ML20070P098

Reactor Containment Bldg Integrated Leak Rate Test

ML20070P098
Person / Time
Site:	Mcguire
Issue date:	09/28/1982
From:	DUKE POWER CO.
To:
Shared Package
ML20070P093	List: ML20070P089 ML20070P098
References
NUDOCS 8301260141
Download: ML20070P098 (191)

Text

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McGUIRE NUCLEAR STATION 1

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4 REACTOR CONTAINMENT BUILDING i

INTEGRATED LEAK RATE TEST CONDUCTED SEPTEMBER 23-28, 1982 s

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TABLE OF CONTENTS Section Dafinition.of Symbols and Abbreviations I

Introduction II Test Purpose III Summary IV Test Organization V

Test Background Information VI Test Method Calculation Technique Test Activity Flow Chart Test Acceptance Criteria and Test Result Results of Type B & C Leak Rate Tescs Test Equipment VII Instr'anent Specifications Computer Program Instrument Error Analysis Conclusion VIII ILRT F1,ures IX RTD Locations X

Appendix A Deviations and Formulas for McGuire Containment Leak Rate Computations B Raw and Processed Data C Minute of Test Events (Test Log)

D Attachments to Test Log

-I-DEFINITION OF SYMBOLS AND ABBREVIATIONS ILRT Integrated Leak Rate Test E

Repeatability error e

Absolute error I

Measurement system error F

Temperature, degrees Fahrenheit FOM Figure of Merit L

Maximum allowable leakage rate A

L Containment leak rate during 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> ILRT (UCL) + Lg L

Imposed leak rate for verification O

L n a ame ea ra e ur ng ver f cation C

L Total measured leak rate during 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> ILRT OBSRVD L

95% Upper Confidence Valve of measured leak rate OBSRVD(95%)

of the containment vessel = UCL L

Leak rate of all penetrations, valves, flanges not UX exposed to ILRT test pressure LLRT Local leak rate test P

Pressure P

Design accident pressure psia Absolute pressure psig Gauge pressure R

Temperature, degrees Rankine SIT Structural integrity test T

Temperature T

Dew point temperature dp t

Time V

Containment volume, cubic feet

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II INTRODUCTION The purpose of this report is to provide adequate information so that an objec-tiva 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 confor-mance with the Appendix J of 10CFR50 and all associated ANSI, the absolute method end mass-plot technique which require monitoring the containment vessel tenpara-ture and pressure to determine the change in containment vessel air mass caused by leckage are used as the framework for selecting test equipment, developing test computer programs and test procedures.

The McGuire Unit 2 Containment System consists of a containment vessel and a ssparate reactor building enclosing an annulus.

The following containment vessel spzcifications are used as data base for the containment leak rate test.

- Containment Net Free Volume 1,239,759 ft3 (without ice)

- Design pressure 15 PSIG

- Calculated Peak Accident Pressure 14.8 PSIG

- Test Pressure 15.0 PSIG

- Test Temperature Ambient 52 Resistance Temperature Detectors, three (3) Dewpoint hygrometers and 3 pres-sure sensors are installed at predetermined locations in the containment vessal to datermine the weighted averages of containment vessel temperature, vapor pres-sure and pressure. The McGuire containment vessel leak rate test utilizes a fully cutomatic Data Acquisition System. All raw test data is scanned, printed and re-cordcd on Cassette tape automatically to minimize uncontrolled random errors.

Assigned engineers of Duke Power Company were responsible for draf ting and con-ducting the test. Three 8-hour shif t crews which consisted of one shif t coordina-tor and two technicians were utilized to maintain 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> test activity.

Pressurization for the McGuire Unit 2 ILRT was accomplished by a portable air conpressor/ dryer rented from Ingersol-Rand. The compressor / dryer was rated at 1800ICFM @ 125 PSIG. This compressor supplied air to the Upper and Lower Compart-n:nts only. The Ice Condenser Compartment was pressurized using station Instrument Air through a special -40 F dewpoint dryer. When the test was completed, the containment vessel was depressurized through the Ventilation Evacuation system in ths annulus.

Ihe release rate can be controlled if the air is contaiminated.

Section IX, Figures 2 and 3 show the pressurization and depressurization path used in this test.

III Test Purpose The purpose of the Preoperational Containment Integrated Leak Rate Test is to datarmine the leak rate of the containment vessel under controlled test condi-tions; to verify that there were no unidentified openings in the containment vessel due to incomplete construction; and to evaluate the possibility of ac-curetely measuring the containment leak rate in a shorter period of time.

Tha containment vessel was preconditioned to provide test conditions which satisfy the following:

- The vessel is under calculated accident pressure, 14.8 psig.

- Air temperature and pressure are stable to avoid biasing the leakage characteristics

- The contaimment vessel and all penetrations are lined up as close as 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 post-accident conditions and become an extension of the bound-ary of the containment shall be opened or vented to the containment atmosphere prior to and during the test.

The test utilized highly accurate sensors and an automatic data system te assure tha accuracy and quality of the test data.

Statistical and error propagation analysis are performed on the test data to en-sure that the test results are reliable and accurate.

IV Summary "THE CONTAINMENT VESSEL IN'rEGRATED LEAK RATE AND STRUCTURAL INTEGRITY TEST" was initiated on 9/23/82 and completed on 9/28/82.

It was conducted in compliance with tha McGuire 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 ac-captable upper limit of leakage of radioactive material is not exceeded under dssign accident basis.

The vessel was initially pressurized up to 16.970 PSIG for the Structural Integ-i rity Test.

Pressure was then reduced to 15.0 PSIG and the Integrated Leak Rate Test begun at 0245 (Run 1 ) on 9/26/82 af ter a > 4 hour4.62963e-5 days <br />0.00111 hours <br />6.613757e-6 weeks <br />1.522e-6 months <br /> stabilization period. The tsat result was evaluated acceptable at 1445 on 9/27/82 af ter a 36 hour4.166667e-4 days <br />0.01 hours <br />5.952381e-5 weeks <br />1.3698e-5 months <br /> test run.

At Run 143 computer printout indicated:

The containment vessel leak rate (observed)

= 0.0770901% per day The containment vessel leak rate upper limit (95% UCL) = 0.0876706% per day The containment vessel leak rate lower limit

= 0.0665096% per day Tha 95% upper confidence limit of the leakage rate was less than the acceptance criteria which is 0.15% per day.

Tha verification test to demonstrate the sensitivity and accuracy of test equip-mant started at Run 148 and attained acceptable measured value of 0.3496252% per day at Run 186.

Bassd on the low value of the measured leakage rate compared with the acceptance criteria and the analysis of aAl graphical data, the Containment Vessel leak rate test for McGuire Nuclear Station Unit 2 was declared successfully completed and tsrminated at 0130 on 9/28/82. This test was conducted per test proceddr-TP/.!/A/l:00/29, Containment Initial Integrated Leak Rate Test and Structural Intsgrity Test.

Problems were encountered with the ILRT computer af ter initiation of the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> test and were not cleared up until about 35 hours4.050926e-4 days <br />0.00972 hours <br />5.787037e-5 weeks <br />1.33175e-5 months <br /> later.

From this data we chose our 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> limits (Readings48-143). However, because of these problems and etne bsing essential, the leak rate was considered initial at Reading #1.

So our leak rate included leakage from Readings #1-47.

Later analysis showed that at an ini-tistion point at Reading #48, the leak rate could have been red : ed to L.026685%/

Day observed and L, (95%) to 0.0429875%/ Day. This would also affect the limits i

IV Pcg3 2 for the supplemental verification test equation. We would now have.0469402%/ Day

.05%/ Day; still within the acceptance criteria.

V TEST ORGANIZATION In order to assure that the test is conducted in a safe and efficient manner, as-signed personnel are organized as shown and their responsibility defined.

TEST

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INSTRUMENTATION TEST SUPPORT COORDINATOR GROUPS I

I ASSISTANT TEST COORDINATOR l

l SHIFT SHIFT SHIFT COORDINATOR COORDINATOR COORDINATOR DATA DATA DATA

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SPECIALIST SPECIALIST SPECIALIST DATA DATA DATA TAKER TAKER TAKER Test Coordinator: His lead responsibility is to provide overall planning and efficient execution of the test.

Aesistant Test Coordinator: His lead responsibility is to assume test coordinator responsibilities during his 12 hour1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> shif t.

Only Test and Assistant Test Coordina-tors are on 12 hour1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> shifts.

Instrument Coordinator: His responsibility is to provide test equipment maintenance support to Test Coordinator.

Test Support: Their responsibilities are to furnish technical support to Test Per-sonnel as required in conducting the ILRT, solving test problems, and minimizing schedule delays, Shift Coordinator: Assume general responsibility for ILRT execution on a shif t basis.

Data Specialist: His lead responsibility is to process and edit raw data.

Data Taker:

Record data accurately at correct intervals.

VI TLST 3ACT. GROUND INFOR'uTION TEST METHOD AND CALCULATION TECHNIQUE (DETAIL IN APPENDIX A)

TEST y.ETHOD,:

The absolute method of leakage rate testing is used for the McGuire This requires the determination and calculation of air losses by the test.

containment vessel leakage over a stated period cf time by the means of direct pressure, temperature and humidity observations during the period of the test.

Sensors are properly located to provide an average value of the containment vessel temperature and pressure.

The effect of the partial pressure of water vapor is measured and compensated.

e Upon completion of the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> leak rate test, a test is perfomed to verify the accuracy of the leak rate test.

This requires superimposing a controlled and measurable leak on the containment vessel and the composite leakage of both the containment vessel leaks and the superimposed leak is measured. The difference between the result of the leakage measurement obtained prior to the introduction of the superimposed leak and that of the composite leak determines the accuracy of the leak rate test.

The test enviroment is simulated as close to that of designed accident basis as possible.

All portions of the fluid systems that are postulated as opening directly to the containment or cutside atmosphere under post-accident conditions are openad or vented during the test except systems required to maintain the plant in saf e conditions during the test.

The test pressure is the calculated design basis accident pressure of 14.8 PSIG.

CALCULATICS TECHNIQUE:

Mass of the contair. ment vessel air volume is calculated by the Ideal Gas Law for 24 consecutive hours and plotted against time. The leak rete is obtained by a linear least square fit to the mass plot graph. The 95%

confidence upper limit 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 th2 acceptance criteria to determine the completion of the test.

TEST ACTI'lITY FLOW CHART:

Figure 1, Test Pressure versus Time Curve, provides an overall look of the test activities. This provides critical information for test planning and test execution.

i

VI Pzga 2 TEST ACCEPTANCE CRITERIA AND TEST RESULTS:

Acceptance Criteria 24 Hour Leak Test: The total Containment Vessel Leak Rate (Lg)

's than.75 L

Lg <.75 Lg where L =.20% of the Containment Vessel air mass per day.

A Now L

=L OBSRVD ('

}+b g

AUX where L OBSRVD (95%) Upper Confidence Value of measured leak rate of the containment vessel.

L

= Leak Rate of all penetrations, valves, flanges which cannot AUX be exposed to test pressure due to system operation.

Supplemental Verification Test: The difference between the supplemental verifica-tion and the total measured leak rate is within.25 LA (L

<.25 L

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C 0

OBSRVD A

where L = Total measured leak rate during supplemental test C

L = Imposed Known leakage O

L

=

a measured leak rate during 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> test OBSRVD Tant Results The following are results of McGuire Unit. 2 Preoperatianal ILRT completed on September 28, 1982:

24-Hour Test Results

.0770901 % per day L

=

OBSRVD L

OBSRVD(95%)

Now Ventilation Instrument Air penetration M-359 (2VI) was not exposed to ILRT test conditions because this penetration needed to be available to provide air to the inner seal of the Upper Personnel Air Lock Reactor Door for entry into the pressurized vessel if necessary. This was the only Thru Line Leak Class 2 penetration not exposed to test conditions.

It was, however, tested immediately af ter ILRT on 10/1/82 and the resuAting leakage was 0.00028% per day.

So L

=LOBSRVD(95%) + L g

and L

= 0.0876706%/ Day + 0.00028%/ Day g

L

= 0.0879506%/ Day

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VI Pags 3 Varification Test Results L = 0.3496252%/ Day C

L = 0.276%/ Day O

L

= 0.0770901%/ Day OBSRVD (0.3496252%/ Day - 0.276%/ Day) - 0.0770901%/ Day

<.05%/ Day 0034649%/ Day <.05%/ Day, well within the acceptance critaria.

NOTE: Some questions have been raised concerning inlet pressure measurements for the turbine flowmeter during the supplemental verification test.

See Appendix D Attachment #3.

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RESULTS OF TYPE B AND C LEAK RATE TESTS:

1 Test Final Conservative Test Results TP/2/A/1200/16, Isolation 1452.61 scen

-6 Velves Leak Rate Test

= 4.2199819 x 10 %/ Day TP/2/A/1200/15, Mechanical 1900.0 seem

~0 Psnstrations Leak Rate Test

= 3.4549135 x 10 %/ Day TP/2/A/1200/18, Upper Con-tsinment Personnel Air Lock Lcck Rate Test TP/2/A/1200/19, Lower Con-tainment Personnel Air Lock Lh k Rate Test TP/2/A/1200/17, Fuel Transfer 0.2 seem

-10 Tubs Leak Rate Test

= 5.8102063x 10

%/ Day TP/2/A/1200/20, Equipment 90.0 seem 7

Hatch Leak Rate Test

= 2.6145928x 10 %/ Day TP/2/A/1350/24, Electrical 3.974 seem Penstration 0-Ring Leak Rate

= 1.154488 x 10-8%/ Day Tent Formula Used for Conversion:

S

(%/D y) = 100% x where Sg = Measured leakage of TP in question (lbm/ Day) i m = Mass containment vessel at start of 24 hr. test.(lba).

y

(%/ Day) = 100% P

= 100 P Ty ; where P2 = Test pressure of B or C test (PSIA) 2 2 2 2 R T P V T 2 = Final leakage results (SCFM) 2 y 1 2 P V T = Temp of Vessel at start of 24 Hour Test y 1 y

R T

= 546.17 R 2

P = Pressure of Vessel at start of 24 Hr. Tes y

SCFM = SCCM x (3.5314667 x 10-5)

= 29.355 PSIA 3

V = Volume of Vessel = 1,239,759 ft 1

T = Use 80 F (540 R) as standard for B & C 2

test temperatures

• Thsze tests cannot be completed by due date of this report. When test is completed, results will be submitted to the Nr.C.

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VII Pggn 1 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 dewpoint sensors. All RTD's are wired to the remote scanner / multiplexer unit located inside containment.

Tha signals are then multiplexed and sent to the central data acquisition facility.

All other sensors are wired directly to the data acquisition facility located out-sids containment in a test van.

Instrument Specifications e

Precision Pressure Gauges are Ruska model 6000-801-40 PSIA gauges.

Range: 0 to 40 PSIA Repeatability - 24 Hr: i.0008 PSI; 90 Day: 1 0016 PSI Accuracy: + (.008% Full Scale +.012% Reading) or better, traceable to NBS Output: Direct digital output plus BCD parallel signal for recording.

Tha Dawpoint Temperature Analyzers are General Eastern system 1200 AP sensors with modal 700 aspirators.

Range:

-40 to +120 F Dewpoint Repeatability - 1 05 F Accuracy: 1 4 F dewpoint, tracable to NES Output: Direct digital readout plus 0-50 my signal recording The Resistance Temperature Detectors are Leeds & Northup Catalog number 178055 Range: -100 to +250 F Repeatability - 1 035% Span Accuracy: 1 07 F (32 F and 77 F) 0-120 F = 1 042 F 1 10 F ( ct 120 F)

Element:

Copper Resistance:

100 ohms at 77 F Section IX, Figure 6 shows placement of RTD while Section X, Table 1 gives their general locations.

The Turbine Flowmeter is a Flow Technology model FTC-8C5.0-GJS Flocapsule with model PRI-402A Flow Rate Monitor.

Range:

0.5 to 5 ACFM Repeatability - 1 25% FS Accuracy:

+0.2%, traceable to NBS.

1 0125 ACFM Output: Visual display plus 0-5 VDC signal for recording Tha 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:

- Numation Numeric Display

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Scanner / Programmer

a VII Pega 2 Digital Printer

- Digital Clock

- Cassette tape recorder Section IX, Figure 4 shows the test instrumentation set-up.

COMPUTER PROGRAM To provide on-line data analysis, a computer program is developed using formulas and methods specified in Appendix A.

The Leak Rate Test Program (LRT) reads in-strument readings from a magnetic tape cassette taken from the data recorder on ths Digital Data Surveillance Facility (DDSF).

The raw data from the tape are calibrated using quadratic curve fits. These calibrated data are then checked for validity. Using the mass plot analysis method, the calibrated verified data are j

processed to yield a normalized weight which is the ratio of the mass of air in tha containment at the present tbne to that which was initially present when the test began. Linear regression and confidence interval calculations are then parformed to determine whether the results have converged sufficiently to yield an accurate indication of the actual containment leak rate.

Using the terminal procedures detailed in the user documentation, the test ad-ministrator can run the program from any teletype-compatible terminal device having magnetic tape cassette capability. The program is desinged for inter-active processing so that at each step the user will be queried as to how he 4

wishss the work to be accomplished. Instrument parameters and readings can both entet into the computer system either automatically from cassette or atnually from the terminal keyboard. If any errors are detected in the data, than the user will have the option of correcting the specific error on the co:puter instead of re~ entering all of the data.

_ - + _

VII Pega 3 All data stored in the computer is protected by a password selected at the begin-ning 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 intru-sion 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 re-tcntion requirements of regulatory agencies. The archives can be placed on active storage at any time to verify calculations or generate reports.

• Instrument Error Analysis (Equations used in this section can be found in ANS N274, Draf t Revision 3, November 15, 1978)

Symbols:

FOM = Instrument figure of merit (%/ day) t = Test duration (hr.)

p = Test pressare (PSIA)

P

= Vapor presnure at test time (PSIA) y T = Cont. weighed average absolute test temp. ( F)

= Error associated with measurement of change e

E = Sensor erro.- (Sensitivity)

E = Measurement system error excluding sensor 1.

Pressure:

No. of sensor = 3 Range 0 - 40 PSIA Sensor Error (E ) = 10.008%FS = 0.0032 PSIA Measurement system rupeatability error (Ip) = 10.002%FS = 0.0008 PSIA (E ) + (E )

p p -

= 10.0019044 PSIA e

=1' No. of sensors 2.

Vapor Pressure:

No. of senser = 3 Range

-40 F to 120 F Sensor Error E = 10.40 F or 1 001268 PSIA

• Measurement System Error (I) = 10.05 F or 10001585 PSIA

• E (.001268,2

<,ooo13gs,2-

= 1 0007378 PSIA 8

e

=

py

VII PJgs 4

• At dewpoint of 36 F, the rate of vapor pressure change per 1 F is.00317 PSIA / F 3.

Temperature No. of Sensor = 52 Sensor Error = 1 042 F or 1 042 R Measurement System Error = 1. 15 F or

.15 R

_(.042 R)2 + (.15 R)2~

=

1 0216013 R e

3 T

52 4.

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1 0080566% per day This FOM value indicates that test instrument repeatabi.lity is adequate to provide a precision measurement of maximum allowable leak rate of 0.20%/ day.

Random errors on test results were analyzed under 95% confidence analysis and in-corporated into the test results for acceptance verification.

Tha test method also underwent a required accuracy test at the end of the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> ILRT.

It met the Acceptance Criteria (See test result).

1

UIII CONCLUSION With all conservative factors built in the test results analysis, the following conclusions were made on the McGuire Unit 2 ILRT:

1.

McGuire Unit 2 Containment Vessel is capable of saf ely Containing fission products under designed accident conditions.

2.

With a properly controlled test environment, test acceptance.:ould be attained much earlier than the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> minimum required time for a 24-hour test.

The supplemental test could be achieved in about 6.5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br />.

3.

No identified opening in the McGuire Unit 2 Containment vessel exist due to incomplete construction.

XX ILRT FIGURES

1) Pressure vs Time

2) Depressurization Path

3) Pressurization Path

4) Test Instrumentation System

5) Sectional View of Containment Vessel

6) RTD Locations i

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= s ae 2

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(

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HEMISPHERICAL DOME EL 894'+3" o

dg.7 u

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c EL 83Ef-9" o

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I3 80"

[ VERTICAL

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~ 0.7j TH'K

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~

EL. 72 3'+0' -

m A

N R

O.26TH'K-FLAT LINER PLATE

~

EL.69 4'+ 4's o

252"

=

Figure 5 Sectional View of Containment Vessel 1

Figure 6 RTD LOCATIONS 7

N ORTD 36 RTD370 RTD 4-35 t

OarD 38-42 RTD 4 3-4 7___

bTD32 RTD33O O

O

~

RTD RTD 11,12 10 gHumdity Sensor I

28-29 RTD 30-lumdity

ensor

\\

/

~~

\\

/

2 t

1 UO i

RTD 23-24 l

n

-DTD RTD 22,50 O-48-49

. JJ 52 OTD 14-15 RTD 16-A

' 7' ORTD 2's RTD 19 -20 OTD 18, 2 O

O RTD 26 y

-E 3

,8 T

RTD 2-3 Humdity Sensor b

.T ) 6-7 RTD 8-S 1

~

L J

RTD 1 i

I

X Pags 1 TABLE 1 RTD LOCATIONS LOWER CONTAINMENT (COMPARTMENT VOLUME FRACTION =.297)

RTD #

GENERAL LOCATION COMPARTMENT VOLUME FRACTIONS 1

Wall mounced in incore inst.

.0417 area 2

S.G. D lower support structure

.0566 el. 745' 3

S.G. A lower support structure

.0566 J

el. 745' 4

S.G. B lower support structure

.0566 el. 745' 5

S.G. C lower support structure

.0566 el. 745' 6

Wall mounted in tunnel area

.0297 7

Wall mounted in tunnel area

.0297 8

Wall mounced in tunnel area

.0297 9

Wall mounted in tunnel area

.0297 10 On top of S.G. 2D

.0378 11 On top of S.G. 2C

.0378 12 On top of S.G. 2B

.0378 13 On top of S.G. 2A

.0378 14 On top of RC pump 2D

.0377 15 On top of RC pump 2A

.0566 16 On top of RC pump 23

.0566 17 On top of RC pump 2C

.0377 18 In accumulator room 2D

.0117 19 In accumulator room 2C

.0099 20 In accumulator room 2B

.0112 21 In accumulator room 2A

.0112 22 Wall mounted in room with air

.0345 return fans 23 Mounced on ladder support in

.0438 reactor cavity

^7

^

Page 2 TABLE 1 (Cont.)

RTD #

GENERAL LOCATION CCMPARTMENT VOLUME FRACTIONS 24 Mounced on ladder support in

.0377 reactor internals storage area 25 Column mounted in incore

.0321 insertr.scation area 26 Column mounted near lower con-

.0406 tain==at vent.

Unit 2 D 27 Column mounted near lower con-

.0406 tainment vent.

Unit 2 B UPPER CONTAINMENT (COMPARTMENT VOL1)ME FRACTION =.541) e RTD #

GENERAL LOCATION COMPARTMENT VOLUME FRACTIONS 28 On concrete housing for S.G.

.0763 2D 29 On concrete housing for S.G.

.0763 2A 30 On concrete housing for S.G.

.0763 23 31 On concrete housing for S.C.

.0763 2C 32 on wall between S.G. 2.A & 2 D

.0847 33 On wall between S.G. 2 B & 2 C

.0847 34 On wall below crane track

.1356 el. 838' 35 On wall below crane track

.1356 el. 838' 36 On cont. spray piping 31'6" west

.1271 of center el. 875' t

37 On cont. spray piping 31'6" east

.1271 of center el. 875' i

ICE CONDENSER (COMPARTMENT VOLUME FRACTION =.162)

RTD #

GENERAL LOCATION COMPARTMENT VOLUME FRACTIONS 38-47 Evenly spaced around the upper

.0557 plenum area el. 835' 48-52 Evenly spaced around the lower

.0886 plenum area el. 773' l

t

h APPENDIX A DERIVATIONS AND FORMUI.AS FOR MCGUIRE CONTAINMENT LEAK RATE COMPUTATIONS This appendix presents derivations of formuiss used to develop McGuire leak rate computer program.

Pzgo 1

)

A.1 DEFINITION OF SYMBOLS P

Absolute pressure in the Containment Vessel (PSIA)

=

T Weighted average absolute temperature of the Containment

=

Vessel air compartment ( R)

W Normalized mass of containment vessel air at i data point

=

g (dimension less)

Pv = Partial pressure of water vapor (PSIA) time (min.)

t =

eh V

Assigned volume fraction of k sensor (Fraction of volume)

=

k Recorded temperature of k*

sensor ( R)

T

=

k W

Estimated value of W in the least square fit calculation

=

g b

Slope of the least square fit lina (fraction / min.)

=

OBSRVD[9h)

.'L L

OBSRVD easured conta h ent lea b ge rate M ay)

L

=

OBSRVD y intercept of the least square fit line (dimension less) a =

S

= the variance of W g

g S

= the variance of b b

A.2 SUBSCRIPTS upper containment compartment u =

L lower containment compartment

=

I Ice Condsnser compartment

=

v =

vapor 1

data point at start of test

=

1*

data point (i = 1 to N) i

=

N Final data point of a given set

=

keh,,,,,,

k

=

A.3 MASS PLOT CALCULATION AND STATISTICAL TREATMENT OF LEAK RATE 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. Normalization of W is applied by taking the g

ratio of the i value and that of the initial value.

l Pags 2 The values 0.541, 0.297, 0.162 are the assigned volume fraction for upper, lower, and Ice Compartment.

The average temperature T at each compartment is calculated as the sum of the volume weighed recorded temperatures.

IP-P Y I -P

/ -P P

P

+ 0.29 7

+.162 0.541(T /u L T )g (T )7 i

(p.\\1

[p,p 31 f p,, il 0.541

'}

+ 0.297'

+.162' (T /u (T )g (T )g T=Ekk k = 1 to 27 for lower compartment k = 28 to 37 for upper compartment k

• 39 to 52 fer ice condenser See attached Table 1 for volume fraction of each sensor.

Leakage Rate of the Containment Vessel The graph of W versus time is least square fitted to yield an g

estimated straight line. The rate of the containment vessel air mass losa (or the containment vessel leak rate) is the slope b of the least square fitted line W :

g, h = beg +a g

The value of a'and b can be determined by taking the first partial derivation of the sum of square of deviation Q (Q = I (W - W )2 with respect to a and b and minimize them:

1

\\

6' E (W - W )2 W = bc

+a g.

g _

=0 oa da W -h=W - bt

-a g

1 g

g 6 Z(W - W )2 1

= 2 I (W - bc - a) = 0 1

6a E (W - bt - a) = 0 g

g Na + bet = ZW (1) t g

Psgo 3 6 I(W -0) h = bc

+a 1

g db 6b W

h=W - bt

-a g

g a I(W - )

g

= 2E-t g(W -beg - a) = 0 6b 1

I-tfW - be - a) = 0 (2) g attg + bItg gg

= It W (3) with (1) and (3), a and b can be solved by matrix:

Na + (It ) b = IW (1) g g

(It ) a + (It ) b = It W (3) g gg N

IWg It It W nit W

--(IW ) (It )

g gg gg 1

g b=

(4) 2 N

It nit

-(It )2 g

g Itf2 It g IW It g It W It 2 IW It 2, gt gt y gg g

g (5) a=

=

2 (It )2 N

It nit g

g g

It It 2 g

L

= -b 144000% per day OBSRVD

(

• unless otherwise specified, all summation will be from i = 1 to i = N It is important to emphasize here that the slope b or leak rate is formulated on the following assumptions:

- the deviation of W from the true value are distrubuted according g

to the gas distribution function

- only the W contains random error, not the c g

e

P gs 4 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 evaluate the error effect on the test result. In order to choose a proper statiscical treatment, it is important to identify the

. charac: eristics of the observed data. In the previous derivation, it is found that L s the outce of the calculation OBSRVD from the observed temperature and pressure in the Containment i

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 frc2 the discrete measurement.

The latter requires discrete statistical treatment (X CH1 SQUARE), while the former requires continuous statistical treatment (The t test).

~

The t test, provides information which indicate how much the calculated leak rate deviated from the true value, and at what j

probability.

In other words:

L

= kBSRVD 1 " Deviation" (percent of probability)

For t test method " deviation" is defined as:

Deviation = c Sb

- 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). The value of t is on enclosed Table 2.

-S is the standard deviation of the variance of the containment b

air weight.

Equation (4) indicates that b = f(k' ) and by definition of variance:

S S

(5) b w

where S, is the variance of W :

g i

I

-e_-

.,,.. +,

l Pagn 5

• i)

(6) 2, ("i ~"~

w N-2 The (N-2) is chosen here instead of N because the least square line W is restricted by value of b and at The g

l freedom to evaluate the variance of W is reduced by 2 g

even N data is recorded:

(IWi)

(It )

NIc W 6

gg t

3E

~ (rE )

ob i

i 6W 6W 1et c = nit (In )

g g

nit W

-( g) (It))

6 g1 t

At.

6W 6W g

g 3E

~( i) ( *i) 1 6

ii c

6Wi

,,1_

Nt - It g

g h

Nt - It (7)

=

g g

1 Substitute (7) co (5)

S

,2,

I (Ne - It )

t i

b c

I (N e

- 2Nt Itg + (It ) )

g g

g c

(N It

- 2 nit Itg + N(It ) )

g g

g c

2 2

2 S

(N It

- N(It )')

(8) w g

t 2

Substitutec= hit 2, (7t{)2 to (8):

S Ns w

= She b

=

x m-

Paga 6 nit

- It 1

I 2, gt 2 1

It

=

N 2

SW 8

b 2

2 It

- It g

g N

The identity provides:

It

- E It E(e - E) = It

=

g g

g g

S S

S (9)

S

=

=

=

It

-It I(t -E)

It -E It g

1 y

g N

A.4 Summarization:

The following are the essential equations used in developing ILRT computer program:

0.541 f(P-P )N + 0.297 f (P-p [

+.162 f(P-P )'l 1 y)L II i T Ju i

T L T i

0.541 f(P-P )

+ 0.297 ' (P-P )

+.162 f(P-P )I y

y y/u

(

T /L

\\

T I

( T T = IT V kk 5 = btg+a nit W - (IW ) (It )

g 1

g b=

2

')

nit

- (Itg)'

g 2

IW (It )

(It ) (It W )

1 1

nit

- (Ic )

g y

-b

=

OBSRVD OBSRVD (95%) = L I

OBSRVD b

Pcgs 7 t value is on enclosed cable corresponding to f = N-2 and and 0.975 Z(W - a - be )2 S,2 1

g

=

N-2 S

S b"

It

-tit i

i 4

Page 8 TAar.a 2 Critical Values for Student's t-Distribution

• Pr{ Student's 7 6 tabled valuc} = 7 f

0.75 0.90

0. m.

0.975 0.99 0.995 1

1.0000 3.0777 6.3138 12.7062 31.4387 63.6574 2 0.8165 1.seS6 2.9308 4.3027 4.9644 9.9248 3

0.7649 1.6377 2.3534 3.1424 4.3407 S.8409 4 0.7407 1.3332 2.1318 2.77M 3.7469 4.4041 3

0.7267 1.4739 2.0130 2.3706 3.3649 4.0322 6 0.7176 1.4398 1.9432 2.4469 3.1427 3.7074 7 0.7111 1.4149 1.8944 2.3644 2.9900 3.4995 8

0.7064 1.3968 1.439S 2.3060 2.4MS 3.3334 9 0.7027 1.3830 1.1331

2. 3 22 2.8214 3.2498 to, 0.6998 1.3722 1.8125 2.2221 2.7638 3.M93

. If 0.6974 1.3634 1.7959 2.2010 2.7181 3.1058 12 0.6955 1.3562 1.7823 2.1788 2.M10 3.0345 13 0.6938 1.3302 1.7799 2.1406 2.6303 3.0123 14*.

0.6924 ~

1.3430 1.7613 2.1448 2.6245 2.9768 15 0.6912 1.3406 1.7531 2.131S 2.602S 2.9467 1[ 0.6901 1.3364 1.7459 2.n99 2.3833 2.9208 17 0.6492 1.3334 J 7396 2.10M 2.3669 2J982 la 0.6884

- 1.3304 2.7341

'2.1009 2.3324 2.8734 19 0.M76,

,t 3277*

.1.7291-2.0938 2.339S 2.8609 m

0.6s7o,

- 1.32S3 1.7247 2.osee.

2.32se 2.84S3 2.C7M '

2.3177 2.8314 21 0'.68$4' 2.3232 1.7387 1

22 0.68S4-

'.1.3212 1.7172.

2.0739 2.3083

2. alas 23 0.6453'

• 13195 9 1.~7139-

2.0687 2.4999 2.3073 34* 0.6848.

1.3178 1.7109 2.0639 2.4922 2.7969 25- 0.4844 1.3163 1.7081 2.0595 2.44n 2.7874 26 O.6840 1.3130 1.7056 2.0553 2.47a6 2.7787 27 0'.6837 1.3137 1.7033 2.0518 2.4727 2.7787

'.Ja.

0.6834 1.3125 1.7012 2.0684 2.4671 2.7633 29 0.6a30 1J114 1.6991 2.04S2 2.46 3

~2.7344 Jef 0.6828 1.3184 1.6973 2.0623 2.4573

- 2.7300 31 0.6425~

1.3095 1.6955 2.0395 2.4528 2.7440 32 0.6432 1.3006 1.4939 2.0369 2.4487 2.7385 33 0.6a K "10077 1 6936 2.0345 2.4444 2.7333 34 0.6418, 1.3070 1.6909 2.0322 2.44u 2.7234 33 0.6s14 1.3062 1.68M.

2.0301 2.4377 2.7238

~

36' O.6411 1.3055, 1.6883 2.0281 2.434S 2.7195 37 0.6815

-Es3069.

1.6871 2.0262 2.4314 2.7154 38 0.6410 1.3042 1.6860 2.0244 2.4286 2.71M 39 0.6408 1.3036 1.6849 2.0227 2.4258 2.7079 40 0.6807 1.3031 1.6439 2.t211 1.4233 2.7045 41 0.6405 1.3025 1.6829 2.0195 2.438.

2.7012 42 0.6a04 1.30 m 1.68 3 2.0181 2.4145 2.6901 43 C.6a02 1.3016 1.68H 2.0147 2.4163 2.6931 44 0.6a01 1.30n 1.6802 2.0154 2.4141 2.6923 45 0.6800 1.3006 1.6794 2.0141 2.4121 2.6aN

• D. B. Owen, NAS efsteristimf TaWer. AMi.aa., Wesley PubEshans Co.,1962. (Courtesy Atomic Energy N=: *8er., W m-==_. D.C.)

1 I

i l

1

i Page 9 i

l 1

TAsta2 (Continwd)

Pr(Student's 7 $ tabled value} = 7 1

0.7s 0.30 0.es 0.s7s 0.99 0.995 44 0.6799 1.3002

. 1.67s?

2.0129 2.4102 2.6s70 47 0.H97 1.299C 1.6779 1.01U 2.4083 2.64M 48 0.67M 1.2994 1.6772 2.0106 2.40M 2.6422 49 0.H95 1.2991 1.6766 2.00M 2.4049 2.5800 SS 0.67M 1.2987 1.6739 1.0006 2.4033 2.6778 S1 c.6793 1.2904 1.6733 2.0076 2.40U 2.6757 52 ' O.H92

,1.2900 1.6747

' 2.00M 2.4002 2.6737 "33'.T.679f.

.1.2977 IfG W 2.0037 2.3988.

2.6715 34 0.H91,

,L_2974 T.U36 2.0049 2.3974:

-2.6700 SS 6.67M'

.t.2971 1.6730 2.0060 2.3M1 2.6682 S6 Is.He9 1.2M9 1.H2S 2.0012 2.3948 2.664S 37 ;0.67s8 1.29M 1.6730 2.0023 2.3934 2.6M9 38 "O.HST, 1.2H3

,1.6716 2.0017 2.3934 1.6433 39 0.6787-1.2M1 1.H11 2.0010 2.3912 2.6418 48 30.H86 1.M.-

-hWOW 2.0003 2.3901 2.6403 61 t.6785 1.29M 1.6702 1.9996 2.3890 2.6589 1.9990 2.38e0 2.6575 62 3.6743 1.2954

1. Hee

~ 1.9983 2.3870 2.6561 0

0.H84 1.2951 1.HM M s.6733 1.2M9 1.H90 1.9977 2.3860 2.6549 63 0.6733 1.2947 1.H86 1.9971 2.3851 2.6536

, 64, 0.6782, 3.2MS 1.6683 1.9966 2.3442 2.6534 H

0.H82 1.2M3 -

1. M79

. 1.9960 2.3833 2.6312 es' O.6781 1.2M1 1.M76 1.9933 2.3834 2.6501 69 4.678L 1.2939 1.M72 1.9969 2.3816 /

2.6490 70* ~4:6788; 1.2938 1.6649 1.99M 2.3800 ~

2.6479 71 *0.670s 1.2936 1.M66 1.9939 2.3800 2.6449 72 ~0.6779 1.2934 1.H63 1.9935 2.3793.

2.6439

73. ;0.H79 1.2913 1.H60 1.9930 2.3785 2.6449 74 1.H78 1.2931 1.MS7 1.9925 2J778 2.6439 75 0.HFS 1.2929 1.MS4 1.9921 2.3771 2.6430 74 0.6777 1.2928 1.MS2 1.99U 2.3764 2.6421 77 0.6777 1.2936 1.6649 1.9913 2.3758 2.M12 78 0.6776 1.2925 1.M46 1.9908 2.3751 2.6403 79 0.6776 1.2924 1.6644 1.990$

2.3745 2.09S 30 0.6776 1.2922 1.H41 1.9901 2.3739 2.6387 81 0.6775 1.2921 1.M39

1. N97 2.3733

2. 079 at 0.6773 1.2920 1.6636 1.N93 2.3727 2.6371 83 0.6775 1.2914 -

1.M34 1.N90 2.3721 2.63M 84 0.U74 1.29U 1.6432 1.9884 2.3716 2.6356 SS 0.H74 1.2916 1.6430 1.Ns3 2.3718 2.6349 86 0.6774 1.2915 '

1.H28 1.M79 2.3705 2.6342 i

87 0.6773 1.2914 1.M26

1. N76 2.3700 2.6335 88 0.6773 1.2912 1.M24 1.M73 2.3695-2.6329 89 0.e173 1.2911 1.M12 1.N70 2.3690 2.6322 1

90 0.6772 1.2910 1.6420 1.9867 2.3645 2.6316 l

l l

Pzga 1 APPDTDIX B RAW AND PROCESSED DATA

-m

Page 2 TABLE OF CONTENTS Ssetion I - Leak Rate Determination:

0245 a.m.,

Sept. 26, to 1445 a.m.,

Sept. 27 A.

Mass Plot Analysis - 95% Confidence interval B.

Leak Rate Analysis - Deviation of observations from predictions C.

Normalized Air Weights - Containment and individual compartments D.

Weighted Compartment Averages - Individual compartments E.

Leak Rate Initialization - Compartment volume fractions and calibration curve coefficients for individual instruments F.

Raw Data from Instrument Readings G.

Calibrated Data from Instrument Readings H.

Calibrated Air Weights - Containment and individual compartments I.

Plots of Data Ssction II - Verification of Measured Leak Rate by Imposed Leak of.276% per day:

1600 Sept. 27 to 0130 Sept 28 A.

Mass Plot Analysis B.

Leak Rate Analysis C.

Normalized Air Weights D.

Weighted Compartment Averages E.

Instrument Histories F.

Leak Rate Initialia;ation G.

Calibrated Data from Instrument Readings H.

Trend Test I.

Calibrated Air Weights J.

Plots of Data K.

Raw Data

+

Faga 3 SECIION I

-m ms

-~

a.-

-~.

Prgo 4 p

p p

as a

s.

e a

e a

==

a a

m

.4 3

4 i

I ll iiii!l';

.i!l

!l ly l l 1i i

I i-i

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I i

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. __. RESs 4.T S__OF_f 0NT AINMENT__NASS_F1.OT ANAL _YSIS t %/ DAY )

8100 TIME HINIHtXI OBSERVED HAl(IlSJH IIO DAYsilR LEAK RATE I_EAK RATE LEAK RATE

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Data' 2 94._970 92.720 93.000 85.110 84.050 84.510 83.640 85.530 85.300 ab.800

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Data' 3 84.880 87.680 85.750 84.080 86.180 84.930 85.040 87.830 86.970 87.140 DAtW 4 87.890 86.900 87.090 86.630 86.370 86.290 86.260 30.860 35.530 30.520 DMe' 5 37.840 27.900 38.900 27.540 34.430 29.0"O 33.060 27.340 26.470 26.020 DAt#Li 27 730 26.329 2221020 236 290 239.800 244._450 249 i?O___22138[O 254,_920 256.860 t

s DAIF 7 29.336 29.32l 29.324

-2.410 42.130 48.270 0.013 0.012 O O_12 0.012 t_

79 READING AT 82269:2230 ImHK_1 76 050 83 290 83.440 83 250 83,170 84 290 85.470 8],280 85.970 94,299_

_____ _ [ ~5 s

t DMA: 2 04._i40 92 720 92.970 85.090 84.060 84 2LO 83.660 85.520 85.360 86.830

._ttANV 3 84.830 82.t00 85.770 84.070 86.200 84.920 85.020 87.840 86.910 87 120

_ DNC 4 87.960_,__86.960 87.040 86.6iO 86.330 86.260 86.230 3h440 37_.420 30.290 DAt#: 5 36.240 28.330 34.240 27.230 29.860 28.030 33.420 27.350 26.490 26.060 DAP4; 6 25.770 26.360 226.990 237.110 245.990 248.640 253.710 256.480 ?58.220 258.220 DAt#' 7 29.330 29.347 29.320

-2.350 41.970 48.310 0.013 0.083 0.012 0.012 80 READING AT 82269:2245

~

.. _ imp #' 1 76 8_!O Bh 260 OL450 83.330 83.130 84.760 85.450 82.290 85.960 94.730

__LiA__t#' 2 94.420 222670 9_2 960 85.080 84.010 84.450 83.650 85.540 85.370 86.740

_DN!L3 89:829 82,109 __95,480 84.060 86.190 84.930 84.990 87.840 86.910 87.130 DANK 4 87.990 86.960 87.050 86.570 86.320 86.240 86.220 31.270 31.670 30.180 DN#'5 35.190 20 000 31.180 26.870 28.460 27.610 32.670 27.370 26.480 26.040 2

ImtM: 6 25.750 26.3YO 215.350 228.060 232.710 237.430 239.870 241.460 247 190 251.520

_ DAtM 7 29.330 29,3j5 29_23_2O

-2,500 42 020 48.370 0,013 0 013 0.012 6 }[2 t

2 81 READING AT 82269:2300 DAtat t 76.840 83.350 83.440 83.370 83.130 84.760 85.390 82.200 85.950 94.710 C' _ __EZ DANI' 2 94.420 92 600 92.950 85.054 84.030 84.480 83.720 85.510 85.360 86.670 DANB: 3 84.810 82.710 85.730 84.120 86.160 84.800 84.990 87.840 86.940 87.050

't!

DN N' 4 88.600 86.980 87.050 R6.560 86.330 86.260 86.230 30.620 34.520 30.150

__ImtW 5 35,920 28.000 36.540 27.200 31.900 27.930 31.960 27.3?O 26.490 26.030

~~~~ ~~

DAP4' 6 25.800 26.390 257.280 253.200 258.200 258.t90 258.190 258.190 253.t90 258.I90 (D

BAlW 7 24.335 29.317 29.'321

-2.600 42.030 48.320 0.013 0.013 0.612 0.D32 y

C2 READINO AT 82269:2315 Tild F i~

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DAtr. 3 84.840 82.690 85.740 84.060 06.120 84.870 84.97ts 87.810 86.850 87.050 Data;.4.. 07.860 86.n70

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_ DAt#L2 61,270 82,340 86.230 83.890 86.050 84.710 84.880 87.700 86.770 86.980

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_ PM4L4 _ _ 2k,57Q 26,@99_221,300 242 630 254.810 258.520 258.520 258.520 258.520 258.520

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BAPG 5 38.200 29.600 38.640 27.200 35.750 29.490 13.05n 27.470 26.550 26.050

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.PN#_2 04,409_ _92 11R__HL 260 83,270 05 740 qqtup 8_St460 87_,15q 84,290 84.380

_ [*NAL4 9?.099 __p4,JOO 86,260 85.860 85.530 84.470

85. 360__._.3J. 450 33.7'O 30,540

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-1.630 40.890 48.300 0.011 O 010 0.010 0.010 IC6 FEAOING AT 82270s 1530 l*t4'.

I 76.500 02.670 82.730 82.690 82.580 84.230 85.530 81.830 85.340 93.650

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~ f*N#' 3 84.490 82.100 85.260 83.280 85.700 84.200 84.590 87.120 86.130 86.310

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_ DNe' 5 36.520 29_.190 32.750 27.2*O 28.740 28.110 32.500 27.650 26.690 26.110 Tot #: 6 26.200 26.680 144.030 156.840 161.530 167.170 173.460 176.740 181.410 186.520 D_Atr 7 29.285_._29.266 29.272

-1.680 4 f 316 46!570 0.080 0 664-- 6L664 6 36F-

_ Z Z f_;_ 4 147 F<EADINO AT 82270 1545

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_ POPE 4 97,920

_86.030 86.200 85.830 85.430 84.580 85.330 30.870 31.800 30.260

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t IIke' 5 34.990 28.470 30.300 26.810 27.630 27.470 32.620 27.600 26.690 26.120 L*WJ 26.219__2ft 662 2941222__2Li 329__212,390 221.260 22L b!9_ 222,Z?O 22?t779__2Mi7eo DAt*LI

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___________I n

REPORT SELEEiICNSs TtLveSS F1L9L_ANA(D{$

I

2) t EAl' RATE ANA.l,UJS

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6) INIT[AI12ATION DATA

7) RE Allit4GS s RAW AND CAI.IBRATED On DATA VERIFICATjON TREND TEST, COtFARE TEST

9) C AL.CUI.ATED AIR WEIGHTS IYGIENTER 5.E d C_T_1ON OR 2ERO

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(W8' 3 85.263 83.332 86.865 84.839 86.766 R5.65o 05.749 88.187 87.338 87.664 t

3 IWF 4 83.122 87.267 87.508 86.937 86.790 86.458 86.500 30.227 30.624 29.302 f We' 5 33.597 26.918 30.556 25.444 28.742 26.293 31.508 26.775 25.807 25.o77 f*APet 6 24.934 25.886 0.000 0.000 0.000 0.o00 o.000 0.000 o.000 0.000 IWW 7 29.362 29.34o 29.348

-1.890 37.720 45.300 0.000 o.000 0.00o 0.000

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I in REAllINo AT 82269: 500

~ 86.445 95.959

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PN#' I 76.700 84.o12 B4.o50 84.193 83.932 85.387 86.547 82.741 TWa' 2 95.287 93.o76 93.687 85.713 84.791 85.320 84.472 86.238 85.740 87.507 iWW 3 85.263 83.322 87.285 84.869 86.756 85.68o 85.830 88.167 87.378 87.734

- - - - ~ ~ -

5 rW4: 4 80.122 87.877 8T.508 86.947 B&~ Bio 84.978 es.soo 29.496 3E I38 29339 j

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. pet #' 2 95,267 92.266 93.797 85.703 84.751 85.330 84.442 86.296 es.750 87.40Z 1

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ewe' 1 76.740 83.792 83.950 83.902 83.742 85.237 86.057 82.601 86.345 95.958

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jW5' 2 953 57 ~ 95~.9Y5 93.636 85.55 84.558 85.I50 547 22 867078 85.700 87I257 DAP4: 3 85.153 83.181 86.895 84.579 86.666 85.450 85.709 88.057 87.220 87.583 8

DAf4: 4 88.212 87.227 87.468 86.877 86.790 85.658 86.470 29.877 32.630 29.653

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~ENe' 5 55.~554 25!U93 33.095 26.731 30.376 28.012 33.177 26.745 25.817 25.306 Emee' 6 25.273 25.826 0.000 0.000 0.000 0.000 0.000 0.000 0.000 0.000 l

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24 READING AT 82269: 845 EW #: 1 76.750 83.792 83.940 83.922 83.732 85.227 85.827 82.601 86.345 95.Yl8

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Data: 2 95.137 92.986 93.626 85.532 84351 85.160 84 513 86.166 85 710 B7 M7

- ~ ~ - ~ ~ - - ~ -

~'5ANK 3 85.143 83.171 86.665 84.599 86.656 85.440 85.619 88.007 87.220 87.623

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82 READINo AT 82269:2315

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94 READING AT 82270s_215 1

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APPENDIX C MINUIES OF MAJOR TEST EVENTS

APPENDIX C MINUTES OF MAJOR TEST EVENTS DATE/ TIME COMMENTS 8/26/82 0940 Began Visual Inspection of Containment Vessel and Reactor Build-ing as required by procedure to identify discrepancies which must be cleared up before ILRT. 9/21/82 1340 Connected rented air compressor from Ir.gersoll-Rand to Instrument Air connection. Started ccupressor and field, checked for proper operation. All discrepencies stated in log item 8/26/82 have been cleared. All test instrumentation installed and verified to be in proper working order. Personnel airlocks not completed per their test procedure. However, air locks were unofficially leak-tested to ensure a leak tight barrier for the ILRT. Airlocks will be tested af ter ILRT. 9/23/82 1550 Verified flow paths for pressurization. Made announcement for all personnel to evacuate Containment Vessel. Began pressuriza-tion of Containment Vessel. 9/24/82 1415 Reached 10 PSIG Plateau. Stopped pressurization for vessel in-spection to determine any damage occuring and remove any pres-surized vessels not removed earlier. Ice Condenser AEU's changed to defrost 30 minutes every 3 hours. 9/25/82 0701 Reached Structural Integrity Test pressure (16.97 PSIG) and stop-ped pressurization. 9/25/82 0715 Began depressurizing to test pressure through unit vent. 9/25/82 1130 Stoppad depressurization at approximately 15.1 PSIG. Inspection team entered vessel for another look before beginning 24 hour test. Decided to take exception to penetration M-359 (Air to Upper Reactor Door inn'er seal) in case another entrance was required into vessel. 9/25/82 1959 Discovered problem with computer program. Program does not seem to be using calibrated curves of RTD's. Problem appears to be wrong formulated calibration data. Data is being reformulated for input. 9/25/82 2230 Temperature stabilized. Declared 24 hour ILRT underway. 9/26/82 0720 Dew Point hygrometers began fluctuating. Investigation revealed hygrometers had to be switched to calibrate position which simply heated up aspirator to remove moisture or ice. After this, all aspirator / hygrometers functioned properly. Decided to determine if Ice Condenser dewpoint hygrometer was right by calculations. It showed a negative dewpoint. (See attachment #1 to test log.)

Page 2 DATE/ TIME COMMENTS 9/27/82 0100 All instrumentation and computer program working properly. Continuing with test. 9/27/82 1445 24 hour ILRT declared successful. 9/27/82 1600 Begin supplemental verification test. 9/27/82 1159 Imposed leak rate not corresponding with calculated rate. Investigation reveals problem with the pressure the Turbine Flowmeter sees. Problem cleared up. (See attachments #2 and 3 to test log). 9/28/82 0230 Declared supplemental verification test successful. 9/28/82 C300 Began depressurization through pressure relief valve. 9/29/82 0800 Pressure down to 0.0 PSIG. Entry into containment vessel revealed nothing distorted or abnormal.

I F e APPENDIX D ATTACIDiENTS TO TEST LOG I

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ATTACHMENT #3 October 12, 1982 Memorandum For File

Subject:

McGuire Unit 2 Imposed Leakage Flow Turbine Inlet Pressure Measurement Device At the end of the McGuire Unit 2 ILRT Imposed Leakage Verification it was noted that the leak rate was greater than expected. After examining the turbine flow-meter apperatus it was realized that the valve used to throttle was located downstream from the flow-meter. Since the throttle valve was downstream of the flow-meter air pressure passing through was grerter than atmospheric, this meant the mass of air flowing from containment ',as greater than originally assumed. r The problem was to measure the turbine flow-meter inlet pressure without disturbing the flow. The flow meter was coupled to a rubber hose which was coupled to the imposed leakage path. A device consisting of a hypodermic needle coupled with a piece of tygon hose and a brass fitting was rigged tc:; ether, all -joints were superglued and securely clamped. This device was used in series with a calibrated 0-20 psig test gauge. 1 The hypodermic needle was used to perpendicularly penetrate the rubber hose. After the needle was inserted, all joints were soap bubble tested for leaks, none were detected. The test gauge achieved a pressure of 4.9 psig in approximately 3 seconds. The flow path at the outlet of the ' throttle valve was momentarily blocked, pressure increased rapidly, air was then released and the test gauge returned and maintained 4.9 psig. This demonstrated the repeatability of the device. After the ILRT was complete tae imposed leakage turbine flow meter was brought up to the test shop. A static pressure tap was placed in the turbine flow meter spool piece and a cross calibration was perfonned to demonstrate the validity of the use of the hypodennic needle. The hypodermic device had an excellent corresp)ondence with the static pressure tap. (Refer to data sheet and Figure 1. Also the question was raised about the 10 psig pressure drop from containment to the inlet of the turbine flow meter. Figure 2 depicts the imposed leakage flow path. Large flow restrictions occur at 2WL-370, 2WL-387, 2WL-371 (needle valve).and.at the flange connection to the rubber hose. call of ^these restrictions account for the 10 psig drop. [ A W. M. Suslick Jr. Engineer l WM/tw i Attachment cc: W. A. Haller B. H. Hamilton, MNS J. E. Cole W R. Sipe, MNS J. E. Snyder G. A. Copp M. D. McIntosh,1.00 MNS 1 j File: MC-180.25, 27 - L

II.RT Imposed Leakage Turbine Flow Meter Inlet Pressure Verification Flow Static Pressure Tap (1) Hypodermic Needle (2) Instrument Air (3) (%) (psig) (psig) (psig) 80 2.7 2.7 28 71 4.9 4.9 28 60 7.7 7.7 28 50 11.0 11.0 28 40 14.7 14.7 28 70 1.1 1.2 20 60 3.3 3.4 20 50 6.0 6.0 20 40 9.1 9.0 20 80 5.5 5.5 35 70 8.0 8.0 35 60 11.1 11.1 35 50 14.7 14.7 35 1 Instrument # MCPRF 26020 0-20 psig Heise Gauge 2 Instrument # MCPRF 26089 0-20 psig Heise Gauge 3 Process Gauge Recorded by: 8,!:/'I Date: 9/29/82 -m_.- - mm

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