ML17308A497

Reactor Containment Bldg Integrated Leakage Rate Test Final Rept. W/900621 Ltr

ML17308A497
Person / Time
Site:	Saint Lucie
Issue date:	04/06/1990
From:	Connor J, Mumper D, Sarah Turner FLORIDA POWER & LIGHT CO.
To:	NRC OFFICE OF INFORMATION RESOURCES MANAGEMENT (IRM)
References
L-90-230, NUDOCS 9006260063
Download: ML17308A497 (159)

Text

ACCELERATED DI TRJBUTIONj DEMONS+ATION SYSTEM ri

+~w REGULATORY XNFORMATION DXSTRXBUTION SYSTEM (RIDS)

ACCESSXON NBR:9006260063 DOC.DATE: 90/04/06 NOTARIZED: NO DOCKET FACIL:50-335 St. Lucie Plant, Unit 1, Florida Power & Light Co. 05000335 AUTH. NAME AUTHOR AFFILIATXON TURNER,S. Florida Power & Light Co.

CONNOR,J. Florida Power & Light Co.

MUMPER,D. Florida Power & Light Co. R RECIP.NAME RECIPIENT AFFILIATION sew

SUBJECT:

"Reactor Containment Bldg Integrated Leakage Rate Test Final Rept." W/900621 ltr. D DISTRIBUTION CODE: A017D COPIES RECEIVED:LTR TITLE:

X OR Submittal: Append J Containment Leak~Rate Testing ENCL SIZE:

NOTES A

RECIPIENT COPIES RECXPXENT COPIES ID CODE/NAME LTTR ENCL ID CODE/NAME LTTR ENCL D PD2-2 LA 1 0 PD2-2 PD 5 5 NORRIS,J 1 1 D

INTERNAL: ACRS 6 6 NRR/DST/SPLB 8D 1 1 OC 1 0 OGC/HDS2 1 1 $

E'G FX LE 01 1 1 RES/DE/SEB 1 1 B/RS 1 1 RES/DSIR/SAIB 1 1 RES/DSR/RPS B 1 1 EXTERNAL: LPDR 1 1 NRC PDR 1 1 NSIC 1 1 R'

D NOTE TO ALL "RIDS" RECIPIENTS:

PLEASE HELP US TO REDUCE WASTE! CONTACT THE DOCUMENT CONTROL DESK, ROOM Pl-37 (EXT. 20079) TO ELIMINATEYOUR NAME FROM DISTRIBUTION LISTS FOR DOCUMENTS YOU DON'T NEED!

TOTAL NUMBER OF COPIES REQUIRED: LTTR 24 ENCL 22

P.O. Box14000, Juno Beach, FL 33408-0420 JUN 2 1 1990 L-90-230 10 CFR 50 App J V.B.3 U. S. Nuclear Regulatory Commission Attn: Document Control Desk Washington, DC 20555 Gentlemen:

Re: St. Lucie Unit 1 Docket 50-335 Reactor Containment Building Integrated Leak Rate Test (ILRT)

In accordance with the requirements of Appendix J to 10 CFR 50, the subject report is enclosed.

If you have any questions about this submittal, please contact us.

Very truly yours, D. A. S er ident Vice St. Lu P e

'lant DAS:JWH:kw cc: Stewart D. Ebneter, Regional Administrator, Region Senior Resident Inspector, USNRC, St. Lucie Plant II, USNRC DAS/PSL f186 9006260063 900406 PDR P

ADOCK 05000335 PDC ulC an FPL Group company

(~ 0 l, "e EACTOR CONTAINMENT BUILDING INTEGRATED LEAKAGE RATE TEST FINAL REPORT 8T. I UCfE UNlT IVO.1 NUCLEAR POWER PLANT FT. PIERCE FL.

DOCKET NO. 50-335 rJ

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9006260063

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ST. LUCIE PLANT UNIT NO. 1 NUCLEAR PONER PLANT FT ~ PIERCE, FLORIDA DOCKET NO. 5$ -3~5 REACTOR CONTA INNENT BUILDING INTEGRATED LEAKAGE RATE TEST repared By:

Scott urner Test Director Revie ed By:

Jim on or Per formance Engineer Approved by:

Duane Numper Lead T Engr r D. H. est Technical Supervisor Date of Test Completion:

April 6, 1998

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TABLE OF CONTENTS PacCe INTRODUCTION AND

SUMMARY

TEST DISCUSSION...........................--.-.......--. ~ .....

A. Description of the Containment............................ ~ ~ ~

B. Description of ILRT Instrumentation..............,......... ~ ~

1. Temperature Instrumentation................. 4 2., Humidity Instrumentation.................... 5

3. Pressure Instrumentation.................... 5

4. Flow Instrumentation........................ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 6

5. Instrument Selection Guide ( ISG) Calculation ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 6 C. Containment Pressurization Equipment................... . ~ ~ ~ ~

D. - Description of the Computer Program.................... ~ ~ ~ ~-

E. Description of the Testing Sequence................. - '....

III. ANALYSIS AND INTERPRETATION.................--........-

A. Instrumentation System Performance................. - ~ ~ ~ ~ ~ ~ --

B. Temperature, Stabilization Phase.................... ~ ~ ~ ~ ~ ~ ~ - ~ 12 C. Leakage Survey Phase........................................

D. Integrated Leakage Rate Phase...................... ~ ~ ~ ~ ~ ~ - ~ ~

E. Verification Controlled Leakage Rate Phase............ ~ - ~ ~ ~ ~ 14 IV. F I GURES ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 15 RTD Locations and Volumes 2 RHD Locations and Volumes 3 Flow Diagram for Pressure Sensing and Control led Leakage 4 Flow Diagram for Pressurization System 5 St. Lucie Unit 1 ILRT Seq'uence 6 ILRT Test. Sequence

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Paae V.

~ APPEND I CES ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ s ~ ~ ~ ~ 22 A. Tabulation of "As-Found" and "As-Left" ILRT Results....... - ~ 23

1. Correction of ILRT Results for "As-Found" case........ -- 24

2. Correction of ILRT Results for "As-Left" case......... ~ ~ 25 B. ILRT Comouter-Generated Report................. 26

1. Temoerature Stabilization.................. 29 F igure.....................................

A. Temperature Stabilization 31

2. Integrated Leakage Rate F'gut es Test...............

~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ e o e o a ~ ~ ~ ~ ~ ~ o ~ ~ ~

A. ILRT Weighted Average Temperature B. ILRT Containment Absolute Pressure C. ILRT Weighted Average Vapor Pressure D. ILRT Air Mass E. ILRT Bn-Top Leakage Rates

3. Verification Controlled Leakage Rate Test.. 52 F'gul es ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 55 A. CLRT Weiahted Average Temperature B. CLRT Containment Absolute Pressure C. CLRT Weighted Vapor Pressure D. CLRT Air Mass E. CLRT Bn-Top Leakage Rates

4. Data for Leak Chase Period.................

C. Local Leakage Rate Testing Conducted Since the Last ILRT- - ~ ~

I. INTRODUCTION AND SUNMARY A periodic Type,"A" Integrated Leakage Rate Test (ILRT) was successfully conducted on the primary containment structure of the Florida Power 5 Light Company St. Lucie Plant Unit No. 1 Pressurized Water Reactor. This test was performed at full pressure in accordance with the facility Technical S peci f ications.

This ILRT test was performed using the "Absolute Nethod" of testing in accordance with the Code of Federal Regulations, Title 18, Part 58 Appendix J, 'Primary Reactor Containment. Leakage Testing for Water-Cooled Power Reactors," in accordance with ANSI N45.4 1972, American National Standard, "Leakage Rate Testing of Containment Structures for Nuclear Reactors," and the methodology and calculational requirements of Topical Report BN-TOP-1, Revision 1, "Testing Criteria for Integrated Leakage Rate Testing of Primary Containment Structures for Nuclear Power Plants." The ILRT was performed at a pressure in excess of the calculated peak containment internal pressure related to the design basis accident as specified in the Final Safety Analysis Report (FSAR) and the Technical Speci f ications.

This report describes and presents the results of the periodic Type "A" leakage rate testing, including the supplemental test method utilized for verification. In addition, Florida Power 5 Light Company performs types "B" and "C" testing in accordance with the requirements of 18CFR58, Appendix J, and the Technical Specifications. The results of types "B" and "C" testing performed since the last ILRT are provided in this report ~

The resulting reported "as-found" Type "A" containment leakage at 48 2 pslg

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is 8.195 percent of the contained mass per'ay. This value includes the difference between the as-found and as-lef t, minimum pathway Types "B" and "C" local leakage measurements as required by the NRC I&E Information Notice 85-71. The resulting reported "as-lef t" Type "A" containment leakage at 48.2 psig is 8.181 percent of the contained mass per day. The acceptance criteria for this test as contained in the facility Technical Specifications is that leakage cannot exceed 8.375 percent of the contained V

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air mass per day at 39.6 psig for either the "as-found" or "as-lef t" case.

II. TEST DISCUSSION A. Descri tion of the Containment The containment vessel 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 system design incorporates a free-standing containment vessel surrounded by a low-leakage concrete shield building. A four-foot annular space is provided between the outer wall of the containment vessel and the inner wall of the shield building to allow filtration of containment vessel leakage during accident conditions to minimize of f-site doses ~

The free-standing containment vessel is a two-inch thick right circular cylinder with a one-inch thick hemispherical dome and two-inch thick el lip-soidal bottom. The overal 1 vessel dimensions are 148-foot diameter by 232-foot high. The vessel wall thickness is increased to a minimum of four inches adjacent to all penetrations and openings. The vessel is fabricated of ASIDE-SA 5i6 Grade 7$ ful ly killed pressure vessel quality steel plate.

The net free volume of the containment vessel is 2.5 x 1$ 6 cubic feet.

The containment vessel structure includes one personnel airlock, one emergency escape lock, one fuel transfer tube, one equipment maintenance hatch'nd one seal-welded construction hatch. All process piping and electrical penetrations are welded directly to the containment vessel nozzles with the exception of the main steam, main feed water, and fuel transfer tube penetrations. These penetrations are provided with testable II multiple ply expansion be}lows to allow for thermal growth or building differential motion.

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The containment vessel is designed and constructed in accordance with the requirements for Class NC vessels contained in Section II I of the ASNE Code (1971 Edition) . The containment vessel is code stamped for a design internal containment pressure of 44 psig at a temperature of 264 F. The containment vessel and al 1 penetrations are designed to limit leakage to less than 8.5 percent by weight of the contained air per day at the above design conditions. The calculated peak accident pressure for the design basis accident for the St. Lucie Plant No. 1 is 39.6 psig, in accordance with Technical Specification 3.6. 1.2.a. 1.

B. Descri tion of ILRT Instrumentation The containment system was equipped with instrumentation to permit leakage rate determination by the "absolute method." Utilizing this method, the actual mass of dry air within the containment is calculated.

The leakage rate becomes the time rate of change of this value. The mass of air (9) is calculated according to the Perfect Gas Law as follows:

0= (P-Pv) V RT where: P Containment Total Absolute Pressure Pv Containment Water Vapor Pressure (Average)

V Containment Net Free Volume R Gas Constant T Containment Absolute Temperature (Average)

The primary measurement variables required are containment absolute pressure, containment relative humidity, and containment temperature as a function of time. During the supplementary verification test, containment bleed-off flow is also recorded.

Average containment absolute temperature is determined by measuring discrete local temperatures throughout the containment and applying a mass and volume weighted averaging technique.

The volume fraction for each sensor is determined based upon solid geometrical calculations:

where: T Containment Absolute Temper ature (Average)

T.1 Local Temperature for sensor i Vf; Volume Fraction for sensor i Average containment water vapor pressure is determined by measuring discrete local relative humidities throughout the containment, converting these to local vapor pressures using local group temperatures and applying a mass and volume weighted averaging technique. The volume fractions for

, the relative humidity sensors are determined in the same manner as the temperature sensors above.

(/RH.)

J x (Psat for T.) J

= Pv.

Pv = T (Pv J 4Vf ) / T.

J where: %RH. Humidity for Sensor j TJ'elative Psalm Pv.

for T. Steam Table Saturation Pressure group average temperature near Calculated local vapor pressure for local sensor j for sensor Pv Containment Water vapor pressure (Average)

T Containment Absolute Temperature (Average)

Vf Volume Fract'ion for sensor j Local temperature f or sensor j The Instrument Selection Guide or ISG is used to determine the ability of the instrumentation system to measure the leakage rate. The calculated ISG for this test met all acceptance criteria for all test instrumentation systems.

1. Tem erature Instrumentation Forty precision Resistance Temperature Detectors (RTDs) were located throughout the containment to al low measurement of the weighted average air

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temperature. The location of the temperature detectors in the containment is depicted in Figure 1. Each RTD sensor was supplied with a calibrated resistance versus temperature curve accurate to +8.5 F. The sensitivity and repeatability of each RTD sensor is less than +8.8126 F.

C The signal conditioning circuit and readout for the RTD sensors was a Fluke 2288B data logger o'perating in a constant, cur rent mode. The operating parameters for the RTD constant current card are accurate to

+8.16 F and have a resolution of +8.81 F.

Each RTD was in-situ calibration checked after installation to verify correct operation. The data logger operating as a total loop with an RTD in the circuit has a repeatability of +8 81 F'nd a resolution of

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+8 81 oF

2. Humidi t 'Instrumentation Ten Resistance Humidi ty Detectors (RHDs were located throughout the I

containment to al low measurement of the weighted average containment vapor pressure. The location of the RHDs in the containment is depicted in Figure 2. The calibrated accuracy of the RHDs is +2.5 percent RH, the repeatability of the RHDs is +8. 1 percent RH, and the sensitivity of the RHDs is +8.81 percent RH.

The readout dev'ice used for the RHDs was a Fluke 2288B data logger operating in a voltage measurement mode.

Each RHD was in situ calibration checked af ter instal lation to verify correct operation. The repeatability of the loop is +8.1 percent RH while the resolution of the device is +8.81 percent RH.

3. Pressure In s trumen ta tion Two Volumetric precision pressure moni tors were used to determine containment absolute pressure. The arrangement of tubing connections 5

between the monitors and the containment is sho~n in Figure 3. Ei ther monitor could be used as the primary pressure sensor for leakage rate calculations with the remaining sensor considered as a backup. The calibrated accuracy of the monitor is +8.815 percent of reading. The sensitivity, repeatability, and resolution of the monitor is +$ .881 psi.

Binary Coded Decimal <BCD) output from both monitors was connected to the Fluke 2288B data logger.

4. Flow Instrumentation A variable area float-type rotameter was used to superimpose leakage during the supplementary CLRT. The piping connection between the rotameter and the containment is shown in Figure 3. The accuracy, repeatability, and sensitivity for the rotameter in units of SCFN and converted to equivalent leakage values is given below:

Peak Pressure Rotameter, Equi va 1 en t SCFN L~a~acae Accuracy +8.28 +8.8831 %/day Repeatability +8.85 +8.8888 %/day Sensitivity '+8. 85 +8.8888 //day

5. Instrument Selection Guide ( ISG) Calculation The Instrument Selection Guide is a'ethod of compiling the instrumen-tation sensitivity and resolution for each .process measurement variable used during the ILRT and evaluating the total instrumentation system's ability to detect leakage rates in the range required. The I SG formula is described in American National Standard ANSI/ANS 56.8-1987. Although the ISG is a very conservative measure of sensitivity, the general industry practice for this test has been to require sensitivity at least four times better than the containment allowable leakage or ISG < $ .25La.

The calculated ISG for the instrumentation used for this test was 8 8883 ~

percent per'day, for an 8 hour9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> test. The allowable value for this test is 8.25La or $ .125 percent per day, for an 8 hour9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> test. The ISG calculation met all recommended criteria and demonstrated the ability of the ILRT instrumentation system to measure containment leakage with a sensitivity t

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exceeding that required by the appr opriate industry standards.

C. Containment Pressurization E ui ment The equipment used to pressurize the containment. is shown in Figure 4 ~

The thirteen oil-free industrial diesel-driven air compressors had a total nominal capacity of l2,988 SCFM. The compressed air was then routed to water-cooled af ter-coolers, moisture separators, and refrigerant air dryers. This equipment assured that clean and dry air was used to pressurize the containment.

D. Descri tion of the Com uter Pro ram The Ebasco ILRT computer program is an interactive program written specifically for fast, easy utilization during all phases of the ILRT and CLRT. The program is wri tten in a high-level, compiled, structured language and is operated on a portable NS-DOS personal computer. The program has been verified and meets all requirements of the Ebasco and Florida Power & Light Quality Assurance Programs.

As necessary, data entry and modifications are readily accomplished by the data acquisition team. In addition to extensive data verification routines, the program calculates, on demand, total time and mass point leak rates as wel 1 as the 95 percent Upper Conf idence Level for these leakage rate calculations. Calculations and methodology of the program are derived from American National Standard ANSI N45.4-1972 and Topical Report, BN-TOP-1, Revision l.

Input data may be deleted for a given instrument in the case of a sensor malfunction. The deletion of a given instrument is performed on all samples in the data base. Weighing factors, if applicable, are then recalculated for the remaining instrument sensors of that type (see section III.A).

Data evaluations are enhanced by the flexible display of either sensor variables or various computed values in tabular or graphical form on the computer screen or printer. Data are recorded on magnetic media to prevent

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loss during the testing. Al 1 data are stored on the computer system in use, with retrieval capability to any desired data base throughout the testing .

Ancillary portions of the program assist the user in determining temperature stabilization, determining the ILRT termination criteria, performing ISG calculations, performing in situ instrument loop performance calculations and determining acceptable superimposed CLRT leakage veri-f ication.

Temperature, pressure and humidity data are transmitted from the ILRT instrumentation system to the computer via an RS-252 link at 28 minute intervals (see Figure 5). Computer verification and checking routines supplement data verification by the data acquisition team. Modifications can be promptly made if errors are det'ected.

E. Descri tion of the Testin Se uence Preparations to pressurize the containment for the conduction of the ILRT inc luded internal and ex ternal inspec tions of the containment.

structure; installation and check out of the ILRT instrumentation; Types "B" and "C" Local Leakage Rate Tests; alignment of valves and breakers for test conditions; and the installation and check out of the temporary pressurization facilities. These preparations were completed on April 5, 1998.

Al 1 ILRT instrumentation was declared operable with performance within manufacturers'o)erances. Pressure sensor No. 1 was selected to be the primary pressure instrument, as it had exhibited better repeatability and stability during the in situ testing.

Three penetrations were required to be in service during the ILRT and were not lined up to simulate accident conditions; P-52D ( ILRT Pressure Sensing Line), P-52E ( ILRT Controlled Bleed-of f Line), and P-54 ( ILRT Pres-

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surization Line) . The three ILRT penetrations are used to conduct the test. The minimum pathway leakage for those penetrations, determined during Type "C" local testing, is added to the measured ILRT leakage to account for these penetrations being in service during the test.

Pressurization of the containment started at 8314 hours0.0962 days <br />2.309 hours <br />0.0137 weeks <br />0.00316 months <br /> on April 5, 1998. Figure 6 pictorially depicts the sequence of testing. The pressurization rate was maintained at 4 psi/hr. Early in the pressurization mode, the Assistant Nuclear Plant Supervisor (ANPS) requested that, the test be stopped due to PDIS-25-1B (Containment dP sensor) failing low, which caused FCV-25-8 ( Con t a inmen t Vacuum Breaker) to open on high vacuum. The fuses for FCV-25-8 were pulled, shutting the valve, and pressurization was restarted. Subsequent to completion of the ILRT the PDIS was repaired.

The target pressure of 55. 165 psia was achieved at 138S hours on 4/5/89.

This target pressure was 8.865 psi above the minimum test pressure to account for the expected pressure decrease due to temperature stabilization and to allow for some leakage margin during the test sequence. Data acquisition and analysis during the temperature stabilization phase began at 1318 hours0.0153 days <br />0.366 hours <br />0.00218 weeks <br />5.01499e-4 months <br /> at 28 minute intervals.

The containment temperature stabilization criteria was met at 1718 hours0.0199 days <br />0.477 hours <br />0.00284 weeks <br />6.53699e-4 months <br /> on April 5, 1998, af ter acquisition of four hours of data. During this period, the temperature and pressure decreases followed predictable trends, and the trend of vapor pressure was stable.

Six hours into the ILRT hold time, leakage had increased to greater than

.375 //day in magnitude. Two valves were found to be leaking) MV 87 2A MV-87-2B (Containment Sump Valves) . Both of these valves are in service and covered with water during the design basis accident. They are boundary valves for the ILRT (see sect. I II.C) . These valves were checked shut, MV-87-2A received 'wo turns and MV-87-2B received three turns. The ILRT hold time was restarted at 2318.

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The 8 hour9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> period of leakage measurements started at 2318 hours0.0268 days <br />0.644 hours <br />0.00383 weeks <br />8.81999e-4 months <br /> on April 5, 1998, and was successful ly terminated at 8718 hours0.101 days <br />2.422 hours <br />0.0144 weeks <br />0.00332 months <br /> on April 6, 1998, all other acceptance criteria contained in Bn-Top were met and the ILRT was shown to be successful. The data accumulated displayed the following leakage rates:

Simple BN-TOP-1 Leakage Rate = 8.8694 %/day Fitted BN-TOP-1 Leakage Rate = 8.$ 826 //day 95% Upper Confidence Level (UCL) = 8.1B18 //day Since leakage plot had-a negative skew ( tending to decrease) af ter 8 hours9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br />, the leakage rate was not extrapolated linearly to 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />, using the last 28 data points. The acceptance criteria for this test is 8.75 La or 8.375 %/day.

To verify the results of the ILRT, a verification Controlled Leakage Rate Test (CLRT) was conducted. Using the variable area full-pressure rotameter, a superimposed flow of 19.0 SCFN was'dded to the leakage already present in the containment. This superimposed flow is equivalent to leakage of 8.299 percent per day. A one-hour stabilization period was allowed to lapse after addition of this leakage in accordance with the requirements of Topical Report BN-TOP-1. Data accumulation for the CLRT was started at 8818 hours0.102 days <br />2.449 hours <br />0.0146 weeks <br />0.00336 months <br /> on April 6, 1998 and the CLRT was conducted for a four-hour period. The measured CLRT leakage rates for this period were:

Simple BN-TOP-1 Leakage Rate = 8.3290 %/day Fitted BN-TOP-1 Leakage Rate = 8.3336 %/day The target CLRT leakage for this test was 8.382 +8.125 percent per day, or within the criteria as measured. The ILRT and CLRT were declared successful at 1218 hours0.0141 days <br />0.338 hours <br />0.00201 weeks <br />4.63449e-4 months <br /> on April 6, 1998.

At 1216 hours0.0141 days <br />0.338 hours <br />0.00201 weeks <br />4.62688e-4 months <br /> on April 6, 1998, depressurization of the containment was initiated at a rate of 6 psi/hr. Containment entry for post-test inspection purposes occurred when the containment pressure was approximately $ .5 psig at. 2$ $ $ hours on April 6, 199$ . The post-test V

inspection detected no anomalies or damage other than several crane rail

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lights were out and some paint blisters on the shield wal l.

Corrections were made to the measured ILRT leakage to account for the three penetrations which were in service during the ILRT and to account for the dif t ference between the as-found and as-lef minimum pathway loca).

leakage values as required by NRC I5E Information Notice 85-71.

95% Upper Conf idence Level (UCL) during ILRT 8.181 %/day Corrections for Local Leakage Measurements 8.8137 %/da Total Reported Containment UCL 8.1947 %/day This value satisfies the acceptance criteria for the test of being less than 8.375 percent per day.

III . ANALYSIS AND INTERPRETATION A. Instrumentation S stem Performance All of the forty temperature detectors performed as expected with no anomalous behavior detected by data trend analysis or by the Ebasco ILRT computer program error checking routines. The computer program also determines, the in situ temperature loop repeatability which consists of process measurement variations as wel l as sensor noise. The average in situ loop repeatability for the forty operating temperature sensors was 8.813 0 F. This performance compares well with the vendor-claimed temperature sensor loop repeatability, excluding process variations, as given in Section I I . 81.

Ten relative humidity sensors were installed in the containment for the ILRT. All operated as expected with no anomalous behavior detected by data trend analysis or by the ILRT computer program error checking r outines.

The average in situ loop repeatability for the relative humidity sensors was 8.1 percent RH. This performance compares well with the vendor-claimed humidity sensor loop repeatability, excluding process variations, as given in Section I I . B2.

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I Two pressure sensors were installed for the ILRT, with one utilized for testing and one considered as a spare. Prior to containment pressurization, analysis demonstrated that pressure sensor 1 was more stable over an eight hour period than the other sensor. During the ILRT, the in situ pressure loop repeatability for both sensors was 8.881 psi ~

This performance compares well with the vendor-claimed pressure sensor loop repeatability, excluding process variations, given in Section II.B.3-The variable area rotameter performed as expected with no evidence of unstable reading, float sticking, or moisture in the float tube.

In summary, all of the ILRT test instrumentation performed in an adequate manner to al low dete'rmination of containment leakage rates to the sensi tivity required.

B. Tem erature Stabilization Phase Prior to pressurization of the containment, the atmosphere was very stable with an average temperature of 82.1 F and a maximum spread of'em-perature from the highest reading sensor to lowest reading sensor of 3-9 F. During pressurization, the heat of compression of the air occurs mainly at the top of the containment with colder pressurization air being added at the bottom. At the end of pressurization, the average temperature was 96.4 F with a maximum spread of temperature from the highest reading sensor to lowest reading sensor of 24.4 F.

The results of the four-hour temperature stabilization phase are presented in Appendix B.l. The acceptance criteria given in Topical Report BN-TOP-1, Revision 1, are described in Note 2 in that appendix. The data pr esented shows that a smooth and predictable temperature stabilization occurred. At the end of stabilization, the average temperature was BB-B F and the maximum spread of temper ature f rom the highest reading sensor to the lowest reading sensor was 13. 1 F. This demonstrates that the heat sinks of concrete and steel in the containment, were quickly r eturning the containment atmosphere to a stable condition.

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I C. Leaka e Surve Phase Leakage in excess of .375 La was noted af ter the temperature stabi li-zation phase criteria'had been met. Leakage survey teams were dispatched to investigate the source of leakage. Leakage was found on penetrations 32 and 33 (Containment Sump Suction). Nhile checking the boundary valves shut it, was noted that NV-87-2A required two ful l turns and NV-87-2B required three full turns to be ful ly closed. These two isolation valves are not considered as potential leakage barriers in the Final Safety

'Analysis Report (FSAR) sec tions h. 2. 4. 2 and 6. 2. 4. 4 and thus are not subject to type C or Bypass leakage testing as they will be water covered in a loss of coolant accident and open during the recirculation phase of the transient. Any water leakage through these valves in the closed position wil 1 be returned to the containment. by the Safety Injection System pumps. No potential containment leakage or off-site dose is credible due to seat leakage of these valves in the closed position. Leakage rate measurements on the containment were restarted after the leakage survey phase using the total time leakage rate methods of Topical Report BN-TOP-1, Revision 1. As an additional diagnostic tool, mass point leakage rate measurements, as described in ANSI/ANS 56.8-1981, were conducted in parallel. The mass point leakage calculations are not sensitive to the starting point of the test and wil l detect changes in containment leakage more rapidly than the total time method.

D. Inte rated Leaka e Rate Phase Leakage measurements were started at 2318 hours0.0268 days <br />0.644 hours <br />0.00383 weeks <br />8.81999e-4 months <br /> on April 5, 1998. The total time BN-TQP-1 results for eight hours of leakage measurements are presented in Appendix B.3. A summary of the measur ed leakage af ter eight hours is:

BN-TQP-1 Total Time Simple Leakage Rate 8.869 %/day Fitted Leakage Rate 8.883 %/day Upper Conf idence Level 8. 181 %/day The higher Upper Conf idence Level of the BN-TOP-1 measurements is due

to the nature of performing regression analysis on simple leakage rates instead of regression analysis on masses and the more conservative statistics utilized by BN-TOP-I.

As all acceptance criteria for a Reduced Duration BN-TOP-l ILRT were met at. eight hours as presen ted in Appendix B. 2, the ILRT was dec ared 1 acceptable.. Appendix A presents the corrections to the measured ILRT leakage rates for local leakage rate measurements for both the "as-found" and "as-left" cases.

E. Uerification of Controlled Leaka e Rate Phase Subsequent to the acceptance of the ILRT results, a superimposed leakage equivalent to 8.2'P9 percent per day was added to the existing containment leakage using the variable area rotameter. A one-hour stabilization period was allowed to lapse after addition of this leakage in accordance with the requirements of Topical Report BN-TOP-i.

Leakage measurements were initiated to verify the r esults of the ILRT.

The minimum duration for the Controlled Leakage Rate Phase was determined to be four hours in accordance with Topical Report BN-TOP-I. As presented in Appendix B.3, the leakage measur ements met the acceptance criteria for the veri f ication phase.

BN-TOP-l Total Time Simple Leakage Rate 8.362 %/day Fitted Leakage Rate 8.348 //day 14

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REX:TXCM X 'V I

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RTD LOCATIONS AND VOLUMES 3 RTD's el. 194 VOLUME 242,055 CU FT.

RTD 38 40 9 RTD'S el.

453,235 CU FT 171'OLUME RTD 29 37 10 RTD'S el.

669,627 130'OLUME CU FT RTD 9 18 10 RTD'S el.

600,926 84'OLUME CU FT RTD 19 28 8 RTD'S EL.

534,157 40'OLUME CU FT RTD 1 8 Figure 1

t RHD LOCATIONS AND VOLUMES 3 RHD'S LI ME I el 1,049, 347 171'OL C U FT RHD 8 10 N

4 RHD'S el 900,640 84'OLUME CU FT RHD 4 7 3 RHD'S el 40'OL UME 550,0 13 C U FT RHD 3 1 Figure 2

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FLOW DIAGRAM ILRT PRESSURE SENSING & CONTROLLED LEAKAGE INSTRUMENTS VOLUMETRICS ABSOLUTE PRESSURE SENSOR INSIDE PI OUTSIDE CONTAINMENT CONTAINMENT monitored vent VOLUMEIRICS ABSOLUTE P

PRESSURE 52E CONDENSATE SENSOR POT Pl Fl Fl 52D CONDENSATE POT VARIABL AREA ROTAMETER

ILRT PRESSURIZATION Bc DEPRESSURIZING SYSTEM TO ATMOSPHERE l

outside containment inside containment TO UNIT NO. 2 ILRT PENETRATION I

8" blind I

flange removed I

I for ifrt P 5 drip pot Diesel driven industrial 100% oil free air compressors

~// C (12,900 cfm total)

(13 compressors) 5 refrigerant dryer s a c a/c a/c

ILRT'NSTRUMENTATION DIAGRAM DATA COLLECTION, OUTPUT, AND STORAGE olumetrics Pressure Sensor Fluke IBM PC Data EBASCO Logger Software 40 Printer Printer Humet Diskette Humidity 10 g Data Collection IBM PC Detector EBASCO

• Data Analysis Software Printer Diskette

ILRT TEST SEQUENCE I I I I I I I I I I I I I I I I I I 40

~ 25 A: PRESSURIZATION C

e ~20 B: CONTAINMENT STABILATION PERIOD C: LEAK CHASE PERIOD 10 D: INTEGRATED LEAKAGE RATE TEST E: CONTROLLED LEAKAGE RATE TEST (CLRT)

F: DEPRESSURIZATION o

~~ ~~

y)

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TABULATION OF "AS-FOUND" AND "AS-LEFT" ILRT RESULTS A. Correction of ILRT Results for "AS -FOUND" Case In accordance with NRC 18cE Information Notice 85-71, additions are required to the ILRT results due to repairs and/or adjustments made due to Local Leakage rate testing during an outage in which an ILRT is conducted.

The corrections include only repairs or adjustments made to containment leakage boundaries which were made prior to the ILRT. These corrections are the difference between the pre-repair.and post-repair leakages calculated in the minimum pathway case and corrected for uncertainties in the measurements.

Total Minimum ILRT Penetration Pathwa Leaka e Uncer taint Correction P-11 Purge Supply 82$ $ sccm 1$ 9 sccm 83$ 9 sccm P-43 Rx Drn Tnk pmp suction 15$ sccm 12.8 sccm 163 sccm P-67 Cntnmnt Vacuum Relief 35$ sccm 1.8 sccm 352 sccm P-68 Cn tnmn t Vacuum Relief 14$ sccm 1.8 sccm 142 sccm Personnel Air Lock 162$ $ sccm 1$ 9 sccm 163$ 9 sccm The total local minimum pathway leakage plus uncertainty must be added for the penetrations which are in use during the ILRT and whose containment isolation valves are not tested:

Total Minimum ILRT Penetration Pathwa Leaka e Correction P-52D ILRT Test $ sccm 1.8 sccm 1.8 sccm P-52E ILRT Test $ sccm 1.8 sccm 1.8 sccm P-54 ILRT Pressurization $ sccm 1.8 sccm 1.8 sccm The total "as-found" correction can be found adding the above ILRT corrections.

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Correction of ILRT results for "as-found" case 25281 sccm

.8137 %/day Measured ILRT leakage at a 95% UCL + 8.1S1 %/day Reported "as-found" ILRT results 8.1947 //day Acceptance Criteria (75/ La) 8.375 %/day B. Correction of ILRT Results for "AS-LEFT" Case The only correction for the "as-lef t" ILRT case involves the penetrations which were in use during the test: P-52D, P-52E and P-54. From the above section, the ILRT "as-lef t" correction can be determined. (Note: A conservative implication was made by not performing a root-mean-square summation of the local uncertainties. )

Correction of ILRT results for "as-lef t" case 5.37 sccm 2.95 x 18  %/day Measured ILRT Leakage at a 95 / UCL + 8.181 '//day Reported "as-left" ILRT results 8.181 %/day Acceptance Criteria (75% La) 8.375 %/day

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CDNTAINNENT INTEGRATED LEAKAGE RATE F INAL TEST REPORT PSL I SPRING 98 27

ILRT TEST SEQUENCE PSL 1 SPRING 98 Sequence Started 83: 18 4/85/98 Sequence Ended 19:36 4/86/98 28

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Appendix B.l TENPERATURE STABILIZATION NODE PSL 1 SPRING 98 Sequence Started 13:18 4/85/98 Sequence Ended 17: 18 4/85/98

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PSL 1 SPRING 98 STABILIZATION PERIOD" STARTED AT 13: 18 ON 4/85/98 TEMPERATURE STABILIZATION SAMPLE TIME AVE TEMP DELTA T/HR DELTA T/HR DELTA T/HR NUMBER HOURS DEG F LAST 2 HRS LAST 1 HR CHANGE 1 8.88 95.964 8.888 8.888 8.888 2 8.33 93.798 8.888 8.888 8.888 8.67 92. 61 1 8.888 8.888 8.888 1.8$ 91.848 8.888 -4.124 8.$ $ $

5 1.33 91.279 8.888 -2.511 8.888 6 1.67 9$ .833 $ .888 -1.778 8.888 7 2.88 98.462 -2.751 -1.378 1.373 8 2.33 98.127 -1.831 -1.152 8.679 9 2.67 89.834 -1. 389 -8.'999 8.389 18 3.88 89.547 -1.146 -8.915 8.231 11 3.33 89.38$ -$ .99$ -$ .827 $ .163 12 3.67 89.868 -8.887 -8.774 8.113 13 4.88 88.842 -8.818 -8.7$ 5 8.185 4 NOTES

1) THE 1 HOUR AND 2 HOUR DELTA TEMPERATURE VALUES ARE NQT VALID UNTIL 1 HOUR AND 2 HOURS, RESPECTIVELY, HAVE PASSED IN THE TEST

2) THE STABILIZATION CRITERIA IS MET WHEN:

-THE HOURLY AVERAGE DELTA T FQR THE PRECEDING HOUR DIFFERS FROM THE HOURLY AVERAGE DEI TA T FOR THE PRECEDING 2 HOURS BY LESS THAN 8.5 DEGREES F. OR

-THE HOURLY AVERAGE DELTA T FOR THE PRECEDING 2 HOURS IS LESS THAN 1.8 DEGREES F.

-THE STABILIZATIQN PERIOD IS A MINIMUM OF 4 HOURS

3) THE "4" INDICATES THAT THE STABILIZATION CRITERIA HAS BEEN MET.

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Temperature Stabilization 98 97 96 95 94 Temperature 93 Stabilization criteria 92 met 91 90 89 88 87 85 0.00 1.00 2.00 3.00 4.00 HOURS IN TEST

Appendix B. 2 ILRT TEST NODE PSL 1 SPRING 98 Sequence Started 23: 18 4/85/98 Sequence Ended 87: 18 4/86/98

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PSL 1 SPRING 98 CONTAINMENT INTEGRATED LEAKAGE RATE TEST LEAKAGE RATE IS MEASURED USING THE ABSOLUTE METHOD AND IS COMPUTED USING THE TOTAL TIME METHOD IN STRICT ACCORDANCE WITH TOPICAL REPORT BN-TOP-1 ( REV 1 )

TEST PERIOD STARTED AT 23: 18 HOURS ON 4/85/98 TEST CONDUCTED FOR 8.$ $ HOURS FREESPACE VOLUME OF CONTAINMENT IS 2588888 CU FT CONTAINMENT WAS PRESSURIZED TO 55. 16 PSIA FITTED TOTAL TIME ILRT LEAKAGE RATE Lam 8.883  % /DAY UPPER LIMIT QF 95% CONFIDENCE LEVEL UCL $ .1B1 % /DAY CONTAINMENT DESIGN LEAKAGE RATE La 8.588 / /DAY ILRT ACCEPTANCE CRITERIA 75/. La 8.375 / /DAY

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BN-TQP REDUCED DURATION ILRT TERMINATION CRITERIA

-THE TREND OF THE TOTAL TIME CALCULATED LEAKAGE RATE SHALL INDICATE THAT THE MAGNITUDE QF THE LEAKAGE RATE IS TENDING TQ STABILIZE AT A VALUE LESS THAN OR EQUAL TO 75% QF La.

La = 8.588  % /DAY 75% La = 8.375  % /DAY

.Lam 8.883  % /DAY with a Negative Skew

-AT THE END OF THE ILRT THE UPPER LIMIT OF THE 'P5% CONF IDENCE LEVEL SHALL BE LESS THAN OR EQUAL TO 75% OF La.

UCL = 8.i8i  % /DAY

-THE MEAN OF THE MEASURED LEAKAGE RATES OVER THE LAST 5 HOURS OR 28 DATA SETS, NHICHEVER PROVIDES THE MOST POINTS, SHALL BE LESS THAN OR EQUAL TO 75% OF La.

MEAN QF SIMPLE LEAKAGE FOR SAMPLES = 8.ilh  % /DAY

DESCRIPTION QF VARIABLES AVE TEMP CONTAINMENT MEAN TEMPERATURE CALCULATED FROM VOLUMETRICALLY WEIGHTED RTD SENSOR INDICATIONS.

PRESSURE PRIMARY CONTAINMENT PRESSURE INDICATION.

VAPOR PRES CONTAINMENT VAPOR PRESSURE CALCULATED FROM VOLUMETRICALLY WEIGHTED HUM I D I TY/DEWPO INT SENSOR I ND I CAT I ONS .

LEAK SIM SIMPLE TOTAL TIME MEASURED LEAKAGE RATE.

LEAK F I T LEAKAGE RATE CALCULATED FROM FIRST ORDER REGRESSION OF SIMPLE TOTAL TIME LEAKAGE RATE DATA.

95% UCL UPPER LIMIT OF THE 95/ CONFIDENCE LEVEL OF F I TTED LEAKAGE RATE DATA.

AIR MASS CONTAINMENT AIR MASS.

NOTES FOR TABULAR DATA

1. TABLE VALUES OF ZERO SIGNIFY THE DATA IS NOT APPLICABLE TO THE CALCULATION.

2. "DELETED" SIGNIFIES THE SENSOR WAS DELETED.

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ILRT WEIGHTED AVERAGE TEMPERATURE 88 87 86.

85 HOURS IN TEST

ILRT CONTAINMENT ABSOLUTE PRESSURE 56 55.9 55.8 55.7 55.6 55.5 55A 55.3 55.2 55.1 55 54.9 54.8 54.7 54.6 54.5 54.4 54.3 54.2 54.1 54 HOURS IN TEST

I ILRT WEIGHTED AVERAGE VAPOR PRESSURE 0.3 0.299 0.298 0.297 0.296 0.295 0.294 0.293 0.292 0.291 0.29 0.289 0.288 0.287 0.286 0.285 0.284 0.283 0.282 0.281 0.28

,0 HOURS IN TESl

I ILRT AIR MASS 680 679.5 679 o

678.5 z~

678 Z~+

677.5 5

677 676.5 676 HOVRS IN TEST

I ILRT BN TOP Leakage Rates Relotive to Limits 0.6 La 0.5 OA 75% La 0.3 0.2 0.1 HOURS IN TESl UCL + .

FIlTED LEAKAGE 0 La h 75% La

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ILRT VARIABLE TABLE

SUMMARY

SAM TIME AVE TEMP PRESSURE VAP PRES LEAK SIM LEAK FIT UCL AIRMASS NO HOURS DEB F PSIA  %/DAY  %/DAY  %/DAY LBS 8.88 86.277 55.159 $ .2938 8.8$ 8 8.$ $ 8 8.$ $ 8 678891 2 8.33 86.159 55.147 8.2934 -8.822 8.888 8.888 678893 3 8.67 86.868 55.136 8.2948 8.899 8.888 8.8$ 8 678872 5

1 '8 1.33 85.976 85.865 55.124 55.113 8.2938 8.2942 8.212 8.163 8.214 8.213 8.243 8.539 678831 678838 6 1.67 85.774 55.182 8.2941 8.178 8.219 8.478 678887 7 2 '8 85.673 55.891 8.2944 8.174 8.218'.284 8.434 677993 8 2.33 85.577 55.881 8.2942 8.151 8.489 677992 9 2.67 85.484 55.878 8.2948 8.156 8.197 8.384 677974 18 3.88 85.391 55.868 8.2948 8.148 8.189 8.363 677966 11 3.33 85.299 55.$ 58 8.2937 8.148 $ .188 8.344 677959 12 3.67 85.288 55.841 8.2934 8.122 8.168 $ .325 677964 13 4.88 85.128 55.831 8.2933 8.132 8.162 8.318 677942 14 4.33 85.842 55.822 8.2931 8.123 8.154 8.295 677948 15 4.67 84.954 55.813 8.2929 8.114 8.146 8.282 677948 6 5.$ $ 84.864 55.884 8.2924 8.183 8.137 8.268 677946 5.33 84.798 54.996 8.2922 8.899 8.129 8.255 677942 5.67 84.717 54.988 $ .2921 8.$ 97 $ .122 8 244 677936 19 6.88 84.649 54.988 8.2928 8.188 8.116 8. 23'4 677922 2$ 6.33 84.567 54.972 8.2917 8 '91 $ .11$ 8.224 677928 21 6.67 84.489 54.964 8.2913 8.885 8.184 8.214 677931 22 7.$ 8 84.415 54.956 8.2918 $ .$ 82 $ .$ 99 $ .2$ 6 677928 23 7.33 84. 34'9 54.949 8.2989 8.888 8.894 8.197 677925 24 7.67 84.278 54.942 8.2986 8.869 8.$ S8 8.189 677941 8.88 84.287 54.935 8.2984 8.869 8.883 8.181 677934 41

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SENSOR VOLUME FRACTIONS TEMPERATURE SENSORS 1 to 5 8.826788 8.$ 26788 8.826788 8.826788 8.826788 6 to 18 8.826788 8.826788 8.826788 8.826785 8.826785 11 to 15 8.826785 8.826785 8.826785 8.826785 8.826785 16 to 28 $ .826785 8.826785 8.826785 8.824837 8.824837 21 to 25 8.824837 8.$ 24837 8.824837 8.824837 8.824837 26 to 38 8.824837 8.824837 8.824837 8.$ 28144 8.828144 31 to 35 8.828144 8.828144 8.828144 8.828144 8.828144 36 to 48 8.828144 8.828144 8.832274 8.832274 8.832274 HUMIDITY/DP SENSORS to 5 $ .$ 73335 $ .873335 8.873335 8.898864 8.898864 6 to 18 8.898864 8.898864 8.139913 8.139913 8.139913 NOTE: VALUE OF ZERO INDICATES A DELETED SENSOR.

42

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ILRT TEMPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TEMP 1 TEMP 2 TEMP 3 TEMP 4 TEMP 5 TEMP 6 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F

$ .$ $ 8$ .849 81.377 8$ .33$ 8$ .$ 96 79.654 81.8$ 9

$ .33 8$ .86$ 81.334 8$ .319 8$ .1$ 8 79.654 81.798

$ ~ 67 8$ .827 81.345 8$ .319 8$ .1$ 8 79.643 81.798 4 1.$ $ 8$ .845 81.363 8$ 348

~ 8$ .137 79.661 81.81 5 1 ~ 33 8$ .8$ 9 81.328 8$ .314 8$ .1$ 1 79.659 81.814 6 1.67 8$ .838 81.334 8$ .33$ 8$ .13$ 79.666 81.8$ 9 7 2.$ $ 8$ .S49 81.314 8$ .319 8$ .$ 96 79.643 81.798 8 2.33 8$ 816

~ 81.3$ 3 S$ .33$ 8$ .1$ 8 79.654 81.798 9 2.67 8$ .827 81.3$ 3 8$ .319 8$ .$ 96 79.643 81.798 1$ 3.$ $ 8$ .773 81.281 8$ .31$ 8$ .$ 96 79.643 81.8$ 9 11 3.33 8$ .838 81.27$ 8$ .319 8$ .1$ 8 79.666 81. 798 12 3.67 8$ .849 81.249 8$ .319 8$ .$ 96 79.654 81.8$ 9 13 4.$ $ 8$ .8$ 7 81.238 8$ .31$ 8$ .$ 96 79.643 81.798 14 15 4 '3 4.67 S$ .8$ 7 8$ .784 81.238 81.2$ 7 8$ .31$

8$ .298 8$ .1$ 8 8$ .$ 87 79.654 79.643 81.798 81.798 16 5.$ $ 8$ .795 81.227 8$ .31$ 8$ .$ 76 79.623 81. 798 17 5.33 8$ .784 81.2$ 7 8$ .298 8$ .$ 76 79.632 81.8$ 9 18 5.67 8$ .816 Bi. 185 8$ .298 8$ .$ S7 79.632 81.787 19 2$

6 6.

'$ 8$ .773 8$ .784 81.185 81.165 8$ .298 8$ .298 S$ .$ 65 8$ .$ 76 79'.632 79 '32 81.787 81.787 33'.67 21 8$ .8$ $ 81.147 8$ .28$ 8$ .$ 7$ 79.616 81.78$

22 7.$ $ 8$ .784 81.131 8$ .287 8$ .$ 65 79.623 81.775 23 7.33 8$ .753 81.131 8$ .276 8$ .$ 65 79.612 81.766 24 7.67 8$ .746 81.124 8$ .269 8$ .$ 47 79.6$ 5 81.76$

25 8 '$ 8$ .746 81.136 8$ .26$ . 8$ .$ 47 79.6$ 5 81.769

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ILRT TEMPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TENP 7 TEMP 8 TENP 9 TENP 18 TENP 11 TENP 12 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F I

1 8.88 79.892 79.786 88.684 87.962 88.313 88.886 2 8.33 79.892 79.889 88 '34 87.888 88.154 87.925 3 m.h7 79.881 79.818 88.417 87.618 87.971 87.766 4 1.88 79.987 79.884 88.248 87.495 87.828 87.611 5 1.33 79.896 79.845 88 111 F 87.331 87.667 87.458 6 1 ~ 67 79.892 79.786 87. 914 87.218 87.555 87.315 7 2.88 79.892 79.818 87.795 87.849 87.363 87.142 8

9 2.33 2.67 79.881 79.881 79.818 79.889 87.721 86.898 87 '45 87.$ 26 87.529 86.782 87. 118 86.896 18 3.88 79.881 79.786 87.421 86.652 86.999 86.779 11 3.33 79.881 79.786 87.248 86.535 86.872 86.649 12 3.67 79.869 79.889 87.153 86.485 86.776 86.521 13 4.88 79.881 79.798 86.983 86.288 86.626 86.483 14 4.33 79.881 79.889 86.918 86.158 86.588 86.255 15 4.67 79.881 79.755 86.779 86.853 86.412 86.198 16 5.88 79.869 79.764 86.714 85.956 86.296 86.871 17 5 '3 5.67 79 '69 79.869 79.786 86.533 85.849 86.288 85.963 18 79.755 S6.511 85.741 86.892 85.847 19 6. 88'.33 79.858 79.775 86.383 85.645 ,85.985 85.758 28 79.858 79.755 86.222 85.548 85.911 85.665 21 6.67 79.854 7'9. 759 86.119 85.445 85.786 S5.562 22 7.88 79.849 79.786 86.852 85.344 85.717 85.461 23 24 7.33 7.67 79.858 79.831 79.798 85.965 85 '59 85.681 85.365 79.759 85.895 85.167 85.518 85.262 25 8.88 79.831 79.737 85.777 85.879 85.433 85.174

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ILRT TEMPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TENP 13 TENP 14 TENP 15 TEMP ib TENP 17 TENP 18 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 $ .$ $ 88.13$ 88.139 88.243 88.1$ 8 88.184 88.226 2 $ .33 87.96$ 87.989 88.$ 93 87.'969 88.$ 23 88.$ 67

$ .67 87.833 87.838 87.934 87.796 87.884 87.9$ 6 4 1.$ $ 87.678 87.683 87.8$ $ 87.675 87.74$ 87.783 5 1.33 87.5$ 4 87.522 87.639 87.512 87.567 87.6$ $

6 1.67 87.372 87.387 87.5$ 5 87.38$ 87.432 87.4?9 7 2.$ $ 87.222 87.248 87.334 87.23$ 87.273 87.318 8 2.33 87.$ 94 87.1$ 9 87.216 87.1$ 2 87.154 87.179 2.67 86.953 86.97$ 87.$ 99 86.972 87.$ $ 3 87.$ 6$

1$ 3.$ $ 86.826 86.842 86.949 86 '33 86.887 86.933 11 3.33 86.7$ 7 86.723 86.831 86.7$ 6 86.768 86.8$ 3 12 3.67 86.58$ 86.6$ 4 86.714 86.587 86.649 86.687 13 4.$ $ 86.461 86.476 86.596 86.448 86.532 86.568 14 4.33 86.356 86.379 86.477 86.363 86.4$ 2 86.441 15 4.67 86.248 86.251 86.372 86.244 86 '96 86.333 16 5.$ $ 86.141 86.144 86.253 86.126 86.189 86.226 17 5.33 86.$ 22 86.$ 47 86.157 86.$ 29 86.$ 92 86.118 18 5.67 85.926 85.939 86.$ 61 85.944 85.984 86.$ 22 19 6.$ $ 85.821 85.843 85.942 85.828 85.888 85.915 2$ 6.33 85.745 85.746 85.857 85.729 85.78$ 85.819 21 6.67 85.631 85.632 85.754 85.628 85.688 85.716 22 7.$ $ 85.53$ 85.542 85.654 85.548 85.587 85.626 23 7.33 85.456 85.466 85.568 85.44$ 85.49$ 85.541 24 7.67 85.342 85.365 85.466 85.36$ 85.419 85.449 25 8.$ $ 85.257 85.278 85.389 85.263 85.311 85.353

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ILRT TFNP'ERATURE VARIABLE

SUMMARY

SANPLE DELTA TEMP 19 TEMP 28 TENP 21 TENP 22 TEMP 23 TENP 24 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 8.88 88.845 86.828 86.648 87 '83 87.797 87.239 8.33 87.862 86.889 86.552 87.383 87.721 87.143 8 '7 1.88 87.788

87. 613 86.798 86.766 86.552 86.518 87.241 87.283 87.658 S7.189 87.889 87.614'7.629 5 1.33 87.492 86.728 86.458 87.138 87.$ 29 6 1.67 87.368 86.728 86.545 86.988 87.576 87.848 7 2.88 87.219 86.882 86.597 86. 912 87.479 86.975 8

9 2 '3 2.67 87.183 87.827 86.674 86.567 86.469 86 '69 86.816 86.753 87.383 87.287 86.898 86.981 18 3.8$ 86.938 86.498 86.395 86.635 87.159 86.847 11 3.33 86.684 86.466 86.283 86.583 87 '36 86.777 12 3.67 86.61$ 86.394 86.265 86.411 86.945 86.621 13 14 4

4

'8

'3 S6.545 86.418 86.32$

86.266 86.373 86.168 86.293 86.288 86.848 86 '64 86.643 86.547 15 4.67 86.299 86.168 86.198 86.898 86.632 86.457 16 5.88 86.171 86.874 86.852 86.815 86.529 86.385 17 5.33 86.895 86.868 85.983 85.983 86.428 86.284 18 5.67 85.979 85.995 85.929 85.818 86.332 86.284 19 6.$ $ S5.894 85.899 85.878 85.733 86.267 86.179 28 6.33 85.786 85.838 85.84S 85.631 86.164 86.138 21 22 6 '7 7.88 85.695 85.657 85.753 85.688 85.721 85.624 85.512 85.458 86.868 85.983 86.8$ $

85.968 23 7.33 85.529 85.668 85.548 85.362 85.989 85.S83 24 7.67 85.426 85.568 85.474 85.266 85.882 85.887 25 S.88 85'.341 85.424 85.369 85.183 85.719 85.713

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ILRT TEMPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TEMP 25 TEMP 26 TEMP 27 TEMP 28 TEMP 29 TEMP 3$

NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 $ .$ $ 87.9$ 1 88.$ 53 87.577 87.829 87.992 87.884 2 $ .33 87.678 87.754 87.46$ 87.679 87.842 87.7$ 2

$ .67 87.6$ 4 87.763 87.4$ 7 87.6$ 5 87.694 87.53$

4 1.$ $ 87.443 87.615 87.373 87.648 87 '53 87.424 5 1.33 87.34$ 87.521 87.3$ 4 87.415 87.398 .87.256 6 1.67 87.19$ 87 '36 87.132 87.245 87.268 87.137 7 2.$ $ 87.$ 74 87.35$ 87.154 87.18$ 87.$ 75 86.956 8 2.33 86.944 87.265 87.$ 15 87.$ 41 86.959 86.839 9 2.67 86.816 87.146 86.'885 86.979 86.84$ 86.7$ $

1$ 3.$ $ 86.698 87.$ $ 7 86.812 86.925 86.681 86.539 11 3.33 86.555 86.9$ 6 86.,7$ $ 86.856 86.58$ 86.449 12 3.6? 86.463 86.771 86.619 86.721 86.455 86.313 13 4.$ $ 86.335 86.663 86.492 86.625 86.37$ 86.174 14 4.33 86.217 86.578 86.447 86.464 86.242 86.$ 89 15 4.67 86.1$ 7 86.468 86.326 86.386 86.121 85.999 ib 5.$ $ 86.$ 13 86.354 86.223 86.241 86.$ $ 5 85.831 17 5.33 85.9$ 4 86.273 86.145 86.194 S5.9$ 6 85.764 18 5.67 85.8$ 8 86.176 86.$ 3S 86.$ 97 85.777 85.636 19 6.$ $ 85.732 86.$ 91 85.964 86.$ 32 85.714 85.593 2$ 6.33 85.62$ 85.988 85.87$ 85.952 85.577 85.457 21 6.67 85.524 85.891 85.8$ 7 85.833 85.515 85.36$

22 7.$ $ 85.416 85.784 85.669 85.737 85.418 85.221 23 7.33 85.34$ 85.71$ 85.6$ 4 85.663 85.311 85.179 24 7.67 85.255 85.613 85.5$ 8 85.567 85.226 85.$ 6$

25 8.$ $ 85.173 85.541 85.445 85.493 85.143 85.$ $ $

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ILRT TENPERATURE VARIABLE SUNNARY SANPLE DELTA TENP 31 TENP 32 TENP 33 TENP 34 TENP 35 TENP 36 NUNBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 $ ~ $$ 87.8$ 6 87.92$ 87.991 87.831 87.852 87.782 2 $ .33 87.636 87.75$ 87.843 87.658 87.693 87.623

$ .67 87.464 87.577 87.64$ 87 '76 87.52$ 87.473 4 1.$ $ 87.294 87.416 87.5$ 1 87.359 87.4$ 4 87.334 5 1.33 87.16$ 87.282 87.387 87.214 87.215 87.166 6 1.67 87.$ 53 87.165 87.225 87.$ 74 87.$ 85 87.$ 15 7 2.$ $ 86.883 86.992 87.$ 75 86.924 86.947 86.876 8

9 2 '3 2.67 86.754 86.627 86.885 86.746 86.959 86.8$ 9 86.794 86.635 86.796 86.68$

86.738 86.6$ 8 1$ 3.$ $ 86.488 86.618 86.7$ 1 86.527 86.55$ 86.48$

ll ,

3-33 86.388 86.5$ 6 86.558 86.415 86.418 86.348 12 3.67 86.22$ 86.34$ 86.446 86.269 86.315 86.256 13 4.$ $ 86.1$ 4 86.253 86.316 86.161 86.218 86.159 14 15 4.33 4.67 86.$ 39 85.9$ 8 86.157 86 '27 86.231 86.$ 99 86.$ 44 85.935 86.$ 9$

85.969 86 '$ '9 85.9$ 8 16 5.$ $ 85.774 85.879 85 954 85.818 85.844 85.774 17 5.33 85.662 85.769 85.864 85.7$ 8 85.743 85.684 18 5.67 85.597 85.7$ 4 85.777 85.6$ $ 85.647 85.599 19 6.$ $ 85.492 85.619 85 '92 85.546 85.584 85.512 2$ 6.33 85.41$ 85.516 85.6$ $ 85.423 85.47$ 85.4$ $

21 6.67 85.294 85.42$ 85.493 85.336 85.362 85.312 22 7.$ $ 85.186 85.323 85.397 85.23$ 85.255 85.196 23 7.33 85.122 85.227 85.323 85.143 85.181 85.12$

24 7.67 85.$ 26 85.131 85.2$ 4 85.$ 37 85.$ 62 85.$ $ 3 25 8.$ $ 84.965 85.$ 68 85.153 84.974 85.$ $ 2 84.929

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ILRT TENPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TENP 37 TEMP 38 TEMP 39 TEMP 4$

NUMBER HOURS DEG F DEG F DEG F DEG F

$ .$ $ 88.$ 19 87.677 87.959 87.779

$ .33 87.849 87.516 87.788 87.595

$ .67 87.71$ 87.335 87.6$ 7 87.456 4 1.$ $ 87.572 87.228 87.488 87.313 5 1.33 87.392 87.$ 62 87.311 87.172 6 1.67 87.276 86.921 87.Z$ 4 87.$ 29 7 2.$ $ 87.137 86.751 87.$ 23 86.867 8 2.33 86.998 86.623 86.884 86.728 9 2.67 86.86$ 86.494 86.754 86.59$

1$ 3.$ $ 86.719 86.366 '86.637 86.5$ 5 11 3.33 86.6$ 9 86.265 86.525 86.343 12 3.67 86.484 86.1$ 9 86.38$ 86.236 13 4.$ $ 86.398 86.$ 35 86.Z84 Bb. 151 14 4.33 86.26$ 85.939 86.156 86.$ $ 1 15 4.67 86.15$ 85.784 86.$ 55 85.893 16 5.$ $ S6.$ $ 2 85.67$ 85.941 85.786 17 5.33 85.924 85.592 85.S4$ 85.7$ 1 18 5.67 85.828 85.476 85.744 85.582 19 6.$ $ 85.754 85.422 85.681 85.519 2$ 6.33 85.629 85.265 85.525 85.381 21 6.67 85.544 85.189 85.471 85.287 22 7.$ $ 85.425 85.$ 73 85.332 85.2$ 8 23 7.33 85.371 84.997 85.245 85.112 24 7.67 85.244 84.892 85.16$ 85.$ $ 9 25 8.$ $ 85.172 84'.84$ 85.12$ 84.935

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ILRT PRESSURE AND HUMIDITY VARIABLE

SUMMARY

SAMPLE DELTA PRES 1 PRES 2 HUM '

HUM 2 HUM HUM 4 NUMBER HOURS PSIA PSIA RH RH RH RH 1 8.88 55.161 55.159 39.498 42.698 42.668 48.378 2 8.33 55.158 55.147 39.678 42.848 42.888 48.388 3 8.67 55.137 55.136 39.818 42.968 42.938 48.448 4

5 1 '8 1.33 55.126 55.114 55.124 55.113 39.978 43.118 43.148 48.548 48.168 43.248 43.338 48.828 6 1.67 55.184 55.182 48.298 43.368 43.558 48.778 7 2.88 55.894 55.891 48.488 43.498 43.738 48.958 8 2.33 55.883 55.881 48.548 43.598 43.918 49.128 9 2.67 55 '72 55.878 48.688 43 '98 44.898 49.84$

18 3.88 55.863 55.868 48.828 44.818 44.318 49.228 11 3.33 55.853 55.858 48.978 44.188 44.528 49.258 12 3.67 55.843 55.841 41.118 44.388 44.678 49.348 13 4.88 55.834 55.831 41.258 44.568 44.888 49.318 14 4.33 55.$ 25 55.822 41.3B8 44.758 45.848 49.418 15 4.67 55.816 55.813 41.568 44.958 45.278 49.568 16 5.88 55.$ 87 55.884 41 . 648 45.158 45.458 49.518 17 5.33 54.999 54.996 41.778 45.378 45.638 49.558 18 5.67 54.998 54.988 41.938 45.568 45.$ 18 49.668 19 6.88 54.982 54.988 42.838 45.768 46.838 49.7$ 8 28 6.33 54.974 54.972 42.218 45.978 46.268 49.758 21 6.67 54.966 54.964 42.348 46.288 46.448 49.768 22 7.88 54.959 54.956 42.498 46.428 46.668 49.828 23 7.33 54.952 54.949 42.598 46.668 46.858 49.798 24 7.67 54.944 54.942 42.828 46.988 47.188 49.928 25 8.88 54.936 54.935 43.838 47.158 47.348 49.848

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I LRT HUMIDITY VAR I ABLE

SUMMARY

SAMPLE DELTA HUM 5 HUM 6 HUM 7 HUM 8 HUM 9 HUM 18 NUMBER HOURS  % RH RH RH RH RH RH 1 8.88 47.658 48.368 47.88$ 48.578 49.488 49.678 2 8.33 47.668 48.148 48.368 48.698 49.698 49.798 8.67 48.178 49.218 48.588 48.858 49.888 49.888 4 1.$ $ 48.28$ 49.83$ 48.32$ 48.988 49.968 5$ .87$

5 1.33 48.218 49.638 48.718 49.168 58.888 58.258 6 1.67 48.698 49.548 48.918 49.268 58.228 58.398 7 2.88 48.928 58.838 49.848 49.398 58.368 58.538 8 2.33 49.86$ 58.178 49.148 49.588 58.458 58.658 2.67 49.818 58.298 49.288 49.618 58.688 58.788 f8 3.88 49.488 58.438 49.358 49.748 58.718 58.858 11 3.33 49.S88 58.54$ 49.388 49.888 58.818 58.988 12 3.67 49.588 58.598 49.478 49.918 58.868 51.848 13 4.88 49.658 5$ .72$ 49.528 58.$ 8$ 5$ .998 51.16$

14 4.33 49.788 58.768 49.688 58.878 51.848 51.298 15 4.67 49.78$ 58.87$ 49.64$ 58.16$ 51.19$ 51.378 lb 5.88 49.878 58.958 49.718 58.248 51.298 51.438 17 5.33 49.968 58.98$ 49.888 S8.388 51.348 51.488 18 5.67 58.838 51 '38 49.828 58.368 S1.488 51.578 19 6.88 58.868 51.898 49.888 58.488 51.458 51.658 28 6.33 58.118 51.13$ 49.888 58.558 51.528 51.728 21 6.67 58.218 51 '88 49.89$ 58.588 51.618 51.738 22 7.88 58.228 51.288 49.998 5$ .638 51 618 51.818 23 7.33 58.278 51.288 49.988 58.7$ 8 51 78$ 51.858 24 7.67 5$ .388 51.388 58.828 58.74$ 51.?58 51.888 25 8.88 58.36$ 51.348 58.888 58.788 51.778 51.998

Appendix B. 5 CLRT TEST NODE PSL 1 SPRING 98 Sequence Started 88: 18 0/86/98 Sequence Ended 12:18 4/86/'P8 52

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PSL 1 SPRING 98 CONTAINMENT INTEGRATED LEAKAGE RATE TEST I

SUPPLEMENTAL VER IF CATION TEST LEAKAGE RATE IS MEASURED USING THE ABSOLUTE METHOD AND IS COMPUTED USING THE TOTAL TIME METHOD IN STRICT ACCORDANCE WITH TOPICAL REPORT BN-TOP-1 < REV 1 )

TEST PERIOD STARTED AT 88: 18 HOURS QN 4/86/98 TEST CONDUCTED FOR 4.88 HOURS FREESPACE VOLUME OF CONTAINMENT IS 2588888 CU FT CONTAINMENT NAS PRESSURI ZED TO 54.91 PS I A FITTED TOTAL TIME ILRT LEAKAGE RATE Lam 8.883 / /DAY CONTAINMENT DESIGN LEAKAGE RATE La 8.588 / /DAY SUPERIMPOSED CLRT LEAKAGE RATE Lo 8.299  % /DAY FITTED CLRT TOTAL TIME LEAKAGE RATE Lc 8.334  % /DAY Lo + Lam La/4 <= Lc <= Lo + Lam + La/4 8.299 + 8.883 8.125 <= 8.334 <= 8.299 + 8.883 + 8.125 8.257 <= 8.334 <= 8.587

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DESCRIPTION OF VARIABLES AVE TEMP CONTAINMENT MEAN TEMPERATURE CALCULATED FROM VOLUMETRICALLY WEIGHTED RTD SENSOR INDICATIONS.

PRESSURE PRIMARY CONTAINMENT PRESSURE INDICATION.

VAPOR PRES CONTAINMENT VAPOR PRESSURE CALCULATED FROM VOLUMETRICALLY WEIGHTED HUMIDITY/DEWPOINT SENSOR INDICATIONS.

LEAK S IM SIMPLE TOTAL TIME MEASURED LEAKAGE RATE.

LEAK F IT LEAKAGE RATE CALCULATFD FROM FIRST ORDER REGRESSION OF SIMPLE TOTAL TIME LEAKAGE RATE DATA.

95% UCL UPPER LIMIT OF THE 95% CONFIDENCE LEVEL OF FITTED LEAKAGE RATE DATA.

AIR MASS CONTAINMENT AIR MASS.

NOTES FOR TABULAR DATA

1. TABLE VALUES OF ZERO SIGNIFY THE DATA IS NOT APPLICABLE TO THE CALCULATION.

2. "DELETED" SIGNIFIES THE SENSOR WAS DELETED.

CLRT Weighted Average Temperature 85 84.8 84.6 84A 84.2 83.8 83.6 83A 83.2 82.8 82.6 82A 82.2 82 Time in Hours

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CLRT Containment Absolute Pressure 56 55.9 55.8 55.7 55.6 55.5 55A 55.3 55.2 55.1 55 54.9 54.8 54.7 54.6 54.5 54A 54.3 54.2 54.1 54 Time in Hours

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CLRT Weighted Vapor Pressure 0.3 0.299 0.298 0.297 0.296 0.295 0.294 0.293 0.292 0.291 0.29 0.289 0.288 0.287 0.286 0.285 0.284 0.283 0.282 0.281 0.28 Time in Hours

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CLRT Air Mass 678 677.9 677.8 677.7

~m~M 677.6 8 677.5

~og 677A 677.3 677.2 677.1 677 Time in Hours

CLRT BN TOP Leakage Rates Relative to Limits 0.9 0.8 0.7 0.6 u per limit 0.5 OA 0.3 lower limit 0.2 0.1 Time in Hours III Fitted Leakage + UCL 4 Lo+Lam-La/4 A Lo+Lam+Lc/4

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CLRT VARIABLE TABLE SUNNARY SAN T INE AVE TENP PRESSURF VAP PRES LEAK SIN LEAK F IT AIRNASS NO HOURS DEG F PSIA PSIA //DAY  %/DAY  %/DAY LBS 1 8.88 84.887 54.9$ 6 8.2897 8.888 8.$ 88 8.8$ $ 677832 2 8.33 83.948 54.a97 8.2895 $ .269 8.$ $ 8 8.8$ $ 677887 3 8.67 83.885 54.888 8.2895 8.363 8.888 8.888 677764 4 1.88 83.822 54.888 8.2a93 8.387 $ .332 8.921 677745 5 1.33 83.768 54.871 8.2892 8.343 8.346 8.562 677783 6 1.67 83.787 54.863 8.2898 8.328 8.337 8.486 677682 7 2.88 83.651 54.855 8.2889 8.316 8.338 8.447 677654 8 2.33 83.595 54.846 8.2888 8.332 8.333 8.429 677613 9 2.67 83.539 54.838 8.2887 8.338 8.334 8.417 677584 18 3.88 83.489 54.831 8.2886 8.328 8.331 8.485 677561 11 3.33 83.444 54.823 $ .2887 8.335 8.334 8.481 677516 12 3.67 83.3Sb 54.815 8.2884 8.328 8.333 8.395 677492 13 4.88 83.342 54.888 8.2885 8.329 8.334 8.391 677468

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SENSOR VOLUME FRACTIONS TEMPERATURE SENSORS 1 to 5 8.826788 8.826788 8.826788 8.826788 8.826788 6 to 18 8.826788 8.826788 8.826788 8.826785 8.826785 11 to 15 8.826785 8.826785 $ .826785 8.826785 8.826785 16 to 2$ 8.8267S5 8.826785 $ .826785 8.824837 8.824837 21 to 25 8.824837 8.824837 8.$ 24837 8.824837 8.824837 26 to 3$ 8.824837 8.824837 8.824837 8.828144 8.828144 31 to 35 8.828144 8.828144 8.828144 8.828144 8.828144 36 to 4$ 8.828144 Z.828144 8.832274 8.832274 8.832274 HUM I D I TY/DP SENSORS 1 to 5 8.873335 8.873335 $ .873335 8.898864 8.898864 6 to 18 8.898864 8.898864 $ .139913 8.139913 8.139913 NOTE: VALUE OF ZERO INDICATES A DELETED SENSOR.

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CLRT TENPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TENP 1 TENP 2 TEMP TENP 4 TENP 5 TENP 6 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 8.88 S8.773 S1.188 S8.267 S8.$ 45 79.681 S1.755 2 8.33 S8.742 Si.869 S8.267 S8.$ 45 79.5S9 Si 744

~

8.67 S8.73$ S1.877 S8.245 S8.$ 45 79.5S9 Sl.744 4 1.88 S8.719 S1.869 S8.256 S8.834 79.5S9 S1 ~ 744 5 1.33 S$ .719 S1.$ 77 S8.245 S8.$ 54 79.5S9 S1.744 6 1.67 S8.738 81.$ 69 S8.245 S8.834 79.57S S1.733 7 2.88 S8.753 S1.846 S8.233 S8.834 79.57S S1 ~ 733 S 2.33 S8.719 S1.857 S8.233 S8.823 79.57S S1.722 9 2.67 S8.742 S1.835 S8.245 S8.834 79.57S S1.722 1$ 3.88 S8.762 S1.846 S8.233 S8.845 79.57S S1.722 11 3.33 S8.719 S1.824 S8.233 S8.845 79.57S S1.713 12 3.67 S$ .762 S1.$ 24 S$ .233 S$ .$ 45 79.57S S1 ~ 713 13 4.88 S8.719 S1.824 S8.233 S8.845 79.681 S1.713

l CLRT TENPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TENP 7 TENP 8 TEMP 9 TEMP 1$ TENP 1 1 TENP 12 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 $ .$ $ 79.816 79.764 85 '17, 84.819 85.163 84 '35 2 $ .33 79.827 79.764 85.441 84.743 85.$ 98 84.849 3 $ .67 79.S$ 4 79.764 85.325 84.669 85.$ 14 84.775 4 1.$ $ 79.796 79.755 85.249 84.582 '4.949 84.699 5 1.33 79.8$ 4 79.764 85.249 84.485 84.853 84.614 6 1.67 79.816 79.755 85.11$ 84.434 84.788 84 '49 7 2.$ $ 79.8$ 4 79.732 85.$ 45 84.358 84.714 84.464 8 2.33 79.796 79.721 84.983 84.292 84.65$ 84.399 2.67 79.784 79.721 84.918 84.218 84.587 84.345 1$ 3.$ $ 79.8$ 4 79.721 84.788 84.153 84.511 S4.26$

11 3.33 79.796 84.788 84.$ 91 84.438 84.195 12 3.67 79.796 79.712 84.6?2 84.$ 26 84.373 84.121 13 4.$ $ 7'9. 8$ 4 79.721 84.65$ 83.961 84.319 84.$ 79

I CLRT TENPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TFNP 13 TENP 14 TENP 15 TENP 16 TENP 17 TEMP 18 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 $ .$ $ 85.$ 18 85.$ 26 85.141 85.$ $ 1 85.$ 62 85.114 2 $ .33 S4.942 84.941 85.$ 54 84.928 84.985 85.$ 29

$ .67 84.857 84.867 84.98$ 84.863 84.911 84.953 4 1 ~ $$ 84.783 84.791 84.895 84.778 84.824 84.868 5 1.33 84.696 84.7$ 5 84.S19 84.713 84.761 84.792 6 1.67 84.633 84.64$ 84.745 84.648 84.674 84.718 7 2.$ $ 84.568 84.566 84.669 84.552 84.611 84.642 8 2.33 84.483 84.49$ 84.6$ 4 84.478 84.534 84.579 9 2.67 84.4$ 7 84.416 84.53$ 84.424 84.472 84.5$ 3 1$ 3.$ $ 84.354 84.362 84.465 84.359 84.4$ 6 84.45$

ll 3.33 3.67 84.291 84.226 84.286 84.4$ 3 84.3$ 5 84.2$ 9 84.341 84.267 84.376 84.311 12 84.223 84.338 13 4.$ $ 84.161 84.158 84.273 84.146 84.2$ 2 84.257,

I CLRT TENPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TEMP 19 TENP 2$ TENP 21 TENP 22 TEMP 23 TENP 24 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 $ .$ $ 85.122 85.237 85.143 S4.935 85.482 85.486 2 $ .33 85.$ 25 85.195 85.$ S9 84.85$ 85.4$ 6 85.39$

3 $ .67 84.951 85.1$ 5 85.$ $ 8 84.8$ 3 85.35$ 85.354 4 1.$ $ 84.875 85.$ 74 84.946 84.7$ 7 85.254 85.246 5 1.33 a4.a33 84.993 84.896 84.638 85.2$ 2 85.19?

6 1.67 84.737 84.917 84.811 84.573 85.1$ 6 85.121 7 2.$ $ 84.672 84.852 84.746 84.497 S5.$ 44 85.$ 78 8 2.33 84.6$ 9 84.789 84.67$ 84.446 84.99$ 84.993 9 2.67 84.544 84 '24 84.585 84.37$ 84.925 84.939 1$ 3.$ $ 84.49$ 84.688 84.538 84.312 84.847 84.881 11 3 33 84.394 84.646 84.495 84.249 84.793 84.818 12 3.67 84.329 84.563 84.4$ 3 84.166 84.722 84.769 13 4.$ $ 84.267 84.523 84.352 84.115 84.672 84.7$ 6

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CLRT TEMPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TENP 25 TEMP 26 TEMP 27 TENP 28 TENP 29 TENP 38 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 8.88 84.984 85.278 85.197 85.267 84.872 84.728 2 8.33 84.839 85.285 85.112 85.171 84.887 84.643 3 8.67 84.758 85.126 85.854 85.893 84.729 84.596 4 1.88 84.674 85.852 84.957 85.828 84.632 84.511 5 1.33 84.685 84.969 84.899 84.948 84.572 84.397 6 1 ~ 67 84.548 84.986 84.823 84.872 84.498 84.323 7 2.88 84.466 84.838 84.761 84.889 84.444 84.288 8 2.33 84.379 84.756 84.685 84.733 84.348 84.193 9 2.67 84.327 84.782 84.628 84.668 84.294 84 F 1.38 18 3.88 84.258 84.633 84.553 84.621 84.216 84.861 11 3.33 84.284 84.578 84.488 84.536 84.182 84.818 12 3.67 84.135 84.498 84.439 84.476 84.182 83.938 13 4.88 84.872 84.426 84.378 84.415 84.819 83.875 66

I CLRT TEMPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TEMP 31 TEMP 32 TEMP TEMP TEMP 35 TEMP 36 NUMBER HOURS DEG F DEG F DEG F DEG F DEG F DEG F 1 $ .$ $ 84.695 84.799 84.862 84.694 84.71$ 84.661 2 $ .33 84.577 84.68$ 84.777 84.6$ 9 84.623 84.564 3

4

$ .67 1.$ $

84.521 84.445 84.622 84.559 84.71$ 84.562 84 '87 84.517 84.633 84.485 84.513 84.441 5 1.33 84.334 84.477 84.584 84.4$ 5 84 '41 84.383 6 f..67 84.28$ 84.4$ 3 84.477 84.319 84.345 84.296 7 2.$ $ 84.215'4.151 84.327 84.4$ 3 ,84.243 84.28$ 84.222 8 2.33 84.253 84.349 84.169 84.217 84.157 9 2.67 84.$ 77 84.179 84.264 84.1$ 4 84.132 84.$ 6$

1$ 3.$ $ 84.$ 19 84.121 84.2$ 6 84.$ 26 84.$ 52 83.993 11 3.33 83.954 84.$ 78 84.152 83.983 84.$ 2$ 83.959 12 3.67 83.885 83.9'95 84.$ '92 83.9$ $ 83.928 83.859 13 4.$ $ 83.845 83.944 84.$ 2$ 83.86$ 83.877 83.816 67

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CLRT TEMPERATURE VARIABLE

SUMMARY

SAMPLE DELTA TEMP 37 TEMP 38 TEMP 39 TEMP 4$

NUMBER HOURS DEG F DEG F DEG F DEG F 1 $ .$ $ 84. 9$ 1 84.57$ 84.851 84.673 2 $ .33 84.8$ 5 84.462 84.721 84.6$ 8 3 $ .67 84.747 84.427 84.674 84.523 4 1.$ $ 84.673 84.342 84.578 84.449 5 1.33 84.613 84.261 84.52$ 84.384 6 1.67 84.528 84.185 84.455 84.3$ 8 7

8 2 '$

2.33 84.463 84.4$ $

84.123 84.$ 46 84.379 84.3$ 5 84.234 84.181 9 2 '7 84.3$ 4 83.961 84.231 84.$ 84 1$ 3.$ $ 84..234 83.892 84.173 84.$ 2$

ii 3.67 84.2$ 3 83.85$

83.769 84.131 83.957 83.892 12 84.111 84.$ 59 13 4 '$ 84.$ 6$ 83. 72'9 83.976 83.838 68

CLRT PRESSURE AND HUNIDITY VARIABLE

SUMMARY

SANPLE DELTA PRES 1 PRES 2 HUN 1 HUN 2 HUM 3 HUN 4 NUMBER HOURS PSIA PSIA RH / RH RH RH 1 $ .88 54.988 54.986 43.718 47.868 48.828 49.85$

2 8.33 54.988 54.897 43.988 48.188 48.278 58.888 3 8.67 54.898 54.888 44.238 48.368 48.528 58.888 4 1.88 54.882 54.888 44.468 48.578 48.768 49.998 5 1.33 54.873 54.871 44.688 48.838 48.978 5$ .178 6 1.67 54.865 54.863 44.948 49.878 49.268 58.168 7 2.88 54.857 54.855 45.218 49.318 49.478 58.188 8 2.33 54.849 54.846 45.428 "

49.548 49.738 58.168 2.67 54.848 54.838 45.678 49.8$ 8 49.978 58.198 18 3.88 54.833 54.831 45.898 58.838 58.218 58.268 11 54.825 54.823 46.138 58.278 58.438 58.448 12 3.67 54.817 54.815 46.328 58.518 58.698 58.328 13 4.8$ 54.818 54.888 46.528 58.778 58.928 58.488

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CLRT HUMIDITY VARIABLE

SUMMARY

SAMPLE DELTA HUM 5 HUM 6 HUM 7 HUM 8 HUM HUM 18 NUMBER HOURS  % RH RH RH RH RH RH 1 8.88 58.458 51.438 58.158 58.928 51.838 52.158 2 8.33 58.488 51.448 58.138 58.938 51.938 52.148 3 $ .67 58.538 51.588 58.168 58.958 51.998 52.158 4 1.88 58.568 51.478 58.218 51.858 52.818 52.228 5 1.33 58.588 51.518 58.228 51.84$ 51.998 52.238 6 1.67 58.578 51.538 58.248 51.188 52.888 52.278 7 2.88 58.628 51.548 58.298 51.888 52.128 52.258 S 2.33 58.638 51.638 58.338 51.168 52.148 52.368 9 2.67 58.698 51.618 58.378 51.188 52.198 52.398 18 3.88 58.718 51.688 58.378 51.288 52.228 52.38$

11 3.33 58.728 51.658 58.398 51.248 52.238 52.468 12 3.67 58.788 51.738 58.368 51.248 52.288 52.518 13 4.88 58.838 51 '38 58.448 51.298 52.338 52.55$

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Appendix B. 4 LEAK CHASE PSL 1 SPRING 98 Sequence Started 17: 1$ 4/$ 5/98 Sequence Ended 22:58 4/85/98 71

LEAK CHASE PERIOD Samp l e Time In, Average Pressure Vapor Air number Mode Temperature Pressure Mass 1 8. 88 88 '42 55.463 8.2984 678781 2 8.33 88.627 55.439 8.29 678677 3 8.67 88.427 55.418 8.2988 678656 4 1.88 =

88.238 55.397 8.2981 67864$

5 1.33 88.863 55.37? 8.2981 6?8611 6 1.67 87.897 55.357 8.2896 678577

? 2.8$ 87.729 55.339 $ .2885 678575 8 2.33 87.59 55.321 8.2883 678528 9 2.67 87.449 55.383 8.2876 678498 18 3.8$ 87.381 55.287 8.2868 678486 11 3.33 87.175 55.2?i 8.2858 678458 12 3.67 87.859 55.255 8.2857 678486 13 4.88 86.931 55.24 8.2868 678366 14 4.33 86.814 55.226 8.2861 678346 15 4.67 86.782 55.211 8.2884 678272 16 5.88 86.591 55. 198 '.2982 678227 17 5 ~ 33. 86.49 55.185 8.2917 678173 18 5.67 86.367 55.172 $ .2922 678159

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Appendix C LOCAL, LEAKAGE RATE TESTING CONDUCTED SINCE LAST I LRT

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PEN NAME COMPONENT I.D. DATE AS FOUND AS LEFT 1 MN STM 1A 1 87/2$ /88 8.8 8.8 1 MN STM 1A 2 87/28/88 8.8 $ .8 1 MN STM 1A 1 Sl/83/98 8.8 8.8 1 MN STM 1A 2 Si/83/98 8.$ 8.8 2 MN STM 1B 1 87/28/88 8.$ 8.8 2 MN STM 1B 2 87/28/88 8.8 8.8 2 MN STM iB Si/$ 3/98 $ .$ $ .$

2 MN STM 1B 2 Si/83/98 8.8 8.8 3 FEEDWATER lA 1 87/28laa 8.8 8.8 3 FEEDWATER 1A 2 87/28/88 8.8 8.8 3 FEEDWATER 1A Si/83/98 8.8 8.8 FEEDWATER lA 2 Si/83/98 8.8 8.8 4 FEEDWATER 1B 2 87/28/88 8.8 8.8 4 FEEDWATER iB 1 87/2$ /88 8.$ 8.8 4 FEEDWATER 1B 1 mi/$ 3/98 8.8 8.8 4 FEEDWATER 1B 2 81/83/9$ $ .$ $ .$

7 PRIMARY MAKE UP V15328 87/15/88 7588.8 8.8 7 PRIMARY MAKE UP MV15-1 87/ia/88 168.8 168.8 7 PRIMARY MAKE UP V 15328 88/iS/88 8.8 1128.8 7 PRIMARY MAKE UP V 15328 Si/24/98 38$ .$ 388.8 7 PRIMARY MAKE UP MV15-1 81/24/98 $ .8 8.8 7 PRIMARY MAKE UP MV15-1 83/$ 7/98 8.8 328.8 a SERVICE AIR V18794,18796 $ 8/2$ /88 175.8 175.$

8 SERVICE AIR V 18797 88/28/88 8.8 8.8 8 SERVICE AIR V18798 88/2$ /88 8' 8.8 8 SERVICE AIR V 18795 88/28/88 8.8 8.8 8 SERVICE A IR V18794, 1S796 81/25/9$ 1288.$ 1288.8 8 SERVICE .AIR V}8797 81/25/98 388.8 388.8 8 SERVICE AIR V18798 81/25/98 8.8 8.8 8 SERV I CE A IR V 18795 81/25/9$ 35.$ 35.$

9 INSTRUMENT AIR MV18-1, V18193 88/16/88 5888.8 8.8 9 INSTRUMENT AIR V 18195 Sal 16laa 8.8 8.8 9 INSTRUMENT AIR MV18-1, V18193 88/21/S8 8.8 1588.8 INSTRUMENT AIR MV18-1, V18193 83/21/98 548.$ 548.8 9 INSTRUMENT AIR V 18195 83/21/98 14688$ .8 8.8 INSTRUMENT AIR V 18195 83/24/98 8.8 3888.8 18 CNTNMNT PRG EXH FCV25-4,5 $ 8/89/88 4488.8 $ .$

18 CNTNMNT PRG EXH FCV25-4,5 88/17/88 8.8 388.8 18 CNTNMNT PRG EXH FCV25-4,5 82l ia/98 468.8 8.8 18 CNTNMNT PRG EXH FCV25-4s5 83/84/98 8.8 2888.8 18 CNTNMNT PRG EXH FCV25-4,5 84/84/98 8.8 2258.8 18 CNTNMNT PRG EXH FCV25-4,5 84/ im/98 8.8 228.8 ll 11 CNTNMNT CNTNMNT PRG PRG MU MU FCV25-2,3 FCV25-2,3 88/82/88

$ 8/12/88 45$ .8 8.8 24$ .8 11 CNTNMNT PRG MU FCV25-2,3 81/24/98 988978.8 8.8 il ll CNTNMNT CNTNMNT PRG PRG MU MU FCV25-2,3 FCV25-2,3 82l 19/98 83/il/98 18888.8 8~8 8.8 28888.8 il 11 CNTNMNT CNTNMNT PRG PRG MU MU FCV25-2,3 FVC25-2,3 84/84/98 84/87/98 8.8 8.8 lamm.m 288.8 14 NITROGEN V6779 87/19/88 8.8 8.8 14 NITROGEN V6741 87/19/88 8.8 8.8

NAME COMPONENT I.D. DATE AS FOUND LEFT 14 NITROGEN V6348 87/19/88 8.8 8.8 14 NITROGEN V6779 81/38/9$ 188.8 188.8 14 NITROGEN V6741 81/38/98 8.8 8.8 14 NITROGEN V6348 81/38/98 8.8 8.8 23 CCW TO RCP HCV14-1, 7 87/1S/88 98.8 8.8 23 CCW TO RCP V 14368 87/15/88 8.8 8.8 23 CCW TO RCP V14367 $ 7/.15/88 $ .$ $ .$

23 CCW TO RCP HCV14-1, 7 88/18/88 8.8 2588.8 23 CCW TO RCP V 14368 88/18/88 8.8 8.8 23 CCW TQ RCP V14367 88/18/88 8.8 8.8 23 CCW TQ RCP HCV14-1, 7 87/83/89 8.8 8.8 23 CCW TO RCP HCV14-1, 7 87/12/89 8.8 8.8 23 CCW TQ RCP V 14367 87/12/89 8.8 8.8 23 CCW TO RCP HCV14-1 ~ 7 $ 1/38/98 $ .8 8.8 23 CCW TO RCP V14368 81/38/98 8.8 8.8 23 CCW TQ RCP V14367 81I38/'98 8.$ 8.8 23 CCW TO RCP HCV14-1, 7 83/$ 7/98 8.8 58. 8 24 CCW FROM RCP HCV14-2, 6 87/15/88 8.8 8.8 24 CCW FROM RCP V14415 87/15/88 8.8 8.8 24 CCW FROM RCP V14417 87/15/88 1888.8 8.8 24 CCW FROM RCP HCV14-2, 6 88/18/88 8.8 8.8 24 CCW FROM RCP V14415 88/18/88 8.8 818.8 24 CCW FROM RCP V1441? $ 8/18/88 $ .$ 3$ $ .8 24 CCW FROM RCP HCV14-2, 6 87/13/89 17.9 8.8 24 CCW FROM RCP HCV14-2, 6 87/14/89 8.8 8.8 24 CCW FROM RCP HCV14-2,6 81/38/98 8.8 8.8 24 CCW FROM RCP V14415 . 81/38/98 8.8 8.8 24 CCW FROM RCP V14417 81/38/98 148.8 148.8 24 CCW FROM RCP HCV14-2, 6 83/87/98 8.8 8.8 25 FUEL XFR 1 $ 7/2$ /88 $ .$ $ .$

25 FUEL XFR 1 82/82/98 8.8 8.8 26 LETDOWN V2515 88/12/88 8.8 8.8 26 LETDOWN V2516 88/12/88 17.9 8.8 26 LETDOWN V2516 88/27/88 8.8 38.8 26 LETDOWN V2515 82/26/98 8.8 8.8 26 LETDOWN V2516 82/26/98 17.9 8.8 26 LETDOWN V2516 $ 3/1$ /98 8.$ 45.$

28A S IT SAMPLE FCV83-lE 87/28/88 88.8 88.8 28A S IT SAMPLE FCV83-1F 87/28I88 78.8 78.$

28A S I T SAMPLE FCV83-iF 81/38/98 8.8 8.8 28A S IT SAMPLE FCV83-iF 81/38/98 8.8 8.8 28B RCS HQT LEG V5288 87/28/88 88.8 8.8 28B RCS HQT LEG V5283 87/28/88 48.8 8.8 28B RCS HOT LEG U52$ 8 $ 8/12/88 8.8 1$ $ .8 28B RCS HOT LEG V5283 88/12/88 8.8 55.8 28B RCS HOT LEG V5288 12/88I88 185.8 1$ 5.8 28B RCS HOT LEG SAM VS288 82/81/98 135.8 135.8 28B RCS HQT LEG SAM V5283 82/81/98 8.8 8.8 29A PZR SRG SAMPLE V5281 84/11/88 1285.8 8.8 29A PZR SRG SAMPLE V5284 84/11/88 8.8 8.8 29A PZR SRG SAMPLE V52$ 1 84/13/88 8.8 6S$ .8

?5

I I

NAME COMPONENT I.D. DATE AS FOUND AS LEFT 29A PZR SRG SAMPLE 84/}3/88 8.8 8.8 29A PZR SRG SAMPLE V5281 87/28/88 8588.8 8.8 29A PZR SRG SAMPLE V5284 87/28/88 6788.8 8.8 29A PZR SRG SAMPLE V5281 88/15/BB 8.8 688.8 29A PZR SRG SAMPLE V5284 88/}5/88 8.8 8.8 29A PZR SRG SAMPLE V528} 82/81/98 8.8 8' 29A PZR SRG SAMPLE V5284 82/8} l98 8.8 8.8 29B PZR STM SAMPLE V5285 87/23/87 8.8 8.8 29B PZR STM SAMPLE V5282 87/28/88 8388.8 $ .$

29B PZR STM SAMPLE V5285 . 87/28/88 8.8 8.8 29B PZR STM SAMPLE V52$ 2 $ 8/2$ /88 8.8 $ .$

29B PZR STM SAMPLE V5282 82/81/98 8.8 8.$

298 PZR STM SAMPLE V5285 $ 2/$ 1/9$ 6$ $ .$ 688 8~

3} CNTNMNT VNT HDR V6554 87/28/BB 8.8 8.8 3} CNTNMNT VNT HDR V6555 $ 7/28/88 $ .$ 8.8 31 CNTNMNT VNT HDR V6554 8}/38/98 8.8 8.8 31 CNTNMNT VNT HDR V6555 81/3$ /98 8.8 8.8 41 SIT TEST V87889,V3463 87/2}/88 8.8 8.$

41 SIT TEST V87818 87/21/88 8.8 8.8 41 SIT TEST V$ 7889,V3463 82/82/98 8.8 8.8 41 SIT TEST V878}8 82/82/98 8.8 8.8 42 42 RX RX CAVITY SUMP CAVITY SUMP

'A'5284 LCV87-A,}}B V$ 7}71 88/15/BB 88/15/88 668$ .8 288.8 8.8 8.8 42 RX CAVITY SUMP LCV87-1}A, 11B 88/19/88 8.8 3288.8 42 RX CAVITY SUMP LCV87-1}A,}1B 82/88/98 2288.8 2288.8 42 RX CAVITY SUMP V87171 82/88/98 628.8 628.8 43 RX DRAIN TNK V6381 88/}9/88 588.8 588.8 43 RX DRA IN TNK V6382 88/}9/88 458.$ 458.8 43 RX DRAIN TNK V6381 82/81/98 658.8 8.8 43 RX DRA IN TNK V6382 82/81/98 588.8 8.8 43 RX DRAIN TNK V6381 82/82/98 8.8 488.8 43 RX DRAIN TNK V63$ 2 82/82/98 8.$ 358.8 44 RCP BLEEDOFF SE81-1 87/2$ /88 8.8 8.8 44 RCP BLEEDOFF V25$ 5 87/28/88 8.8 8.8 44 RCP BLEEDOFF SE81-1 88/19/88 $ .8 8.8 44 RCP BLEEDOFF V2585 $ 8/19/88 8.8 8.8 44 RCP BLEEDOFF SE81-1 82/82/98 8.8 8.8 44 RCP BLEEDOFF V2585 82/82l98 8.8 8.8 46 RFL CVTY PRF RT V87}89,872 88/}5/88 88.8 8' 46 RFL CVTY PRF RT V87}67 88/}5/88 8.$ 8.8 46 RFL CVTY PRF RT V87}89>872 88/2}/88 8.8 188.8 46 RFLNG CVTY PURF V87189, 2$ 6 82/27/98 8$ $ .$ 8$ $ .8 46 RFLNG CVTY PURF V87167 $ 2/27/98 25.8 25.8 47 RFL CVTY PRF SP V87 }88, 871 $ 8/}5/88 $ .$ 8.8 47 RFL CVTY PRF SP V87169 88/}5/88 8.8 8.8 47 RFLNG CVTY PURF V$7}88, 17$ $ 2/27/9$ 8.$ $ .$ 47 RFLNG CVTY PURF V87169 82/27/'98 258.8 25$ .8 48A H2 SMP TO 'A'2 FSE27-1 $ 7/19/88 $ .$ 8.$ 48A SMP TO FSE27-2 87/}9/88 8.8 8.8

                                                                       }8.$
                   'A'2 48A     SMP TO    'A'2 FSE27-3             $ 7/}9/88       18.8 48A     SMP TO          FSE27-4             87/19/88          8.8        8.8

I I I I I

PEN NAME COMPONENT I.D. DATE FOUND LEFT 48A H2 SMP TO 2 FSE27-8 $ 7/19/88 76.8 76.$ 48A SMP TO 'A'2 FSE27-1 81/38/98 8.8 8.8 48A SMP TO 'A'2 FSE27-2 81/3$ /98 8.$ 8.8 48A SMP TO 'A'2 FSE27-3 81/38/98 8.8 8.$ 48A SMP TO FSE27-4 $ 1/3$ /98 8.8 8.$

                   'A'
                   'A'2 48A      SMP   TO                     FSE27-8          81/38/98          8.8     8.8 48C H2 SMP     FROM            'A'Z   V27181           87/18/88      428.8    428.$

48C SMP FROM 'A'2 FSE27-il 87/18/88 8.8 8.8 48C SMP FROM 'A'2 FSE27-11 $ 8/24/89 8.8 8.8 48C SMP FROM 'A:, V27181 81/38/98 8.8 8.8 48C H2 SMP FROM 'A'2 FSE27-il 81/38/98 8.8 8.8 51A SMP FROM 'B'2 V27 182 88/19/88 58.8 58.8 51A SMP FROM 'B'2 FSE27-18 88/19/88 8.8 8.8 51A SMP FROM 'B'2 V27182 81/38/98 48.8 48.$ 51A SMP FROM 'B'2 FSE27-18 81/38/98 8.8 8.8 51C SMP TO 'B'2 FSE27-5 87/19/88 8.$ 8.8 51C SMP TO 'B'2 FSE27-6 87/19/BB 288.8 288.8 51C SMP TQ 'B'2 FSE27-7 87/19/88 8;8 8.8 51C SMP TO 2 FSE27-9 87/19/88 288.8 288.8 51C SMP TQ 2 FSE27-5 81/38/98 8.8 8.8 51C SMP TO FSE27-6 81/38/98 $ .8 8.8 81/38/98 8.8 8.8

                       'B'H2 51C      SMP    TO       'B'2 FSE27-7 51C      SMP    TO                    FSE27-9          81/38/9$          8.8     8.8 82/18/88 2831998. 8       8.8
                        'B'AD 52A         MON SUP                   FCV26-1 52A RAD, MON'UP                       FCV26-2          82/18/88     1188.8       8.8 52A RAD     MQN  SUP                  FCV26-1          82/12/88          8.8  458.8 52A RAD     MON  SUP                  FCV26-1          87/19/88      388.8       8.8 52A RAD     MON  SUP                  FCV26-2          87/19/88      3$ 8.$      8.$

52A RAD MON SUP FCV26-1 $ S/18/88 8.$ 55.8 52A RAD MON SUP FCV26-1 81/31/98 48.8 8.$ 52A RAD MON SUP FCV26-2 81/31/98 188.8 8.8 52A RAD MON SUP FCV26-1 83/27/98 8.8 288.8 52A RAD MON SUP FCV26-2 83/27/98 8.8 68.$ 52B IODINE RAD MON FCV26-3 87/18/88 36888.8 8.8 52B IODINE RAD MON FCV26-4 87/18/88 388.8 3$ 8.$ 52B IOD INE RAD MQN FCV26-3 88/89/88 8.8 42$ .8 52B IODINE RAD MQN FCV26-3 81/31/98 48.8 $ .8 52B I OD I NE RAD MON FCV26-4 81/3'1/98 5616286.8 8.8 52B IODINE RAD MON FCV26-3 83/27/98 8.8 95.8 52B IODINE RAD MQN FCV26-4 83/27/98 8.8 288.8 52B IODINE RAD MON FCV26-3 84/12/98 8.8 888.$ 52C RAD MON RET FCV26-5 85/16/88 288.8 8.8 52C RAD MON RET FCV26-6 85/16/88 48.8 8.8 52C RAD MON RET FCV26-6 85/18/88 8.8 8.8 52C RAD MON RET FCV26-5 87/19/88 148.8 8.8 52C RAD MON RET,, FCV26-6 87/19/88 17 ' 8' 52C RAD MON RET FCV26-5 81/31/98 48.8 8.8 52C RAD MON RET FCV26 81/31/98 38.8 38.8 52C RAD MON RET FCV26-5 83/27/98 8.8 35.8 52D ILRT CLRT V88148, 143 83/22/87 8.8 8.8 52D ILRT CLRT V88148, 143 87/18/88 388.8 8.8 77

I I I I I I

NAME COMPONENT I.D. DATE AS FOUND AS LEFT 52D ILRT CLRT V88142 87/iB/BB 8.8 8.8 52D ILRT CLRT V88148, 143 $ 1/31/9$ 388.8 8.'8 52D ILRT CLRT V88142 81/31/98 8.8 8.8 52D ILRT CLRT V$ 8148, 143 84/89/98 8.$ 7B8.8 52D ILRT CLRT V88 142 84/89/98 8.8 8.8 52E ILRT PRESS V88139, 144 83/23/B7 8.8 258.8 52E ILRT PRESS V88139,144 87/1B/BB 8.8 8.8 52E ILRT PRESS V88141 87/iB/BB 8.8 8.8 52E ILRT PRESS V88139,144 81/31/98 8.8 8.8 52E ILRT PRESS V88141 81/31/98 $ .8 8.8 52E ILRT PRESS V88139, 144 84/$ 9/98 8.8 1B.8 52E ILRT PRESS V88141 84/89/98 8.8 1B.8 54 ILRT PZR V88181 83/23/B7 8.8 1588.8 54 ILRT PZR V88181 87/12/BB 1858.$ 8.8 54 ILRT PZR V88 181 8B/17/BB 8.8 2588.$ 54 ILRT PZR V881$ 1 81/29/98 8.8 8.8 54 ILRT PZR V88181 84/89/98 8' 968.8 56 H2 PURGE MAKEUP V25-11, 12 83/27/B7 8.8 78.8 56 H2 PURGE MAKEUP V25-11,12 87/22/BB B8.8 B8.8 H2 PURGE MAKEUP V25-11,12 81/24/98 78.8 78 ' H2 PURGE FILTER V25-13, 14 83/27/B7 8.8 125.8 H2 PURGE FILTER V25-13>14 87/22/BB 98.8 98.8 H2 PURGE FILTER V25-13, 14 $ 1/24/9$ 2$ 8.$ 288.8 5B H2 PRG FLTR BYP V25-15, 16 83/27/B7 8.8 268.8 5B H2 PRG FLTR BYP V25-15, 16 87/21/BB 278.8 278.8 5B H2 PRG FLTR BYP V25-15s 16 81/24/98 388.8 3$ 8.8 67 CNTNMNT VAC RLF V25-2$ 87/21/BB 588.$ 5$ $ .$ 67 CNTNMNT VAC RLF FCV25-7 87/21/BB 688.8 6$ 8.8 67 CNTNMNT VAC RLF FCV25-7 $ 2/23/9$ 4$ $ .8 $ .$ 67 CNTNMNT VAC RLF V25-28 82/26/98 688.8 688 ' 67 CNTNMNT VAC RLF FCV25-7 $ 3/12/9$ $ .$ 5$ .$ 6B CNTNMNT VAC RLF V25-21 87/21/BB 1B68$ 8.8 8.8 6B CNTNMNT VAC RLF FCV25-B 87/21/BB 8.$ $ .$ 6B CNTNMNT VAC RLF FCV25-21 8B/89/BB 8.8 7888.8 6B CNTNMNT VAC RLF FCV25-21 88/19/BB 8.8 6B$ $ .$ 6B CNTNMNT VAC RLF FCV25-B 82/23/98 148.8 8.8 6B CNTNMNT VAC RLF FCV25-21 $ 2/2B/9$ 9788.$ $ .$ 6B CNTNMNT VAC RLF FCV25-21 83/12/98 8' 98.8 6B CNTNMNT VAC RLF FCV25-B 83/14/98 8.8 8.$ Ai ELECT PEN NA 87/21/BB 8.8 8.$ Ai ELECT PEN NA 82/87/98 8.8 8.8 A2 ELECT PEN NA 87/21/BB 8' 8.8 A2 ELECT PEN NA $ 2/87/98 8.8 8.8 A3 ELECT PEN NA 87/21/BB 8.8 8.8 A3 ELECT PEN NA 82/87/98 8.8 8.8 A4 ELECT PEN NA 87/21/BB 8.8 8.8 A4 ELECT PEN NA 82/87/98 8' 8.8 A5 ELECT PEN NA 87/21/BB 8.$ 8.8 A5 ELECT PEN NA 82/87/98 8' 8.8 A6 ELECT PEN NA 87/21/BB 8.8 8.8 A6 ELECT PEN NA 82/87/98 8.8 8.8 7B

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PEN NAME COMPONENT I.D. DATE AS FOUND AS LEFT A7 ELECT PEN NA 87/21/SS $ .8 A7 ELECT PEN NA 82/87/9$ 8.8 AS ELECT PEN NA 87/21/SS 8.8 8 ' AS ELECT PEN NA 82/87/98 8.$ 8.8 A9 ELECT PEN NA 87/21/SS 8.8 8.8 A9 ELECT PEN NA 82/87/98 8.8 8' A18 ELECT PEN NA 87/21/SS 8.8 8.8 A18 ELECT PEN NA 82/$ 7/98 8.8 8.8 Bi ELECT PEN NA $ 7/21/SS $ .$ $ .$ Bi ELECT PEN NA 82/87/98 8.8 8.8 B3 ELECT PEN NA 87l21/SS 8.8 8.8 B3 ELECT PEN NA 82/87/98 8.8 8.8 B4 ELECT PEN NA $ 2/87/98 8.8 8.8 B5 ELECT PEN NA 87/21/SS 8.8 8' B5 ELECT PEN NA 82/87/98 8.8 8.8 B6 ELECT PEN NA 87/21/SS 8.8 8.8 B6 ELECT PEN NA 82/87/98 8.8 8.8 B7 ELECT PEN NA 87/21/SS 8.8 8.8 B7 ELECT PEN NA 82/87/98 8.8 8.8 BS ELECT PEN NA 87/21/SS 8.8 8.8 BS ELECT PEN NA 82/$ 7/9$ 8.8 8.8 B9 ELECT PEN NA 87/21/SS 8.8 8.8 B9 ELECT PEN NA $ 2/87/98 8.8 8.8 B4 ELECT PEN NA 87/21/SS 8.8 8.8 C1 ELECT PEN NA $ 7/21/SS $ .$ 8.$ C1 ELECT PEN NA 82/87/98 8.8 8.8 C2 ELECT PEN NA 87/21/SS 8.8 8.8 C2 ELECT PEN NA 82/87/98 8.8 8.8 C3 ELECT PEN NA $ 7/21/SS 8.8 8.8 C3 ELECT PEN NA 82/87/98 8.8 8.8 C4 ELECT PEN NA 87/21/SS 8.8 8.8 C4 ELECT PEN NA $ 2/87/9$ $ .$ $ .$ C5 ELECT PEN NA 87/21/BS $ .8 8.8 C5 ELECT PEN NA 82/$ 7/98 8.8 8.8 C6 ELECT PEN NA 87/21/SS 8.8 8.8 C6 ELECT PEN NA 82/87/98 8.8 8.8 C7 ELECT PEN NA 87/21/SS 8.8 8.8 C7 ELECT PEN NA 82/87/98 8.8 8.$ CS ELECT PEN NA $ 7/21/SS 8.$ 8.$ CS ELECT PEN NA 82/87/98 8.8 8.8 C9 ELECT PEN NR 82l87/98 8.8 8.8 C18 ELECT PEN NA 87/21/SS 8.8 8.8 C18 ELECT PEN NA 82/87/98 8.8 8' Di ELECT PEN NA 87/21/SS 8.8 8.8 Di ELECT PEN NA $ 2/87/98 8.8 8.8 D2 ELECT PEN NA 87/21/SS $ .8 8.$ D2 ELECT PEN NA 82/87/9$ $ .$ 8.8 D3 ELECT PEN NA 87/21/SS 8.8 8.8 D3 ELECT PEN NA 82/87/98 8.8 8.8 D4 ELECT PEN NA , 87/21/SS 8.8 8.8 D4 ELECT PEN NA 82/87/98 8.8 8.8

I PEN NAME COMPONENT I.D. DATE AS FOUND AS LEFT D6 ELECT PEN NA 87/21/88 8.8 8.$ D6 ELECT PEN NA 82/87/98 8.8 8.8 D7 ELECT PEN NA 87/21/88 8.8 8.$ D7 ELECT PEN NA 82/87/9$ 8.$ 8.8 DB ELECT PEN NA 87/21/88 8.8 8.8 DB ELECT PEN NA 82/87/98 8.8 8.8 D9 ELECT PEN NA 87/21/88 8.8 8.$ D9 ELECT PEN NA 82/87/98 8.8 8.8 D18 ELECT PEN NA 87l21/88 8.$ $ .$ D18 ELECT PEN NA 82/87/98 8.8 8.8 Ei ELECT PEN NA 87/21/88 8.8 $ .8 Ei ELECT PEN NA 82/87/98 8.8 8.8 E3 ELECT PEN NA $ 7/21/88 8.$ $ .$ E3 ELECT PEN NA 82/$ 7/98 8.8 8.8 E4 ELECT PEN 0 RING $ 7/12/88 8.$ $ .$ E4 ELECT PEN 0 RING 88/16/88 8.8 8.8 E4 ELECT PEN 0 RING 81/24/9$ 8.$ 8.8 E4 ELECT PEN 0 RING 82/87/98 8.8 8.8 E4 ELECT PEN 0 RING 84/82/98 8.8 8.8 E5 ELECT PEN NA 87/21/SB 8.8 8.$ E5 ELECT PEN NA 82/87/98 8.8 8.8 E7 ELECT PEN NA 87/21/88 8.$ 8.8 E7 ELECT PEN NA 82/87/9$ 8.8 $ .8 E9 ELECT PEN NA 87/21/88 8' 8.8 E9 ELECT PEN NA 82/87/98 8.8 8' EMEX EMRG EXP HATCH STRONG BACK 88/13/87 $ .$ 8.8 EMEX EMRG EXP HATCH STRONG BACK 82/11/88 8.8 8.8 EMEX EMRG EXP HATCH STRONG BACK 88/18/88 2238.$ 2238.8 EMEX EMRG EXP HATCH STRONG BACK 82/81/89 218888.$ 8.8 EMEX EMRG EXP HATCH STRONG BACK 82/81/89 8.8 1238.8 EMEX EMRG EXP HATCH STRONG BACK 87/25/89 4842.$ 4842.8 EMEX EMRG EXP HATCH STRONG BACK 83/86/98 7438.8 7438.8 EMEX EMRG EXP HATCH STRONG BACK 84/18/98 8.8 8.8 FXFR FUEL XFR FLNG 0 RING 87/12/88 8.8 8.8 FXFR FUEL XFR FLNG 0 RING 88/17/88 8.$ 8.8 FXFR FUEL XFR FLNG 0 RING 81/28/98 8.8 8.8 FXFR FUEL XFR FLNG 0 RING 83/25/98 8.8 8.8 MHG MA INT HATCH GASKET 18/89/87 8.8 $ .8 MHG MA INT HATCH GASKET 18/14/87 8.8 8.8 MHG MAINT HATCH GASKET 87l 12/88 8.8 8.8 MHG MA INT HATCH GASKET 88/22/88 8.$ 8.8 MHG MAINT HATCH GASKET 86/29/89 8.8 8.8 MHG MA INT HATCH GASKET 87/13/89 8.8 8.8 MHG MAI NT HATCH GASKET 81l23/98 8.$ 8.8 MHG MA INT HATCH GASKET 84/18/98 8.$ 8.8 PRSN PERSONNEL HATCH STRONG BACK 88/13/87 282$ .$ 2828.$ PRSN PERSONNEL HATCH STRONG BACK 82/ii/88 5848.$ 5848.8

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PEN NAME COMPONENT I.D. DATE AS FOUND AS LEFT PRSN PERSONNEL HATCH STRONG BACK 88/18/88 3888.8 388$ .8 PRSN PERSONNEL HATCH STRONG BACK $ 1/31/89 4538.8 4538.8 PRSN PERSONNEL HATCH STRONG BACK 87/26/89 6517.8 6517.$ PRSN PERSONNEL HATCH STRONG BACK 83/28/98 28888.8 $ .8 PRSN PERSONNEI HATCH STRONG BACK 83/29/98 8.8 3888.$ A summary for the Type B and C Local Leakage Rate Tests since the last ILRT are as follows (all values in sccm) . YEAR BYPASS TYPE B TYPE C TOTAL 1987 11585 41.6 4638 14689 1988 15328 6838 8766 38116 1989 1171$ 18568 8766 31836 1998 11313 11238 2438 24981 Note: Per the plant Technical Specifications the limit for total Bypass leakage is less than .27 La (245,888 sccm) and the limit for total Type B and C leakage is less than .6 La (544,$ $8 sccm). LOCAL LEAKAGE RATE PROBLEMS SINCE LAST ILRT On February 18, 1988 Containment Radiation Monitor isolation valve FCV-26-1 was found to have a leakage rate of approximately 188 scfm. This value was in excess of the plant' Technical Specif ication limit of 8.27 La (245,153 sccm) . This was reported on Licensee Event Report ¹335-88-$ 82. The valve was repaired and the as-left leakage was 458 sccm. The outside valve on this penetration was 1188 sccm, thus the as-found as well as the minimum pathway leakage for this penetration was 1188 sccm. 81

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