ML17228A264

Reactor Containment Bldg ILRT Rept

ML17228A264
Person / Time
Site:	Saint Lucie
Issue date:	05/20/1993
From:	Dillon P, Hartranft K EBASCO SERVICES, INC.
To:
Shared Package
ML17228A263	List: ML17228A262 ML17228A264
References
NUDOCS 9308260374
Download: ML17228A264 (103)

Text

ST. LUCIE NUCLEAR PLANT UNIT 1 Jensen Beach, Florida Docket Number 50-335 Reactor Containment BLIjidjng Integrated Leakage Rate Test ILRT AlR MASS 3993 St. Lucie Unit P1 ILRT Containment Alr Mass (LBS) 676,000

.'ir Mass Fitted Mas 675,800 675,600 675,400 675,200 675,000 0 i 2 3 4 5 6 7 8 Time In Hours ASGO An ZNSZRCHEngineering and Construction Company 9308260374 930823 PDR ADOCK 05000335 P P,DR

A t CONTAINMENT INTEGRATED LEAKAGE RATE FINAL COMPUTER GENERATED TEST REPORT 1993 ST. LUCIE UNIT 41 ILRT Prepared for Florida Power and Light Prepared by:

K. Hartranft Test Engineer Approved by:

Dillon Manager of Testing Date of Test Completion: May 20, 3993

TABLE F CONTENTS

~Pa e I. INTRODUCTION AND

SUMMARY

II. TEST DISCUSSION A. Description of Containment B. Description of ILRT Instrumentation

1. Temperature Instrumentation

2. Humidity Instrumentation

3. Pressure Instrumentation

4. Flow Instrumentation

5. Instrument Selection Guide gSG) Calculation C. Containment Pressurization Equipment D. Description of the Computer Program E. Description of the Testing Sequence III. ANALYSIS AND INTERPRETATION 12 A. Instrumentation System Performance 12 B. Temperature Stabilization Phase 13 C. Leakage Survey Phase 13 D.. Integrated Leakage Rate Phase 14 E. Verification Controlled Leakage Rate Phase 15 IV. FIGURES RTD Location and Volume RHD Location and Volume Flow Diagram for Pressure Sensing and Controlled Leakage Flow Diagram for Pressurization Systems Flow Diagram ILRT Data Collection, Storage, and Analysis

V APPENDICES A. Tabulation of "As-Found" and "As-Left" ILRT Results B. ILRT Computer-Generated Report

1. Test Sequence

2. Temperature Stabilization

3. Integrated Leakage Rate Test 4 Verification Controlled Leakage Rate Test

5. Non-Test Period Data C. Local Leakage Rate Testing Conducted Since the Last ILRT

I. INTR DUCTION AND

SUMMARY

A periodic Type "A" Integrat'ed Leakage Rate Test (ILRT) was successfully conducted on the primary containment structure of the Florida Power & Light Company St. Lucie Plant Unit No. 1 Pressurized Water Reactor. This test was performed at full pressure in accordance with the facility Technical Specifications.

This ILRT was performed using the "Absolute Method" of testing in accordance with the Code of Federal Regulations, Title 10, Part 50, Appendix J, "Primary 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 Specifications.

This report describes and presents the results of this periodic Type "A" leakage rate testing, including the supplemental Controlled Leakage Rate Test (CLRT) method utilized for verification. In addition, Florida Power & Light Company performs Types "B" and "C" testing in accordance with the requirements of 10CFR50, 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 .319 percent of the I

containment mass per day. This value includes the difference between the as-found and as-left minimum pathway Types "B" and "C" local leakage measurements as required by the NRC I&E Information Notice 85-71. The resulting reported "as-left" Type "A" containment leakage at 41.86 psig is .293 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 0.375 percent of the contained air mass per day for either the "as-found" or "as-left" case.

II. TEST DISCUSSION A. Descri tion of the ontainment 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 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 off-site doses.

The free-standing containment vessel is a two-inch thick hemispherical dome and two-inch thick ellipsoidal bottom. The overall vessel dimensions are 140-foot diameter by 232-foot high. The

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essel wall thickness is increased to a minimum of four inches adjacent to all penetrations arid openings. The vessel is fabricated of ASME-SA 516 Grade 70 fully killed pressure vessel quality steel plate. The net free volume of the containment vessel is 2.5 x 10'ubic feet.

The containment vessel structure includes one personnel airlock, one emergency escape lock, one fuel transfer tube, one equipment maintenance hatch and 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 feedwater, and fuel transfer tube penetrations. These penetrations are provided with testable multiple ply expansion bellows to allow for thermal growth or building differential motion.

The containment vessel is designed and constructed in accordance with the requirements for Class MC vessels contained in Section III of the ASME Code (1971 Edition). The containment vessel is code stamped for a design internal containment pressure of 44 psig at a temperature of 64'F. The containment vessel and all penetrations are designed to limit leakage to less than 0.5 percent by weight of the contained air per day at the above design conditions. The

culated peak accident pressure for the design basis accident for the St. Lucie Plant Unit No.

is 39.6 psig.

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 (Q) is calculated according to the Perfect Gas Law as follows:

Q=~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; The average containment absolute temperature is determined by measuring discreet local temperature throughout the containment and applying a mass and volume weighted averaging technique. The volume fraction for each sensor is determined based iupon solid geometrical calculations. The average containment absolute temperature is found using:

Vf; where: T - Containment Absolute Temperature (Average)

T; - Local Temperature for Sensor i Vf; - Volume Fraction for Sensor i

verage containment water vapor pressure is determined by measuring discreet relative umidities throughout the containment, converting this to local vapor pressures using local group temperatures, steam tables, and applying a mass and volume weighted averaging technique. The volume fractions for the relative humidity sensors are determined in the same manner as for the temperature sensors above. The average containment water vapor pressure is determined by:

Pvj = (%RH)j x (Psat for TLocalj) 100 Pvj VFj Pv = TE i TLocalj where: Pv Containment Water Vapor Pressure (Average)

Pvj Calculated Local Vapor Pressure for Sensor ~

Volume Fraction for Sensor j T" Containment Absolute Temperature (Average)

TLocalj Local Group Average Temperature Near Sensor j Relative Humidity for Sensor j

[%RH)j Steam Table Saturation Pressure 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 the acceptance criteria for all test instrumentation systems.

1, Tem erature Instrumentation Forty (40) precision Resistance Temperature Detectors (RTDs) were located throughout the containment to allow measurement of the weighted average air 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 +0.5'F. The sensitivity and repeatability of each RTD sensor is less than +0.01'F.

The signal conditioning circuit and readout for the RTD sensors was a Fluke data logger perating in a constant current mode. The operating parameters for the RTD constant current I

card are accuracy of +0.16'F and resolution of +0.01'F.

ch RTD was in-situ calibration checked after installation to verify correct operation, The data ogger operating as a total loop with an RTD in the circuit had a repeatability of J0.02'F and a resolution of +0.01'F.

2. Humidit Instrumentation Ten (10) Resistance Humidity Detectors (RHDs) were located throughout the containment to allow 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 +0.25 percent RH, and the sensitivity, of the RHDs is +0.1 percent RH.

The readout device used for the RHDs was a Fluke data logger. The repeatability of this device is'0.01 percent RH while the resolution of the device is +0.01 percent RH.

ch RHD was in-situ calibration checked after installation to verify correct operation.

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3. Pressure Instrumenta ion Two Volumetrics precision pressure monitors measure containment absolute pressure. Figure 3 depicts the arrangement of the tubing connections between the monitors and the containment.

Either monitor could be used as the primary pressure sensor for leakage rate calculations with the remaining sensor as a backup. The calibrated accuracy of the monitors is +0.015 percent of reading. The sensitivity, repeatability, and resolution of the monitors is +0.001 psi. Binary Coded Decimal (BCD) output from both monitors connects to the Fluke data logger.

4. Flow Instrumentation A variable area float-type rotameter was used to superimpose leakage during the supplementary

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CLRT. The piping connection between the rotameter and the containment is shown in Figure 3.

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he accuracy, repeatability, and sensitivity for the rotameter in units of SCFM and converted o equivalent leakage values is given below:

Equivalent

~SFM ~Leaka e Peak Pressure Rotameter Accuracy +0.20 +0.0031 %/day Repeatability +0.05 +0.0008 %/day Sensitivity +0.05 +0.0008 %/day

5. Instrument election Guide S alculation The Instrument Selection Guide is a method of compiling the instrumentation sensitivity and resolution for each process measurement variable used during the ILRT and evaluating the total instrumentation systems'bility to detect leakage rates in the range required. The ISG formula is described in the American National Standard ANSI/ANS 56.8-1987. Although the ISG is a very conservative measure of sensitivity, the general industry practice as for this test has been o require sensitivity at least four times better than the containment allowable leakage or ISG < 0.25La.

The calculated ISG for the instrumentation used for this test was .0027 percent per day, for an 8-hour test. The allowable value for this test is 0.25La or 0.125 percent per day, for an 8-hour test. The ISG calculation met all recommended criteria and demonstrated the ability of the ILRT instrumentation system to measure containment leakage with a sensitivity exceeding that required by the appropriate industry standards.

C. ntainment Pressurization ui ment The equipment used to pressurize the containment is shown in Figure 4. The ten oil-free industrial diesel-driven air compressors had a total nominal capacity of 13,200 ACFM. The compressed air was then routed to water-cooled aftercoolers, moisture separators, and refrigerant air dryers. ~ This equipment assured that clean, and dry air was used to pressurize the ontainment. ~

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 written in a high level, compiled, structured language and operated on an MS-DOS personal micro-computer. The program has been verified and meets all requirements of the Ebasco Quality Assurance Program.

Normal data entry to the computer is automatic via the data logger, As necessary, data entry and modifications are readily accomplished manually by the data acquisition team. Besides providing extensive data verification routines, the program calculates total time and mass point leakage rates and the 95 percent Upper Confidence Level for these leakage rate calculations.

Methodology and calculations in the program drive from American National Standards ANSI N45.4-1972, American National Standard ANSI/ANS 56.8-1987, and Topical Report BN-TOP-1, Revision 1. Containment air mass is determined from mass weighted sensor readings as described in EPRI Report NP-2726, November 1982.

A given instrument may be deleted from the calculations ifa sensor malfunctions. The deletion of a given instrument is performed on all samples in the data base. Volume fractions for the remaining instruments of that type are then recalculated based upon the placement and the amount of containment volume sensed'by these instruments.

,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 is recorded on magnetic media to prevent loss during the testing. All data is stored on the computer system in use, with retrieval capability to any desired database throughout the testing.

Two computer systems are utilized, one for data acquisition and one for data analysis.'ne computer can serve for both data acquisition and data analysis in the case of equipment malfunction.

Data rejection based upon the Chauvenet criterion may be utilized in the analysis, if required.

Ancillary portions of the computer program assist the user in determination of temperature tabilization, determining the ILRT termination criteria, performing ISG calculations, performing in-situ instrument loop performance calculations and determination of acceptable superimposed CLRT leakage verifications.

Temperature, pressure, and humidity data transmit from the ILRT instrumentation system to the computer via an RS-232 link at 20 minute intervals. Figure 5 depicts the connection between the ILRT instrumentation system and the computer analysis system.

E. Descri tion of the Testin S uence The ILRT instrumentation system checks found RTD-33 recording eratically. RTD-33 was declared inoperable prior to pressurization and deleted from the ILRT. The volume fractions for the remaining RTD channels was recalculated following the deletion of RTD-33. All other ILRT instrumentation was declared operable with performance within manufacturer's tolerances.

ressure sensor No. 2 was selected to be the primary pressure instrument, as it had exhibited better repeatability and stability during the in-situ testing.

Two penetrations were required to be in service during the ILRT and were not lined up to simulate accident conditions, P-52D gLRT Pressure Sensing Line) and P-52E gLRT Controlled Bleedoff Line). These two ILRT penetrations are used to conduct the test and cannot be positioned in the post-accident lineup. 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 (refer to Appendix A).

Preparations to pressurize the containment for the conduct of the ILRT included internal and external inspections of the containment structure; installation and checkout of the ILRT instrumentation; Types "B" and "C" local leakage rate tests; alignment of valves and breakers for test conditions; and the installation and checkout of the. temporary pressurization facilities.

These preparations were completed on May 19, 1993.

ressurization of the containment structure started at 0320 hours0.0037 days <br />0.0889 hours <br />5.291005e-4 weeks <br />1.2176e-4 months <br /> on May 19, 1993, at an average ressurization rate of 4.5 psi/hr. Appendix B.1 presents a figure entitled "ILRT Testing Sequence" that depicts the sequence of testing.

During the initial stages of pressurization, fan cooler units 1B and 1D were in service and utilized to provide a better mixing of pressurization air with the initial containment atmosphere.

Fan cooler 1D was removed from service at 0420 hours0.00486 days <br />0.117 hours <br />6.944444e-4 weeks <br />1.5981e-4 months <br /> and 1B was removed at 0430 hours0.00498 days <br />0.119 hours <br />7.109788e-4 weeks <br />1.63615e-4 months <br /> after both reached 155 amps for operation.

Pressurization was secured at 12:39 hours on May 19, 1993, at a final pressure of 56.56 psia (41.86 psig). This pressure is 2 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 for the temperature stabilization phase was begun at 12:42 hours n May 19, 1993. Plots of containment air mass versus time demonstrated that leakage might exist above the "as found" ILRT acceptance criteria at a 95% upper confidence level. At 14:30 hours, the leakage survey teams found that the containment emergency sump suction isolation valves MV-07-2A and 2B were leaking air into the safety injection system. As these valves are not containment leakage paths in accordance with the FSAR and technical specifications, a decision was made to manually tighten these valves with no penalty to the "as-found" ILRT values. These valves were manually tightened shortly after 14:45 hours on May 19, 1993, and the stabilization phase was extended to monitor whether this correction was acceptable. The containment stabilization was met at 16:42 hours on May 19, 1993, after four hours of data acquisition to assure stabilization. Stabilization was extended and with air mass, temperature, and pressure demonstrating smooth and expected behavior, all stabilization criteria contained in Topical Report BN-TOP-1 were declared met.

Integrated leakage rate measurements were initiated at 18:25 hours on May 19, 1993. At 20:10 hours, the control room reported a pressurizer low level indication. Charging was initiated at 20:30 hours and completed at 21:10 hours, increasing the pressurizer level 20%, or 44 gallons

er minute for 48 minutes (2112 gallons or volume of 282.3 ft'). The decrease in pressurizer vel was caused by an approximate 1.87 gpm reactor coolant leak in the shutdown cooling system outside of containment. This leak could not be isolated without altering the ILRT valve lineup. This net loss of RCS inventory was equivalent to a .004 %/day containment leak. The decision was made to complete the ILRT with this RCS leak present. Conducting the ILRT with this RCS leak gives an overly conservative representation of containment leakage.

It was determined that the change of 282.3 ft in volume provided by charging the pressurizer would adversely affect leakage observations made thus far during the test. The addition of 2112 gallons provided a decrease in containment volume and was observed by the ILRT instrumentation as a leak into containment. Thus the 48 minutes of "in leakage" analyzed with the predictable trends observed from 18:25 to 21:10 on May 19, 1993 provided overall leakage rates which might be suspect to CLRT acceptability.

The determination was to restart the test following the charging of the pressurizer to obtain test ata which would provide a predictable trend and provide for a more solid assurance of CLRT confirmation.

The ILRT was restarted at 21:05 hours on May 19, 1993 and after eight hours of ILRT data accumulation, all Topical Report BN-TOP-1 acceptance criteria for the ILRT were met with stable and predictable trends. The ILRT was officially terminated at 05:05 hours on May 20, 1993.

At 05:05 hours, a super-imposed flow equivalent to .293 %/day was initiated using the rotameter. This flow was maintained during the required BN-TOP-1 controlled leakage rate test (CLRT) stabilization period of approximately one hour.

At 06:05 hours, on May 20, 1993, the leakage rate measurements for the CLRT were initiated.

Stable and acceptable leakage rate measurements were observed for four hours. At 10:05 hours, all Topical Report BN-TOP-1 criteria were met for the CLRT verification test, and the test was eclared acceptable.

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epressurization of the containment structure was initiated at 10:07 hours on May 20, 1993, at rate of 6 psi/hr. At .5 psig, a containment entry was made to conduct the post-ILRT containment inspection. The only damage observed included several broken light bulbs which were left lying at the at the polar crane elevation.

The ILRT test sequence was officially terminated at 18:00 hours on May 20, 1993, with less than .4 of a psig in the containment.

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III. ANALYSIS AND INTERPRETATION A. In trumentation S stem Performance Only the RTD-33 temperature detector, which was deleted prior to the pressurization of the containment, failed to perform properly. All of the remaining temperature detectors performed as expected with no anomalous behavior detected by the Ebasco ILRT computer program error checking routines. This computer program also determines the in-situ temperature loop repeatability which consists of process measurement variations as well as sensor noise. The average in-situ loop repeatability for the 39 operating temperature sensors was

.013'F, with the worst sensor exhibiting an in-situ loop repeatability of .041'F. This performance compares well with the vendor-claimed temperature sensor loop repeatability, excluding process variations, of 0.02'F as given in Section II.B.1.

Ten relative humidity sensors were installed in the containment for the ILRT. The ten operating

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hannels for humidity operated as expected with no anomalous behavior detected by the ILRT

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computer program error checking routines. The average in-situ loop repeatability for the relative

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humidity sensors was .100 percent RH, with the worse sensor exhibiting an in-situ loop repeatability of .229 percent RH. This performance is better than the vendor claimed humidity sensor loop repeatability, excluding process variations, of 0.25 percent RH as given in Section II.B.2.

Two pressure sensors were installed for the ILRT, with one utilized for testing and one considered as a spare. Prior to containment pressurization, computer 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 0.0010 psi. This performance compares well with the vendor-claimed pressure sensor loop repeatability, excluding process variations, of 0.0015 psi as given in Section II.B.3.

The variable area rotameter performed as expected with no evidence of unstable readings, float ticking, or moisture in the float tube.

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In summary, all of the ILRT test documentation performed in an adequate manner to allow etermination of containment leakage rates to the sensitivity required.

B. Tem rature Stabilizati n Pha e Prior to pressurization of the containment, the atmosphere was very stable with an average temperature of 85.53'F and a maximum spread of temperature from the highest reading sensor to lowest reading sensor of 2.4'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 100.72'F with a maximum spread of temperature from the highest reading sensor to lowest reading sensor of 26.46'F.

The results of the temperature stabilization phase are presented in Appendix B.2. The acceptance criteria given in Topical Report BN-TOP-1, Revision 1, are described in Note 2 in that appendix. The data presented shows that a smooth and predictable temperature stabilization

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ccurred. ~ At the end of stabilization, the average temperature was 92.6TF with a maximum spread of temperature from the highest reading sensor to the lowest reading sensor of 11.2'F.

This demonstrates that the heat sinks of concrete and steel in the containment were quickly returning the containment atmosphere to a stable condition.

C. Leaka e Surve Phase As the containment began to stabilize, a preliminary review of leakage rate demonstrated excessive leakage values. Leakage survey teams reported that a leak on both containment emergency sump suction lines had been found by venting air from the outboard side of isolation valves MV-07-2A and 2B. Observations by the leakage survey team allowed for the possibility that these two emergency sump suction isolation valves were not fully closed.

These two isolation valves are not considered as potential leakage barriers in the Final Safety Analysis Report (PSAR) Sections 6.2.4.2 and 6.2.4.4, as they will be water covered in a Loss f Coolant Accident and open during the recirculation phase of the transient. Any water leakage 13

through these valves in the closed position will be returned to the containment by the Safety jection System pumps. No potential containment leakage or off-site dose is credible due to seat leakage of these valves in the closed position.

These two isolation valves were then manually closed with subsequent containment leakage rates reduced.

No other appreciable leakage was noted by the survey teams and the ILRT phase was initiated.

D. Inte rated Leaka e Rate Phase Leakage measurements were started after stabilization and resolution of pressurizer level changes at 21:05 hours on May 19, 1993. As previously mentioned in Section II Part E, the charging of the pressurizer was observed as "in leakage" during the test and, when coupled with the predictable leakage data, warranted restart of the ILRT test sequence, The level change decrease) over the period of the test, however, was not viewed as a problem. The slow and gradual decrease in pressurizer level would be observed as a leak by the ILRT instrumentation (because a decrease in level means a proportionate increase in containment volume). Therefore, the leakage rate observed would be conservative in that it was accounting additionally for pressurizer level decrease. It would be expected that this predictable trend would be confirmed with the CLRT but may be low within the CLRT acceptability range.

Stable leakage rates were measured by both the total time method and mass point method. The total time BN-TOP-1 results for eight hours of leakage measurements are presented in Appendix B.3. A summary of the measured leakage by both methods after eight hours is:

BN-TOP-1 ANSI 56.8 Total Time ~Mass Pain Simple Leakage Rate 0.116 %/day 0.116 %/day Fitted Leakage Rate 0.154 %/day 0.123 %/day Upper Confidence Level 0.293 %/day 0.133 %/day 14

The higher upper confidence level of the BN-TOP-1 measurements

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is due to the nature of rforming regression analysis on simple leakage rates instead of regression analysis on masses and the more conservative statistics utilized by BN-TOP-1.

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The measured leakage rates and upper confidence levels for both calculated methods were slowly decreasing with time.

As all acceptance criteria for a Reduced Duration BN-TOP-1 ILRT were met at eight hours as presented in Appendix B.2, the ILRT was declared 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. As a result of the Type "B" and "C" local leakage rate testing and repairs performed during the refueling outage, additions to the "as-found" Type "A" ILRT results were necessary to NRC Information Notice 85-71. These additions were for the reduction in minimum pathway leakage due to repairs. These leakage reductions have been corrected for uncertainties prior to being added to the measured ILRT values (refer to Appendix A).

Verification ontrolled Leaka e Rate Phase to the acceptance of the ILRT results, a superimposed leakage equivalent to 0.293

'ubsequent 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-1.

Leakage measurements were initiated to verify the results 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-1. As presented in Appendix B.4, the leakage measurements met the acceptance criteria for the verification phase. Leakage results for both the total time and mass point method are:

BN-TOP-1 ANSI 56.8 Total Time Mass Point Simple Leakage Rate 0.353 %/day 0.353 %/day Fitted Leakage Rate 0.328 %/day 0.348 %/day

The acceptance criteria for this test is leakage between .322 and .572 percent per day. Results ere expected to be low within this range due to pressurizer level change and the conservatism of the measured leak as previously discussed in Section IIIPart D. The results of the CLRT are acceptable.

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szcnox cv RTD LOCATION/VOLUME ST. LUCIE UNIT NO. 1 FLORIDA POWER 8c LIGHT COMPANY 3 RTD'S AT EL 194'OLUME 242,055 CU FT RTD 38-40 9 RTD'S AT ELEVATION 171'OLUME 453,235 CU FT RTD 29-37 10 RTD'S AT ELEVATION 130'OLUME 669,627 CU FT RTD 9-18 10 RTD'S AT ELEVATION 84'OLUME 600,926 CU FT RTD 19-28 8 RTD'S AT ELEVATION 40'OLUME 534,157 CU FT RTD 1-8 FIGURE 1 EBASCO PLANT OPERATIONS &, BEITERMENT

RHD LOCATION/VOLUME ST. LUCIE UNIT NO. 1 FLORIDA POWER 8c LIGHT COMPANY 3 RHD'S AT ELEVATION 171'OLUME 1,049,347 CU FT RHD 8-10 4 RHD'S AT ELEVATION 84'OLUME 900,640 CU FT RHD 4-7 3 RHD'S AT ELEVATION 40'OLUME 550,013 CU FT RHD 1-3 FIGURE 2 EBASCO PLANT OPERATIONS Ec BETTERMENT

X~'LOW D RAM ILRT PRESSURE SENSING 4 CONT LED LEAKAGEINSTRUMENTS INSIDE CONTAINiVfHNT AINMHN'I'I OIJISIDE COYf 3/8" 'fUBING 1Q" TUBING (TYP.)

P DIGITAL 52H PRESSURE GAUGE TO ATMOS-DIGITAL VARIABLEAREA LLRTEST PRESSURE ROTAMHTHR GAUGE 1" PIPE 1Q" DRAIN & TEST Fl P

52D LLR TEST SEISMIC CLASS 1 ~ V2" DRAIN & TEST FIGURE 3

FLOW IAGRAM ILRT PRESSURIZING & DEPRESSURIZING SYSTEM TO AIMOSPIIRRE TO i&ITM. 1 ILRT PRNRIRA'IION t9 I SEISMIC CLASS I FLANCR (fYPJ Pl I

BLLiD DRIP REMOVE FOT FOR ILRT S" BYPASS LVVIDR 3(i" LLTR DRAIN I DRAIN OVIDOORS AVXIIIARY BLDO OVISIDR LNSIDR IllROTILE COÃIAlhMLVf COVfAINMRNT VALVE WAIXROVf WAIXRL I DIESEL DRIVEN LKNKIRIAL OIL FREE ADI COMPRRSSORS

<ILIMCFM TOTAL)

WATER 0Vf WAIXRLI FIGURE 4

FLOW D AGRAM ILRT DATA COLLECTION, STORAGE R ANALYSIS DIGITAL PRESSURE GAUGE 40 FLUKE RTD DATA LOGGER 10 2 RHD HUMETER O

0 DATA COLLECTION DATAANALYSIS COMPUTER COMPUTER EBASCO SO&"I'WARE EBASCO SOFTWARE PRINTER DIS KEPI'E (TYPICAL)

O O 0 (TYPICAL) 0 EBASCO PLANT Ol'ERATIONS 8c BETTERMENT FIGURE 5

1 szerroi v wrrmnrczs

APPENDXX A TABULATIONOP "AS-POUND" AND "AS-LEFT" ILRT RESULTS

APPENDIX A TABULATIONOF "AS-POUND" AND "AS-LEFT" ILRT RESULTS Correction of ILRT Results for "As-Found" Case In accordance with NRC ISAAC Information Notice 85-71, the following additions are required to the ILRT results due to repairs and/or adjustments made due to local leakage rate testing during the 1993 refueling outage. 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.

Minimum Pathway ILRT

, ~Penetrati n Leaka e Difference gnncertaint . ~orrection P-11 Containment Purge Exhaust 42,000 sccm 1,900 sccm '3,900 sccm P-52A Sample to Rad Monitor 830 sccm 11'.5 sccm 841.5 sccm P-52B Sample to Rad Monitor 870 sccm 11.5 sccm 881.5 sccm P-52C Rad Monitor Return 30 sccm 1.6 sccm 31.6 sccm P-54 ILRT Press. Station 300 sccm 98.1 sccm 398.1 sccm P-68 Cont. Vacuum Relief 1100 sccm 98.1 sccm 1198.1 sccm

The total local minimum pathway leakage plus uncertainty must be added for the penetrations hich are in use during the ILRT and whose containment isolation valves are not tested:

Total Minimum ILRT Penetration Correction P-52D ILRT Test 575 sccm 11.5 sccm 586.5 sccm P-52E ILRT Test 15 sccm 1.6 sccm 16.6 sccm The total ILRT "as-found" correction can be found adding the above ILRT corrections (NOTE:

A conservative simplification was made by not performing a root-mean-square summation of the local uncertainties).

Correction of ILRT results for "as-found" case 47250. 8 sccm or

.026 %/day Measured ILRT leakage at a 95% UCL .293 %/day Reported "as-found" ILRT results .319 %/day Acceptance criteria (75% La) .375 %/day Correction of ILRT Results for "As-Left" Case The only correction for the "as-left" ILRT case involves the penetrations which were in use during the test, P-52D and P-52E. From the above section, the ILRT "as-left" correction can be determined:

Correction of ILRT results for "as-left" case 603.1 sccm or 3.3x10'/day Measured ILRT leakage at a 95% UCL .293 %/day Reported "as-left" ILRT results .293 %/day Acceptance criteria (75% La) .375 %/day A-2

APPENDIX B ILRT COMPVTER-GENERATED REPORT

ILRT TEST SEQUENCE 1993 ST. LUCIE UNIT 1 PERIODIC TEST Sequence Started 03:19, 5/19/93 Sequence Ended 19:10, 5/20/93 EBASCO SERVICES INC.

Plant Operations A Betterment Dept.

ILRT TEST SERVICES APPENDIX B.1

ILRT TESTING SEQUENCE 1998 St. Lucie Unit P1 ILRT Pressure In Pslg D

A - Pressurization

--- B - Stabilization 30 C - ILRT D - CLRT E - Depressurization 20 10 0

0 5 10 $5 20 25 30 Time ln Hours EBASCO Rant Operdfae 4 Betterment

l 11 i.

i r

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I

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W i I I

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TEMPERATURE STABILIZATIONMODE 1993 ST. LUCIE UNIT 1 PERIODIC TEST Sequence Started 12:42, 5/19/93 Sequence Ended 18:22, 5/19/93 EBASCO SERVICES INC.

Plant Operations A Betterment Dept.

P ILRT TEST SERVICES APPENDIX B.2

PSL1 Spring 93 ILRT Program Rev 9 0 STABILIZATION PERIOD STARTED AT 12:42 TEMPERATURE STABILIZATION ON 5/19/93 SAMPLE TIME AVE TEMP DELTA T/HR DELTA T/HR DELTA T/HR NUMBER HOURS DEG F LAST 2 HRS LAST 1 HR CHANGE

0. 00 100.627 0.000 0.000 0.000 0.33 98.417 0.000 0.000 0.000 0.67 97.252 0.000 0.000 0.000 1.00 96.514 0.000 -4.113 0.000 1.33 95.976 0.000 -2.441 0.000 1.67 95.525 0.000 1 ~ 727 0.000 2.33 94.820 -1.798 -1.156 0.642 2.67 94.518 -1.367 -1.007 0.360 3.00 94.256 -1.129 -0.887 0.242 3.33 94.004 -0.986 -0.816 0.170 3.67 93.776 -0.875 -0.742 0.133 12 4.00 93.564 -0.789 -0.692 0.097 4.33 93.363 -0.729 -0. 642 0.087

4. 67 93.172 -0.673 -0.604 0.069 15 5.00 93.001 -0.628 -0.564 0.064 16 5.33 92.824 -0.590 -0.538 0.052 5.67 92.666 -0.555 -0.506 0.049

N OTES

) THE 1 HOUR AND 2 HOUR DELTA TEMPERATURE VALUES ARE NOT VALID UNTIL 1 HOUR AND 2 HOURS~ RESPECTIVELY'AVE PASSED IN THE TEST

2) THE STABILIZATION CRITERIA IS MET WHEN:

-THE HOURLY AVERAGE DELTA T FOR THE PRECEDING HOUR DIFFERS FROM THE HOURLY AVERAGE DELTA T FOR THE PRECEDING 2 HOURS BY LESS THAN 0.5 DEGREES F. OR

-THE HOURLY AVERAGE DELTA T FOR THE PRECEEDING 2 HOURS IS LESS THAN 1.0 DEGREES F.

-THE STABILIZATION PERIOD IS A MINIMUM OF 4 HOURS

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

TEMPERATURE STABIILIIZA7IIGM 1993 St. Lucia Unit P1 ILRT Ternpmdure fn Degrees F 102 94 92 0 0.5 1 1.5 2 2.6 3 3.5 4 4.6 6 6.5 6 Time tn Hours

ILRT TEST MODE 1993 ST. LUCIE UNIT 1 PERIODIC TEST Sequence Started 21:05, 5/19/93 Sequence Ended 05:05, 5/20/93 EBASCO SERVICES INC.

Plant Operations 8c Betterment Dept.

ILRT TEST SERVICES APPENDIX B.3

4 I PSL1 Spring 93 ILRT Program Rev 9 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 21:05 HOURS ON 5/19/93 TEST CONDUCTED FOR 8.00 HOURS FREESPACE VOLUME OF CONTAINMENT IS 2500000 CU FT CONTAINMENT WAS PRESSURIZED TO 55.57 PSIA FITTED TOTAL TIME ILRT LEAKAGE RATE Lam 0.154 /DAY UPPER LIMIT OF 954 CONFIDENCE LEVEL UCL 0.293 /DAY CONTAINMENT DESIGN LEAKAGE RATE La 0.500 ~o

/ DAY ILRT ACCEPTANCE CRITERIA 7 5~o La 0.375 /DAY

BN-TOP'EDUCED DURATION ILRT TERMINATION CRITERIA E TREND OF THE TOTAL TIME CALCULATED LEAKAGE RATE SHALL NDICATE THAT THE MAGNITUDE OF THE LEAKAGE RATE IS TENDING TO STABILIZE AT A VALUE LESS THAN OR EQUAL TO 75% OF La.

La = 0.500  % /DAY 75% La = 0.375  % /DAY Lam = 0.154  : /DAY with a Negative Skew AT THE END OF THE ILRT THE UPPER LIMIT OF THE 95~o CONFIDENCE LEVEL SHALL BE LESS THAN OR EQUAL TO 75% OF La.

UCL = 0 293 ~o /DAY

-THE MEAN OF THE MEASURED LEAKAGE RATES OVER THE LAST 5 HOURS OR 20 DATA SETS'HICHEVER PROVIDES THE MOST POINTS~ SHALL BE LESS THAN OR EQUAL TO 75% OF La.

MEAN OF SIMPLE LEAKAGE FOR SAMPLES = 0 126 ~o /DAY

ILRT VARIABLE TABLE

SUMMARY

S TIME AVE TEMP PRESSURE VAP PRES LEAK SIM LEAK FIT UCL AIR MASS HOURS DEG F PSIA PSIA 4/DAY ~o/DAY ~o

/ DAY LBS 1 0. 00 91. 618 55.573 0.3728 0.000 0. 000 0.000 675621 2 0.33 91.515 55.563 0.3716 -0.193 0. 000 0.000 675639 3 0.67 91.410 55.551 0.3723 0.039 0.000 0.000 675614 4 1.00 91.310 55.540 0.3732 0.108 0.135 0.781 675591 5 1.33 91.212 55.529 0.3738 0. 142 0.185 0.551 675568 6 1.67 91.119 55.519 0.3743 0. 144 0.203 0.515 675554.

7 2.00 91.018 55.509 0.3741 0. 114 0.193 0.498 675557 8 2.33 90.934 55.499 0.3740 0. 125 0.190 0.469 675539 9 2.67 90.850 55.490 0.3739 0. 117 0.183 0.443 675533 10 3.00 90.773 55.481 0.3743 0. 129 0.182 0.423 675512 11 3.33 90.700 55.473 0.3744 0. 125 0.179 0.405 675503 12 3.67 90.630 55.465 0.3742 0. 125 0. 176 0.390 675492 13 4.00 90.560 55.457 0.3740 0. 123 0. 173 0.377 675482 14 4.33 90.498 55.449 0.3739 0. 130 0.172 0.366 675463 15 4.67 90.434 55.442 0.3739 0. 126 0. 170 0.356 675456 16 5.00 90.379 55.435 0.3738 0. 131 0. 169 0.347 675437 17 5.33 90.321 55.428 0.3737 0. 131 0. 168 0.340 67542.5 18 5.67 90.265 55.422 0.3736 0. 126 0.166 0.332 675421 19 6.00 90.212 55.415 0.3734 0. 130 0.165 0.326 675402 20 6.33 90.163 55.409 0.3732 0. 129 0.163 0.320 675391 21 6.67 90.107 55.403 0.3732 0. 125 0.161 0.314 675387 22 7.00 90.057 55.397 0.3728 0. 122 0.159 0.308 675381 23 7.33 90.014 55.391 0.3726 0.126 0.158 0.303 675360 2 7.67 89.971 55.386 0.3724 0.124 0.156 0.298 "675355 8.00 '9.919 55.381 0.3722 0.116 0.154 0.293 675360

lllLRT AlllR MASS 1993 St. Lucie Unit P1 ILRT 678,000 Air Mass Fitted M 875,800 675,800 675,400 675,200 675,000 0 'j 2 3 4 5 6 7 8 Thne ln Houm

1993 St. Lucie Unit 41 ILRT 0.2 0.$

%.2 Simple Leakage Rate

+ ed e Rata 0 1 2 3 4 5 6 7 8 HRSCO Rant Operithmi 4 Bethrrnont

IILRY LEAKAGE RAYES REILAYIIVEYG LIIMIIYS 1993 St. Lucis Unit P1 ILRT Rtted Leakage Rate

+UCL 0.

Deign Leakage (La)

"-Allovrable Leakage 0.6 0.4 0.2 2 3 4 5 6  ? 8 EBA8CO Rant Opera5one 4 Betterment

ILRT WEIGHTED AVERAGE TEMPERATURE 1993 St. Lucie Unit P1 ILRT empsrature ln Degrees F 92 9'1.8 91.6 9'l.4 9'1.2 91 90.8 90.6 90.4 90.2 90 89.8 0 2 3 4 5 6 7 8 Time fn Hours

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ILRT CONTAINMENTABSOLUTE PRESSURE 1993 St. Lucis Unit P1 ILRT Pressure tn Psfa 55.8 55.35 0 2 3 4 5 8 7 8 Toms In Hours EBASCO Rant Operdhee 5 Betterment

f

~ .

'E 0 I

ILRT WEIGHTED AVERAGE VAPOR PRESSURE 1993 St. Lucie Unit 41 ILRT Press ure In Psfa 0.4 0.395 0.39 0.385 0.38 0.375 0.37 0.365 0.36 0.355 0.35 0 1 2 3 4 5 6 7 8 Time ln Hours

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SENSOR VOLUME FRACTIONS TEMPERATURE SENSORS 0.026708 ,0. 026708 0.026708 0. 026708 0.026708 6 to 10 0.026708 0.026708 0.026708 0.026785 0.026785 11 to 15 0.026785 0.026785 0.026785 0.026785 0.026785 16 to 20 0.026785 0.026785 0.026785 0.024037 0.024037 21 to 25 0.024037 0.024037 0.024037 0.024037 0.024037 26 to 30 0.024037 0.024037 0.024037 0.022662 0.022662 31 to 35 0.022662 0.022662 0.000000 0.022662 0.022662 36 to 40 0.022662 0.022662 0.032274 0.032274 0.032274 HUMIDITY/DP SENSORS 1 to 5 0.073335 0.073335 0.073335 0.090064 0.090064 6 to 10 0.090064 0.090064 0.139913 0.139913 0.139913 NOTE: VALUE OF ZERO INDICATES A DELETED SENSOR.

ILRT VARIABLE

SUMMARY

SAM LE DELTA TEMP 1 TEMP 2 TEMP 3 TEMP 4 TEMP 5 TEMP 6 N HOURS DEG F DEG F DEG F DEG F DEG F DEG F

0. 00 86. 602 87.246 86.925 86. 177 85.550 85.705 2 0.33 86.591 87.246 86.925 86. 200 85.561 85.739 3 0.67 86.602 87.235 86.894 86. 177 85.550 85.728 4 1.00 86.580 87.235 86.925 86. 177 85.538 85.748 5 1.33 86.586 87.219 86.932 86.184 85.545 85.755 6 1.67 86.577 87.219 86.901 86.173 85.556 85.743 7 2.00 86.580 87.203 86.905 86.188 85.550 85.739 8 2.33 86.559 87.192 86.905 86.188 85.561 85.728 9 2.67 86.571 87.181 86.894 86.188 85.550 85.728 10 3.00 86.571 87.192 86.883 86.177 85.527 85.717 11 3.33 86.571 87.161 86.894 86.166 85.550 85.705 12 3.67 86.577 87.156 86.921 86.173 85.568 85.723 13 4.00 86.559 87.150 86.905 86.177 85.550 85.717 14 4.33 86.535 87.145 86.910 86.215 85.556 85.712 15 4.67 86.548 87.138 86.914 86.166 85.538 85.705 16 5.00 86.559 87.107 86.894 86.188 85.561 85.705 17 5.33 86.559 87.138 86.914 86.177 85.561 85.705 18 5.67 86.591 87.084 86.937 86.200 85.570 85.694 19 6.00 86.580 87.107 86.905 86.200 85.561 85.685 20 6.33 86.566 87.091 86.910 86.162 85.577 85.681 21 6.67 86.580 87.064 86. 914 86.177 85.581 85.663 22 7.00 86.580 87.084 86.905 86.200 85.581 85.651 23 7.33 86.597 87.069 86.910 86.184 85.577 85.647 24 7.67 86.580 87.042 86.914 86.209 85.592 85.643 5 8.00 86.591 87.031 86.914 86.200 85.570 85.643

ILRT VARIABLE

SUMMARY

SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 TEMP 12 N HOURS DEG F DEG F DEG F DEG F DEG F DEG F 0.00 87. 264 85.470 93.955 92.978 93.644 93.241 2 0.33 87. 264 85.470 93.796 92.861 93.494 93.176 3 0.67 87.252 85.461 93.635 92.722 93.344 93.111 4 1.00 87.252 85.450 93.527 92.581 93.205 92.886 5 1.33 87.270 85.457 93.384 92.471 93.082 92.785 6 1. 67 87.259 85.457 93.279 92.342 92.954 92.689 7 2.00 87.264 85.428 93.153 92.228 92.829 92.523 8 2.33 87.252 85. 42,8 93.037 92.098 92.702 92.435 9 2.67 87.252 85.417 92.907 92.001 92.585 92.307 10 3.00 87.241 85.408 92.811 91.896 92.489 92.253 11 3.33 87.241 85.417 92.705 91.777 92.393 92.092 12 3.67 87.248 85.403 92.604 91.698 92.281 92.025 13 4.00 87.252 85.408 92.501 91.595 92.178 91.856 14 4.33 87.248 85.414 92.412 91.505 92.089 91.820 15 4.67 87.241 85.396 92.340 91.424 91.997 91. 717 16 5.00 87.241 85.374 92.266 91.337 91.912 91. 632 17 5.33 87.230 85.385 92.179 91.251 91.836 91. 515 18 5.67 87.241 85.385 92.094 91.186 91.751 91.450 19 6.00 87.241 85.374 92.020 91.101 91.698 91.461 20 6.33 87.248 85.392 91.962 91.034 91.619 91. 403 21 6. 67 87.241 85.374 91.870 90.942 91.'537 91.322 22 7. 00 87.241 85.374 91.794 90.897 91. 463 91. 181 23 7.33 87.248 85.372 91.726 90.829 91.396 91. 179 24 7.67 87.241 85.385 91.666 90.769 91. 367 91. 096

'25 8.00 87.230 85.374 91.601 90.715 91.282 90.999

ILRT VARIABLE

SUMMARY

S DELTA TEMP 13 TEMP 14 TEMP 15 TEMP 16 TEMP 17 TEMP 18 N HOURS DEG F DEG F DEG F DEG F DEG F DEG F

0. 00 93.104 93.320 93.338 93.465 93.409 93.318 2 0.33 92.945 93.149 93.199 93.337 93.259 93.168 3 0. 67 92.710 93.064 93.111 93.219 93.111 93.018 4 1.00 92.634 92.913 93.015 93.068 92.969 92.890 5 1.33 92.394 92.790 92.916 92.936 92.848 9.2. 780 6 1.67 92.374 92.662 92.766 92.786 92.708 92.661 7 2.00 92.152 92.536 92.683 92.663 92.582 92.527 8 2.33 92.013 92.419 92.567 92.535 92.466 92.408 9 2.67 91.895 92.311 92.502 92.439 92.358 92.312 10 3.00 91.798 92.183 92.394 92.343 92.250 92.204 11 3.33 91.747 92.087 92.298 92.235 92.153 92.099 12 3.67 91.635 91.997 92.188 92.146 92.063 92.009 13 4.00 91.521 91.882 92.096 92.042 91.971 91.915 14 4.33 .91.431 91.781 91.995 91.964 91.881 91.825 15 4.67 91.393 91.689 91.912 91.861 91.789 91.722 16 5.00 91.285 91.624 91.859 91.785 91.704 91.660 17 5.33 91.274 91.518 91.720 91.711 91.639 91.583 18 5.67 91.158 91.464 91.614 91.626 91.553 91.509 19 6.00 91.093 91.357 91.592 91.561 91.488 91.436 20 6.33 91.046 91.278 91.534 91.491 91.421 91.389 21 6.67 90.985 91.206 91.334 91.422 91.338 91.285 22 7.00 90.900 91. 141 91.272 91.337 91.264 91.220 23 7.33 90.864 91.096 91.267 91.279 91.216 91.185 24 7.67 .90.837 91. 045 91.207 91.229 91.156 91.102 8.00 90.741 90.982 91.090 91.153 91.102 91.050

ILRT VARIABLE

SUMMARY

SAM E. DELTA TEMP 19 TEMP 20 TEMP 21 TEMP 22 TEMP 23 TEMP 24 N HOURS DEG F DEG F DEG F DEG F DEG F DEG F

0. 00 '2:293 92.591 92.545 92.506 92.936 92.649 2 0.33 92.240 92.517 92.494 92.432 92.862 92.562 3 0.67 92.154 92.452 92.417 92.368 92.809 92.499 4 1.00 92.067 92.409 92.375 92.294 92.735 92.423 5 1.33 92.000 92.335 92.298 92.209 92.670 92.349 6 1.67 91.977 92.248 92.224 92.144 92.605 92.284 7 2.00 91.897 92.203 92.177 92.065 92.495 92.217 8 2.33 91.832 92.151 92.150 92.014 92.444 92.145 9 2.67 91.769 92.073 92.103 91.947 92.388 92.078 10 3.00 91.684 92.012 91.989 91.886 92.316 92.027 11 3.33 91.661 91.969 91.955 91.821 92.262 91.953 12 3.67 91.572 91.895 91.881 91.759 92.188 91.888 13 4.00 4.33 91 '11 91.873 91.806 91.839 91.771

'91.716 91.647 92.112 92.067 91.823 91.767 14 91.444 15 4.67 91.426 91.754 91.720 91.597 91.996 91.706 16 5.00 91.372 91.669 91 '57 91.532 91.951 91.641 17 5.33 91. 276 91.637 91.603 91.459 91.877 91.599 18 5.67 91.244 91.584 91 '16 . 91.394 91.803 91.523 19 6.00 91.168 91.518 91.473 91.351 91.759 91.460 20 6.33 91.144 91.494 91.385 91.304 91.703 91.402 21 6.67 91.072 91.487 91.356 91.244 91.662 91.363 22 7.00 91.029 91.433 91.314 91.201 91.600 91.310 23 7.33 90.962 91.377 91.244 91.145 91.541 91.242 24 7.67 90.913 91.402 91.184 91.094 91.492 91.180 8.00 90.922 91.343 91. 128 91.038 91.445 91.124

ILRT VARIABLE

SUMMARY

DELTA TEMP 25 TEMP 26 TEMP 27 TEMP 28 TEMP 29 TEMP 30 HOURS DEG F DEG F DEG F DEG F DEG F DEG F

0. 00 92.412 91. 870 90.623 92.488 93.548 93.387 2 0.33 92.315 91.773 90.547 92.436 93.364 93.205 3 0.67 92.251 91.708 90.462 92.371 93 '71 93.001 4 1.00 92.177 91.623 90.385. 92.264 92.978 92.808 5 1.33 92.089 91.526 90.300 92.210 92.785 92.627 6 1.67 92.038 91.483 90.258 92.125 92.658 92.476

, 7 2.00 91.948 91.427 90.191 92.058 92.472 92.313 8 2.33 91.897 91.364 90.130 92.006 92.357 92.198 9 2.67 91.841 91.288 90.040 91.928 92.225 92.066 10 3.00 91.780 91.259 89.980 91.847 92.111 91.960 11 3.33 91.738 91.171 89.938 91.825 92.014 91.855 12 3.67 91.662 91.129 89.861 91.760 91.918 91.758 13 4.00 91.619 91.086 89.819 91.717 91.810 91.662 14 4.33 91.552 90.996 89.763 91.650 91.732 91.572 15 4.67 91.500 90.936 89.711 91.556 91.660 91.489 16 5.00 91.438 90.915 89.649 91.621 91.575 91.415 17 5.33 91.384 90.862 89.584 91.525 91.490 91.328 18 5.67 91.319 90.774 89.541 91.525 91.413 91.254 19 6.00 91.256 90.731 89.476 91.429 91.351 91.189 20 6.33 91.198 90.653 89.452 91.393 91.261 91.121 21 6.67 91.138 90.615, 89.391 91.290 91.209 91.050 22 7.00 91.084 90.572 89.358 91.267 91.124 90.985 23 7.33 91.037 90.502 89.324 91.211 91.077 90.917 24 7.67 90.965 90.431 89.261 91.160 91.050 90.868 25 8.00 90.932 90.386 89.237 91.115 90.949 90.790

ILRT VARIABLE

SUMMARY

DELTA TEMP 31 TEMP 32 TEMP 33 TEMP 34 TEMP 35 TEMP 36 HOURS DEG F DEG F DEG F DEG F DEG F DEG F 0.00 92.011 93.283 DELETED 93.415 93.474 94.859 2 0.33 91.839 93.133 DELETED "93.244 93.326 94.708 3 0.67 91.647 92.963 DELETED 93.039 93.122 94.494 4 1.00 91.443 92.790 DELETED 92.855 92.949 94.310 5 1.33 91.262 92.608 DELETED 92.673 92.745 94.128 6 1.67 91.090 92.438 DELETED 92.491 92.586 93.977 7 2.00 90.916 92.283 DELETED 92.336 92.431 93.824 8 2.33 90.802 92.137 DELETED 92.213 92.294 93.687 9 2.67 90.692 92.025 DELETED 92.091 92. 173 93.554 10 3.00 90.589 91.922 DELETED 91.986 92.059 93.462 11 3.33 90.471 91.803 DELETED 91.869 91.951 93.365 12 3.67 90.352 91.718 DELETED 91.781 91.855 93.277 13 4.00 90.267 91.610 DELETED 91.685 91.780 93.181 14 4.33 90.178 91.523 DELETED 91.586 91.702 93.091 15 4.67 90.086 91.429 DELETED 91.503 91.608 93.010 16 5.00 90.021 91.343 DELETED 91.428 91.523 92.944 17 5.33 89.925 91.258 DELETED 91.341 91.437 92.848 18 5.67 89.860 91.193 DELETED 91.278 91.372- 92.762 19 ,6. 00 89.798 91.128 DELETED 91.181 91.276 92.708 20 6.33 89.720 91.050 DELETED 91.112 91.220 92.641 21 6.67 89.648 90.989 DELETED 91.074 91.159 92.578 22 7.00 89.595 90.915 DELETED 90.977 91.072 92.515 23 7.33 89.536 90.846 DELETED 90.930 91.038 92.447 24 7.67 89.456 90.785 DELETED 90.880 90.966 92.375 25 8.00 89.409 90.718 DELETED 90.791 90.908 92.317

ILRT VARIABLE

SUMMARY

SAM LE DELTA TEMP 37 TEMP 38 TEMP 39 TEMP 40 N HOURS DEG F DEG F DEG F DEG F

0. 00 93.508 93.441 93.479 93.323 2 0.33 93.327 93.226 93.275 93.130 3 0.67 93.123 93.076 93.127 92.969 4 1.00 92.930 92.937 92.997 92.841 5 1.33 92.780 92.809 92.847 92.720 6 1.67 92.609 92.626 92.677 92.527 7 2.00 92.434 92.442 92.502 92.336 8 2.33 92.309 92.294 92.343 92.177 9 2.67 92.197 92.131 92.168 92.005 10 3.00 92.071 91.994 92..033 91.877 11 3.33 91.975 91.835 91.883 91.727 12 3.67 91.870 91.716 91.765 91.594 13 4.00 91.782 91.589 91.657 91.480 "14 4.33 91.695 91.488 91.558 91.402 15 4.67 91.612 91.385 91.475 91.287 16 5.00 91.527 91.297 91.390 91.202 17 5.33 91.462 91.246 91.314 91.128 18 5.67 91.377 91.159 91.229 91. 063 19 6.00 91.312 91.062 91.155 90. 967 20 6.33 91.233 91.006 91.077 90.909 21 6.67 91.139 90.935 91.016 90.839 22 7.00 91.088 90.870 90.940 90.763 23 7.33 91.030 90.802 90.873 90.707 24 7.67 90.992 90.742 90.812 90.635 5 8.00 90.891 90.664 90.745 90.570

ILRT VARIABLE

SUMMARY

SAMP E DELTA PRES 1 PRES 2 HUM 1 'UM 2 HUM 3 HUM 4 N HOURS PSIA PSIA ~o RH >o RH  % RH. 4 RH

0. 00 55.573 55.579 44.290 49.710 52.350 46.180 2 0.33 55.563 55.568 44.630 50.090 52.730 46.670 3 0.67 55.551 55.557 45.110 50.450 53.100 47.220 4 1.00 55.540 55.545 45.590 50.870 53.550 47.670 5 1.33 55.529 55.535 45.960 51.210 53.880 48.130 6 1.67 55.519 55.524 46.420 51.580 54.360 48.380 7 2.00 55.509 55.514 46.850 51.970 54.740 48.680 8 2.33 55.499 55.505 47.330 52.350 55.100 48.690 9 2.67 55.490 55.495 47.700 52.740 55.630 48.890 3.00 55.481 55.486 48.120 53.100 55.950 49.080 ll 10 12 3.33 3.67 55.473 55.465 55.478 55.470 48.660 49.080 53.420 53.770 56.220 56.630 49.210 49.230 13 4.00 55.457 55.462 49.350 54.080 56.910 49.310 14 4.33 55.449 55.454 49.860 54.350 57.240 49.310 15 4.67 55.442 55.447 50. 130 54.660 57.550 49.370 16 5.00 55.435 55.440 50.490 54.940 57.950 49.420 17 5.33 55.428 55.433 50.790 55.200 58.290 49.450 18 5.67 55.422 55.427 51.190 55.430 58.580 49.460 19 6.00 55.415 55.420 51.470 55.640 58.880 49.460 20 6.33. 55.409 55.414 51.750 55.850 58.980 49.470 21 6. 67 55.403 55.408 52.060 56.060 59.360 49.580 22 7.00 55.397 55.402 52.210 56.250 59.510 49.380 23 7.33 55.391 55.397 52.510 56.440 59.640 49.480 24 7.67 55.386 55.391 52.800 56.550 59.880 49.330 25 8.00 55.381 55.386 52.970 56.740 60.090 49.250

XLRT VARIABLE

SUMMARY

SAM E' DELTA HUM 5 HUM 6 HUM 7 HUM 8 HUM 9 HUM 10 HOURS ~o RH ~o RH ~o RH ~o RH ~o RH >o RH 0.00 48.910 46.890 47.360 53.970 54.290 55.720 2 0.33 49.420 47.320 47.960 53.830 53.950 54.470 3 0.67 49.930 47.880 48.450 53.810 53.880 54.560 1.00 50.440 48.260 49.000 53.940 54.000 54.600 5 1.33 50.830 48.730 49.440 54.030 54.160 54.580 6 1.67 51.140 49.190 49.850 54.020 54.230 54.610 7 2.00 51.370 49.150 50.150 54.070 54.080 54.610 8 2.33 51.600 . 49.430 50.350 53.990 53.980 54.540 9 2.67 51.790 49.380 50.550 53.940 53.990 54.440 10 3.00 51.890 49.900 50.750 53.940 54.030 54.490 11 3.33 52.000 50.030 50.900 53.970 53.990 54.500 12 3.67 52.060 50.150 50.880 53.960 53.990 54.480 13 4.00 52.080 50.210 50.930 53.990 54.000 54.450 14 4.33 52.150 50.160 51.010 54.000 54.000 54.460 15 4.67 52.200 50.240 51.060 53.980 54.070 54.490 16 5.00 52.230 50.330 '51.060 54'.010 54.030 54.480 17 5.33 52.270 50.380 51.060 54.080 54.050 54:480 18 5.67 52.310 50.410 51.080 54.010 54.050 54.560 19 6.00 52.350 50.430 51.160 54.050 54.080 54.500 20 6.33 52.360 50.500 51.110 54.090 54.070 54.500 21 6. 67 52.370 50.510 51.150 54.080 54.100 54.510 22 7. 00 52.420 50.530 51.170 54.030 54.080 54.550 23 7.33 52.470 50.500 51.180 54.060 54.110 54.510 24 7.67 52.490 50.570 51.200 54.080 5.4. 120 54.530 8.00 52.520 50.570 51.230 54.090 54.160 54.530

CLRT TEST MODE 1993 ST. LUCIE UNIT 1 PERIODIC TEST Sequence Started 06:05, 5/20/93 Sequence Ended 10:05, 5/20/93 EBASCO SERVICES INC.

Plant Operations A Betterment Dept.

ILRT TEST SERVICES APPENDIX B.4

PSL1 Spring 93 ILRT Program Rev 9 CONTAINMENT INTEGRATED LEAKAGE RATE TEST SUPPLEMENTAL VERIFICATION 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 06:05 HOURS ON 5/20/93 TEST CONDUCTED FOR 4.00 HOURS FREESPACE VOLUME OF CONTAINMENT IS 2500000 CU FT CONTAINMENT WAS PRESSURIZED TO 55.36 PSIA FITTED TOTAL TIME ILRT LEAKAGE RATE Lam 0 154 ~o /DAY CONTAINMENT DESIGN LEAKAGE RATE La 0.500 4 /DAY SUPERIMPOSED CLRT LEAKAGE RATE Lo 0.293 ~o /DAY FITTED CLRT TOTAL TIME LEAKAGE RATE Lc 0.328 ~o /DAY La/4 <= Lc <= La/4 1

Lo + Lam Lo + Lam +

0.293 + 0.154 0.125 <= 0.328 <= 0.293 + 0.154 + 0.125 0.322 <= 0.328 <= 0.572

DESCRXPTION OF VARIABLES AVE TEMP CONTAINMENT MEAN TEMPERATURE CALCULATED FROM VOLUMETRICALLY WEXGHTED RTD SENSOR INDICATIONS.

PRESSURE PRIMARY CONTAINMENT PRESSURE XNDICATION.

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

LEAK SIM SXMPLE TOTAL TIME MEASURED LEAKAGE RATE.

LEAK FIT LEAKAGE RATE CALCULATED FROM FIRST ORDER REGRESSION OF SIMPLE TOTAL TIME LEAKAGE RATE DATA.

95a UCL UPPER LXMIT OF THE 95~o CONFIDENCE LEVEL OF FITTED LEAKAGE RATE DATA.

AIR MASS CONTAINMENT AXR MASS.

NOTES FOR TABULAR DATA

1. TABLE VALUES OF ZERO SIGNIFY THE DATA XS NOT APPLICABLE TO THE CALCULATXON.

2. "DELETEDII SIGNIFIES THE SENSOR WAS DELETED.

CLRT VARIABLE TABLE

SUMMARY

S TIME AVE TEMP PRESSURE VAP PRES LEAK SIM LEAK FIT UCL AIR MASS N HOURS DEG F PSIA PSIA 4/DAY 4/DAY 4/DAY LBS 0.00 89.784 55.359 0.3718 0. 000 0.000 0.000 675262 2 0.33 89.747 55.351 0.3717 0.556 0.000 0.000 675209 3 0.67 89.704 55.345 0.3715 0.378 0.000 0.000 675191 4 1.00 89.663 55.338 0.3714 0.373 0.344 1.028 675157 5 1.33 89.619 55.331 0.3710 0.352 0.322 0.640 675129 6 1.67 89.585 55.324 0.3709 0.372 0.327 0.582 675087 7 2.00 89.547 55.318 0.3707 0.355 0.323 0.530 675062 8 2.33 89.512 55.311 0.3705 0.367 0.328 0.512 675021 9 2.67 89.478 55.305 0.3706 0.363 0.329 0.496 674989 3.00 89.438 55.299 0.3704 0.350 0.326 0.477 674967 ll 10 12 3 '3 3.67 89.412 89.380 55.293 55.287 0.3702 0.3700 0.357 0.356 0.327 0.328 0.467 0.460 674927 674894 13 4.00 89.345 55.281 0.3700 0.353 0.328 0.452 674864

CLRT AIR MASS 1993 St. Lucie Unit P1 ILRT Contalnmsnt Nr Mass (LBS) 675,400 Air Mass 675,300 Fitted Ma 675,200 675,'100 675,000 674,900 674,800 0 0.5 1.5 2.5 3.5

'Hme tn Houm EBASCO Phnt Operations 8 Betterment

~*

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CLRT COMPUTED LEAKAGE RATES 1993 St. Lucie Unit P1 ILRT Plat par Goy Sy Raaht 0.8 Simple Leakage

+'itted Leakage 0.6 0.4 0.3 0.2 0 0.5 1.5 2.6 3.5 EBISCO Plaat Opera5one 4 Bettoaneot

IL I 4

i it 1

i I

1 1$

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it IU u

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CLRT LEAKAGE RATES RELATIVE TO LIMITS 199$ St. LUcie Unit 41 ILRT Percent par Day By%cfght 0.6 0.55 0.5 Nnhnum Aooeptable OA6 Madmum Accaptabie Leo

+Rttad Uakago 0.4 0.

0.3 0 0.6 '1.6 2 2.5 3 3.6 4 4.5 5 Time fn Houra EBA8CO Piant Opera5ona 4 SNennent

7 M

C

~

ll 0

CLRT WEIGHTED AVERAGE TEMPERATURE 1993 St. Lucie Unit P1 ILRT TcmpersNuro In Degrees F 89.9 89.7 89.6 89.4

.3 0 0.5 1.5 2.6 3.6 Time tn Houro

~ E.

IP

CLRT CONTAINMENTABSOLUTE PRESSURE 1993 St. Lucie Unit rir1 ILRT 65.38 55.32 55.3 65.28 55.28 55.24

.2 0 0.5 1.5 2.5 3.5 Tlmo In Hauro EBAKCO Rant Oporaticrre 5 BittermorN

\

I 1

1 a 1 IJ

CLRT WEIGHTED AVERAGE VAPOR PRESSURE 1993 St. Lucis Unit 41 ILRT Pressure tn Psla 0.38 0.375 0.37 0.385 0.38 0 0.5 2.5 3.5 Time tn Hours

I" 4 ~

'I Il lt C

L, L

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SENSOR VOLUME FRACTIONS TEMPERATURE SENSORS 5 0. 026708 0. 026708 0.026708 0. 026708 0.026708 o 10 0.026708 0.026708 0.026708 0.026785 0.026785 11 to 15 0.026785 0.026785 0.026785 0.026785 0.026785 16 to 20 0.026785 0.026785 0.026785 0.024037 0.024037 21 to 25 0.024037 0.024037 0.024037 0.024037 0.024037 26 to 30 0.024037 0.024037 0.024037 0.022662 0.022662 31 to 35 0.022662 0.022662 0.000000 0.022662 0.022662 36 to 40 0.022662 0.022662 0.032274 0.032274 0.032274 HUMIDITY/DP SENSORS 1 to 5 0.073335 0.073335 0.073335 0.090064 0.090064 6 to 10 0.090064 0.090064 0.139913 0.139913 0.139913 NOTE: VALUE OF ZERO INDICATES A DELETED SENSOR.

CLRT VARIABLE

SUMMARY

SAMPLE DELTA TEMP 1 TEMP 2 TEMP 3 TEMP 4 TEMP 5 TEMP 6 N HOURS DEG F DEG F DEG F DEG F DEG F DEG F 0.00 86.580 87.019 86.937 86.209 85.581 85.598 2 0.33 86.597 86.995 86.943 86.227 85.577 85.604 3 0.67 86.597 86.972 86.943 86.238 85.588 85.595 4 1.00 86.591 86.968 86.914 86.231 85.581 85.589 5 1.33 86.580 86.957 86.937 86.231 85.604 85.577 6 '.67 86.591 86.957 86.905 86.220 85.592 85.577 7 2.00 86.591 86.968 86.914 86.231 85.612 85.555 8 2.33 86.602 86.945 86.914 86.242 85.592 85.566 9 2.67 86.591 86.923 86.914 86.242 85.612 85.555 3.00 86.580 86.925 86.220 85.612 85.546 ll 10 12 3.33 3.67 86.602 86.591 86.934 86.945 86.923 86.905 86.925 86.253 86.253 85.604 85.612 85.535 85.524 13 4.00 86.602 86.923 86.925 86.231 85.624 85.512

CLRT VARIABLE

SUMMARY

SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 ~ TEMP 12 NUM R HOURS DEG F DEG F DEG F DEG F DEG F DEG F 0.00 87.241 85.354 91. 431 90.522 91.078 90.806 0.33 87.248 85.372 91. 373 90.497 91.054 90.750 3 0.67 87.248 85.349 91. 310 90.443 90.989 90.706 4 1.00 87.241 85.354 91. 261 90.383 90.908'0.897 90.656 5 1.33 87.241 85.354 91.218 90.372 90.528 6 1.67 87.241 85.354 91.164 90.297 90.866 90.497 7 2.00 87.241 85.343 91.111 90.244 90.770 90.409 8 2.33 87.241 85.343 91.057 90.212 90.747 90.400 9 2.67 87.252 85.331 91.014 "90.158 90.651 90.293 10 3.00 87.241 85.343 90.981 90.082 90.640 90.293 11 3.33 87.241 85.343 90.938 90.051 90.609 90.250 12 3.67 87.252 85.331 90.896 90.008 90.533 90.239 13 4.00 87.241 85.331 90.842 89.986 90.490 90.154

CLRT VARIABLE

SUMMARY

SAMPLE DELTA TEMP 13 TEMP 14 TEMP 15 TEMP 16 TEMP 17 TEMP 18 NUM HOURS DEG F DEG F DEG F DEG F DEG F DEG F

0. 00 90.557 90.766 90.994 90.972 90.897 90. 867 0.33 90.522 90.762 90.882 90.936 90.862 90. 819 3 0.67 90.459 90.687 90.817 90.871 90.808 90.768 4 1.00 90.430 90.607 90.821 90.822 90.758 90.696 5 1.33 90.365 90.553 90.736 90.759 90.695 90.696 6 1.67 90.334 90.541 90.682 90.726 90 '41 90.620 7 2.00 90.291 90.476 90.651 90.672 90.610 90.589 8 2.33 90.248 90.422 90.682 90.629 90.556 90.535 9 2.67 90.206 90.371 90.586 90.576 90.502 90.504 10 3.00 90.152 90.326 90.521 90.524 90.448 90.439 11 3.33 90.110 90.306 90.532 90.502 90.406 90.396 12 3.67 90.076 90.252 90.458 90.470 90.383 90.385 13 4.00 90.033 90.220 90.405 90.417 90.340 90.331

CLRT VARIABLE

SUMMARY

SAMPLE DELTA TEMP 19 TEMP 20 TEMP 21 TEMP 22 TEMP 23 TEMP 24 N HOURS DEG F DEG F DEG F DEG F DEG F DEG F 0.00 90.772 91.186 90.959 90.901 '91.288 90.978 2 0.33 90.747 91.133 90.926 90.859 91 '57 90.913 3 0. 67 90.716 91.079 90.874 90.794 91 '14 90.871 4 1. 00 90.644 91.036 90.840 90.774 91.150 90.806 5

6 1 '3 1.67 90.601 90.559 90.962 90.875 90.766 90.733 90.709 90.666 91.096 91.053 90.774 90.732 7 2.00 90.516 90.884 90.666 90.610 91.017 90.673 8 2.33 90.494 90.735 90.648 90.581 90 '68 90.624 9

10 2 '7 3.00 90.440 90.409 90.801 90.753 90.605 90.538 90.539 90.492 90.935 90.890 90.591 90.577 11 12 3 '3 3.67 90.324 90.335 90.724 90.661 90.531 90.477 90.451 90.420 90.861 90.807 90.528 90.485 13 4.00 90.281 90.639 90.432 90.377 90.753 90.441

CLRT VARIABLE

SUMMARY

SAMPLE DELTA TEMP 25 TEMP 26 TEMP 27 TEMP 28 TEMP 29 TEMP 30 N HOURS DEG F DEG F DEG F DEG F DEG F DEG F

0. 00 90.753 90.260 89.060 90.936 90.804 90.599 2 0.33 90.719 90.195 88.984 90.862 90.739 90.556 3 0.67 90.656 90. 175 88.961 90.828 90.674 90.502 4 1.00 90.634 90. 121. 88.930 90.786 90.620 90.460 5 1.33 90.569 90.056 88.845 90.721 90.566 90.395 7

l. 67 2.00 90.518 90.471 90.035 90.000-88.834 88.789 90.690 90.634 90.535 90.479 90.363 90.316 8 2.33 90.453 89.948 88.737 90.593 90.418 90.267 9 2.67 90.399 89.928 88.706 90.551 90.385 90.224 3.00 90.363 89.869 88.639 90.495 90.340 90.166 ll 10 12 3.33 3.67 90.314 90.280 89.820 89.777 88.599 88.567 90.443 90.412 90.299 90.268 90.128 90.085 13 4.00 90.238, 89.755 88.534 90.390 90.223 90.052'

CLRT VARIABLE

SUMMARY

SAMPLE DELTA TEMP 31 TEMP 32 TEMP 33 TEMP 34 TEMP 35 TEMP 36 N HOURS DEG F DEG F DEG F DEG F DEG F DEG F 0.00 89.210 90.550 DELETED 90. 633 90.720 92.148 2 0.33 89.177 90.496 DELETED 90.557 90.655 92.094 3 0.67 89.123 90.442 DELETED 90.514 90.612 92.040 4 1.00 89.071 90.357 DELETED ~

90.460 90.558 91.986 5 1.33 88.984 90;314 DELETED 90.406 90.504 91.955 6 1.67 88.975 90.272 DELETED 90.364 90.462 91.901 7 2.00 88.928 90.247 DELETED 90.308 90.403 91.856 8 2.33 88.877 90.164 DELETED 90.278 90.354 91.816 9 2.67 88.835 90.142 DELETED 90.236 90.332 91.773 3.00 ll 10 12 3.33

3. 67 88.768 88.750 88.685 90.074 90.045 90.014 DELETED DELETED DELETED 90.177 90.150 90.117 90.264 90.235 90.181 91.714

91. 687

91. 654 13 4.00 88.654 89.938 DELETED 90.052 90.150 91.600

f~

CLRT VARIABLE

SUMMARY

SAMPLE DELTA TEMP 37 TEMP 38 TEMP 39 TEMP 40 NUM HOURS DEG F DEG F DEG F DEG F 0.00 90.734 90.485 90.575 90.389 0.33 90.691 90.431 90.523 90.342 3 0. 67 90.615 90.388 90.447 90.288 4 1. 00 90.573 90.334 90.404 90.218 5 1.33 90.530 90.270 90.351 90.176 6 1.67 90.487 90.227 90.297 90.122 7 2.00 90.420 90. 171 90.261 90.080 8 2.33 90.369 90. 131 90.212 90.026 9 2.67 90.349 90.088 90.158 89.983 10 3.00 90.290 90.041 90.111 89.938 11 3.33 90.252 90.003 90.084 89.907 12 3.67 90.230 89.970 90.039 89.853 13 4.00 90.176 89.918 90.008 89.822

CLRT VARIABLE

SUMMARY

SAMPLE DELTA PRES 1 PRES 2 HUM 1 HUM 2 HUM 3 HUM 4 NUY HOURS PSXA PSIA ~o RH ~o RH 4 RH 4 RH

0. 00 55.359 55.364 53.530 57. 190 60.520 49'80 2 0.33 55.351 55.356 53.740 57.350 60.640 49.540 3 0.67 55.345 55.350 53.870 57.480 60.780 49.580 4 1.00 55.338 55.343 54.050 57.650 60.890 49.660 5 1.33 55.331 55.336 54.150 57.810 60.960 49.610 6 1.67 55.324 55.330 54.280 57.950 61.060 49.650 7 2.00 ~ 55.318 55.323 . 54.420 58.090 61.110 49.700 8 2.33 55.311 55.317 54.580 58.170 61.230 49.610 9 2.67 55.305 55.310 54.650 58.280 61.350 49.820 10 3.00  : 55.299 55.304 54.790 58.360 61.410 49.880 11 3.33 55.293 55.298 54.890 58.470 61.480 49.860 12 3.67 55.287 55.292 54.990 58.580 61.540 49.910 13 4.00 55.281 55.286 55.100 58.640 61.610 49.860

CLRT VARlABLE

SUMMARY

SAMPLE DELTA HUM 5 HUM 6 HUM 7 HUM 8 HUM 9 HUM 10 N HOURS % RH 4 RH 4 RH ~o  % RH ~o RH RH'4.160 0.00 52. 57'0 50.680 51.310 54. 150 54.570 2 0.33 52.630 50.670 51.310 54.180 54.250 54.630 3 0.67 52.630 50.690 51.340 54.170 54.270 54.640 4 1.00 52.680 50.730 51.350 54.210 54.330 54.600 5 1.33 52.680 50.770 51.380 54.190 54.250 54.630 6 1.67 52.700 50.800 51.390 54.190 54.240 54.650 7 2.00 52.760 50.660 51.420 54.230 54.320 54.670 8 2.33 52.790 50.770 51.440 54.250 54.350 54.660 9 2.67 52.790 50.750 51.490 54.250 54.340 54.720 10 3.00 52.820 50.770 51.510 54.260 54.420 54.710 11 3.33 52.850 50.780 51.520 54.270 54.410 54.750 12 3.67 52.860 50.900 51.530 54.240 54.350 54.740 13 4.00 52.940 50.940 51.550 54.240 54.480 54.820

APPENDIX C LOCAL LEAKAGE RATE TESTING CONDUCTED SINCE THE LAST ILRT

REFUELING OUTAGE TYPE B TESTING SINCE LAST ILRT 1991 REFUELING OUTAGE

.ja'>gj?Q"q j

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PATH!!,'AIN STEAM BELL TAP ¹1 8 10/21/91 20 20 20 20 1A TAP ¹2 8 10/21/91 20 20 20 20 MAIN STEAM BELL TAP ¹1 8 10/21/91 20 20 20 20 18 TAP ¹2 8 10/21/91 20 20 20 20 FEEDWATER BELL TAP ¹1 8 10/21/91 20 20 20 20 1A TAP ¹2 8 10/21/91 20 20 20 20 FEEDWATER BELL TAP ¹1 8 10/21/91 20 20 20 20 18 TAP ¹2 8 10/21/91 20 20 20 20 25 FUELTRANS BELL TAP ¹1 11/27/91 20 20 20 20 GASKET E-4 OUTAGE AUX. PEN. INTERSPACE 12/13/91 20 20 20 20 GASKET MAINT. HATCH INTERSPACE 12/13/91 20 20 20 20 GASKET FUELTRANSFER INTERSPACE 12/06/91 20 20 20 20 A-1 THRU E-10 ELEC. PEN. N/A 10/29/91 20 20 20 20 TOTAL 260 260 260 260 TYPE 8 KAGE

REFUELING OUTAGE TYPE C TESTING SINCE LAST ILRT 1991 REFUELING OUTAGE AS:,FOUND'<

RATION': 'jTYP,E"::,'.,"TEST;

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$ KN: '<4<:"..< x<<:".<:N PRIMARY MAKEUP V-15328 '0/25/91 20 20 40 40 BYPASS WATER MV-15-1 LEAKAGE SERVICE AIR V-18-794 10/26/91 420 420 820 820 BYPASS V-18-796 LEAKAGE V-18-797 V-18-798 V-18-795 INSTRUMENT AIR V-18-195 10/26/91 900 900 52,000 52,000 BYPASS MV-18-1 LEAKAGE V-18-193 10 CONTAINMENT FCV-25-4 10/21/91 400 400 800 800 PURGE EXHAUST FCV-25-5 CONTAINMENT FCV-25-2 10/21/91 10 10 20 20 PURGE EXHAUST FCV-25-3 14 NITROGEN V-6779 10/24/91 20 20 40 40 BYPASS SUPPLY V-6741 LEAKAGE V-6340 23 RCP COOUNG HCV-14-1 10/26/91 35 35 40 40 BYPASS HCV-14-7 LEAKAGE V-14368 V-14367 RCP COOUNG HCV-14-2 10/28/91 20 20 40 40 BYPASS HCV-14-6 LEAKAGE V-14415 V-14417 LETDOWN V-2515 11/04/91 20 20 20 20 BYPASS UNE V-2516 LEAKAGE 28A SIT SAMPLE FCV-03-1E 10/26/91 20 20 20 20 BYPASS FCV-03-1F LEAKAGE 288 HOT LEG SAMPLE V-5200 10/26/91 20 20 60 60 BYPASS V-5203 LEAKAGE 29A PRESS. SAMPLE V-5201 10/26/91 20 20 20,000 20 BYPASS V-5204 LEAKAGE 298 PRESS. SAMPLE V-5202 10/26/91 1500 1500 6000 6000 BYPASS V-5205 LEAKAGE 31 RCB VENT HEADER V-6554 C 10/28/91 20 20 20 20 BYPASS V-6555 .LEAKAGE 41 SIT TEST UNE V-07009 C 0/28/91 400 120 800 1800 BYPASS V-3463 LEAKAGE 42 RX CAVllYSUMP LCV-07-11A 1/19/91 550 550 1100 1100 BYPASS LCV-07-118 LEAKAGE V-07171 43 RDT PUMP SUCTION V-6301 1/16/91 80 80 120 120 BYPASS V-6302 LEAKAGE 44 RCP BLEED-OFF 1-SE-01-1 C 0/28/91 20 20 20 20 BYPASS V-2505 LEAKAGE UEL POOL CLEANU V-7189 0/25/91 10 10 50 50 BYPASS V-7206 LEAKAGE V-07167 47 UEL POOL CLEANU V-07188 10/25/91 20 20 500 500 BYPASS V-07170 LEAKAGE V-07169

REFUE LING OUTAGE TYPE C TESTING SINCE LAST ILRT 1991 REFUELING OUTAGE

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48A H2 SAMPLE FSE-27-1 0/23/91 20 20 80 80 FSE-27-2 FSE-27-3 FSE-27-04 FSE-27-08 48C H2 SAMPLE V-27-101 0/23/91 20 20 8900 8900 FSE-27-11 51A H2 SAMPLE V-27-102 0/23/91 20 20 40 40 FSE-27-11 51C H2 SAMPLE FSE-27-5 0/22/91 20 20 60 60 FSE-27-6 FSE-27-7 FSE-27-9 52A RCB ATMOS FCV-26-1 0/22/91 1100 1100 1300 '300 BYPASS RAD MONITORS- FCV-26-2 LEAKAGE 52B RCB ATMOS FCV-26-3 0/22/91 1240 1240 1500 1500 BYPASS RAD MONITORS FCV-26-4 LEAKAGE

'2C RCB ATMOS FCV;26-5 0/23/91 90 90 1100 1100 BYPASS RAD MONITORS FCV-26-6 LEAKAGE ILRT TEST V-00140 0/22/91 600 600 1200 1200 BYPASS CONNECllON V-00143 LEAKAGE ILRT TEST CONNECllON V-00142 V-00139 V-00144 V-00141 0/22/91 10 10 20 20 BYPASS LEAKAGE 54 ILRT TEST V-00101 0/20/91 1100 0 2200 2100 BYPASS CONNECTION LEAKAGE 56 HYDROGEN V-25-11 C 0/21/91 35 35 70 70 BYPASS PURGE MAKEUP V-25-12 LEAKAGE 57 HYDROGEN PURGE V-25-13 0/21/91 47.5 47.5 95 95 BYPASS TO FILTER V-25-14 LEAKAGE 58 HYDROGEN PURGE V-25-15 0/21/91 200 200 400 400 BYPASS FILTER BYPASS V-25-16 LEAKAGE 67 CONTAINMENT V-25-20 1/11/91 750 750 2000 2000 VACUUM REUEF FCV-25-7 68 CONTAINMENT V-25-21 1/1 1/91 180 180 1500 1500 VACUUM REUEF FCV-25-8 TOTAL TYPE C NON- BYPASS 1,420 1,420 13,400 6,200 LEAKAGE TOTALTYPE C BYPASS 8,517.5 7,137.5 89,655 71,675 LEAKAGE OTAL

, TYPE C YPASS 9.937.5 e,SS7.S 103,055 77,875 KAGE PLANT UMIT 544,786 SCCM

~I REFUELING OUTAGE TYPE B TESTING SINCE LAST ILRT 1993 REFUELING OUTAGE

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~">>~ A . Mz,g>>..,$ ." %,~;:...:.y,';%j<; j">> '.Pq~,.yg MAIN STEAM BELL TAP ¹1 8 3/31/93 20 20 20 20 1A TAP ¹2 8 3/31/93 20 20 20 20 MAIN STEAM BELL TAP ¹1 8 3/31/93 20 20 20 20 18 TAP ¹2 8 3/31/93 20 20 20 20 FEEDWATER BELL TAP ¹1 8 3/31/93 20 20 20 20 1A TAP ¹2 8 3/31/93 20 20 20 20 FEEDWATER BELL TAP ¹1 8 3/31/93 20 20 20 20 18 TAP ¹2 8 3/31/93 20 20 20 20 25 FUELTRANS BELL TAP ¹1 4/8/93 20 20 20 20 GASKET E-4 OUTAGE AUX. PEN. INTERSPACE 3/31/93 20 20 20 20 GASKET MAINT. HATCH INTERSPACE 8 3/31/93 40 115 40 115 GASKET F U EL TRAN SF E R INTERSPACE 8 4/3/93 20 20 20 20 A-1 THRU E-~ ELEC. PEN. N/A 8 4/5/93 17.9 17.9 17.9 17.9 277.9 352.9 277.9 352.9

REFUELING OUTAGE TYPE C TESTING SINCE LAST ILRT 1993 REFUELING OUTAGE

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PRIMARY MAKEUP V-15328 C '/9/93 20 20 500 500 BYPASS WATER MV-15-1 LEAKAGE SERVICE AIR V-18-794 4/10/93 620 620 1520 1520 BYPASS V-18-796 LEAKAGE V-18-797 V-18-798 V-18-795 INSTRUMENT AIR V-18-195 4/9/93 125 125 3000 3000 BYPASS MV-18-1 LEAKAGE V-18-193 10 CONTAINMENT FCV-25-4 4/1/93 375 375 750 750 PURGE EXHAUST FCV-25-5 CONTAINMENT FCV-25-2 4/1/93 50,000 8,000 100,000 16,000 PURGE EXHAUST FCV-25-3 14 NITROGEN V-6779 4/3/93 17.9 17.9 47.9 47.9 BYPASS SUPPLY V-6741 LEAKAGE V-6340 23 RCP COOUNG HCV-14-1 4/6/93 20 20 30 30 BYPASS HCV-14-7 LEAKAGE V-14368 V-14367 RCP COOUNG HCV-14-2 4/6/93 30 30 430 30 BYPASS HCV-14-6 LEAKAGE V-14415 V-14417 26 LETDOWN V-2515 4P/93 20 20 20 20 BYPASS UNE V-2516 LEAKAGE 28A SIT SAMPLE FCV-03-1E C 4/5/93 130 130 180 180 BYPASS FCV-03-1F LEAKAGE 28B HOT LEG SAMPLE V-5200 C 4/2/93 17.9 17.9 950 950 BYPASS V-5203 LEAKAGE 29A PRESS. SAMPLE V-5201 4/3/93 20 20 580 975 BYPASS V-5204 LEAKAGE 29B PRESS. SAMPLE V-5202 4/3/93 25 25 25 25 BYPASS V-5205 LEAKAGE 31 RCB VENT HEADER V-6554 4P/93 17.9 17.9 17.9 17.9 BYPASS V-6555 LEAKAGE 41 SIT TEST UNE V-07009 4/3/93 200 200 400 400 BYPASS V-3463 LEAKAGE 42 RX CAVITYSUMP LCV-07-11A 4/13/93 180 180 360 360 BYPASS LCV-07-11 9 LEAKAGE V-07171 43 RDT PUMP SUCTION V-6301 4/3/93 2000 2000 2100 2100 BYPASS V-6302 LEAKAGE 44 RCP BLEED-OFF 1-SE-01-1 4/8/93 135 135 150 150 BYPASS V-2505 LEAKAGE UEL POOL CLEANU V-7189 4/3/93 10 10 20 20 BYPASS V-7206 LEAKAGE V-07167 47 UEL POOL CLEANU V-07188 4/1 2/93 10 10 20 20 BYPASS V-07170 LEAKAGE V-07169

REFUELING OUTAGE TYPE C TESTING SINCE LAST ILRT 1993 REFUELING OUTAGE

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FNUMBER~>;. ."-':,'T EST;i@ MDATEY'>:j i'; MIN "PATH '. 'AX:"PATH ".': MAX"PATH,'i jREMARKS I 48A H2 SAMPLE FSE-27-1 4P/93 30 30 80 80 FSE-27-2 FSE-27-3 FSE-27-04 FSE-27-08 48C H2 SAMPLE V-27-101 4P/93 20 20 9100 20 FSE-27-11 51A H2 SAMPLE V-27-102 4/8/93 40 40 40 40 FSE-27-11 51C H2 SAMPLE FSE-27-5 4/8/93 20 20 90 57.9 FSE-27-6 FSE-27-7 FSE-27-9 52A ROB ATMOS FCV-26-1 4/6/93 950 120 1000 3000 BYPASS RAD MONITORS FCV-26-2 LEAKAGE 52B ROB ATMOS FCV-26-3 4/6/93 1000 130 1200 9800 BYPASS RAD MONITORS, FCV-26-4 LEAKAGE 52C RCB ATMOS FCV-26-5 4/6/93 50 20 950 700 BYPASS RAD MONITORS FCV-26-6 LEAKAGE ILRT TEST V-00140 C 3/31/93 575 575 1150 1150 BYPASS CONNECTION V-00143 LEAKAGE ILRT TEST CONNECTION V-00142 V-00139 V-00144 V-00141 3/31/93 15 15 30 30 BYPASS LEAKAGE 54 ILRTTEST V-00101 3/31/93 1200 900 2400 1800 BYPASS CONNECTION LEAKAGE 56 HYDROGEN V-25-11 3/31/93 32.5 32.5 65 BYPASS PURGE MAKEUP V-25-12 LEAKAGE 57 HYDROGEN PURGE V-25-13 3/31/93 47.5 47.5 95 95 BYPASS TO FILTER V-25-14 LEAKAGE 58 HYDROGEN PURGE V-25-15 3/31/93 150 150 300 300 BYPASS FILTER BYPASS V-25-16 LEAKAGE 67 CONTAINMENT V-25-20 4/12/93 500 2600 2600 3500 VACUUM REUEF FCV-25-7 68 CONTAINMENT V-25-21 , 4/12/93 1500 400 1600 1600 VACUUM REUEF FCV-25-8 TOTALTYPE C NON-BYPASS 52,485.00 11,485.00 114,260.00 22,047.90 LEAKAGE TOTAL TYPE C BYPASS 7,618.70 5,588.70 17,540.80 27,285.80 LEAKAGE OTAL

.TYPE C YPASS 60,103.70 17,073.70 131,800.80 49,333.70 KAGE PLANT UMIT 544.786 SCCM