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| DUKE POWER COMPANY CATAWBA NUCLEAR STATION UNIT I REACTOR CONTAINMENT BUILDING INTEGRATED LEAK RATE TEST
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| I DUKE POWER COMPANY CATAWBA NUCLEAR STATION UNIT 1 REACTOR CONTAINMENT BUILDING
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| . INTEGRATED LEAK RATE TEST
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| (?REOPERATIONAL)
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| CONDUCTED JANUARY 10 - 18, 1984 Prepared By: -
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| R. A. Jones V Test Er,'if n'*.er Reviewed By: s W. F. B ve4 Perfo ance ingineer Approved By: M' (yW.Cox' Superintendent of Technical Services
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| TABLE OF CONTENTS I. . DEFINITION OF SYMBOLS AND ABREVIATIONS 1 II. INTRODUCTION 3 III.' TEST PURPOSE 4 IV.
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| ==SUMMARY==
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| 5 V. TEST-ORGANIZATION 6 VI. TEST BACKGROUND INFORMATION 7 A. Test Method 7
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| 'B. Calculation Technique 7 C. Test Activity Flow Chart 7 D. Test Acceptance Criteria and Test Results 7 E. Determination of Periodic Reduced Pressure 14 Test Acceptance Criteria F. Results of Type B & C Leak Rate Tests 14 VII. TEST EQUIPMENT 15
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| < A .- Instrument Specifications 15 B. Computer Program .16 C. Instrument Error. Analysis 17
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| -VIII. CONCLUSION 19 IX. ILRT FIGURES 20 X. RTD LOCATIONS 25 XI. APPENDICES 28 A. Derivations and Formulas for Catawba Containment Leak Rate Comoutations
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| -B. Raw and Processed Data C. Test Log
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| 'D. -Ice Condensor Temperature Stabilitation Crfteria
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| .E. Reduced Pressure Leak Rate Test Discussion L
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| 7 t
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| Pags 1 of 27 I. DEFINITION OF SYMBOLS AND ABBREVIATIONS
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| 'ILRT-Integrated Leak Rate Test l
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| E- Repeatability error l I
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| ;- e ,.
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| Absolute error I Measurement system error
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| 'F Temperature, degrees Fahrenheit FOM Figure of Merit l L, 0.20%,by weight of the containment air per 24 hours at P,,
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| -14.68.psig L, Measured overall integrated containment leakage rate. It is 5 0.75 L, L
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| t Maximum all wable reduced pressure (7.34 psig) test-leak rate.
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| Determined during the preoperational test and is equal to l L, (Lg ,/L ,) with L /L ,5 0.7 I L,g Measured overall integrated containment leakage rate during reduced pressure test. It is 5 0.75 Lt
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| [
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| LR Total observed leak rate during the ILRT.
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| LR(95%) 95% upper confidence level of observed leak rate of'the containment vessel L .
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| Leak rate of all penetrations, valves, flanges which cannot be exposed to test pressure.
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| L .
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| Total observed leak rate during the supplemental test
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| ( L, The known leakage rate superimposed on the containment during the supplemental test.
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| l LLRk' Local leak rate test
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| ! P ~ Pressure P, Design accident pressure psia absolute pressure psig Gauge pressure
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| o.p Pags 2 of.27
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| .s
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| .x
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| 'R ~ Temperature, degrees Rankine ,
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| t ~
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| SIT Structural integrity-t'est
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| 'T- Temperature 1
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| T -
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| dp Dew point temperature t Time
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| '. 'V Containment volume, cubic feet i
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| i '.
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| J i
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| J.
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| 4 .-
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| i 1
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| 1 i y T( ',
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| : 4. .
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| l' I
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| m 1.
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| 4 k
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| 4
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| .) -
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| f 4
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| 1 E
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| i' 2
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| ff Paga 3 of 27 II. INTRODUCTION
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| ~
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| The purpose of this report is to provide adequate information so that an objective review of the test can be performed. This will ensure that the test results reflect truly the leakage characteristic of the as-built containment. In conformance with the Appendix J of 10CFR50 and
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| -associated ANSI standards, the absolute method and mass plot techniques, which require monitoring the containment vessel temperature and pressure to determine the change in containment vessel air mass caused by leakage, are used as the framework for selecting test equipment, developing test computer programs and test procedures.
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| -The Catawba Unit 1 Containment System consists of a containment vessel and a separate reactor building enclosing an annulus. The following containment vessel specifications are used as base data for the containment leak rate test.
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| - Containment Net Free Volume 1,187,136 ft8 (2/3 ice load)
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| - Design pressure 15 PSIG
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| - Calculated Peak Accident Pressure 14.68 PSIG
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| - Test Pressure 3 14.68 PSIG for Full Pressure Test 3 7.34 PSIG for Reduced Pressure Test
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| - Test Temperature Ambient 52 Resistance Temperature Detectors, 3 Dewpoint hygrometers and 3 pressure sensors are installed at predetermined locations in the containment vessel to determine the weighted averages of containment vessel temperature, vapor pressure and pressure. The Catawba containment vessel leak rate test utilizes a fully automatic Data Acquisition System.
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| All raw test data is scanned, printed and recorded on Cassette tape automatically to minimize uncontrolled random errors. Assigned engineers of Duke Power Company were responsible for drafting and conducting the test. Three 8-hour shift crews which consisted of one shift coordinator and two technicians were utilized to maintain 24 hour test activity.
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| Pressurization for the Catawba Unit 1 ILRT was accomplished by 3 diesel driven portable air compressors / dryers rented from Atlas-Copco. Each compressor / dryer was rated at 1500 CFM @ 102 PSI. These compressors supplied air directly to Upper and Lower Containment and to the Ice Condenser through a special -40*F dewpoint dryer. When the test was completed, the containment vessel was depressurized through the containment hydrogen sample and purge system in the annulus and the containment air release and addition system in the Auxiliary Building.
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| The release rate can be controlled if the air is contaminated. Section IX, Figures 2 and 3 show the pressurization and depressurization path used in this test.
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| Page 4 of 27 III. TEST PURPOSE The purpose of the Preoperational Containment Integrated Leak Rate Test l 1s to determine the leak rate of the containment vessel under controlled test conditions; to verify that there were no unidentified openings in the containment vessel due to incomplete construction; and to evaluate
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| ; the possibility of accurately measuring the containment leak rate in a
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| . shorter period of time and/or at a reduced pressure.
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| The containment vessel was preconditioned to provide test conditions which satisfy the following:
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| -- The vessel is under calculated accident pressure, 14.68 psig for the Full Pressure Test and 7.34 psig for the Reduced Pressure Test.
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| - Air temperature and pressure are stable to avoid biasing the leakage characteristics.
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| l
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| - The containment vessel and all penetrations are lined up as close as i possible to the predicted post-accident condition; i.e., those portions of the fluid system that are part of the reactor coolant pressure boundary and are opened directly to the containment atmosphere under h post-accident conditions and become an extension of the boundary of the l containment shall be opened or vented to the containment atmosphere l prior to and during the test.
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| The test utilized highly accurate sensors and an automatic data system to g assure the accuracy and quality of the test data.
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| Statistical- and error propagation analyses are performed on the test data to ensure that the test results are reliable and accurate.
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| Pags 5 of 27 IV. SUMHARY
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| ~
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| The Containment Vessel Integrated Leak Rate and Structural Integrity Test was initiated on 1/10/84 and completed on 1/18/84. It was conducted in compliance with the Catawba FSAR and Title 10, Code of Federal Regulations, Part 50, Appendix J, which states that the containment vessel is subject to a test to assure that an acceptable upper limit cf leakage of radioactive material is not exceeded under dssign accident basis.
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| The vessel was initially pressurized up to 16.892 psig (112.6% of design pressure) and held for 10 minutes for the Structural Integrity Test.
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| Pressure was then reduced to 5 85% or P, and held for 22 hours to allow for outgassing. Pressure was then increased to 314.68 ps;g and the full pressure ILRT was begun at 0305 on 1/12/84 aft 3r a > 4 hour temperature stabilization period. Minor problems were encountered with the ice
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| -condenser temperatures and are discussed fully in Appendix D to this report. The test was evaluated as acceptable at 0850 on 1/13/84 using 24 hours of test data with the following results:
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| LR = 0.1043024%/ Day LR(95%) = 0.110752%/ Day The 95% UCL was less than the acceptance criteria of 0.15%/ day.
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| I The supplemental verification test began at 1020 on 1/13/84 and was determined acceptable at 1610 on 1/13/84 with an observed leak rate of 0.2983907%/ day.
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| l The vessel was then depressurized to 5 85% of gP held for 3 24 hours to allow for outgassing in preparation for the reduced pressure test.
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| Pressure was then increased to 3 7.34 psig and the reduced pressure test
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| ,, was begun at 0600 on 1/15/84 after a > 4 hour temperature stabilization
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| (- period. Problems were initially encountered in obtaining an acceptable leak rate and are discussed fully in Appendix. E to this report. The test was evaluated as acceptable at 1740 on 1/17/84 using 24 hours of test data with the following results:
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| LR = 0.0617871%/ Day-LR(95%) = 0.0677562%/ Day The supplemental verification test began at 1805 on 1/17/84 and was determined acceptable at 0030 on 1/18/84 with an observed leak rate of 0.1408520%/ Day.
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| 'D2is test was conducted per test procedure TP/1/A/1200/06, Conteiament L Initial Integrated Leak Rate Test and Structural Integrity Test.
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| I
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| pegs 6 of 27 V. TEST ORGANIZATION In order to assure that the test is conducted in a safe and e5ficient manner, assigned personnel are organized as shown and their responsibility defined.
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| TEST INSTRUMENTATION COORDINATOR TEST SUPPORT ,
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| , COORDINATOR GROUPS I
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| 1 ASSISTANT TEST COORDINATOR f l i SHIFT SHIFT SHIIT COORDINATOR COORDINATOR COORDINATOR DATA DATA DATA COORDINATOR COORDINATOR COORDINATOR DATA DATA DATA TAKER TAKER TAKER Test Coordinator: His lead responsibility is to provide overall planning and efficient execution of the test.
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| i Assistant Test Coordinator: His lead responsibility is to assume test coordinator responsibilities during his 12 hour shift. Only Test and Assistant Test Coordinators are on 12 hour shifts.
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| 1 Instrumentation Coordinator: His responsibility is to provide test equipsent maintenance support to Test Coordinator.
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| Test Support Groups: Their responsibilities are to furnish technical support to Test personnel as required in conducting the ILRT, solving test 4
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| problems, and minimizing schedule delays.
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| shift Coordinator: Assume general responsibility for ILRT execution on a shift basis.
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| Data Coordinator: His lead responsibility is to process and edit raw data.
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| Data Taker: Record data accurately at correct intervals.
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| l Ptss 7 of 27 i
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| i i
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| l VI. TEST BACKGROJND INFORSIATION i
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| A. Test Method: The absolute method of leakage rate testing is used l , for the Catawba test. This requires the determination and I
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| : j. calculation of air losses by the containment vessel leakage over a '
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| ; stated period of time by the means of direct pressure, temperature 1 and dowpoint observations during the period of the test. Sensors l
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| ; are properly located to provide an average value of the containment vassal temperature and pressure. The effect of the partial pressure of water vapor is measured acd compensated.
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| /,
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| I Upon completion of the 24 hour leak rate test, a test is performed to verify the accuracy of the leak rate test. This requires 3 auperimposing a controlled and measurable leak on the containment vessel and the composite leakage of both the containment vessel
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| [i and the superimposed leak is measured. The difference between the result of the leakage measurement obtained prior to the l introduction of the superimposed leak and that of the composite leak determines the accuracy of the leak rate test.
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| i The test environment is simulated as close to that of designed
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| } accident basis as possible. All portions of the fluid systems that
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| ; are postulated as opening directly to the containment or outside i
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| atmosphere under post-accident conditions are opened or vented
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| { during the test except systems required to maintain the plant in
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| ; safe conditions during the test.
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| i The test pressure is the calculated design basis accident pressure 1
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| j of 14.68 psig for the full pressure test and 7.34 psig per the reduced pressure test.
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| B. Calculation Tec'aaique: Mass of the containment vessel air volume is calculated by the Ideal Gas Law for 24 consecutive hours and plotted against time. The leak rate is obtained by a. linear least t
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| square fit to the mass plot graph. The 95% confidence upper limit
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| ; of the leak rate is calculated by applying the Student T Distribution Test on the leak rate test result. This upper limit is compared with the acceptance criteria to determine the completion of the test. See also Appendix A.
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| C. Test Activity Flow Chart: Figure 1, Containment Pressure versus l Time provides an overall look of the test activities. This'provides information for test planning and test execution.
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| , .D. Test Acceptance Criteria And Test Results-i 1.a. Structural Integrity Test Acceptance Criteria:
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| i-
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| -The Containment Structural Integrity Test.is acceptable if .1 a pressure of at least 16.5 psig is maintained for 10 j minutes without any apparent changes in appearance of or i
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| , other abnormal degredation of the containment. vessel '
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| , surfaces.
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| i' '
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| i' j 4
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| Pagt 8 of 27 The Reactor Building Structural b.tegrity Test is acceptable if a visual inspection detects no abnormal degredation or
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| -~
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| changes in appearance.
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| 1.b. Structural Integrity Test Results:
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| No apparent changes in appearance or abnormal degradation of the containment vessel surfaces were detected after a >
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| 10 minute hold at 16.892 psig.
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| The Reactor Building Inspection detected no abn rmal degradation or changes in appearance.
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| ] 2.a Hot Penetrations Leakage Test Acceptance Criteria:
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| The hot penetration soap bubble test detects no leakage for those penetrations listed in the test procedure per Tech Spec 4.6.1.2.e.
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| 2.b Hot Penetrations Leakage Test Results:
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| No leakage was detected for those penetrations listed in the test procedure.
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| 3.a. Full Pressure Test Acceptance Criteria:
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| Tne measured overall integrated containment leakage rate (L,) is less than or equal to 0.75 L, with the test pressure > 14.68 psig. L, 5 0.75 L, where L, = 0.20 percent by weight of the containment air per 24 hours @ P, (14.68 psig)
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| L ,5 0.15%/ Day.
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| Also, L ,= LR(95%) + L where LR(95%) = 95% Upper Confidence Level of observed leak rate of the Containment Vessel and L = Leak rate of all penetrations, valves, flanges which cannot be exposed to test pressure due to system operation.
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| The difference between the supplemental verification test and the total observed leak rate is within 0.25 L,:
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| (L - L,) - LR $ 0.25 L, Where L,= Total observed leak rate during supplemental test L,= The known leakage rate ruperimposed on the containment during the supplemental test 1
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| 1
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| ~
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| Pags 9 of 27 The quantity of air bled from containment during the supplemental test must be equivalent to 75 to 125% of the leakage rate,L,.
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| 0.75 L, 5 L,5 1.25 L, 3.b Full Pressure Test Results:
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| 24-Hour Test Result (0850, 1/12/84 to 0950, 1/13/84)
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| LR = 0.1043024 %/ Day LR(95%) = 0.1107552 %/ Day The following penetration were not exposed to test pressure due to system alignment required by ILRT. They were type C tested and the leakage added to L .
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| Penetration # System Reason M373 NF Ice Condenser required to be in operation.
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| M372 NF Ice Condenser required to be in operation.
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| M204 VQ Flowpath for turbine flowmeter during imposed leak rate test.
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| M346 VY Relief valve for containment connected to this penetration.
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| CNIP-1 MIS MI ILRT Pressure sensing line.
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| CNIP-1MI6 MI ILRT Pressure sensing line.
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| CNIP-1MI7 MI ILRT Pressure sensing line.
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| The following penetrations were not exposed to test pressure due to following reasons:
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| Penetration # System Reason M230 RN This penetration is supplied by seal water injection system (NW) going to the inside and outside isolation valves. Both valves are being changed to flex-wedge gate design in order to prevent excessive leakage. A type C test is not required on valves 1RN484A and IRN487B since they are supplied by '
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| NW. Reverse check 1RN485 is type C tested and its leakage is included in L,,,.
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| t v -,
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| Psga 10 of 27 Penetration # System Reason M240 RN This penetration has the outside isolation valve supplied by hV.
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| The inside check unit is type C tested, however, it was noticed to be leaking excessivly prior to beginning the 24 hour leak rate test and so the penetration was isolated. Maintenance was performed on 1RN438 and valve internals were rebuilt / replaced. Type C test was performed on 1RN438 and results added to L .
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| Lower Air Lock IAE Temporary gasket was installed on Emerg. Air Penetration penetration prior to ILRT. Type B test results will be added to L .
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| Lower Air Lock IAE Viewport glass installed was not Rea nor Door Viewport QA approved. Type B test results will be applied to L .
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| Upper Air Lock IAE Pressurization fixture was installed Emerg. Air Peneration on penetration to allow entry into containment during inspections.
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| Type B test result will be added to L .
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| Upper and Lower IAE Check valves in line are to be Air Lock replaced with different valves Equalization Lines (2) which will seat properly at lower pressure. Once valves are replaced type C test will be performed and results added to L .
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| Containment Atmos. MI Due to oversight in test procedure, H2 Lever Xmitter line up for these penetrations was Penetratior_s (4) not specified. Type C test will be performed and result added to L .
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| ; Determination of L, :
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| Leakage %/ Day Leakage Penetration System -8 (scem) x 2.1476x10 secs = %/ Day M373 NF 1 x 2.1476x10 -8 = 2.1476x10"O M372 NF 13.97 x 2.1476x10 -8 = 3.0002x10'I M204 VQ 30.3 x 2.1476x10' = 6.5072x10'
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| Paga 11 of 27 Leakage %/ Day Leakage
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| ~
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| Penetration System (seem) x 2.1476x10 ' seem = t/ Day M346 97.0 x 2.1476x10' -6 VY = 2.0832x10 CNIP-1 MIS
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| -8 -8 MI 1.31 x 2.1476x10 = 2.8134x10 CNIP-1MI6
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| -8 -8 MI 1.82 x 2.1476x10 = 3.9086x10 CNIP-1MI7 1.78 x 2. N76x10 -8 -8 MI = 3.8227x10
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| ~
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| 11.2 -8 ~
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| M230 RN x 2.1476x10 = 2.4053x10 M240 170.8 x 2.1476x10" -6
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| , RN = 3.6681x10 Lower Air Lock IAE 2.3 x 2.1476x10 -8 = 4.9395x10
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| -8 Emerg. Air Penetration 1.36 x 2.1476x10 -8
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| ~
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| Lower Air Lock IAE = 2.9207x10 Reactor Door Viewport Upper Air Lock IAE x 2.1476x10
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| ~
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| -8 2.4 = 5.1542x10 Emerg. Air Penetration
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| -8 -8 Upper Air Lock IAE 2.0 x 2.1476x10 = 4.2952x10 Equalization Line Lower Air Lock IAE 5.2 -8 ~
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| x 2.1476x10 = 1.1168x10 Equalization Line 4 Cont. Atmos. MI
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| * x 2.1476x10' =
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| * H L***l 2
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| Xaitter Penetrations (4)
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| ~0 Total L, = 7.3543x10 %/ Day
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| *This penetration cannot be leak tested by due date of this report.
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| Once leak rate is determined it will be added to L and submitted to the NRC in a separate letter. Note that calculations for L , and Lg , will also be revised to reflect this new value.
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| Therefore, L, = LR(95%) + L,
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| = 0.1107552%/ Day + 0.0000074 %/Da7
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| = 0.1107626 %/ Day Which is within Acceptance Criteria of 5 0.15 %/ Day
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| Psga 12 of 27 Supplemental Verification Test Results:
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| ~
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| L = 0.2983907%/ Day L, = 0.2024%/ Day LR = 0.1043024%/ Day (L - L ) - LR' $ 0.25 L, (0.2983907-0.2024) - 0.1043024 5 0.050%/ Day 0.0083117 5 0.050%/ Day which is within Acceptance Criteria 0.75 L,5 L,5 1.25 L, 0.75 (0.20) $ 0.2024 5 1.25 (0.20) 0.15%/ Day 5 0.2024%/ Day 5 0.25%/ Day Which is within Acceptance Criteria.
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| 4.a Reduced Pressure Test Acceptance Criteria: -
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| * Note that L is calculated in Section VI.E. of this report and is equal to 0.122%/ Day.
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| The measured overall integrated containment leakage rate (L g ,) is less than or equal to 0.75 L with the test pressure > 7.34 psig. ,
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| Lg ,5 0.75 L gwhere Lg = 0.10 percent by weight of the containment air per 24 hours @ P (7.34 psig)
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| L 5 0.075%/ Day tm Also, L = LR(95%) = L, Where LR(95%) = 95% Upper Confidence Level of observed leak rate of the Containment Vessel And L = Leak rate of all penetrations, valves, flanges which cannot be exposed to test pressure due to system operation.
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| The difference between the supplemental verification test and the total observed leak . ate is within 0.25 Lg :
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| (Lc ~
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| o) - LR $ 0.25 Lg Where L c = Total observed leak rate during supplemental test L, = The known leakage rate superimposed on the containment during the supplemental test 1
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| ]
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| I P g2 13 cf 27 The quantity of air bled from containment during the supplemental that must be equivalent to 75 to 125% of the leakage rate L . ~
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| 0.75 L $ L,5 1.25 L 4.b. Reduced Pressure Test Results:
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| 24-Hour Test Results (1740, 1/16/84 to 1740, 1/17/84)
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| LR = 0.0617871%/ Day LR(95%) = 0.0677562%/ Day Therefore, L, = LR(95%) + L,
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| = 0.0677562%/ Day + 0.0000074 %/ Day
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| = 0.0677636 %/ Day Which is within Acceptance Criteria of
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| $ 0.092%/ Day (75% of g L as deterr.ined in Section VI.E. of this report)
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| Supplemental Verification Test Results:
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| L = 0.140852%/ Day L,= 0.1010%/ Day LR = 0.0617871%/ Day Lg= 0.122%/ Day (Lg - L,) - LR 1 0.25 L (0.140852 - 0.1010) - 0.0617871 $ 0.25 (0.122) 0.02193%/ Day $ 0.031%/ Day Which is within Acceptance Criteria 0.75 Lg 5 L,5 1.25 L ,g using L =g0.122%/ Day 0.75 (0.122) $ 0.1010 $ 1.25 (0.122) 0.092%/ Day $ 0.1010%/ Day 3 0.153%/ Day Which is within Acceptance Criteria. -
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| a
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| l Pegs 14 of 27 E. . DETERMINATION OF PERIODIC REDUCED PRESSURE TEST ACCEPTANCE CRITERIA 10CFR50,AppendixJ,.III.A.4.1(iii)requiresusingtheIe'akage rates obtained during the preoperational tests for the full pressure and reduced pressure tests to calculate the acceptance criteria for future reduced pressure tests. Using values obtained during the preoperational Integrated Leak Rate Test, an acceptance value of 0.118%/ day is obtained for future reduced pressure tests.
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| L ,(full pressure leak rate) = 0.1107626 %/ day Lg, (reduced pressure leak rate) = 0.0677636 %/ day L', = 0.20 %/ day Lg =
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| L, (L g,/L ,) = 0.20 (0.0677636/0.1107626)
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| = 0.1223583 %/ day Lg = 0.122 %/ day Also the ratio L g,/L , must be less than 0.7 Lg,/L , = 0.0677636/0.1107626
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| = 0.6117913 < 0.7 F. RESULTS OF TYPE B AND C LEAK RATE TESTS Test Final Conservative Test Results TP/1/A/1200/16, Containment 812.98 seca Isolation Valve Leak Rate Test = 1.7460x10' %/ Day TP/1/A/1200/16A, Containment 1915.1 seca Purge Isolation Valve Leak Rate Test = 4.1129x10" %/ Day TP/1/A/1200/16B. Additional 191.51 seca*
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| Containment Isolation Valve Leak Rate = 4.1129x10'0 %/ Day Test TP/1/A/1200/17, Fuel Transfer 1.89 seca Tube Leak Rate Test = 4.0590x10'O %/ Day TP/1/A/1200/18 Upper Personnel 344 seca Inck Leak Rate Test = -6 7.3877x10 %/ Day TP/1/A/1200/19, Lower Persornel 803 seca I4ck Leak Rate Test = 1.7245x10
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| -5
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| %/ Day TP/1/A/1200/20, Equipment Match 191.5 seca Leak Rate Test = ~0 4.1127x10 %/ Day l
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| l 1
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| Pcgo 15 of 27 TP/1/A/1200/25, Electrical 96.37 seem Penetration Leak Rate Test -6
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| = 2.0696x10 %/ Day r
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| PT/1/A/4200/01P, NF Penetration 11.38 sccm Leak Rate Test
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| = 2.4440x10' %/ Day PT/1/A/4200/01R, M301 Penetration 2.0 . scem Leak Rate Test -8
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| = 4.2952x10 %/ Day
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| *Value does not include Cont. Atmos. H2 Level Transmitter penetra-tions (4) as discussed in Section VI. D.3.b of this report. Once leak rate for these penetrations is determined it will be submitted to the NRC in a separate letter.
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| VII. TEST EQUIPMENT The ILRT instrumentation system is designed to accurately record test parameters. The system consists of a central data acquisition system with a remote scanner / multiplexer unit and individual temperature, pressure, and dowpoint sensors. All RTD's are wired to the remote scanner / multiplexer unit located inside containment. The signals are then multiplexed and sent to the central data acquisition facility.
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| All other sensors are wired directly to the data acquisition facility 1
| |
| located outside containment in a test van.
| |
| A. Instrument Specifications i
| |
| Precision Pressure Gauges are Ruska Model 6000-801-40 PSIA gauges.
| |
| Range: 0 to 40 PSIA Repeatability - 24 Hr: i .0008 PSI:
| |
| 90 Day: i .0016 PSI Accuracy: i (.008% Full Scale + .012% Reading) or better, traceable to NBS
| |
| , Output: Direct digital output plus BCD parallel signal for recording.
| |
| The Dowpoint Temperature Analyzers are General Eastern system 1200 AP sensors with Model 700 aspirators.
| |
| Range: -40 to +120*F Dewpoint Repeatability -1.05'T Accuracy: 1.4*F dowpoint, traceable to NBS
| |
| : Output: Direct digital readout plus 0-50 mV signal recording The Resistance Temperature Detectors are Leeds & Northup Catalog Number 178055 Range: -100 to +250*F
| |
| | |
| i Pcgs 16 of 27 Accuracy: 1.40*F over 32 to 100*F -.
| |
| Element: Copper ,
| |
| i Resistance: 10 ohns at 77*F Section IX, Figure 5 shows placement of RTD's while Section X gives their general locations.
| |
| l 1
| |
| The Turbine Flowmeter is a Flow Technology Model PTC-8C5.0-GJS
| |
| : j. Flocapsule with Model PRI-402A Flow Rate Monitor.
| |
| i Range: 0.5 to 5 ACFM Repeatability - i.25% FS Accuracy: i0.2%, Traceable to NBS. i.0125 ACFM 4 L Output: Visual display plus 0-5 VDC signal for recording 4
| |
| The Data Acquisition Facility is a Leeds and Northup Catalog Number ,.
| |
| 70072-409-4999-6-000000-0600-00-001-301-099 Digital Data
| |
| * Surveillance Facility with the following features:
| |
| ) - Nunation Numeric Display
| |
| ) - Scanner / Programmer j - Digital Printer *
| |
| - Digital Clock
| |
| - Cassette Tape Recorder j Section IX, Figure 4 shows the test instrumentation set-up.
| |
| B. Computer Protram
| |
| }
| |
| To provide on-line data analysis, a computer program is developed j using formulas and methods specified in Appendix A. The Leak Rate j
| |
| Test Program (LRT) reads instrument readings from a magnetic tape
| |
| ! cassette taken from the data recorder on the Digital Data l Surveillance Facility (DDSF). The raw data from the tape is i
| |
| calibrated using quadratic curve fits. This calibrated data is l then checked for validity. Using the mass plot analysis method, the
| |
| , calibrated verified data is processed to yield a normalized weight i
| |
| which is the ratio of the mass of air in the containment at the
| |
| ! present time to that which was initially present when the test i began. Linear regression and confidence interval calculations are i
| |
| then performed to determine whether the results have coveraged i* sufficiently to yield an accurate indication of the actual containment leak rate. c 1
| |
| j Using the terminal procedures detailed in the user documentation, the
| |
| } test administrator can run the program from any teletype-compatible j terminal device having magnetic tape cassette capability. The program is designed for interactive processing so that at.each step the user will be queried as to how he wishes the work to be j accomplished. Instrument parameters and readings can be entered f ._
| |
| .-, .,w~ , ,-n , , - .. , , - . . - , , , , - - - , - ,r.- ,. , , , . - ~ , - ~-
| |
| | |
| u-Page 17 of 27 into the computer system either automatically from cassette or manually from the terminal keyboard., If any crrors are detected in
| |
| ~
| |
| tbs data, t- S the user will have the option of correcting the specific error on the computer instead of re-entering all of the data.
| |
| All data stored in the computer is protected by a password selected at the beginning of the test and must be specified each time the program is run to gain access to the data. This provides some measure of protection against inadvertent intrusion during the conduct of the test. At the conclusion of the test all of the stored data, from raw instrument readings through intermediate results to the final results, will be copied to an archival storage medium to satisfy long-term retention requirements of regulatory agencies. The archives can be placed on active storage at any time to verify csiculations or generate reports.
| |
| C. _ Instrument Error Analysis (Equations used in the section can be found in ANS N274, Draft Revision 3, November 15, 1978)
| |
| Symbols:
| |
| FOM = Instrument Figure of Merit (*./ day) t = Test duration (hrs)
| |
| P = Test pressure (PSIA) (use 14.68 psig for Full Pressure Test, 7.34 psig for Reduced Pressure Test)
| |
| P y = Vapor pressure at test time (PSIA)
| |
| T = Cont. weighted average absolute test temp. ('F) (Assume 76.63*F) e = Error associated with measurement of change E = Sensor error (Sensitivity)
| |
| I = Measurement system error excluding sensor
| |
| : 1. Pressure:
| |
| No. of sensors = 3 Range 0 - 40 PSIA Sensor Error (Ep) = 10.008*JS = 0.0032 PEIA Measurement system repeatability error ~ (Ip) = 20.002*JS =
| |
| 0.0008 PSIA
| |
| [(Ep )8 .+ (Ip )s j I e =i = 20.0019044 PSIA P
| |
| (No. of Sensors)I
| |
| : 2. Vapor Pressure:
| |
| No. of sensors = 3 Range -40*F to 120*F _,
| |
| Sensor Error E = 10.40*F or i .001268 PSIA *
| |
| | |
| )
| |
| l Pcg2 18 cf 27 l
| |
| Measurement System Error (I) = 10.05'F or 1.0001585, PSIA *
| |
| [(.001268)8 + (.0001585)2]I e py = 3 I = i .0007378 PSIA
| |
| *At dowpoint of 36'F, the rate of vapor pressure change per l'F is .00317 PSIA /*F
| |
| : 3. Temperature No. of Sensor = 52 Sensor Error = 1 0.40*F or 1 0.40*R Measurement System Error = 1.15'F or i .15'R
| |
| [(.4*R)8 +( .15*R)*]
| |
| e = 52 I = 1 .0592420*R T
| |
| : 4. FOM (Figure of Merit)
| |
| +2e 1/2 FOM = i 2400 2e + 2e py T p
| |
| t (p / kp / T
| |
| ~
| |
| =1 2400 24 2[.0019044\8 + 2 [.0007378 \ + 2 [0592420\8 1/2
| |
| _ ( 29.376 / ( 29.376 / ( 536.3 / ,
| |
| = i .0184585% per day for Full Pressure Test (Note that value is 5 0.25L, = 0.05)
| |
| ~
| |
| =i 2400 8 2/.0019044 +
| |
| 24 2 /.0007378\8 + 2[.0592420f1/2
| |
| ( 22.036 ( 22.036/ \ 536.3 / ,
| |
| = i 0.0203922% per day for Reduced Pressure Test (Note that value is 3 0.25L, = 0.031)
| |
| These FOM values indicate that test instrument repeatability is adequate to provide a precision measurement of maximum allowable leak rate for both Full and Reduced Pressure Leakage Tests.
| |
| Random errors on test results were analyzed under 95% confidence analysis and incorporated into the test results for acceptance verification.
| |
| The tests (both Full Pressure and Reduced Pressure Tests) also underwent required accuracy tests at the end of the 24 hour ILRTs.
| |
| They met the Acceptance Criteria (See test results).-
| |
| | |
| ~
| |
| Pcg3 19 of 27 VIII. CONCLUSION With all conservative factors built in the test results analys~is, the following conclusions were made on the Catawba Unit 1 ILRT:
| |
| : 1. Catawba Unit 1 Containment Vessel is capable of safely containing fission products under designed accident conditions.
| |
| : 2. With a properly controlled test environment, test acceptance could be attained much earlier than the 24 hour minimum required time for a 24-hour test.
| |
| : 3. No unidentified opening in the Catawba Unit 1 Containment vessel exists due to incomplete construction.
| |
| | |
| Prgs 20 of 27 IX. ILRT FIGURES
| |
| : 1. Containment Pressure vs Time
| |
| : 2. RTD Locations and Pressurization /Depressurization Paths
| |
| : 3. Pressurization System
| |
| : 4. Test Instrumentation System l
| |
| s
| |
| , ,- . . . , . - - ,. - ~
| |
| | |
| FfGURE 1 Page 21 of 27
| |
| - _.__ . _+_.._. .__._ _. _ .. ... 4 g,
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| | |
| 4 FIGURE 2 RTD Locations and Pressurization /
| |
| Depressurization Paths
| |
| . .g i @ '
| |
| : 9. c
| |
| .u .
| |
| a - m-- -
| |
| p a ,_ - .-
| |
| graC104 ELDL saatt-cenas STM.
| |
| .%,mu . STM.
| |
| EN. GEN. '
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| G.D* 'A'
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| | |
| 4 Page 23 of 27-L ( l I la i I: 1 13 e
| |
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| fl
| |
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| |
| | |
| i 4
| |
| m2 F'
| |
| Turbine -' Flow I
| |
| Flow M. Display i
| |
| RTD's * *** **" "*
| |
| Display Dewpoint Sensor '
| |
| Numatron Fressure Sensor slock ~ -
| |
| Computer i .
| |
| I Frinter I 2 gnetic Tape Reader b -
| |
| i i i
| |
| Intercoupler : Magnetic Tape i
| |
| CONTAINMENY VESSEL. Cassete Unit 2 f N i -
| |
| ILR T van a o
| |
| -h FIGURE 4 O Test Instrumentation System 4
| |
| | |
| m Psgs 25 of 27 X. RTD LOCATIONS LOWER CONTAINMEhT (CONTAINMENT VOLUME FRACTION = 0.2676)
| |
| RTD # GENERAL LOCATION COMPARTMEhT VOLUME FRACTION 1 Wall mounted in incore inst. area 0.0528
| |
| ( 2 S.G. D lower support structure el. 570' O.0530 3 S.G. A lower support structure el. 570' O.0530 4 S.G. B lower support structure el. 570' O.0530 5 S.G. C lower support structure el. 570' O.0530 6 Wall mounted in tunnel area 0.0327 7 Wall mounted in tunnel area 0.0327 8 Wall mounted in tunnel area 0.0327 9 Wall mounted in tunnel area 0.0327 10 On top of S.G. 1D 0.0530 11 On top of S.G. 1C 0.0530 12 On top of S.G. 1B 0.0530 j 13 On top of S.G. IA 0.0530 14 On top of NC Pump 1D 0.0530 15 On top of NC Pump ,1A 0.0530 l
| |
| 16 On top of NC Pump 1B 0.0530 17 On top of l'C Pump 1C 0.0530
| |
| , 18 In Accumulator Room 1D 0.0120 19 In Accumulator Room IC 0.0101 20 In Accumulator Room 1B 0.0116 21 In Accumulator Room 1A 0.0116 I
| |
| i l
| |
| l 4
| |
| | |
| Pcg2 26 of 27 RTD # GENERAL LOCATION CONTAINMENT VOLUME FRAC, TION 25 Column mounted in incore 0.0533 instrumentation area 26 Column mounted near lower 0.0419 containment vent 27 Column mounted near lower 0.0399 containment vent UPPER C0hTAINMENT (CONTAINMENT VOLUME FRACTION = 0.5875)
| |
| RTD # GENERAL LOCATION COMPARTMENT VOLUME FRACTION 28 On concrete housing for S.G. 1D 0.0590 29 On concrete housing for S.G. 1A 0.0590 30 On concrete housing for S.G. 1B 0.0590 31 On concrete housing for S.G. 1C 0.0590 32 On wall between S.G. lA & ID 0.1150 33 On wall between S.G. IB & IC 0.1150 34 On wall below crane track el. 665' O.1100 35 On wall below crane track el. 665' O.1100 36 On cont. spray piping 31'6" of 0.0950 center el. 707' 37 On cont. spray piping 31'6" of 0.0950 center el. 707' 22 Wall mounted in room with air 0.0200 return fans 23 Mounted on ladder support in 0.0590
| |
| , reactor cavity 24 Mounted on ladder support in 0.0450 reactor internals storage area l
| |
| l i
| |
| h
| |
| | |
| P g2 27 ef 27 ICE CONDENSER (CONTAINMEhT VOLUME FRACTION = 0.1449)
| |
| RTD # GENERAL LOCATION COMPARTMENT VOLUME FRACTION 38-47 Evenly spaced around the upper 0.0559 Each plenum area el. 669' 48-52 Evenly spaced around the lower 0.0882 Each plenum area el. 600'
| |
| | |
| w I
| |
| APPENDICES 48 i
| |
| i 1
| |
| L
| |
| | |
| ~
| |
| APPENDIX A DERIVATIONS AND FORMULAS FOR CATAWBA CONTAINMENT LEAK RATE COMPtTTATIONS This appendix presents derivations of formulas used to develop the Catawba leak rate computer program.
| |
| b
| |
| : w. - . _ _ - - . _ _ _ - - - - _ _ _ . . _ _ . _ _ _ _ . - . . .---.____----_---_-_--_--_-__.-___.--__-__.__.--___.a --
| |
| | |
| \
| |
| l 1
| |
| Pcg3 1 ef 8 DEFINITION OF SYMBOLS P = Absolute pressure in the Containment Vessel (PSFA)
| |
| T = Weighted average absolute temperature of the Containment Vessel air compartment (*R) th Wg = Normalized mass of containment vessel air at i data point (dimension less)
| |
| P, = Partial pressure of water vapor (PSFA) t = time (ein) th Yk = Assigned volume fraction of k sensor (Fraction of volume) th Tk= Recorded temperature of k sensor (*R)
| |
| Wg = Estimated value of Wg in the least square fit calculation b = Slope of the least square fit line (fraction / min.)
| |
| LR(95%) = 95% confidence value of LR LR = Measured containment leakage rate (%/ day) a = y intercept of the least square fit line (dimensionless)
| |
| S=8 the variance of W W i S 8 = the variance of b b
| |
| SUBSCRIPTS u = upper containment compartment L = lower containment compartment I = Ice Condenser compartment .
| |
| v = vapor 1 = data point at start of test th i = 1 data point (i = 1 to N)
| |
| N = Final data point of a given set th k = k sensor MASS PLOT CALCULATION AND STATISTICAL TREATMENT OF LEAK RATI DATA Normalized Containment Vessel Air Mass The air mass of the Containment Vessel is calculated using ideal gas law compensated for partial water vapor pressure. Air mass of 3 compartments (lower, upper, Ice) are determined separately and combined to yield the whole containment Vessel to simplify the calculation. Normalisation of W gis th applied by taking the ratio of the i value and that of the initial value.
| |
| | |
| Pego 2 cf 8 The values 0.5875, 0.2676, 0.1449 are the assigned volume fraction f,or upper containment, lower containment and Ice Condenser The average temperature T at each compartment is calculated as the sum of the volume weighted recorded temperatures.
| |
| L L $
| |
| 0.5875[P-P v l ) + 0.2676[P-Ph v I+ 0.1449[-P 1 v ) l T / (T /
| |
| V
| |
| = T/u L 1 1 1 4
| |
| P-P )
| |
| 0.5875[P-P v + 0.2676 v i+ 0.1449lf-P v T
| |
| u I
| |
| N T
| |
| /L (T I
| |
| IV T = Ikk k= 1 to 21, 25 to 27 for lower containment k= 22 to 24, 28 to 37 for upper containeent ,
| |
| k= 39 to 52 for ice condenser See Section X for voluee fraction of each sensor.
| |
| Leakaze Rate of the Containment Vessel The graph of W g versus time is least square fitted to yield an estimated straight line. The rate of the containment vessel air sans loss (or the e containment vessel leak rate) is the slope b of the least square fitted line W g Og = bt, + a
| |
| 'Ihe value of a and b can be determined by taking ghe first partial derivation of the sum of square of deviation Q (Q = I (Wg-w}8)withrespecttoaandb g
| |
| and minimise them:
| |
| s - A 6 I (W g - Wg )8 Wg = btg+a
| |
| : g. -
| |
| =0 4 sa aW g 6a Wg-Wg btg-a
| |
| | |
| ~
| |
| Peso 3 of 8 l
| |
| - 4 . .
| |
| l 8 1 (W -
| |
| W ):
| |
| l - i 1 -
| |
| = 2 1 (W g - btg - a) = 0 da 1 (W g - btg - a) = 0 Na + bitg=Wg (1)
| |
| A - ^
| |
| 4 1 (W g -W g )8 Wg = btg+a g= - -
| |
| =0 4 6b ob Wg -W g =W g - bt g -a
| |
| - +
| |
| 6 1 (W g - Wg )8
| |
| -'= 2 1-ti (Wg - bt g- a) = 0 eb '
| |
| 1-tg(W g - bt g a) = 0 (2) alt g+b1ta g ggggg (3) with (1) and (3), a and b can be solved by matrix:
| |
| Na + (Itg ) b = N g (1)
| |
| (It ) a + (It ) b = It W 8
| |
| (3) i L Li N IW g Itg Itg Wg N1tg Wg - (Wg ) (Itg) be I')
| |
| N It g N1tg8 - (It g)8 It g It g8 l
| |
| t l
| |
| | |
| P:ss 4 of 8 l ,
| |
| I"i I*i 1 It W It 8 IW It 8 - It It W '
| |
| l a= ii i = i i i i i (5)
| |
| N It g N1tg8 -
| |
| (It g )"
| |
| It g It ga LR = b 144000% per day .
| |
| (*unless otherwise specified, all summation will be from i = 1 to i = N !
| |
| It is i* rtant to emphasise here that the slope b or leak rate is formulated on the allowing t assumptions:
| |
| - the deviation of Wgfrom the true value are distributed according to the gas distribution function [
| |
| - only the Wg contains randos error, not the t g
| |
| +
| |
| t I
| |
| f l
| |
| l I
| |
| f r
| |
| i I
| |
| | |
| Pegs 5 of 8 The Confidence Limit of the Slope of the Least Square Line .,
| |
| As indicated in the error analysis, the random error is a major contribution which deviates the test result from the true value. Due to the random {
| |
| characteristics of this error, only statistical treatment can possibly i evaluate' the error effect on the test result. In order to choose a proper I statistical treatment, it is important to identify the characteristics of the l observed data. In the previous derivation, it is found that LR is the !
| |
| outcome of the calculation from the observed temperature and pressure in the Containment Vessel using the ideal gas law and curve fitting method. It is now obvious that the observed data is a continuous measurement which is completely different from the discrete measurement. The latter requires discrete statistical treatment (x chi 2 SQUARE), while the former requires continuous statistical treatment (The t test).
| |
| The t test provides information which indicates how much the calculated leak rate deviated from the true value and at what probability.
| |
| In other words: -
| |
| L(TRUE) = LR 1 " Deviation" (percent of probability)
| |
| For t test method " deviation" is defined as:
| |
| Deviation = t S b
| |
| - t is a tabulated value which corresponds to the number of Data sets taken and the required probability (in this case 95% is chosen on popular basis).
| |
| -S is the standard deviation of the variance of the containment air weight.
| |
| b Equation (4) indicates that b = f (Wg ) and by definition of variance:
| |
| 6b f
| |
| =
| |
| S b
| |
| I 6W) g S ,8 (5) where S,8 is the variance of Wg :
| |
| 2 =
| |
| (W -
| |
| a - bt )8 S i i (6) w N-2 f
| |
| -a., .-*%+~ =
| |
| .m-3 9
| |
| | |
| .y__._ . _ _ . - - _ __ - - - - - - - - - _ - _
| |
| l Paga 6 of 8 The (N-2) it, chosen here instead of N because the least square line W g is ,
| |
| restricted by value of b and a. The freedom to evaluate the variance of W is l g
| |
| reduced by 2 even though N data is recorded.
| |
| (It )
| |
| 6 (NItW-(IV1) ii i nit * - (It )*
| |
| 6b = i i 6W 6W g let c = nit 8g -
| |
| (It g)8 6
| |
| nit W ii
| |
| -(IW)(It)\
| |
| i i /
| |
| c 6b =
| |
| 6W g 6W 1 6(NItW 11
| |
| - (IW ) (It ) /\
| |
| i i
| |
| = c 6W
| |
| = 1 Nt g- It g c
| |
| [ 6b 8
| |
| = 1 Ihit -
| |
| It 8
| |
| (7) 6W, C* i i Substitute (7) to (5) 8 S
| |
| 8 S = w I (Nt -
| |
| It )8 b cV i i 8
| |
| S
| |
| = w 8 2 I (N t - 2Nt It + (It )2)
| |
| ? i i i i 8
| |
| S
| |
| = w (N It 8 8 -
| |
| 2 nit It + N(It )*)
| |
| c' i i i i
| |
| | |
| r- .
| |
| Psg3 7 of 8 ,
| |
| \
| |
| l 8 ~~
| |
| S 8
| |
| = w (N It 2
| |
| - N(It )2) c2 i i (8)
| |
| Substitute c = nit g 8 - (It g)8 to (8):
| |
| S
| |
| * 8 b
| |
| 2 c = S e w/N nit 8 - It
| |
| * c = i i = It 8 - It
| |
| * N N i i N .
| |
| 8 S8 = SW b Itg * - It 8 i
| |
| N The identity provides:
| |
| _ (It ) _
| |
| i I(tg - t)2 = It g8 -
| |
| = It g 8 -
| |
| t It, N
| |
| 2 2 S S S8 S* = w = w = v (9) b It 8-It 8 I(t -t)2 It 2-t It i i i i i N
| |
| 1 I
| |
| l l
| |
| l
| |
| | |
| Paga 8 of 8 Summarization:
| |
| The following are the essential equations used in developing ILRT computer program:
| |
| 0.5875 (P-P ) + 0.2676 (P-P ) +0.1449[(P-P)
| |
| W = \T u \ T /L \T I 0.5875[(P-P + 0.2676 (P-P +0.1449[(P-P v -
| |
| qT u \T v )L (T v/I T = IT V kk W = bt +a -
| |
| nitg Wg -
| |
| (IWg ) (Itg) b=
| |
| nit g 2 -
| |
| (Itg)2 IWg (Itg 8) -
| |
| (Itg ) (Itg W) a=
| |
| nitg* - (It )8 g LR = -b LR(95%) = LR i tS b t value corresponds to f = N-2 and 0.975 I(W - a - btg )2 I
| |
| S 8 =
| |
| W N-2 S8 i S = v b
| |
| It 8 -tit
| |
| - 1 L -.
| |
| | |
| N 1
| |
| l O
| |
| APPENDIX B RAW AND PROCESSED DATA I
| |
| i I
| |
| i l
| |
| | |
| " ~
| |
| i _'
| |
| f l
| |
| l f.
| |
| INITIALIZATION DATA I
| |
| t Y
| |
| | |
| ( ,.
| |
| 6 . . . . . ~ . -.
| |
| LEAR RATE INITIAt.IZATION
| |
| . L 8
| |
| E. 2 %
| |
| a a
| |
| N-CUP STRUMENT(TA IFC Nrft.N f NTS .
| |
| 26.8% BLbG UOLl.INE
| |
| ~~
| |
| , 1
| |
| , , ..- '."'BRMIS 10 5.0528 1'PT Vol
| |
| '
| |
| * TYP''~ 2 Rt X 8 82 T-'5 . ~~-.997 6.7500E-0 B t K 7 4 3.O.3v;;363 . . c. - .. . . . . - - f . u , a
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| -~ ~'-' ~ ~ ~ " ' ~ ' ' * ~ ~ ' * ~ ~ ~ ~ ~
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| 105 0.0530 2 0.710(C-05 .9/719 O. 4970 e
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| e o ~~'0.0 U. O}2 277 -'2 2' .~~~ .8500E*0g ~~"W796
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| .2600E-Os 0.999,1 4 v. -0,
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| " P."",JT INSTRUMENT VOL TYP ~T0f m s. d i x s2) e . va - -.- vvi sv. a.;.Ja.w.w n , .. . . ru.a .r.:r.;: . < - c . um ra.v 4, ;. .. : ; s em.a "
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| 29.398
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| 84.117 . 0.000 73.962.. 73.102
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| BANK 2 84,810 85.038 73.164 73.691 72.687 70.323
| |
| * >SANBC.3_ 71.591 66.54A 70.878 70.036 70.590 70.25' 71.312 -71.396. '
| |
| BAPet 4 70.I55 69.940 70.II3 70.079 71.051 _70.121 ._71.525 -_.70 11A__ ____ _ . . . _ .;*
| |
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| |
| * JWOL 7 29.375 29a.400 71. '.e4 3 83.705 29.372- _2.210- 40.2ZO 40.620 0.000 0.900 0. 9)<? o.Doo _ _ . _ . - a ;
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| 2 84.770 .SS.028_.84.077 73.?g2 ,_73.164 .73.671 _ 72.527 _ 20.313 . .- e (a '3 71.571 66.516 70.894 70.0.,6 71.312 _ 71.39A
| |
| * 70.610 71.071 70.101 . . . . . . .
| |
| 70.242 70.426 71.564
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| 2.990 40.260 . 40.600 C.000 0.000 o,000 o.000 a,
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