT to be that the leakage:of air from containment not exceed 0.04437 percentage per hour (1.06488 percent per day) of containment air mass at a reduced pressure of P. /2.

The second ob)ective of this CILRT was to determine if any degradation of the structure forming the containment may have occurred since the performance of the preoperational CILRT.

A pretest inspection of the containment surface was performed to identify the presence of any gross deformities of the structure.

I

The final objective was to evaluate several significant changes of the equipment used to conduct the test.

These changes included additional compressed air capacity for containment pressurization and the revision of all test instrumentation to provide for the computer-directed automatic acquisition and reduction of test data.

Previously used for the unit 2 CILRT conducted in June

1978, these changes were implemented by the Tennessee Valley Authority to determine whether test accuracy could be improved substantially while reducing the time required to conduct future tests.

B.

Test Results The leakage rate measured in the 24-hour CILRT was 0.00709 percentage of containment air mass per hour (0.17014 percentage per day) at a reduced pressuxe of 25 psig.

The observed 95-percent upper confidence limit for this measured leak rate was 0.00718 percentage of containment air mass per hour (0.17236 percentage per day).

This measured leak rate renresents 15.98 percent of that'..al'lowed under t

technical specification 4.7.A.2.

k After the completion of the CILRT, a", supplemental forced leakage verification test was conducted to check the results of the CILRT.

A Forced leak of D.S6936 percentage of containment mass per day was imnosed on the containment.

Ttce leak rate measuxed for the 4-1/3-hour vertification test was 0.95442 percentage of containment air mass per day.

Agreement as prescribed by Appendix J between the CILRT and the verification test was -0.0544LT which is wel:l..

within the +0.250 L required by technical specification.

t

~J Sr

A oretest inspection of the containment surfaces revealed no abnormal degradation of the reactor. building containment structure.

No sil.nificant leakage paths other than those identified ns part oF the types B and C test program were found in the performance of the CII,RY or the supplemental verification test.

Th>> local leak rate for t'>e CRD hatch, penetration X-G, Followinp the CILRT is added to the CII'.RT results to ensure that all leo!'ath..

are accounted

"or.

The X-6 local leak rate was 0.0001,"(:PH,

~ r which does not chanpe the CILRT results

~

3.0

('onduct of Test Prior to the start oF the CILRT local leak xate tests on the contain-ment closures (hatches

~ith resilkent

. eals),

bellows, and electrical penetrations were conducted fn conformance with surveillance instruction r

BP SI 4.7.A.2.p-2. 'ocal leak rate tests on the valves forming the boundary of the primary containment were conducted in conformance with surveillance instruction BP SI 4.7.A.2.g-3.

The single personnel

'I air lock was tested separately in conformance with BF SI 4.7.A.2.g-l.

A summary of all LIRT testing performed

. ince the preoperational

(,'ILRT is included in Appendix 3 of this 'report.

The followinv is a sequence of significant events during the CILRT.

Date and Time

'Event,,

ll-21-79 1603 11-21-79 2000 11-21-79 2110 Started nrossurization of drywell.

Isolated air comoressors.

Containment pressure at 39.76 p:ia.

Completed topping off containment pressure with service air to 40.2961 psia.

r

11-21-79 2 l30 11-22-79 1800 Started stabilization period and containment leak checks.

Data being acquired every 10 minutes.

Repressurizing drywell to ensure drywell does not go below 25 psig.

Pressure in drywell at 25.2 psig.

Containment leak rate exceeding allowable limit but decreasing.

11-22-79 '105 Completed repressurizing containment to 40.3974 psia.

11-22-79 0420 Opened valve 32-1452 to provide a vent path.

Ghange to SI 4.7.A.2 was released to list 32-1452 11-23-79 0920 a.. open on valve lineup sheet-.

The existence of valves 2-1393 and 2-1390 was verified.

Previously operations reported they I

could not be found.

(They were verified in the I

proper position following the CILRT.)

11-23-79 1130 An NRC inspector discovered the drywell air compressor receivers charged at 36 psig.

The lines to the drywell were verified vented between the receiver and'he drywell.

SI 4.7.A.2 changed to allow the receivers to remain charged.

11-23-79 1500 Containment leak rate has gone slightly negative.

11-23-79 2030 Sharp drop in average temperature starting at approximately 1200 hours0.0139 days <br />0.333 hours <br />0.00198 weeks <br />4.566e-4 months <br /> noted.

Noted increase in reactor pressure vessel water il level.

Notified shift engineer to maintain constant water level.

Vj

11-23-79 2240 11-24-79 1230 Discussed reactor pressure vessel level changes with shift engineer.

He stated the loss of a 500-KVA feeder and slow transfer to a backup had caused the loss of shutdown cooling and therefore reactor water temperature increase.

Discovered the suppression chamber water level was decreasing in the CILRT computer printout and was increasing in operations readout.

A check showed the suppression chamber water level calibration data had been entered in reverse.

Recomputing the containment leak rate with the correct calibration data entry gave a positi've 11-24-79 2025 leak rate of approximately 0.03 percent per day.

The test was officially stopped.

Initiated a forced leak of approximately 324.5 SCFH through a calibrated mass flowmeter.

11-25-79 0046 Data is being ac'quired every 7 minutes.

Completed 4-1/3-hour verification test.

Agree-.

ment in accordance with 10 CFR 50, Appendix J, within 4 percent.

4.0 Measurements and Calculations A.

Test Equipment The test equipment used for the CILRT at Browns Ferry unit 3 was acquired for its improved accuracy over previous CILRT equipment.

Table 1 lists the equipment,

range, accuracy, and repeatability.

All test equipment was calibrated by'he Tennessee Valley Authority

V P'

Central Laboratories or other facilities with standards traceable to the National Bureau of Standards.

After the installation of all special test equipment inside containment, each sensor was checked for functional operation.

Upon test completion and depressurization, each sensor was again checked to ensure adherence to calibration.

B.

Sensor Location Table 2 lists the final volumetric weighting factor for each temperature and dewpoint sensor based on a 2-compartment model.

Figures l through 7 identify sensor locations.

The pressure sensors were divided up so that two sensors measured drywell oressure through pressure transmitter line PT 64-50 and two sensors measured torus pressure through pressure transmitter line PT 64-20.

A fifth pressure sensor measured the barametric pressure at the test station.

C.

Computer-Based Acquisition and Data Reduction System Containment oarameter measurements for the Browns Ferry un t 3

CILRT were made and collected by a microprocessor-based data acquisition system.

This raw data was automatically presented to a portable minicomputer system for correction to calibration curves and reduction to containment leak rate.

Statistical confidence levels of the calculated results were reported auto-matically to the test director as the data was acquired.

Figure 8

depicts the functional relationship of the acquisition and data analysis system.

All calculations performed by the minicomputer system were in conformance with the procedures outlined in ANS N-274'draft).

4

Source listings for all computer programs are on file with the Division of Nuclear Power, Controls and Test Branch, in Chattanooga, Tennessee.

Table 3 identifies the principal function of each computer program.

D.

Instrument Rejection The data presented in this report reflects the test results following the deletion of certain sensors due to equipment failure.

The following table lists the sensor deleted by location, as shown in figures 1 through 7, and the reason for the sensor being deleted.

Sensor Location RTD-4 and RTD-6 RTD-23 Discussion Due to damage to signal cables following the CILRT, a calibration check in place could not be accomplished.

Initial calibration check was out of tolerance and the sensor was deleted at the beginning HE-1, HE-7 and HE-8 of the CILRT.

Instrument response was erratic compared with known conditions in the initial stages of I

the CILRT.

The HE-7 sensor was found inoperative Pressure in post test calibration.

The HE-8 sensor was found to have a loose wire in the post test calibration.

It was suspected that the dewcell solution was disturbed on the HE-1 sensor.

During the CILRT, pressure sensor number 1

Sensor No.

1 indicated low with a continuous rising value

throughout the test.

This erratic behavior was duplicated during post test calibration at the TVA Central Laboratories.

5.0 Data Analysis The previous sections of this report have described the general test conduct, calculation methods, and test equipment.

In this section the events and problems that influenced the test results are discussed and used to dew conclusions on the performance of the Browns Ferry unit 3 CILRT.

A.

Discussion of Craphical Results Figure 9 is a graph of the calculated containment air mass for the CILRT.

The graph axes are absolute air mass versus test time.

The slope of the least squares fit line to this data is the reported leak rate.

Figure 10 is a graph of the calculated containment air mass leak rate versus test time for the CILRT.

Figure 11 is a graph of containment average pressure versus test time, and figure 12 is a graph of containment average temperature versus test time.

An abrupt change in test conditions is shown in the graphs approximately 7 hours8.101852e-5 days <br />0.00194 hours <br />1.157407e-5 weeks <br />2.6635e-6 months <br /> after the start of the CILRT.

(The test was started at approximately 1230 hours0.0142 days <br />0.342 hours <br />0.00203 weeks <br />4.68015e-4 months <br /> on November 23.)

The official test log recorded at 8:30 p.m.

on November 23 that a level change in the reactor pressure vessel was noted.

The shift engineer was contacted and he stated that the loss of a 500-KVA feeder line and a slow transfer to a backup had caused the loss of shutdown cooling and the reactor water temperature had increased accordingly.

This was reflected by the unstable containment leak rate at this point in the test and resulted in an extended test period to a,}.;low restahilization.

The graphs indicated that stabilized containment conditions and a stabilized leak rate were being approached when the effect of the loss of shutdown cooling and reinitiation of shutdown cooling created unstable conditions.

After an extended stabilization period, the containment mass 3eak rate approached a stabilized level closely approximating that observed after 6 to 7 hours8.101852e-5 days <br />0.00194 hours <br />1.157407e-5 weeks <br />2.6635e-6 months <br /> (approximately the time of loss of shutdown cooling).

8.

Instrumentation Performance The instrumentation error analysis of appendix A indicates that the instrumentation used in the unit 3 CILRT was extremely accurate in the determination of the containment leak rate, abd it far surpassed the recommendation of N27A that the measuring system be capable of detecting 0.25 L.

Using the ISG,.guidelines as t

developed in appendix A, the CILRT duration could be reduced to I

8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> without imoact if stable conditions were present.

The loss of 3 RTD's, 3 dewcells, and 1 pressure sensor had no significant effect on the ISG due to the number of sensors employed initially (see paragraph 4.0.D).

C'

-6.0 Tabulated Test Results

Vt 6.1 25-Psig CILRT

0

TENNESSEE VALLEY AUTHORITY CGNTAINNEHT LEAKAGE HEASUREHEHT TEST SUNHARY HOURS AVERAGE SAHPLE SINCE TEHPERATURE START (DEG Fe)

CORRECTEB PRESSURE (PSIA)

TOTAL HASS OF AIR (LBH)

P-T-P

TOTAL TINE LEAK RATE'EAKRATE (X PER BAY)

(X'PER BAY)

HASS LEAK RATE (X PER BAY) 113 114 115 116 117 1(8 119 120 121 122 123 124 125 126 127 131 132 133 134 135 136 137 138 139 140 141 142 143 144 145 146 147 148 149 150 151 2

155 156 157 DeDDD Oe167 0.333 Oe500 De667 0.833 ieDDD 1

167 1.334 1.500 ie667 le833 2.0DO 2el&7 2e333 2.500 2e&67 2e834 3e000 3ei67 3e333 3e500 3e667 3eS33 4e000 4ei67 4e334 4e500 4e667 4e833 5e000 5 1&7 5e333 5e500 5e667 5e834 6e000 6.167 6e297 be4&4 6e&31 6e7.98 he965 7e131 7e298 71e2128 71ei999 7ie1997 71e2017 7iei876 7iel850 71ei742 71ei&56 7iei&29 7ie1512

.71e1434 7ie1381 71ei253 7iel059 71e0950 7ie0821 7ie0672 71e0590 7ie0462 71e0389 7ie0191 71e0029 70e9834 70e9677 70e9578 70e9413 70e9280 70e9159 70e9037 70e8933 70e8790 70e8618 70e8417 70e8323 70e 8164 70e8088 70e7918 70e7818; 70e7727 70e7641 70e7519 70e7409 70e7233

70e7192, 70e7097 40ei708 40ei701 40ei698 40el&96 40ei&90 40e1689 40ei&84 40ei683 40ei&73 40ei660 40eid43 40ei&38 40ei630 40eihii 40e1597 40e1583 40e1573 40e1562 40ei536 40e1528 40e1518 40e1479 40,1466 40e1452 40ei441 40ei423 40e1403 40ei389 40,1377 40e1356 40ei334 40e1319 40ei312 40e1298 40ei284 40e1252 40e1232 40e1223 40e1224 40eil86 40e1185 40e1180 40eii70 40e1156 40eil44 61464e84 61465e21 61461e69 61461ei4 61459e80 61458e21 61458e27 61455e&6 6145&e45 61453e87 61452e77 61451.81 61450e71 6145ie76 61449e4'9 61450e24 61448e40 61448e80 6144he40 61445e63 61445e85 61440e73 61443eii 61442e31 61442e95

'61442eli 6144ie36 61441e06 61440e03

'1439e39 61437ei2 61437e83 61437e55 61439e92 61438e25 61434e02 61433e23 61435e42 61434e62 61430e61 6143le89 61434e71 61433e34 61432e22 61432e55 Oe0000000

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Oe2309273 Oe2285777 Oe2230273 Oe2189118 Oe2149741 Oe2106264

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l7 TENNESSEE VALLEY AUTMORITY CONTAINHENT LEAKAGE HEASUREHEHT TEST SUHHARY SAMPLE MOURS AVERAGE SINCE TEHPERATURE START (DEG Fe)

CORRECTED PRESSURE (PSIA)

TOTAL MASS OF AIR (LBH)

P"T-P LEAK RATE (X PER DAY)

TOTAL TIHE LEAK RATE (X PER DAY)

HASS LEAK RATE (X PER DAY) 158 159

~

160 161 162 163 164 165 166 167 168 169 170 171 172 176 177 178 179 180 181 182 183 184 185 186 187 188 189 190 191 192 193 194 195 196 197 201 202 7e 464 7e631 7e797 7e964 8ei31 8e298 8e465 8eh31 8e798 Re964 9ei31 9>25'7 5'e 464 9eh31 9e798 9.965 10e 131 10e298 10e464 10eh31 10e797 10e964 iiei31 lle298 lie46S ile 631 ile798 lle964 12ei31 12e297 12e464 12e631 12e75'8 12.965 13e131 13e298 13e464 13eb31 13e797 13e964 14e131 14e322 14e465 14e631 14e798 70e 70f 1 70e6930 70e6$ 61 70e6821 70eb557 70e6664 70e6645'0e6460 70e6364 70eb251 70ebih8 70e607$

70e55'74 70e5881 70e5593 70e5SOO 70e5516 70e5401 70e5393 70e5181 70e5035 70e4875 70e4693 70e4601 70e4462 70e4270 70e4157 70e4023 70e3896 70e3797 70e3712 70e3621 70e3510 70e3344 70e3252 70e3145 70e3002 70e2873 70e2777 70e2656 70e2621 70e245'4 70e235'7 70e224f 70e21D 40eff40 40eiliO 40eii02 40e105'2 40eiiSO 40ei 1 f9 40eilii 40ei085'0ei086 40ei080 40 1074 40el059 40.1048 40.1003 40e0942 40e0947 40e0938 40e0937 40e0936 40e0922 40e0908 40e0897 40e08'96 40e0880 40e0870 40e0868 40e0852 40e0826 40e0815 40e0809 40e0799 40e0796 40e07$ 6 40e0781 40e0780 40e0770 40e0768 40e0753 40e0750 40e0705 40e0704 40e0704 40e06$ 4 40e0668 40e0675 61432e09 61427e97 61426e54 61425e25'14ibe44 61414e78 61417e46 61414e35'1416efb 61415e02 614ihe27 61415e04 61415e62 61413e87 61412e87 61413ef4 61410e80 61412e74 61411e96 61412e73 61410e83 61410e87 61412e01 61410e64 614iie28 6141 1 e80 61409e40 61406e36 61406e26 61404e89 61404ei6 61404e64 61403e79 61404e26 61403e99 61402eii 61403e70 61400e93 6140ie67 61395e50 61395e20 61396eli 61394e05 bf35'Oe68 61393e97 Oei073919 Oe9641225 Oe3359689 Oe2924617 2e0801601 Oe3894037

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TEttttESSEE VALLEY AUTHORITY COttTAIttttEtiT LEAKAGE MEASUREMENT TEST

SUMMARY

SAMPLE HOURS AVERAGE SINCE TEtlPERATURE START (DEG Fe)

CORRECTED PRESSURE (PSIA)

TOTAL HASS OF AIR (LBH)

P-T-P

'EAK RATE (X PER DAY)

TOTAL TIHE LEAK-RATE (X PER DN)

HASS LEAK RATE (X PER DN) 203 204 205 206 207 208 209 210 211 212 213 214 215 226 217 222 222 223 224 225 226 227 228 229 230 231 232 233 234 235 236 237 238 239 240 241 42 4

245 246 247 14>964 15>231 25>297 25>464 15>631 15>798 15>965 ih>132 16>298 26>464 16>632 16.857 17>024 17ei91 17>358 17 524 17>691 17>858 18>024 18>191 28>357 18>524 18>691 18.858 29.024 19>191 19 358

,29>524 19>691 19>857 20>024 20>191 20>358 20>524 20>692 20 858 21 024 22 229 21>395 21>562 21>729 21>895 22>062 22 228 22>395 70>1984 70>1903 70>1787 70>2625 70>1560 70>1381 70>1213 70>1076 70>0905 70>0830 70>0685 70>0584 70>0483 70.0301 70>0249 70>0148 69>9997 69>9851 69>9716 69>9632 69>9518 69>9362 69>9260 69>9127 69>8983 69>8807 69>8793 69>8623 69>8504 69>8387 69>S263 69>8209 69>8023 69>7875 69>7715 69>7637 69>7475 69>7362 69>7358 69>7383 69>7255 69>6998 69>6909 69>67'?4 69>6673 40>0661 40>0661 40>0665 40>0644 40>0626 40>0598, 40>0594 40>0583 40>0580 40>0571 40>0562 40>0548 40>0555 40>0554 40>0548 40>0547 40>0539 40>0531 40>0519 40>0463 40>0457

'0>0442 40>0433 40>0430 40>0427 40>04?5 40>0426 40>0428 40>0398 40>0392 40>0383 40>0376 40>0360 40>0322 40>0316 40>0325 40>0280 40>0248 40>0241 40>0220 40>0207 40>01S9 40>0182 40>0186 40>0180 62391>46 61393>52 61394>04 61393>55 61388eiO 61386>56 61387>21 61385>70 62387>77 62386>84 61385>75 61384>83 62386>00 62387>13 61386e76 62385>90 61386>05 623S5>62 61386>02 61377>29 61376>56 61375>76 61373>57 61375>85 61374>82 62373>38 61372>60 62374>39 61373>24 61375>23 61376>47 61375>95 61375>80 62370>53 61371>32 61370>26 6136'6>15 62362>05 61367>20 62366>91 61367>23 61366>33 61363>23 61363>33 61361>02 0>5905673

-0>4828376

-0>1221556 0.1261322 i>2822550 0>3594045

-0>1518133 0>3545631

-0>4847120 Q>2286146 0>2560695 O>1592560

-0>2734546 "0>2673054 0>0877948 0>2020842

-0>0365819 O>2024291

-0>0955324 2 0458398 O>2699606 0>1884255 0>5144880

-0>5332886 0>2425440 0>3366145 0>2820322

-0>4217282 0>2698422

-0>4685708

-0>2899621 0>1240269, 0>0347585 i>2384454

-0>1856997 0>2716853

'-O>9436203 0>7S57423

-1>2120737 0>0676972

-0>0503157 0>1874470 0>7254679

-O>0238918 0>5425265 0>1924626 0>2840262 0>1807000 0>1800023 0>1916993 0>1934673 0>1898576 0>1925507 0>2846279 0>1849683 0>1856)90 0>1853215 0>1808248 0>2764941 0>1756397 O>1758881 0>1738830 0>1)32136 0>1707357 0>1879248 0>2877599 0>1877635 0>2906632 0>2842593 0>1847656 0>1860826 0>1860454 0>2808753 0>1826264 0>1761884, 0>1723045 0>1719055 0>2707800 0>2)94244

.0>1764700 0>1772290 0 1832781 0>1890653 Oei'?81927 0>2773361 0>1755872 0>1756750

,0>2798276 0>2783042 0>1810134 0.2804013 0>1801497 0>1795370 0'1790860 0>1793369 0>1796091 0>1796760 0>1799159 0>1796819 0 2795585 0>1795342 0>1794622 0>1792070 0>1784329 0>1778757 0>2773128 0>2766886 0>1759546 0>1752773 0>1754645 0>2756560.

0>2758978'>1762327 0>1762411

=

0>i/62589 0>064138 0>2765259'il)63110 0>1761126 0>1757736 0>1752274 0>1747123 0>2741532 0)2739074 0>1736759 0>1)33900 0>2734486 0>1737982 0>1736309 0>1734712 0>2732988 0>1729385 0>2729174 0>1727846 0>1728197

0 HOURS AVERAGE SANPLE SINCE TEMPERATURE START (DES Fe)

CORRECTED PRESSURE (PSIA) TENNESSEE VALLEY AUTHORITY CONTAIHNEHT LEAKAGE NEASURENEHT TEST SUNNARY

'OTAL MASS P"T-P OF AIR LEAK RATE (LDN)

(X PER DAY)

TO)AL TINE lEAK RATE (X PER DAY)

MASS LEAK RATE,

'Z PER DAY) 248 249 250 251 252 253 254 255 256 257 258 22e562 69e6514 22e729 69e6437 22e895 6'9e6295 23.062 69e6283 23e229 69e6233 23e395 69e6195 23e562 69e6093 23e728 69e6086 23e895 69e5975 24e062 69e5929 24e229 69e5904 40e0183 40e0177 40e0177 40e015$

40e0181 40e0153 40e 0144 40e0127 40e0133 40e0124 40e0121 61362e46 6136ie92 61362e85 61360e84 61363e83 61360ei8 61361.23 61357e51 61359e70 61358e75 61359e30

-Oe3400113 Oei262558

-Oe2177878 Oe4711691

-Oe7008299 Oe8591782

-Oe2470315 Oe8748367

-Oe5123838 Oe2223905

-Oei271784 0 1771781 Oe1768024 Oei739396 Oe1760862 Oel697905 Oe1746797 Oe1716939 Oel766104 Oe1718016 Oe1721485 Oe1700870 Oei726379 Oei724615'ei721881 Oe1720734 Oei716177 Oe1714178 Oei710819-Oe1710778 Oe1707552 Oei705299 Oei701370

6.2 25-Psig VeriHcation

'I

TEHHESSEE VALLEY AUTHORITY COHTAIHHEHT LEAKAGE HEASUREHEHT TEST SUNMARY KOURS AVERAGE SAHPLE SIHCE TEHPERATURE START (DEG Fe)

CORRECTED PRESSURE (PSIA)

TOTAL HASS OF AIR (LBM)

P-T-P LEAK RATE (X PER DAY)

TOTAL TIHE LEAK RATE (X PER DAY)

MASS LEAK RATE (X PER DAY) 2 3

4 5

6 7

8 '

10 11

'2 13 15 16 20 21 22 23 24 26 27 28 29 30 31 32 33 34 35 36 37 38 Oe000 0 116 Oo233 Oo350 Oo467 0.583 Oe700 Oo817 Oo933 le050 lo}67 io283 le400 ie517 ieh33 le750 io866 lo983 2o}00 2o216 2o333 2o450 2e566 2o684 2o800 2o917 3.033 3o}50 3.267 3o383 3o500 3oh}7 3e733 3e850'e967 4e083 4o200 69o}131 69o1071 69e}099 69o1099 69e}036 69o}029 69e0870 69e0921 69e0831 69e0799 No 0709 69e0707 69e0638 69e0559 69e0586 69o0472 69o0469 69e0414 69.0460 No 0395 69e0492 69.0475 69e0573 69o0628 69e0596 69o0706 69.0689 69o0772 69.0762 69o0872 69e0900 No0804 69e0890 69e0878 69o0966 69e0934 69o}023 39o9727 39e9688 39e9663 39e9639 39o9605 39o9580 39e9563 39e9546 39o9532 39.9521 39o9487 39e9470 39e9466 39e9456 39o9447 39o9433 39o9423 39o9379 39o9368 39o9356 39o9327 39e93}i 39o9293 39o9288 39o9252 39o9248 39o9229 39e92}3 39o9215 39o9199 39o9182 39e9149 39e9146 39e9133 39o9133 39e91}9 39e9i 61338o76 61337e82 61336e80 61333o94 61330o86 61327o73 61325e57 6132}oil 61318e61 6}315o63 61310o90 61306o92 61304eii 61302o05 61299o26 61296o80 61296e00 61288o91 61287e98 61286o70 61281e42 61280oii 61275e03 61273e79 61268e78 61267e32 61265o25 6126}e68 61262o05 61257e34 61255o3i 61251e}6 61249e08 61247e35 61245o73 612Qe54 6124}e86 Oe0000000 Oe3162969 Oo3399259 Oe9573372 ie0342803 io0500834 Oe7213702 io5004359 Oo8402004 io0030299 io5774120 ie337979} Oe9441309 Ooh877189 Oe9402663 Oo8260537 Oe2692334 2o3701384 Oo3099867 OeQ21485'e7648201 Oe4400772 le7091124 Oo4125661 ieh8N535 Oe4887836 Oo6964017 1e}948045 -Oe}248382 1 5860928 Oo6777964 io3970191 Oo6992141 Oo5809457 'o5407581 Oi7400233 Oe5639101 Oo0000000 Oo3162969 0e3281088 Oe5387189 Oo6623945 Oe7398079 Oe7367003 Oo8455637 Oe8448642 Oo8623770 Oe9341350 Oo9707301 'e9684762 Oo9467557 Oe9462529 Oe9382176 Oo8964602 Oo9834337 Oe9460713 Oe9190485 Oo9614478 Oe9366456 Oe9716234 Oo947}9}7 Oe9778844 Oe9583325 Oe9482442 , Oo9573631 Oo9}87880 Oe94}N03 Oo9328251 Oo9477106 Oo9399277 Oe9290423 Oe9175478, Oo9124528 Oo9027636 Oe0000000 Oe3183742 Oe3324614 Oe5}87048 Oo6601660 Oe7561610 Oe7872975 Oe8594470 Oo89}43}8 Oo9148088 Oe9562413 Oe9950010 io0178281 io0225793 io0226537 ie0192497 'o0018464 io0137950 ie0117584 1.0012789 io0032640 Oo9985846 io0026690 Oo9994502 io0037799 ie0023235 0.9993846 0499784}} Oe9886810 Oe9857483 Oe9813900 Oe9796185 Oo9772544 Oe9727916 Oe9669954 Oo961}034 0o9544159

Tables and Figures 'k / I )~ IE 1'

I i

~ ~ ) goo TE-4 El, 625 '~ / I) ~ ~ ~ El. 654 " m. El. 654 J" Located. inside drywell head I 0 // '/ I, I i .AS TE-2 El. 646 Located inside HFV E.N 70 / / r ~ ~ / ~ / TE-3 El. 625 o Place-Z( 6'ZB'-0'IGURE l 0 RID Location, 4 required Lower RTD 3 feet below grating (=Z"3 Lnd TE"4)

~ ~ 160 '\\ \\ \\ P"Q 90 270 'E-2 ~ El. 615. (0 PLAN jL 5/6'-0'IGURE 2 46N962 Q Dewcell Location, 1 required Lower dewcell 1/2 foot below grating

~ ~ I 1

~ ) l80 I J I l / TE~5 El. 606 J;r 0 bJ, f C) G 0'b, o~ P b 1 4. -- 2700 J/ u G J 1 0 00 PLAN-EL, 604'W lJ)p of otocl Cl 6N'-ll'IGURE 3 48k<981 4 RTD Location, 3 required. HTD located. 2 feet above grating (TH-5 and TE-6 ) TE-7 located between RPV and. sacrificial shield.

~ ( 180 90 -' I/ J( TE-ll El. 583 ~ << ~ ~ ~ I I ~ TE-10 + Zl. 583 1 TE-'12 V l. TE>>8 I ~ ~ E. 583 TE 13 I

. <

( ~i r \\ ~ ' ~ '( <<\\ J 4 ~ 7 TE 15 a " El. 583 V. ( ' <<TE>>14 , El. 583-r -'. ~i=.-.. I J II J E.: El. 583 <<K<< HE 3 \\ El. 583 ~'TE-'9 Zl. 583 ~ ( ( ~ ~ (' ( I ,r r ~ <<<<' ~. / I 0. 0 PLAy -ZC 584;'ll'ip of>/~i/ Sd4 9)i 404917 'FIGURE 4 RTD Location, 8 required Lower RTD 2 feet below grating II <<7 Q DewceU. Location, 2 required. Lower dewceU. 2 feet below grati I ~ rl 180 4 4 ~ ~" ~ ~ G TE~21 ( El. 561 f ce TE-20 El. 561 Ir 4 Q V I 4 I' 90

u. >

lk~ // ]y I 4 ~I P.. t(('t.~ -. - ~.. I'I I ~4 ill>4 ~.. TE-18 ~ ' ~ IC r. ~ J'E-19 t El. 561 ~ 4 gt ~4 4 /4 i Cnd of rfraf:ng I i/ 4 .8 I 'r TE-17 zz. 561 g 44 4I I 'I HE-7 El. 561

Located, drywel1 y

TE-24 El, 561 Located drygeU-4 ~ 4 ~ ~ 4 TE~22 El. 561

. 0 I(I JI l

I TE~23 El. 561 ~ I rs I 44 I TE-16 El. 561 'fwlr'i HE-5 El. 561 4 ~ f I~ Ip PLAN EI 5M' yp of Iform t'ISSJ dl 4I8I4ISI6 FIGURE 5 RTD Location, 9 required Lower RTD 2 feet below grating Q Dewcell Location, 3 required Lower dewceU. 2 feet below grating ~ ~ 180. r I TE-28 .l.i-El. 540 XZ~27 El. 5'E>>9 El. 54O I I ~ ~ ~ "/g ',.::i' ~ I I II

"-'HE-10 El. 540 i

~

-/5 TE-29

. El. 540 '8 0 TE-26 El. 540 / ~ /C' I I ~'~ TE>>30 El. 540 I ~ ' / (0 Suppzw~naion Chamber Wa13nmy Grating PTGURE 6 O'ewcell Location, 3 required Q RTD Location, 6 required RtlD and Dewcell to be tied to top of handrail g ~ Walkway Elevation El = 537.G I ~ I ~7-2. I Pr rvrr> ~ ~ Jrr>J>rf trr t> $ N>I'lt 4 t~ lrrJ >r ~ r ~ trrfot ~>l 4 I 4 ~ I ea b , ~ H] I ~ I f ~a ~i >.* ~ aecrrnn o-~ FIGURE 7 E r COI~VUZI;-.r. Or SC, ACCUXSXTXOI< ANn GRATA aCOUC rXON SVSTEV MINI COMPUTER SYSTEMi Tt<0 MENSOR QUART Z MANOMETC R DATA ACQUISITION UNIT (AUTO DATA N I N E) TWO MENSOR QUART2 MANOMETER SUPPRFSSION CHAHBHR SENSING REACTOR LINC LT 3 53 TCST STATION T EM PE RATUR E TORUS LEV L LT 64-54 ERIC P RESSURE TRQ~QH.MHM. DRYMELL SE NSING LINC MULTIPLC X UNIT A hULTI PLEX UNIT 8 T RANSDUCER SIGNAL CONDITIONING 30 RTD TEMPERATURE TRANSDUCERS fg DEWPOINT, T RANSDUGERS et~. NASS PLOT etc+. et~. N A S et~. - I .N et~. 'L B N-et080 t 4 1 etude t t sesc48 et 848. TINE t'.HOURSO FIGURE 9 0 8.48 MASS LEAK RATE PLOT ,. L E e.sa A K R A T E 8.18 D 'A e ee Y el-FKEHQ l 1 N12iS7 =a.'ie B 5'. 18. TINE CHOURSO FIGURE 10 1S. 0 AVERAGE PRESSURE PLOT p 4B.158 R S S U R E 4S, 188 I N P SI A 81~~) 11s1een 48.888 B. 18. TIME (HOURS) FIGURE ll 7l.58 AVERAGE TEMPERATURE PLOT 7$.88 E M P D 78.SS E G R E E S F 78.88 81~8 41 I88180 B. S. 18. TIME (HOURS) FIGURE 12 !S. .GLK 1 Measured Parameter '.fanuf ac turer and '<odel '."o. Aporoximate Number Used Instrumen~t S ecificstiun Containment Temperature Leeds 6.'Iorthrup Model No. 178055 30 Range: Accuracy: Repeatability: 0-250 ~ 0 loF +0.01 F Con tainmen t Pressure '.fensor Corpora tion Model No. 10100-001 Range: Accuracy: Repeatability: 0-100 psia, 400,000 counts F.S. +0.015% reading +0.0005% reading Containment Dewpoint Foxboro Corporation Model No. ?701 RG Range: Accuracy: Repeatability: -50 to +142 F +1 F dewpoint +Oe10 F Analog to Digital Converter Acurex Corp. Autodata Nine Accuracy: +0.001 F dewpoint +0.001 F temperature +1 count pressure Atmosoheric Pressure Mensor Corp. Model No. 10100-001 Range: Accuracy: Repeatability: 0-30 psia, 400,000 counts F.S. +0.015% reading +0.0005% reading Verification Fischer-Porter Rotameter Flow 3/8" Model No. FP3F-3/8-25-5 1" ".fodel No. FP135-G-10/55 OR Teledyne-Hastings Mass Flowmeter Model No. AHI;5 with H-3M Transducer Range: Accuracy: Range: Accuracy 3/8" tube 0-90,000 SCCM; 1" tube 0-230,000 SCCM +1% F.S. 0-5 SCF.'f +1% F.S. Mensor Chamber Temperature Suppression Chamber water Level Reactor Vessel Mater Level" Princo ASTM 19I. Plant Process Transmitter Model I,T 64-54 Plant Process Transmitter Model LT-3-53 Range: Accuracy: Range: Accuracy: Plunge'. Accuracy: 49 to 57 C +0.12 C +25 inches of water +5 % F.S. 0-60 inches of water +5% F.S. TAHLI'. 2 VOLUMETRIC WEIGHTING GROUPS Sepment Number Number of Tran s<lucers Segment Volume Volumetric Weir,ht Per Sensor By Compartment (Percent) See Note Temperature III: IIT. IV V VI VII VIII 1 7 8 2 1 1 1 6 8,300.87 50,299.72 55,908.76 30,862.61 5,585.39 8,101.92 7,545.95 133,240.00 4.9824 4.3130 4.1947 6.1748 3.3525 4.8629 4.5292 16.6667 1)ewpolnt IVIII III IV, V, VI, VIT. VIII 2 2 58,600.59 55,908.76 52,095.87 133,240.00 17.5867 16.7788 31.2691 50.0000 tlote: Sepment VIII, consists of the suppression chamber and is considered here as a independent volume from the drywell. TABLI". 3 CONTAINMENT L'AGE MEASUREMENT MINICOMPUTER ROUTINF.

SUMMARY

Routine Name FORE a. Automatically acquire, store, and correct raw data to calibration curves. b. Calculate volumetric weighted containment air mass and leak rate as defined by ANS N-274 (draft). c. Print for each sample a summary with average parameters and containment leak rate. LIST. Provide a summary for all samples from test start of average parameters, including calculated containment leak rate. TALLY a. Calculate statistical confidence levels for the measured leak rate from the test start. b. Provide a summary comparison of reportable leak rates as defined by ANS N-274 (draft). BASE a. Allow test director to change the sample considered the test base. b. Provide

a. summary: for-each~ sample leak rate recalculated with a shift in the test base.

APPENDIX A INSTRUMENTATION ERROR ANALYSIS

APPENDIX A Instrumentation Frror Analysis: (as defined in Appendix G, ANS N274 Draft 82, Revision 3) Assumed conditions at the time of the test: P = 25 + 14.696 ~ 39.696 psia 7 ~ 459 67ot82 ~ 541i67oR Td ~ 60 F dewpoint dp t = 24 hours Using the absolute method: 1. Total absolute pressure: Number of sensors: 3 (see note 1) Range: 0-100 psia 5feasurement system xepeatability error (E ) ~ +0,0005% reading ~ +0.000198 psia 1 x 100 psia ~ 0.00025 psia 400,000 + (E )2+(i ) ~ +.0001841 psia p (i/sensors) ~ 2. )later vapor pressure Number of sensors: 7 (see note 2) 0 Sensor repeatability error (E): +0.1 F 0 Heasurement system errox (()> excluding sensor: +0.001 F + [(00~) + (() ] epv I~ f/sensors H ~ +0.1 F (0.0092 psia/ F) = +0.00092 psia pv +0.001 F (0.0092 psia/ F) = +0.0000092 psia pv e ~ +0.0003477 psia pv 3. Temperature Number of sensors: 27 (see note 3) Sensor repeatability error (E): +0.01 R Measurement system error (g) excluding sensor: +0.00loR eT ~ + 1 ff sensors eT +0.001934oR ISG 2400 ISG = + t e P 2 2 e e + 2 '.2 ISG + 2400 24 2 60.0001841 + 2 0.0003477 + 2 0.001934 39,696 39.696 541.67 XSG = +0.001484 %/day Notes: 1. Test started with four pressure

sensors, subsequent checks revealed one pressure= sensor was erratic.

2. Test started with ten dewcells. Three dewcells were found to be inoperative during functional testing. 3. Test started with 30 RTD's. Three RTD's were found inoperative during the functional testing.

~y h APPENDIX A DEFINITION OF SYMEOLS dp t Absolute pressure, psia Temperature, degrees Rankine Temperature, dewpoint Time, hours Measurement system repeatability error E Error associated with the sensor ISG Instrumentation selection guide Error associated with measurement of change in a given parameter Subscripts Temperature Pressure PV - Vapor pressure

pi APPPNDIX 3 SlRHARY OE TYPES 8 AND C TESTING PERFORMED ON BROWNS PERRY NUGLEAR PLANT UNIT 3 TABLE OF CONTFNTS

1. 0 Introduc tion 2.0 Summary 3.0 Analysis of Data Tables:

B<<l 8-2 8-3 8-4 8-5 8-6 APPENDIX B

1. 0 Introd uc tion Appendix J to 10CFR50 and Browns Ferry technical specifications require that the total leakage.from all penetrations subject to types B and C

testing be less than 0.60 La for return to power operations. Technical specification 4.7.A.2.i requires that the leakage through each main-steam isolation valve be less than 11.5 SCFH, in addition to the total leakage requirement. This appendix presents a summary of all local leak rate testing performed on Browns Ferry unit 3 since the completion of the preoperational CILRT. An analysis and interpretation of conditions contributing to the failure of meeting either the acceptance criteria of technical specifications or Sections III.A.5(b), III.B.3, and III.C.3 of Appendix J are included. 2.0 Summary Tables B-l, B-2, B-4, and B-5 lists the type B and type C testing performed on Browns Ferry unit 3 since the preoperational tests. Testing was performed in accordance with plant approved surveillance instruc-tions BF SI 4.7.A.2.g-l, BF SI 4.7.A.2.g-2, and BF SI 4.7.A.2.g-3 which are on file at the plant site. Table B-3 summarizes cycle 1 test results and Table B-6 summarizes cycle 2 test results. Four out of eight of the main steam isolation valves required rework to meet the 11.5 SCFH limit during cycle 1 testing. And five out of eight of the main steam isolation valves required rework to meet the 11.5 SCFH limit during cycle 2 testing. The total as left leakage was 180.2821 SCFH during cycle 1 testing and 106.3427 SCFH during cycle 2

testing. Both as left totals were well below the 60 percent La limit of 655.9216 SCFH. The total leakage of isolation valves that terminate below the suppression chamber water level was 1.5043 CFH for cycle 1 tests and 1.2972 CFH for cycle 2 tests. The total leakage for isolation valves that are located in closed loop seismic class 1 lines that are water sealed was 2.9566 CFH for cycle 1 tests and 7.3845 CFH for cycle 2 tests. 3.0 Analysis of Data To facilitate testing and prevent the draining of large volumes of contaminated water to the drain sumps, TVA proposed testing certain non-water sealed valves with water and converting the measured leakage to an equivalent air leakage (reference J. E. Gillelands letter to James P. O'Reilly, Office of Inspection and Enforcement, dated August 14, 1978). This was accomplished during cycle 1 testing on those valves noted in Table B-l. It was felt that the total leak rate penalty for using the water to air conversion was more severe than TVA should accept, therefore a technical specification change was submitted requiring all valves that are not water sealed during a DBA be tested with air. The cycle 2 testing reflects this change. The total type B and C leakages prior to the return to power was significantly below the 60 percent L limit even though the total leakage is derived from the largest leak of the two isolation valves for type C leak tests.

The main steam isolation valves are tested with air applied between the inboard and outboard isolation valves. This tends to lift the inboard main steam isolaion valves off the seat. Three out of four outboard main steam isolation valves were less than 11.5 SCFH during initial cycle 1 tests and two out of four outboard main steam isoltion valves were less than 11.5 SCFfl during initial cycle 2 tests. Ilow-

ever, one out of four inboard main steam isolation valves was less than 11.5 SCFH during cycle 1 and during cycle 2 tests.

It is believed the direction the test pressure is applied to the inboard main steam isolation valves contributes to the increased failure

TABLE B-1 TYPE C TEST SP9fARY TESTING FDR CYCLE 1 UNIT 3 T.A. Water test (Isolation valves that terminate below the suppression chamber water level) Penetration Number X-210 System Nama Auxiliary Boiler Steam Supply 12-738 12-741 Remarks Test Date 9-9-78 9-9-78 Individual Leakage ~(S CPN 0.0000 0.0000 Penetration Leakage (SCFH) 0.0000 X-225A X-225B Water Quality And Sampling System 43-28A 43-.28B Water Quality And Sampling System 43-29A 43-29B 10-18-78 10-18-78 10-18-78 10-18-78 0.0027 0.0061 0.0030 0.0055 0.0061 0.0055 X-227A Core Spray-Torus High Level 75-57/58 75-57/58 A.F. A.L. 9>>12-78 10-27-78 12.0896 0.0738 0.0738 X-213B X-212 Torus Drain 74-722 74-722 RCIC Turbine Exhaust 71-14/580 71-14/580 A.F. A.L. A.F. A.L. 9-14-78 11-24-78 9-12-78 . 10-8-78 0.0639 0.3015 1.1522 0.4158 0.3015 0.4158

TYPE C TF.ST

SUMMARY

TESTING FOR CYCLE l UNIT 3 I.A. Hater Test (Cont.) Penetration Number System Naraa Remarks Test Date Individual Leakage (SCFH) Penetration Leakage (SCFH) X-221 RCIC Pump Discharge 71-32/592 71-32/592 A.F. A.L. 9-12-78 10-15-78 9.5294 0.0075 0.0075 X-214 HPCI Turbine Exhaust 73-23/603 73-23/603 A.F. A.L. 9-12-78 10-8-78 35.2174 0.684? 0.6847 X-222 HPCI Pump Discharge 73-24/609 9-16-78 0.0094 0.0094 I.BE Mater Test (Isolation valves located in closed loop, seismic class 1 lines that are water sealed.) X-13A LPCI Injection 74-53 74-54 9-10-78 9-14-78 0.4095 0.5589 0.5589 X-211A RHR Return to Torus/ Pump Test 74-57/58 74-57/58 A.F. A.L. 9-10-78 10-7-78 42.6316 0.0360 0.0360 X-39A Containment Spray 74-60/61 74-60/61 A.F. A.L. 9-10-78 10-13-78 13.5000 1.3613 1.3613 X-13B LPCI Infection 74-67 74-68 9-25-78 9-25-78 0.1592 0.7364 0.7364

~ > C l I 0 I I il 1 l I

I.B. Mater Test (Cont.) TABLE B-1 TYPE C TEST

SUMMARY

TESTING FOR CYCLE 1 UNIT 3 Penetration Number X-211B System Nama RHR Return to Torus/ Pump Test 74-71/72 74-71/72 Remarks A.F. A.L. Test Date 9-15-78 10-15-78 Individual Leakage ~HCFH) 0.8833 0.1980 Penetration Leakage (SCFH) 0.1980 X-39B Containment Spray 74-74/75 9-17-78 0.0030 0.0030 X-l7 Head Spray In)ection 74-77/78 9-11-78 0.0387 0.0387 X-16A Core Spray Injection 75-25 75-26 9-.11-78 9-11-.78 0.0027 0.0135 0.0135 X-16B Core Spray Injection 75-53 75-54 9-11-78 9-11-78 0.0108 0.0090 0.0108 II Air Test X-7A HSIV Line A 1-14 1-15 1-14 1-15 A.F. A.F. A.L. A.L. 9-15-78 9-15-78 10-19-78 10-18-78 1843.4169 0.0000 1.8283 1.2767 1.8283

~ ~ 4 $ ~ 0

II Air Test (Cont.) TABLE B-1 TYPE C TEST SlkÃARY TESTING FOR CYCLE 1 UNIT 3 Penetration Number System Name Remarks Test Date Individual Leakage (SCFH) Penetration Leakage (SCFH) X-229e Containment Air Monitor 76-225 76-225 76-226 76-226 A.F. A.L. A.P. A.L. 9-13-78 9-28-78 9-18-78 9-28-78 10.5215 0.0790 0.4827 0.1185

0. 1185 X-5lb Containment Air Monitor 76-229 76-229 76-230 76-230 A.P.

A.L. A.F. A.L. 9-13-78 10-19-78 9-16-78 9-28-78 64.8848 0.1327 4.2126 0.0308 0.1327 X-220b Containment Air Monitor 76-237 76-237 76-239 76-239 A.P. A.L. A.F. A.L. 9-13-78 9-28-78 9-18-78 9-28-78 0.4647 0.0922 0.3511 0.0792 0.0922 X-220a X-462 Containment Air Monitor 76-242 76-243 Containment Air Monitor 76-248 76-248 76-250 76-250 A.P. A.L. A.P. A.L. 9-13-78 9-18-78 9-13-78 9-28-78 9-16-78 9-28-78 0.0000 0.1536 6.7077

0. 1185 0.4388 0.1400 0.1536 0.1400

TABLE B-1 TYPE C TEST

SUMMARY

TESTING FOR CYCLE 1 UNIT 3 II Air Test (Cont.) Penetration 'Number System Name Remarks Test Date Individual Leakage (SCFH) Penetration Leakage SCFH) X-7B MSIV Line B 1-26 1-27 1-26 A.F. A.L. 9-16-78 9-16-78 9-28-78 442.4096 8.9452 6.8367 8.9452 X-7C X-7D MSIV Line C 1-37/38 MSIV Line D 1-51 1-52 1-51 1-52 A.F. A.F. A.L. A.L. 9-15-78 9-17-78 9-17-78 10-8-78 10-7"78 9.5892 1997.1238 50.7588 6.2249 5.5045 9.5892 6.2249 X-8 X-48 Main Steam Drain 1-55/56 1-55/56 Control Air Suction 32-62/63 A.F. A.L. 9-13-78 11-13-78 9-13-78 18.3628 2.6573 0.3551 2.6573 0.3551 X-25 Containment Purge And Inerting Supply 64>>17/18/19/76-24 64-17/18/19/76-24 A.F. A.L. 9-12-78 11-8-78 32.5608 8.9200 8.9200

~ ~

TABLE B-l TYPE C TEST SUMQEY TESTING FOR CYCLE 1, UNIT 3 II Air Test (Cont.) Penetration Number System Name Remarks Test Date Individual Leakage (SCFH) Penetration Leakage (SCFH) X-205 Torus Vacuum Relief 64-20 C.V. 64-21 C.V. 76-17/18/19-Purge 76-17/18/19-Purge 84-8B/601-CAD 84-8C/603-CAD A.P. A.L. 9-9-78 9-9-78 9-10-78 10-31-78 9-9-78 9-9-78 1.4301 1.7357 14.0420 0.6814 0.0000 1.4899 1.4301 1.7357 0.6814 1.4899 X-18 X-19 Drywell Sump Discharge 77-2A/2B 77-2A/2B Dryvell Sump Discharge 77-15A/15B 77-15A/15B A.P. A.L. A.F. A.L. 10-27'78 11-5-78 10-27-78 11-3-78 40.6333 0.9522 14.1333 2.3894 0.9522 2.3894 X-22 X-41 Control Air Di'scharge 32-336 32-336 32-2163 Recirculation Hater Quality Sampling 43-13 43-13 4.3-14 43-14 A.F. A.L. A.P. A.L. A.F. A.L. 9<<12-78 10 16-78 9-12-78 9-13-78 11-20-78 9-13-78 10"16-78 2.8627 0.0708 0.0764 3.2033 1.5974 6.7985 0.0286 0.0764 1.5974

TABLE B-l TYPE C TEST

SUMMARY

TESTING FOR CYCLE 1 UNIT 3 II Air Test (Cont.) Penetration Number

System Name Remarks Tes t Date Individual Leakage (SCFH)

Penetration Leakage (SCFH) X-231 Ventilation 64-29/30/32/33/84-19 64-29/30/32/33/84-19 A.F. A.L. 9-12-78 9-29-78 261.9077 4.2485 4.2485 X-26 X-10 Drywell Ventilation Exhaust 64-31/34/139/140/84-20 RCIC Steam Supply 71-2/3 71-2/3 A.F. A.L. 9-10-78 '-9-78 9-19-78 1.7456 78.5700 0.3541 1.7456 0.3541 X-ll HPCI Steam Supply 73-2/3 9-10-78 0.0000 0.0000 X-512 Containment Air Monitor 215 76-215 76-217 76-217 A.F. A.L. A.F. A.L. 9-13-78 10-20-78 9-16-78 9-28-78 8.0668 0.2171 0.5773 0.0570 0.2171 X-229'ontainment Air Monitor 76-220 76-220 76-222 76-222 ,A.F. A.L. A.F. A.L. 9-13-78 9-28-78 9-18-78 9-28-78 28.0583 0.1360 0.1536 0.1185

0. 1360

TABLE B-1 TYPE C TEST SUM'fARY TESTING FOR CYCLE 1 UNIT 3 II Air Test (Cont.) Penetxation Number X-46b System Name Containment Air Monitor 76-253 76-253 76-254 76-254 Remarks A.F. A.L. A.F. A.L. Test Date 9-13-78 9-28-78 9-15-78 9-28-78 Individual Leakage (SCFH 48.2252 0.1097 1.4042 0.0528 Penetration Leakage SCFH 0.1097 X-25 X-50a 6 b X-50c Containment Puxge and Inerting Supply 84-8A/600 84-8D/602 Radiation Monitoring System 90-254A/254B/255 90-254A/254B/255 Radiation Monitoring System 90-257A/257B A.F. A.L. 9-9-78 9-9-78 9-11-78 10-6-78 '9-11-78 0.0325 0.0000 1.5056 0.7047 0.0284 0.0325 0.0000 0.7047 0.0284 III Water Tests Converted to Equivalent Air Leakage e Penetration Number System Meme Test Remarks Date Individual Leakage SCFH Convert To Air ~SCPH Penetration Leakage (SCFH X-14 RWCU Suction 69-1 69-2 '69-2 A.F. A.L. 10-12-78 10-13-78 11-20-78 -Water Test 0.0963 0.8901 0.0540 10.8356 62.0204 6.8828 loe8356

TABLE 8-1 TYPE C TEST SUHHARY TESTING'OR CYCLE 1 ~ UNIT 3 III Water Test Converted to Equivalent Air Leakage (Cont.) Penetration Number System Name Tes t Remarks Date Individual Leakage (SCFH) Convert Penetration Tor Air Leakage X-12 Shutdown Cooling Suction 74-47 74-48 74-661/662 10-12-78 10-14-78 10-12-78 Water Test 0.1228 0.0585 0.0047 13.1122 7.3288 1.0138 13.1122 Standby Liquid Control Infection 63-525 63-525 63-526 63-526 A.F. A.L. A.F. A.L. 9-14-78 10-15-78 9-14-78 10-15-78 6.3138 288.4216 0.0662 8.0754 1.0523 70.7242 0.0743 8.8408 8.8408 X-9A X-9B Feedwater Line A 3-558 3-554/73-45 3-554/73-45 3-554/73-44 3-554/73-44 3-554 Feedwater Line B 3-572 3-568/71-40/69-579 3-568/71-39/69-579 3-568 69-579 71-39 71-40 85-576 A.F. A.L. A.F. A.I. A.F. =A.F. A.F. A.L. A.L. A.L. A.L. A.L. 9-12-78 9-12-78 10-11-78 9-12-78 10-11-78 9-12-78 10-10-78 10-9-78 10-15-78 0.5310 22.0913 0.6429 22.0913 0.1161 22.0913 0.2835 2.1774 2.1720 0.0 0.0198 0.1035 0.1089 0.0243 41.3558 770.4444 48.0494 770.4444 12.5476 770.4444 25.2771 125.1158 124.8723 0.0 3e1328 11.4662 11.9330 3.6788 48.0494 25.2771

TABLE B-1 TYPE C TEST

SUMMARY

TESTING FOR CYCLE 1 UNIT 3 III Water Test Converted to Equivalent Air Leakage (Cont.) Penetration Number System Name Tes t Remarks Date Individual Convert Penetration Leakage To Air Leakage (S CFH) ~SCPH (SCFH) X-36 CRD Return Line 85-573 85-576 85-576 9-15-78 9-14-78 9-15-78 0.0329 1.2160 0.0243 4.6659 3.6788 This leakage p'ath no longer exists due to CRD reroute during refuel outage. TABLE B-2 TYPE B TEST

SUMMARY

TESTING FOR CYCLE 1 UNIT 3 BELLOWS Leakage Path 7A inboard outboard 78 inboard outboard 7C inboard outboard 7D inboard outboard 8 inboar'd outboard 9A inboard outboard 9B inboard outboard 10 inboard outboard 11 inboard outboard 12 inboard outboard 13A inboard outboard 13B inboard outboard 14 inboard outboard 16A inboard outboard 16B inboard outboard 17 inboard outboard

Leakage, SCFH As Found 0.0019 0.0019 0.0016 0.0019 0.0006 0.0013 0.0025 0.0013 0.0003 0.0005 0.0006 0.0015 0.0012 0.0012 0.0003 0.0013 0.0005 0.0007 0.0013 0.0013 0.0021 0.0015 0.0024 0.0015 0.'+0006 0.0011 0.0005 0.0015 0.0002 0.0007

'.0003 0.0006 ~ AS. Found Date 10/22/78 10/22/78 10/22/78 10/22/78 10/23/78 19/23/78 10/23/78 10/23/78 10/25/78 10/25/78 10/23/78 10/23/78 10/23/78 10/23/78 10/23/78 10/23/78 10/23/78 10/24/78 10/23/78 10/23/78 10/25/78 10/25/78 10/25/78 10/25/78 10/22/78 10/22/78 10/22/78 10/22/78 10/22/78 10/22/78 10/22/75 10/22/78

Leakage, SCFH As Left 0.0019 0.0019 0.0016 0.0019 0.0006 0.0013 0.0025 0.0013 0.0003 0'0005 0.0006 0.0015 0.0012 0.0012 0.0003 0.0013 0.0005 0.0007;,

0,0013 0.0013 0.0021 0'0015 0.0024 0.0015 0.0006 0.0011 0.0005 0.001S 0.0002 0.0007,, 0.0003 0.0006's Left Date 10/22/78 10/22/78 10/22/78 10/22/78 10/23/78 10/23/78 10/23/78 10/23/78 10/25/78 10/25/78 10/23/78 10/23/78 10/23/78 10/23/78 10/23/78 10/23/78 10/23/78 10/24/78 '0/23/78 '0/23/78 10/25/78 10/25/78 10/25/78 10/25/78" 10/22/78 10/22/78 10/22/78 10/22/78 10/22/78 10/22/78 10/22/78 10/22/78 ELECTRICAL TABLE B-2 TYPE B TEST

SUMMARY

TESTING FOR CYCLE 1 UNIT 3 Leaka e Path 100A EC B BD C BE D BF E BG F BH G DC 101A AB B AA C AF D AE 102 CA 103 DG 104A ED R DB C BC D CB E EE F EF 1058 AC C AD D EG Spare 106A DA B BA 107A BA B 108A EA B DE 109 DD llOA EB llOR DF 219 FH

Leakage, SCFH As Found 0.0613 0.0250 0.0365 0.0000 0.0607 0.0000 0.0672 0.0000 0.0000 0.0766 0.0779 0.0306 0.0000 0.0649 0.. 0389 0.0779 0.0000 0.0240 0.0002 0.0247 0.0613 N/A 0.0153 0.0913 0.0000 0.0510 0.0000 0.0771 0.0387 0.0520 0.0000 0.0001 As Found Date 9/16/78 9/16/78 9/16/78 9/17/78 9/17/78 9/17/78 9/16/78 9/17/78 9/17/78 9/16/78 9/17/78 9/16/78 9/17/78

. 9/16/78 9/16/78 9/16/78 9/17/78 9/17/78 9/17/78 9/17/78 9/17/78 N/A 9/16/78 9/16/78 9/16/78 9/16/78 9/17/78 9/17/78 9/16/78 9/17/78 9/17/78 9/17/78

Leakage, SCFH As Left 0.0613 0.0250 0.0365 0.0000 0.0607 0.0000 0.0672

'.0000 0.0000 0.0766 0.0779 0.0306 0.0000 0.0649 0.0389 0.0779 0.0000 0.0240 0.0002 0.0247 0.0613 N/A 0.0153 0.0913 0.0000 0.0510,, 0.0000 0.0771 0.0387 0.0520 0.0000 0.0001 As Left Date 9/16/78 9/16/78 9/16/78'/17/78 9/17/78 9/17/78 9/16/78 9/17/78 9/17/78 9/16/78 9/17/78 9/16/78 9/17/78 9/16/78 9/16/78 9/16/78 9/17/78 9/17/78 9/17/78 9/17/78 9/17/78 N/A 9/16/78 9/16/78 9/16/78 9/16/78 9/17/78 9/17/78 9/16/78 9/17/78 9/17/78 9/17/78

~ ~ g ~ 0' TABLE 8-2 TYPE B TEST

SUMMARY

TESTING FOR CYCLF. 1 UNIT 3 RESILIENT SEALS Lea~ka e Paeh lA 1R 4 6 35A 35R 35C 35D 35E 35F 35G 47 200A 2008 Drywell Head AZ Oo 45o 90o 135o 180o 225o 270o 315o 213A Personnel Air Lock

Leakage, SCFH As Found 0.0151 3.6550 0.0003 0.0276 0.0000 0.0000 O.OOOO 0.0000 0.0000 0.0000 0.0032 0.0001 0.0126 0.0009 0.0058 0.0002 0.0002 0,0001 0.0002 0.0006 0.0001 0.0001 0.0001 0.0001 52.4444 As Found Date 9/9/78 9/9/78 9/15/78 9/9/78 9/16/78 9/16/78 9/16/78 9/16/78 9/16/78 9/16/78'.

9/16/78 . U/k6/7,8.,:, 9/8/78 9/9/78 9/9/78 9/14/78 9/14/78 9/14/78 9/14/78 9/14/78 9/14/78 9/14/78 9/14/78 11/6/78 10/26/78

Leakage, SCFH As Left 0.0019 0.0035 0.0003 0.0001 0.0000 0.0000 0.0000 0.0000 0.0000 0.0000 0.0032 0.0001 0.0126 0.0009 0.0198 0.0002 0.0002 0.0001 0.0002 0.0006 0.0001 0.0001 0.0001 0.0001 15.9469

~ As Left Date 11/1/78 11/3/78 9/15/78 11/2/78 9/16/78 9/16/78 9/16/78 9/16/78 9/16/78 9/16/78 9/16/78 11/6/78 9/8/78 9/9/78 11/20/78 9/14/78 9/14/78 9/14/78 9/14/78 9/14/78 9/14/78 9/14/78 9/14/78 11/6/78 11/30/78

~ p ~ ~ TABLE B-3 TOTAL LEAKAGE SUMHARY TESTING FOR CYCLE 1 UNIT 3 Type B Leakage: I. Bellows II. Electrical III. Resilient Seals 0.0367 SCFH 1.0532 SCFH 15.9910 SCFH Type C Leakage: I. Air Tested Isolation Valves II. Isolation Valves Tested With Mater And Converted To Equivalent Air Leakage III. Isolation Valves That Terminate Below Suppression Chamber Water Level (See Note 2) IV. Isolation Valves That Are Located in Closed-Loop, Seismic Class I Lines That Are Water.Sealed (See Note 1) 57.0861 SCFH 106.1151 SCFH 1.5043 CFH 2.9566 CFH Note 1: This leakage is not included in the total leakage rate but is reported per paragraph III. A. 1(d) of 10CFR50, Appendix J. Note 2: This leakage shall not be included in the total leakage rate if the total water leak rate is less than 20,781 cubic feet per 30 days or 28.86 SCFH. Total Leakage Prior To Return To Power Operation (Type B 6 C Leakage) 180.2821 SCFH

TABLE B-4 TYPE C TEST SUNNY TESTING FOR CYCLE 2 UNIT 3 Penetration Number System Name Test Date Remarks I.A Water Test (Isolation valves that terminate below suppression pool water level) Individual Leakage (SCFH) Penetration Leakage {SCFH) X-212 X-221 RCIC Turbin Exhaust 71-14/580 71-14/580 RCIC Pump Discharge 71-32/592 A.F. A.L. 8-29-79 9-4-79 8-27-79 44-1818 0.1422 0.1598 0.1422 0.1598 X-214 X-222 X-2138 X-227A HPCI Turbine Exhaust 73-23/603 73-23/603 HPCI Pump Discharge 73-24/609 Torus Drain Core Spray-Torus High Level 75-57/58 A.F. A.L. 8-26-79 9-6-79 8-26-79 8-28-79 8-24-79 34.5000 0.6018 0.0000. 0.2807 0.0639 0.6018 0.0000 0.2807 0.0639 X-225A Water Quality and Sampling System 43-28A 43-28B 8-"28-79 8-28-79 0.0009 0.0030 0.0030 X-225B Water Quality and Sampling System 43-29A 43-29B 8-28-79 8-28>>79 0.0100 0.0070

0. 0100

I.A Water Test (Cont.) TABLF. B-4 TYPE C TEST SUMQRY TESTING TOE CYCLE 2 UNYT 3 Penetration Number X-210 System Name Auxiliary Boiler Steam Supply 12-738 12-741 Remarks Test Date 8-27-79 8-27-79 Individual Leakage (SCFH) 0.0045 0.0015 Penetration Leakage (SCFH 0.0015 X-228 Demineralized Water 2-1143 8-28-79 0.0340 0.0343 I.B Mater Test (Isolation valves Located in closed-loop, seismic class 1 lines that are water sealed.) X-13A LPCI Injection 74-53 74-54 8-23-79 8-23-79 0.0585 0.8486 0.8486 X-13B X-211A X-211B X-39A LPCI Injection 74-67 74-68 74-68 RHR Return to Torus/ Pump Test 74-57/58 RHR Return to Torus/ Pump Test 74-71/72 Containment Spray 74-60/61 A.P. A.L. 8-25-79 8-25-79 10-25-79 8-23 9-11-79 8-22-79 0.2277 4.1860 1.2176 0.5857 1.2176 3.4884 1.2176 0.5857 1.2176 3.4884

0

TABLE B-4 TYPE C TEST

SUMMARY

TESTING FOR CYCLE 2 UNIT 3 I.B Water Test (Cont.) Penetration Number X-39B System Name Containment Spray 74-74/75 Remarks Test Date 8-26-79 Individual Leakage (SCFH) 0.0000 Penetration Leakage (SCFH) 0.0000 X-17 Head Spray Infection 74-77/78 8-24-79 0.0000 0.0000 X-16A Core Spray Infection 75-25 75-26 75-26 A.F. A.L. 8-23-79 8-23-79 11-1-79 0.0099 39.1935 0.0180 0.0180 X-16B Core Spray Injection 75-53 75-54 75-54 A.F. A.L. 8-25-79 8-25-79 10-19-79 0.0000 0.0054 0.0090 0.0090 II Air Test X-7A X-7B MSIV Line A 1-14 1-15 1-15 1-14 MSIV Line B 1-26/27 1-26/27 A.F. A.F. A.L. A.L. A.F. A.L.

8-29-79 8-29-79 8-29-79 9-11-79 8-23-79 9-10-79 1215.6889 433.9335 0.8912 7.7338 1715.7145 0.1535 7.7338 0.1535 X-7C MSIV Line C

1-37/38 8-23-79 0.5885 0.5885

II Air Test (Cont.) TABLE B-4 TYPE C TEST

SUMMARY

TESTING FOR CYCLE 2 UNIT 3 Penetration Number X-25 X-205 X-231 System Name Containment Purge and Inerting Supply 64-17/18/19,76-24 -" 64-17/18/19,76-24 Torus Vacuum Relief 64-20/C.V. 64-21/CiV. Ventilation 64-29/30/32/33,84-19 64-29/30/32/33,84-19 Remarks Test Date 8-25-79 11-25-79 8-24-79 8-24-79 8-26-79 11-24-79 Individual Leakage ~SCPH) 5.5586 6.4438 0.7021 0.3426 2.9620 9.7439 Penetration Leakage (SCFH 6.4438 0.7021 0.3426

9. 7439 X-26 X-20 Drywell Ventilation Exhaust 64-31/34/139/140984-20 64-31/34/139/140,84-20 Demineralized Water 2-1192 2-1192 2-1383 A.F.

A.L. 8-26-79 11-29-79 8.9957 9.9463 8.7680 0.5946 0.0000 9.9463 0.5946 X-10 X-ll RCIC Steam Supply 71-2/3 HPCI Steam Supply 73-2/3 8-24-79 8-24-79 0.3335 1.3077 0.3335 1.3077

~ ~

0 TABLE 8-4 TYPE C TEST

SUMMARY

TESTING FOR CYCLE 2 UNIT 3 II Air Test (Cont.) Penetration Number X-205 System Name Torus Vacuum Relief 76-17/18/19 76-17/18/19 Remarks A.F. A.L. Test Date 8-24-79 11-29-79 Individual Leakage (SCFH) 385.5555 0.0000 Penetration Leakage (SCFH 0.0000 X-51A Containment Air Monitor 76-215 76-217 8-30-79 8-28-79 0.0833 0.0000 0.0833 X-229f Containment Air Monitor 76-220 76-220 76-222 A.F. A.L. 8-31-79 9-7-79 8-29-79 46.9963 0.0000 0.0000 0.0000 X-229e Containment Air Monitor 76-225 76-226 8-30-79 8-29-79 0.0527 0.0263 0.0527 X-51b X-220b X-220a Containment Air Monitor 76-229 76-230 76-230 Containment Air Monitor 76-237 76-239 Containment Air Monitor 76-242 76-243 A.F. A.L. 8-30-79 8-28-79 9-"7-:7.9 8-30-79 8-31-79 8-30-79 8-30-79 0.0439 0.8322 0.0000 0.0000 0.0000 0.0000 0.0000 0.0439 0.0000 0.0000

l ~ ) E i

II Air Test (Cont.) TABLE B-4 TYPE C TEST

SUMMARY

TESTING FOR CYCLE 2 UNIT 3 Penetration Number System Name Remarks Test Date Individual Leakage ~SCPH Penetration Leakage X-7D.'SIV Line D 1-52 1-51 1-51 A.F. A.L. 8-31-79 8-31-79 9-5-79 3.0907 3184.0302 3.4282 3.4282 X-8 Main Steam Drain 1-55/56 1-55/56 A.F. A.L. 8-28-79 10-6-79 61.5014 ~ 0.1238 0.1238 X-18 X-19 Drywell Sump Discharge 77-2A/2S. Drywell Sump Discharge 77-15A/158 8-28-79 8-28-79 0.0263 0.2108 0.0263 0.2108 X-22 Control Air Discharge 32-336 32-336 32-2136 A.F. A.L. 8-27-79 9-24-79 8-27-79 4.1249 0.7752 0.0000 0.7752 X-48 X-21 Recirculation Hater quality Sampling 43-13 43-14 Control Air Suction 32-62/63 Service Air 33-1070 33-785 8-24-79 8-24-79 8-26-79 11-19-79 11-20-79 0.4464 0.1863 0.0000 0.1513 1.9791 0.4464 O.OOOO 1.9791

TABLE B-.4 TYPE C TEST SlM4AEY TESTING FOR CYCLE 2 UNIT 3 II Air Test (Cont.) Penetration Number X-46a System Name Containment Air Monitor 76-248 76-250 Remarks Test Date 8-30-79 8-28-79 Individual Leakage (SCFH) 0.0000 0.0000 Penetration Leakage (SCFH) 0.0000 x-46b Containment Air Monitor 76-253 76-254 8-30-79 8-28-79 0.0263 0.0000 0.0263 X-25 Containnent Purge and Inerting Supply 84-8A/600 84-8D/602 8-25-79 8-25-79 0.0000 0.0000 0.0000 X-205 X-50a&b X-50c x-14 Torus Vacuum Relief 84-8B/601 84-8C/603 Radiation Monitoring System 90-254A/254B/255 Radiation Monitoring System 90-257A/257B 90-257A/257B RWCU Suction 69-1 69-2 69-2 A.F. A.L. A.F. A.L. 8-28-79 8-25-79 8-26-79 '8-26-79 9-5-79 9-17-79 9-17-79 9-30-79 0.0000 0.0000 0.0000 2.1063 0.0549 1.5473 104.0087 0.3410 0.0000 0.0000 0.0549 1.5473

s ~ )4

II Air Test (Cont.) TABLE B-4 TYPE C TEST SiRMARY TESTING FOR CYCLE 2, UNIT 3 Penetration Number System Name. Remarks Test Date Individual Leakage (SCFH) Penetration Leakage (SCFH) X-42 X-12 Standby Liquid Control In)ec tion 63-525 63-525 63-526 63-526 Shutdown Coaling Suction 74-48 74-47 74-661/662 A.F. A.L. A.F. A.L. 8-27-79 9-18-79 8-27-79 9-20-79 9-14-79 9-14-79 9-12-79 3.3758 0.9726 17.1472 0.0883 0.1964 0.1500 0.0000 0.9726 0.1964 9A Feedwater Line B 3-558 3-558 69-624 3-554 3-554 73-45 73-45 73-44 73-.44 3-572 3-572 3-568 3-568 69-579 85-576 71-40 71-40 71-39 A.F. A.L. A.F. A.L. A.F. A.L. A.F. A.L. A.F. A.L. A.F. A.L. A.F. A.L. 0.0834 8.9093 0.0 6.5822 0.0000 248.9661 10.3022 82.1657 0.0000 35.2110 17.7008 181.0088 0.9292 0.0000 0.0000 124.7873 2.8099 0.0000 10.3022 17.7008

J l; TABLE B-5 TYPE B TEST SUK(ARY TESTING FOR CYCLE 2 UNIT 3 BELLOWS Leakage Path 7A inboard outboard 78 inboard outboard 7C inboard outboard 7D inboard outboard 8 inboard outboard 9A inboard outboard 9B inboard outboard 10 inboard outboard 11 inboard outboard 12 inboard outboard 13A inboard outboard 13B inboard outboard 14 inboard outboard 16A inboard outboard 16B inboard outboard 17 inboard outboard

Leakage, SCFH As Found 0.0004 0.0004 0.0000 0.0006 0.0003 0.0004 0.0000 0.0000 0.0003 0.0001 0.0000 0.0004 0.0000 0'e 0003 0.0001 0.0003 0.0007 0.0001 0.0002 0.0002 0.0000 0.0000 0.0002 0.0002 0.0006 0.0004 0.0000 0.0000 0.0001 0;0002 0.0001 0.0000 As Found Date 9/3/79 9/3/79 9/2/79 9/2/79 9/3/79 9/3/79 9/3/79 9/3/79 9/3/79 9/2/79 9/2/79 9/2/79 9/3/79 9/3/79 9/3/79 9/3/79 9/3/79 9/3/79 9/2/79 9/2/79 9/2/79 9/2/79 9/2/79 9/2/79 9/2/79 9/2/79 9/1/79 9/1/79 9/1/79 9/1/79 9/2/79 9/2/79
Leakage, SCFH As Left 0.0004 0.0004 0.0000 0.0006 0.0003 0.0004 0.0000 0.0000 0.0003 0.0001 0.0000 0.0004 0.0000 0.0003 0.0001 0.0003 0.0007 0.0001 0.0002 0.0002 0.0000

'.0000~ 0.0002 0.0002 0.0006 0.0004 0.0000 0.0000 0.0001'.0002 0.0001 0.0000 's Left Date 9/3/79 9/3/79 9/2/79 9/2/79 9/3/79 9/3/79 9/3/79 9/3/79 9/3/79 9/2/79 9/2/79 9/2/79 9/3/79 9/3/79 9/3/79 9/3/79 9/3/79 9/3/79 9/2/79 9/2/79 9/2/79 9/2/79 9/2/79 9/2/79 9/2/79 9/2/79 9/1/79 9/1/79 9/1/79 9/1/79 9/2/79 9/2/79

TABLE B-5 TYPE H TEST SUGARY TESTING FOR CYCLE 2 UNIT 3 ELECTRICAL Lea~ka e Path 100A EC 100B BD 100C BE 100D BF 100E HG 100E HH 100G DC 101A AB 101B AA 101C AF 101D AE 102 CA 103 'C 104A ED 104H DH 104C HC 104D CB 104E FF 104F EF 105A Spare 105H AC 105C AD 105D EG 106A DA 106B BB 107A HA 107B 108A EA 108B DF. 109 DD 110A EB 110B DF 219

Leakage, SCFH As Found 0.0000 0.0076 0.0305 0.0061 0.0244 0.0122 0.0305 0.0517 0.0000 0.0612 0.0195 0.0229 0.0061 0.0258 0.0906 0.0323 0.0'426 0.0128 0.0000 0.0184 0.0153 non"-testable 0.0000 0.0000 0.0153 0.0075 0.0000 0.0128 0.0194 0.0323 0.0243 0.0)00 W

W As Found,, Date 8/29/79 9/2/79 9/3/79 8/31/79( 9/3/79 9/3/79 9/3/79 8/30/79 8/31/79 8/30/79 9/2/79 8/30/79 9/3/79 9/2/79 9/1/79 9/2/79, 8/31/79 9/3/79 8/31/79 8/30/79 8/30/79 8/30/79 8/29/79 8/29/79 8/29/79 >9/2/79 8/31/79 8/30/79 8/30/79 9/3/79 9/1/79

Leakage, SCFH As Left 0.0000 0.0076 0.0305 0.0061 0.0244 0.0122 0.0305 0.0517 0.0000 0.0612 0.0195 0.0229 0.0061 0.0258 0.0906 0.0323 0.0426 0.0128 0.0000 0.0184 0.0153 0.0000 0:.0000 0.0153 0.0075 0.0000 0.0128 0.0194 0.0323 0.0243 0.0000 As Left'ate 8/29/79 9/2/79 9/3/79'/31/79 9/3/79 9/3/79 9/3/79 8/30/79 8/31/79 8/30/79 9/2/79 8/30/79 9/3/79 9/2/79 9/1/79 9/2/79 8/31/79 9/3/79 8/31/79 8/30/79 8/30/79 8/30/79 8/29/79 8/29/79 8/29/79 9/2/79 8/31/79 8/30/79 8/30/79 9/3/79 9/1/79 TABLE B-5 TYPE B TEST

SUMMARY

TESTING FOR CYCLE 2 UNIT 3 RESILIENT SEALS

Leakage, SCFH As Found As Found Date
Leakage, SCFH As Left As Left Date lA Equip 1B Equip 4

OR)A 6 CRD 35A TIP 35B TIP 35C TIP 35D TIP 35E TIP 35F TIP 35G TIP 47 POT 200A SC 200B SC Drywell Head AZ 0 Shear 45o Shear 90o Shear 135o Shear 180o Shear 225o Shear 270o Shear 315o Shear X-213A Personnel Air X-2 0.0209 291.4713 0.0001 0.0004 0.0000 0.0000 0.0001 0.0000 0.0000 0.0000 0.0065 0.0001 0.0252 0.0016 0.1103 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0000 0.0001 0.0000 Lock II 15145.4856 8/22/79 8/22/79 8/22/79 8/24/79'/31/79 8/31/79 8/31/79 8/31/79 8/31/79 8/31/79 9/1/79 9/2/79 8/25/79 8/25/79 8/22/79 8/28/79 8/28/79 8/28/79 8/28/79 8/29/79 8/28/79 8/28/79 8/28/79 8/28/79 8/22/79 0.0029 0.0124 0.0001 0.0001 0.0000 0.0000 0.0001 0.0000 0.0000 0.0000 0.0000 0.0001 0.0000 0.0000 0.0539 0.0001 0.0001 0.0001 0.0001 0.0001 0.0001 0.0000 0.0001 0.0000 29.0142 12/5/79 11/15/79 8/22/79 12/1/79 8/31/79 8/31/79 8/31/79 8/31/79 8/31/79 8/31/79 9/21/79 9/2/79 11/20/79 12/3/79 12/2/79 8/28/79 8/28/79 8/28/79 8/28/79 8/29/71 8/28/79 8/28/79 8/28/79 8/28/79 ll/21/79

TABLE B-6 TOTAL LEAKAGE SUN'IARY TESTING FOR CYCLE 2 Type B Leakage I. Bellows II. Electrical III. Resilient Seals 0.0066 SCFH 0.6221 SCFH 29.0845 SCFH Type C Leakage I. Air Tested Isolation Valves II. Leakage Total From Isolation Valves That Terminate Below Suppression Chamber Water Level. (See Note 2) 76.6295 SCFH 1.2972 CFH III. Leakage Total From Isolation Valves Located In Closed Loop, Seismic Class 1 Lines That Are Water Sealed. (See Note 1) 7.3845 CFH Note 1: This leakage is not included in the total leakage rate but is reported per paragraph III, A.l(d) of 10CFR50, Appendix J. Note 2: This leakage shall not be included in the total leakage rate if the water leak rate is less than 20,781 cubic feet per 30 days or 28.86 SCFH. Total Leakage Prior to Return to Power Operation 106.3427 SCFH (Type B 6 C Leakage)

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