ML19257A911
ML19257A911 | |
Person / Time | |
---|---|
Site: | McGuire |
Issue date: | 01/03/1980 |
From: | DUKE POWER CO. |
To: | |
Shared Package | |
ML19257A908 | List: |
References | |
NUDOCS 8001090377 | |
Download: ML19257A911 (200) | |
Text
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1708 045
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MCGUIRE NUCLEAR STATION UNIT 1 REACTOR CONTAINMENT BUILDING INTEGRATED LEAY RATE TEST t
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1708 046
s TABLE OF CONTENTS Page TABLE OF CONTENTS i LIST OF ILLUSTRATIONS ii INTRODUCTION
SUMMARY
I INTRODUCTION 1 TEST PURPOSE 2 TEST ORGANIZATION 3 TEST BACKGROUND INF0kMATION 4 TEST EQUIPMENT 8 DATA ANALYSIS AND INTERPRETATION 13 CONCLUSION 14 APPENDICES A Derivations and Formulas for McGuire Leak Rate Computations B Raw and Processed Data of the Test C Minutes of Test Events (Test Log)
D Test Procedure (Copy)
E Isolation Valves Leak Test Summary i
1708 047
LIST OF ILLUSTRATIONS Figure 1 Test Activity Flow Chart -
Figure 2 Containment Building Volume Boundaries Figure 3 Containment Building Volume Boundaries Figure 4 Containment Shell Layout Figure $ Test Instrumentation System Figure 6 RTD's Location Figure 7 RTD's Location Figure 8 RTD's Location Figure 9 RTD's Location Figure 10 RTD's Location Figure 11 Pressurir,ation System Figure 12 Containment Compartment Average Temperature Figure 13 Containment Compartment Average Pressure Figure 14 Containmer. Compartment Vapor Pressure Figure 15 Containme 2t Normalized Air Weight ii 1708 048
LNTRODUCTION
SUMMARY
The purpose of this report is to provide appropriate personnel adequate data for an independent review of the McGuire Unit I containment leak rate pre-operational test. The Containment Vessel Integrated Leak Rate Test and Structural Integrity Test were started on August 14, 1979 and completed on August 23, 1979. These tests were conducted in accordance with the provisions of Appendix J to 10CFR50 to assure that an acceptable upper limit of leakage is not exceeded under design basis accident conditions.
Assigned engineers from McGuire Nuclear Station were responsible for develop-ing the test procedure and conducting the test. Three 8-hour shift crews which consist of one test supervisor and four technicians were utilized to maintain 24-hour test activity.
In conformance with the requirements of Appendix J to 10CRF50 and appropriate ANSI standards, the absolute method and mass plot techniques were used as the framework for selecting test equipment and developing test computer programs and test procedures. These require monitoring the containment vessel temperature and pressure to determine the change in containment vessel air mass caused by leakage.
The McGuire 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 data base for the containment leak rate test.
- Containment Net Free Volume 1,239,467 ft 3
- Design Pressure 15 psig
- Calculated Peak Accident Pressure 14.8 psig
- Test Pressure 14.8 psig
- Test Temperature Ambient Fifty-two Resistance Temperature Detectors, three dewpoint hygrometers and three pressure sensors are installed at predetermined locations in the contain-ment vessel to determine the weighted averages of containment vessel tempera-ture, vapor pressure and pressure. In addition to the above sensors, the McGuire containment vessel leak rate test is the first test conducted by Duke to utilize a fully automatic Data Acquisition System. All raw test data are scanned, printed and recorded on cassette tape automatically to minimize uncontrolled random errors.
The vessel was initially pressurized to 16.875 PSIG for the Structural Integrity Test. Pressure was then reduced to 14.8 PSIG and the Integrated Leak Rate Test begun et 0705 on August 21, 1979 after a 4-hour stabilization perioo. The test result was evaluated as acceptable at 0705 on August 22 1979 after a 24-hour test run. At Run 174 computer printout indicated:
The containment vessel leak rate = 0.1070897% per day The containment vessel leak upper limit = 0.11365.96% per day The containment vessel leak lower limit = 0.1005199% per day The upper 95% confidence limit of the leakage rate was less than the acceptance criteria which is 0.15% per day.
I 1708 049
The value of 0.1144983% per day, which would be acceptable compared with the acceptance criteria value, was achieved at Run 121, 11 hours1.273148e-4 days <br />0.00306 hours <br />1.818783e-5 weeks <br />4.1855e-6 months <br /> after initiation.
However, the test was continued to Run 174 to satisfy the requirement of 24-hour test duration which is incorporated to assure the complete stabiliza-tion of the measured result leakage rate. The verification test to demonstrate the sensitivity and accuracy of test equipment started at Run ISS and attained acceptable measured value of 0.2824652% per day at Run 230.
Based on the low value of the measured leakage rate compared with the accep-tance criteria and the analysis of all graphical data, the Containment Vessel leak rate test for McGuire Nuclear Station Unit I was delcared successfully completed and terminated at 2105 on August 23, 1979.
" 1708 050
INTRODUCTION The purpose of this report is to provide adequate information so that an objective review of the test can be performed. In this report, the test purpose and test organization are presented, followed by sections concerning test background information, test equipment, data analysis and test conclu-sion. Appendices are also included to provide details of computer programs, calculation method, instrument locations, and other related information.
d 1 1708 051
TEST PURPOSE The purpose of the Containment Integrated Leak Rate Test is to determine the leak rate of the containment vessel under controlled test conditions.
The following test conditions were established in the containment vessel prior to conduction of the test:
- The vessel is under calculated peak accident pressure, 14.8 psig.
- Air temperature and pressure are stable to avoid biasing the leakage characteristics.
- The containment vessel and all penetrations are lined up as close as possible t the expected post-accident condi-tion; i.e., those port.ans 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 boundary of the containment are opened or vented to the containment atmosphere prior to and during the test.
The test utilized highly accurate sensors and an automatic data system to assure the accuracy and quality of the test data.
Statistical and error propagation analysis are performed on the test data to ensure that the test results are reliable and accurate.
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TEST ORGANIZATION Organization In order to assure that the test is conducted in a safe, timely, and accurate manner, assigned personnel are organized as shown below and their responsi-bility clearly defined.
Test , Test Coordinator Support A V _
Test Test Test Supervisor Supervisor Supervisor 4 Technicians 4 Technicians 4 Technicians Responsibility Test Coordinator: His lead responsibility is to assure the test is performed in a safe, timely and accurate manner.
Test Supervisor: His lead responsibility is to help the test coordinator conduct the test in his assigned shift. His duties include supervising 4 technicians in gathering, processing, analyzing data and solving any related problems arising during his assigned shift.
Data Taker: His duties are to operate the Data Acquisition System, to process data and generate computer printout, and to perform data plotting.
Instrumentation Maintenance Technician: His responsibility is to provide on-line test equipment maintenance support to the Test Supervisor.
Support Groups: Their responsibilities are to provide general support to the Test Coordinator upon request.
3 1708 053
TEST BACKGROUND INFORMATION Test Method and Calculation Technique (Detail in Appendix A)
Test Method .
The absolute method of leakage rate testing is used for the McGuire test This requires the determination and calculation of air losses from the cc c. sin-ment vessel over a stated period of 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 la measured and compensated.
Upon completion of the main leak rate test, a test is performed 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 deter-mines the accuracy of the leak rate test.
The test environment is simulated as close as possible to that of the design basis accident. All portions of the fluid systems that would be open directly to the containment or outside atmosphere under post-accident conditions are opened or vented during the test, except systems required to n.aintain the plant in safe conditions during the test.
A test pressure is the calculated peak accident pressure of 14.8 psig.
Calculation Technique Mass of the containment vessel air volume is eticulated by the Ideal Gas Law for 24 consecutive hours and plotted against time. The leak rate is obtained by a linear least square fit to the mass plot graph. The 95% confidence upper limit of the leak rate is arrived 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.
Test Activity 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.
Contaianent Specifications - Containment Description Concrete Containment -
The concrete containment (Reactor Building) is a reinforced concrete structure composed of a right cylinder with a shallow dome and flat circular foundation
, 1708 054
slab. The Reactor Building houses the Containment Vessel and is designed to provide a biological shielding as well as missile protection for a steel containment shell.
A five foot annular space is provided between the Contaiunent Vessel and Reactor Building shell for control of Containment external temperatures and pressures. The annular space also provides a controlled air volume for filtering and access to penetrations for testing and inspection.
The Reactor Building has a cylinder radius of 62 ft. 6 in., a thickness of 3 f t. O in. and a do.ne thickness of 2 f t. 3 in. The height of the Reactor Building is approximately 177 feet. The structural outline of the Reactor Building is sho;.n on Figure 2 and Figure 3.
Steel Containment The Containment Vessel is a freestanding weldM steel structure with a vertical cylinder, hemispherical dome and a flat base. The Containment shell is anchored to the Reactor Building foundation by means of anchor bolts around the circumference of the cylinder base. The base of the Containment is 1/4 in.
linear plate encased in concrete atd anchored to the Reactor Building founda-tion. The base liner plant functiota only as a leak-tight membrane and is not designed for structural capabilities. The Containment Vessel has a diameter of 115 ft. and overall height of 171 ft. 3 in. Other details are shown in Figure 3.
The Containment Vessel is designed to assure that an acceptable upper limit of leakage of radioactive material is not be exceeded under design basis accident conditions.
The Containment Vessel utilizes the ice condenser concept for energy absorp-tion during a loss-of-coolant accidenc. The rapid energy absorption capability maintains the Containment Vessel design pressure at a low level as well as reducing the peak duration.
The use of the ice condenser requires that the Containment Vessel is divided into three major volumes. The lower volume houses the Reactor Coolant System, the intermediate volume houses the ice condenser energy absorption system, and the upper volume contains the air after passing from the lower volume through the ice condenser. This three compartment concept is used to locate ILRT test sensors and localize test calculations.
Containment Vessel Specifications The following are the containment vessel specifications which are used as a data base for the leak rate test program:
Containment Vessel Net Free Volume = 1239467 ft 3 Design Pressure = 15 psig .
Calculated Peak Accident Pressure = 14.8 psig 1708 055 5
Test Acceptance Criteria and Test Result Acceptance Criteria ILRT: 95% confidence value of the measured leak rate L 0.15 percent by weight of the containment volume per day"(95%) does not exceed (L,,(95%) $ .15% per day)
Supplemental Verification Test: The difference between the supplemental test result (L T) and the measured leak rate (L ) is within .25 L *where L *= .20%.
(.15% per day 5 LT ~b am $ .25% per day) **
L,, = Measured leak rate of the Containment Vessel L**(95%)
= 95% upper confidence value of the measured 1eak rate of the Containment Vessel L = Measured leak rate of the Containment after T
a known leak L, was imposed L, = Max allowable leak rate = .20% per day In the preoperational test, the Containment Vessel is strength-tested at 112.5%
of the design pressure (15 psig). The Acceptance Criteria requires that no physical deformation exists on the Containment Vessel under test pressure.
Test Result The following are results of McGuire Unit 1 ILRT test which was performed on August 21, 1978.
24-Hour Test Result:
L,, = 0.10708% per day L ,(95%) = 0.11565% per day Verificatian Test Result:
L - L,, = (0.2824652 - 0.1070897) - 0.17538% per day These results are well within the Test Acceptance Criteria.
Local Leak Test Results of Penetrations Which Were Not Exposed to ILRT Test Pressure Due to Operational and Technical Problems Before and during the course of McGuire Unit 1 ILRT Test, the following pene-trations were not exposed to the ILRT Test pressure:
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Penetrations Reason IM240 (1RV) Need cooling water IM390 (IRV) for air conditioner IM385 (IRV) to operate Operator IM279 (IRV) Aid Computer -
M279 (INF) Glycol line to operate M373 (INF) ice condenser M372 (INF) AHU M216 (INC) Mistake in valve line up M355 (IKC) Mistake in valve line up Upper and Lower Air locks were not in Personnel Air Lock normal operation condition Local leak tests were performed after the ILRT as per McGuire Unit 1 TP/1/A/1200/16, Isolation Valve Preoperational Leak Test and results were as follows:
Penetrations Results (1/ Day)
~
IM240 (IRV) E.642 x 10 ?~
IM390 (IRV) 2.922 x 10 ?-
1M385 (IRV) 1.276 x 10 ?
IM279 (RV) 4.527 x 10 ?-
IM373 (INF) 4.733 x 10 ?
1M372 (INF) 6.585 x 10 ?
1M216 (INC) 4.115 x 109 M355 (1KC) 4.115 x 109 Upper and Lower Note 1 Personnel Air Lock Note 1: Due to pending modification work, air locks were not available for testing. Test will be performed in January 1980 and follow-up report will be submitted.
1708 057 7
TEST EQUIPMEFT Test Instrumentation In order to provide adequate and accurate data for the containment vessel leak rate determination, the following instrumentations are utilized:
Temperature Measurement 52 Leed and Northrup Resistance Temperature Detectors are used and distributed as follows:
- Upper containment: 10
- Lower containment: 27
- Ice condenser: 15 Each RTD has the following specifications:
Operating range 32 F to 250 F Accuracy t.07F (32 to 95 F) 1.14F (0 to 150 F) 0.5F (-100 to +250)
Element Copper Resistance 100 0 to 77 F Repeatability 0.042 F (0 to 120 F)
Pressure Measurement Three high precision Ruska pressure gauges are used and distributed as follows:
- Upper containment: 1
- Lower containment: 1
- Ice condenser: 1 Each has the following specifications:
Range 0 to 40 psia Accuracy (.006% full scale + .012% reading)
Repeatability (24 hr.) 1.008 psi _
Repeatability (90 days) 1.006 psi 1708 058 8
Dew Point Measurement Three General Easter Dew Point Hydrometers are used and distributed as follows:
- Upper containment: 1
- Lower containment: 1
- Ice condenser: 1 Each of the following specifications:
Range -40F to 80 F Accuracy 0.4 F (from 6 F to 200 F)
Repeatability 0.05 F Turbine Flow Meter One Flow Technology Turbine flow meter is used to set the imposed leak. It has the following specifications:
Range 0.5 SCFM to 5 SCFM Accuracy 10.2%
Repeatability 1.0125 SCFM Repeatability 0.25% FS Data Acquisition System (DAS)
The Leed and Northrup Data Acquisition System is used to multiplex, scan, program, print and record all signals from seasors. The DAS consists of the following:
- Numatron numeric display
- Scanner / Programmer
- Digital printer
- Digital clock
- Cassette tape recorder Figure 5 represents the system concept of the Test Instrumentation. Care has been taken to minimize the number of penetrations needed to set up the system by placing the scanner inside the containment vessel. .
Figures 6 through 10 provide locations of each sensor as they are installed in the Containment Vessel.
, 1708 059
Pressurization and Depressurization System The station instrument air system is used to pressurize the containment vessel. This system (Figure 11) consists of three air compressors and an arrangement of air coolers, dryers, and filters to provide 1500 SCFM of 35 F dewpoint to the containment vessel and -40 F dewpoint air to the Ice Condenser.
Connections are provided for the addition of temporary compressors into the system. The station air system is also used as a backup system if necessary.
Once the test is completed, the containment vessel is depressurized using the hydrogen purge penetrations. The release rate can be controlled if the air is contaminated. Air is released to the atmosphere through the contain-ment annulus.
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 instrument readings from a magnetic tape cassette taken from the data recorder on the Digital Data Surveillance Facility (DDSF). The raw data from the tape is calibrated using quadratic curve fits. This calibrated data is then checked for validity. Using the mass plot analysis method the calibrated, verified data is procecced to yield a normalized weight which is the ratio of the mass of air in the contain-ment at the present time to that which was initially present when the test began. Linear regression and confidence interval calculations are then per-formed to determine whether the results have converged sufficiently to yield an acceptance rate of leakage from the containment.
Using the terminal procedures detailed in the user documentation, the test administrator can run the program from any teletype-compatible terminal device having magnetic tape cassette capability. The program is designed for inter-active processing so that at each step the user will be queried as to how he wishes the work to be accomplished. Instrument parameters and readings can both enter into the computer system either automatically from cassette or manually from the terminal keyboard. If any errors are detected in the data, then 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 inter-mediate results to the final results, will be copied to an archival storage medium to satisfy long-term retention requirements. The archives can be placed on active storage at any time to verify calculations or generate reports.
to 1708 060
Printed reports available through the program are classified as either interim or final. Interim reports reflect the calculations for the current time period or periods and are intended to keep the test administrator abreast of the current status of the test. Final reports are relatively voluminous and are intended for high-speed terminal output using faster line printers. Final reports are intended for inclusion in the Integrated Leak Rate Test Summary issued by the test engineer. .,
Instrument Error Analysis (Equations used in this section can be found in ANS N274, Draft Revision 3, November 15, 1978.)
Symbols:
FOM = Instrument figure of merit (%/ day) t = Test duration (hr.)
p = Test pressure (psia)
Py = Vapor pressure at test time (psia)
T = Cont. weighed average absolute test temp. ( F) e = Error associated with measurement of change I = Sensor error (sensitivity)
- 1. Pressure:
No. of sensors = 3 Range 0 - 39.999 psia Sensor Error (E p) = i0.002%FS = .000799 psia
_ _ g (E )2 + (y )2 e =1 - E E - = .0004613 psia P 3 ',
- 2. Vapor Pressure:
No. of sensor = 3 Range -40 F to 80 F 11 1708 061
Sensor Error E = 0.35 F or .002597 psia
- Measurement System Error (I) = 10.05 F or .00371 psia *
,PV=[(.00297)2+ h
(,oo371)g .002744\ psia -
3
- 3. Temperature:
No. of sensor = 52 Sensor Error = t.042 F or t.042 R Measurement System Error = t108 F or .108 R h
. k.042R)2+ (.108 R)$ = .0160696 R
,T -
b 52
- 4. FOM (Figure of Merit):
2400 PV b FOM = 2 +2 ,
b
= ,2400 .0160696Y 24 2[.0004613Y+2[\29.5/.002744Y+2[\5
( 29.5 /
= 1.00139% per day This FOM value indicates that test instrument repeatability 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 incorporated into the test results for acceptance verification.
Test instruments also underwent a required accuracy test at the end of 24 hr.
ILRT. These instruments met their acceptance criteria (see test result). ,
- At dewpoint of 53 F, the rate of vapor pressure change per 1"F is
.00742 psia / F.
12 1708 062
DATA ANALYSIS AND INTERPRETATION One of the most critical factors which determines whether the measured leak rate reflects the leak characteristics of the building is the test environ-ment. It must be controlled in such a way that test data are not biased to indicate anything other than the leak rate of the building. By virtue of the test method which utilizes temperature and pressure change as an indica-tion of leakage, anything other than leakage that causes these parameters to change must be eliminated or neutralized. The following factors that can bias the data are identified:
- 1. Temperature and Pressure Unstabilization:
McGuire Unit 1 ILRT underwent a long period of holding to ensure that temperature was stabilized. Temperature / pressure were plotted every 15' as per Figures 12, 13, and 14. The graph indicated that temperature varied less than .5 F/hr. and pressure fluctuated less than .01 psig/hr.
This ensured that these parameters did not bias the test data.
- 2. Air Source Leaking into the Building During the Test:
Care had been taken to isolate and vent all air penetrations that pene-trate the building before and during the course of the test. (See Test Major Event in Appendix D).
- 3. Leak Rate Trend:
Even though the test result is verified against a required acceptance criteria, it is recognized that the test can not be considered " pass" at the first moment its result meets the acceptance criteria. It is understood that if the Containment Building leaks, its rate will be constant. So the trend of the leak rate is monitored to determine the appropriate " pass" time.
McGuire Unit 1 data (see Appendix C) indicated that the leak rate began to stabliize at reading number 121, 11 hours1.273148e-4 days <br />0.00306 hours <br />1.818783e-5 weeks <br />4.1855e-6 months <br /> after starting time.
The test was continued to meet the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> required minimum time and ended at reading number 174.
The leak rate was 0.11366% per day.
The same trend was observed for the imposed leak rate (Verification Test) test. The leak rate began to stabilize at reading No. 206, 5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> after starting time. The fic'1 leak rate was L = 0.2825%/
T day (Acceptance Criteria: .15%/ day $ ;y - 0.1071%/ day 5 25%/ day. The test ended at reading number 230, 11 flours after starting time at the request of an NRC Inspector. ,
13 1708 063
CONCLUSION With all conservative factors built in the test result analysis, the following conclusions were made on the McGuire Unit 1 ILRT:
~
- 1. McGuire 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 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 less than 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br />.
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APPENDIX A DERIVATIONS AND FORMULAS FOR MCGUIRE CONTAINMENT LEAK RATE COMPUTATIONS This appendix presents derivations of formulas used to develop McGuire leak rate computer program. O e e 1708 080
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_,h data point (dimension less) ',, P = Partial pressure of water vapor (PSIA) t = time (min.) th V k
= Assigned volume fraction of k sensor (Fraction of volume)
T k
= Recorded temperature of k sensor ( R) h1= Estimated value of W in the least square fit calculation b = Slope of the least square fit line (fraction / min.)
L (95%) = 95% confidence value of L , L = Measured containment leakage rate (%/ day) a = y intercept of the least square fit line (dimension less) S y = the variance of W S = the variance of b b A.2 SUBSCRIPTS u = upper containment compartment L = lower containment compartment I = Ice Condenser compartment V = vapor 1 = data point at start of test i = 1* data, point (i = 1 to N) N = Final data point of a given set k = kth , 9 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 f th ratio of the i value and that of the initial value. 1708 081 A-1
The values 0.5 u , 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. i'* - fp-p 3 1 fp-p 11 fp_p
- V ' V 0.541 I
+ 0.299 + .162 (T
T Jg 7
~
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+ 162 (T )7 (T /u T=Ikk k = 1 to 27 for upper compartment k = 28 to 37 for compartment k
- 39 to 52 for compartmant 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 f estimated straight line. The rate of the containment vessel air mass loss (or the containment vessel leak rate) is the slope b of the least square fitted line W : W = btf+a 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: I A 6Q , __ (i ~ i . =0 i i+ 6a 62 . W 1
-W f =W f - bt f -a 6 I(W 1 E)2 = 2 I (Wf - bt - a) = 0 -
6a . I (Wf - bt - a) = 0 Na + bit = IW f (1) 1708 082 A-2
g , 6 E(W i -0) 1
-=0 hi = bti+a 6b 6b W h=W g g bt -a 6 I(W1-W g )2 6b ~ i( i~ i ~ *} " - t (2)
I-tfW - be - a) = 0 artg + bit = It W (3) with (1) and (3), a and b can be solved by matrix: Na + (It g) b = IW g (1) (It ) a + (It ) b = It W 1 (3) N IW 1 It It W nitg W - (IW ) (It ) b= 2 (4) N It 1 nit -(It t)2 It It 2 f IW It 2 It W It g2 IW It - It It W 11 a= = 2 (5) N It nit - (It g)2 It It 2 Lam = -b 14000% per day (
- unless otherwise specified, all summation will be from i = l_ 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 to the gas distribution function - only the W1contains random error, not the t i_3 1708 083
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 errer, only statistical treatment can possibly evaluate the, error effect on the test result. InordertochooseaproEer statistical treatment, it is important to identify the characteristics of the observed data. In the previous derivation, it is found that " Lam" 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 SQUARE), while the for:aer 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 probability. In other words: L(TRUE)
~
am i " 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). The value of t i: on enclosed Table 2. -S b is the standard deviation of the variance of the containment air weight.
Equation (4) indicates that b = f(W ) and by definition of variance: S "Z S (5) b w where Sy is the variance of W : 1 1708 084 A-4
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2 , IN 1 1) (6) 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 a. The freedom to evaluate the variance of Wg is reduced by 2 even N data is recorded: '.. nit g1 W - (IW1) (It ) t 6 nit - (It y) 6b " f 6W 6W 1 let c = nit g - (It g) 6 nit g1 W - (IW g) (It)) t
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~
Substitute c = nit - (It,) to (8) : S = NS W ,3 b N 1708 085 A-5
nit - It I i
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2 SW b 2 7t - It g _ ~ N '.. The identity provides:
?
I(t g- E) = It -
= It g -t It g S S S 2, w w w s , ,
(9) It -It E(t g-t) Itg -E It g f N A.4 Summarization: The following are the essential equations used in developing ICRT computer program: 0.541 I(P-P )I + 0.297 I(P-P + .162 f(P-P ) i T [u L T t T II i 0.541 f(P-P ) + 0.297 I(P-Py )
+ .162 f(P-P y )
(T /u A T /L \ T/I T = IT V kk W = btg+a nit11 W - (IW 1) (It ) 2 nit - (It g)2 IW1 (It i) - (Itg) (It W 11 )
~ ~
nit g - (Itg) Lam = -b Lam (95%) = Lam + tS b 1708 086 A-6
t value is on enclosed table corresponding to f = N-2 and and 0.975 U(W i
- a - bt1)
S ,2 = N-2 9 [3 2 W 1/2 '.. s .} I(t t-c) e e e ' A-7 1708 087
TABLE 1 LOWER CONTAINMENT (COMPARTMENT VOLUME FRACTION = .297) .RTD # GENERAL LOCATION COMPARTMENT VOLUME FRACTIONS ~ i -1 Wall mounted in incore inst. .0417 area 2 S.G. D lower support structure .0565 el. 745' 3 S.G. A lower support structure .0565 el. 745' 4 S.G. B lower support structure .0565 el. 745' 5 S.G. C lower support structure .0565 el. 745' 6 Wall mounted in tunnel area .0297 7 Wall mouni 'n tunnel area .0297 8 Wall mounted in tunnel area .0297 9 Wall mounted in tunnel area .0297 10 On top of S.G. 1D .0377 11 On top of S.G. 1C .0377 12 On top of S.G. .3 .0377 13 On top of S.G. lA .0377 14 On top of RC pump 1D .0377 15 On top of RC pump 1A .0565 16 On top of RC pump 1B .0565 17 On top of RC pump 1C .0377 18 In accumulator room 1D .0117 19 In accumulator room 1C .0099 220 In accumulator room 1B .0112 . 21 In accumulator room 1A .0112 - 22 Wall mounted in room with air .0345 return fans 23 Mounted on ladder support in .0438 reactor cavity
,_ , 1708 088
TABLE 1 (Cont.) RTD # GENERAL LOCATION COMPARTMENT VOLUME FRACTIONS 24 Mounted on ladder support in .0377 - reactor internals storage area (
.25 Column mounted in incore .0321 instrumentation area 26 Column mounted near lower con- .0406 tainment vent. Unit ID 27 Column mounted near lower con- .0406 tainment vent. Unit IB UPPER CONTAINMENT (COMPARTMENT VOLUME FRACTION = .541)
RTD # GENERAL LOCATION COMPARTMENT VOLUME FRACTIONS 28 On concrete housing for S.G. .0762 1D 29 On concrete housing for S.G. .0762 1A 30 On concrete housing for S.G. .0762 1B 31 On concrete housing for S.G. .0762 1C 32 On wall between S.G. lA & 1D .0848 33 On wall between S.G. 1B & IC .0848 34 On wall below crane track .1355 el. 838' 35 On wall below crane track .1355 el. 838' 36 On cont. spray piping 31'6" west .1271 of center el. 875' 37 On cont. spray piping 31'6" east .1271 of center el. 875' 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'
} {}@ ()bh A-9
TAsi.: 2 Critical Values for Student's t-Distribution
- I Pr{ Student's t $ tabled value) - 7 .
f 0.75 0.90 0.95 0.975 0.99 0.9 5 1 1.0000 3.0777 6.3138 12.7062 31.8207 43.6574 2 0.8165 1.8454 2.9200 4.3027 6.9646 9.9248 3 0.7649 1.6377 2.3534 3.1324 4.5407 5.6409 4 0.7407 1.3332 2.1314 2.7764 3.7449 4.6041 5 0.7267 1.4759 2.0150 2.5706 3.3649 4.0322 6 0.7176 1.43 M 1.9432 2.4449 3.1427 3.7074 7 0.7111 1.4149 1.8946 2.3646
- 2.9980 3.4995 8 0.7064 1.3968 1.8595 _ 2.3060 2.8 M5 3.3554 9 0.7027 1.3830 1.8331 2.2622 2.8214 3.2498 10, 0.6998 1.3722 1.8125 2.2281 2.708 3.1693
. If 0.6974 1.3634 1.7959 2.2010 2.7131 3.1058 12 0.6955 1.3562 1.7823 2.1788 2.6410 3.0545 U 0.6938 1.3502 1.7709 2.1604 2.6503 3.0123 14' O.6924 1.3450 1.760 2.1448 2.4245 2.9768 U 0.6912 1.3406 1.7531 2.13 U 2.6025 2.9467 16 0.6901 1.3368 1.7439 2.1199 2.5835 2.9208 17 0.6492 1.3334 1.73M 2.10M 2.5669 2.8982 18 0.6884 - 1.3304 1.7341 ~2.1009 2.5524 2.8784 19 0.6476 ,t 3277' 1.7291- 2.0930 2.5395 2.8609 20 0.68J0, 1.3 253 1.7247
- 2.0860 2.5280 2.8453
~ ~
21 0.6854" 2 1J232 1.7207 2.07M 2.5177 2.8314 22 0.68.58 11.3212 1.7171 2.0739 2.5083 2.8188 23 0.6433 *1.3195 t 1.7139- :2.0647 2.4999 2.8073 24' O.6848 1.3178 1.7109 2.009 2.4922 2.7H 9 25- 0.6444 1.310 1.7041 2.0595 2.4831 2.7874 24 O.6440
~
1.3150 1.7054 2.0555 2.4786 2.7787 27 0.6437 1.3 U 7 1.7033 2.0518 2.4727 2.7707 28- 0.6434 1.3125 1.7011 2.0444 2.4671 2.7633 ' 29~ 0.6430 1J114 1.6991 2.0452 2.4420 "2.7564 30! 0.6428 1.3104 1.6973 2.0423 2.4573 2.7500 31 0.6825 '1.3095 1.6955 2.0395 2.4528 2.7440 32 0.6822 1.3084 1.6939 2.0369 2.4487 2.7385 33 0.6420' *1.3077 1.6936 2.0345 2.4448 2.7333 34 0.6818 1.3070 1.6909 2.0322 2.4411 2.7284 35 0.6414 1.3062 1.68 M . 2.0301 2.4377 2.7238
~
36' O.6811 1.3055 1.6883 2.0281 2.4345 2.7195 37 0.68 12' -133049 1.6871 2.0262 2.4314 2.7154 38 0.6810 1.3042 1.6860 2.0244 2.4286 2.7116 39 0.6408 1.3036 1.6449 2.0227 2.4258 2.7079 40 0.6807 1.3031 1.6839 2.0211 2.4233 2.7045 41 0.6805 1.3025 1.6829 2.0195 2.4208 . 2.7012 42 0.6804 1.3020 1.6820 2.0181 2.4185 2.6 H1
. 43 0.6801 1.3016 1.6811 2.0167 2.4163 2.6951 ~
44 0.6801 1.3011 1.6802 2.0154 2.4141 2.6923 45 0.6800 1.3006 1.67M 2.0141 2.4121 2.68'M
~ ?D. B. Owen, Handbook e/ Statistical Tabler. Addison, Wesley Publishina Co.,1962. (Courtesy ~~
Atomic Energy Commission, Washin8 ton. D.C) 1708 09u D**D P f'W Qm ' eh knL 1 k} L A-10
TA8ut 2 (Continwd)
- Pr(Student's t $ tabled value} - 7 f 0.75 0.90 0.95 0.975 0.99 0.99F 46 0.67M 1.3002 1.6787 2.0129 2.4102 2.H10 1.2998 1.6779 2.0117 2.4083 2.6444 47 0.6797 0.6796 1.29M 1.6772 2.0106 2.4066 2.6422 48 1.2991 1.67H 2.0096 2.4049 2.6800 49 0.6795 1.6759 2.0086 2.4033 2.6778 50 0.67M 1.29e7 0.6793 1.2984 1.6753 2.0076 2.4017 2.6757 31 1.2980 1.6747 2.0066 2.4002 2.6737 32 ' O.6792 2.3984. -2.6718
~ 33'/0.679f $.'1.2977 If6741- 2.0057 T.6736 2.0049 2.3974 2.6700 54 0.6791 ff.2974 2.us2 2.3961 .t.2971 1.6730 2.0040 SS ,0.6790 1.2969 1.6723 2.0032 2.3944 1.6645 $6 30.6789 2.6649 1.2966 1.6720 2.002S 2.3936 57 10.6788 2.3924 2.6633 $4 0.6787 1.29 0 1.U16 2.0017 9.6787- 1.2961 1.6711
- 2.0010 2.3912 2.6418 59 60 'O.6786- h2954 - - 1.670F ' 2.0003 2.3901 2.6603 61 0.6785 1.2954 1.6702 1.9996 % )s90 2.6589 62 0.6783 1.2954 1.6698 1.9990 2.3440 2.6575 63 0.6784 1.2951 1.66 M 1.9943 2.3870 2.6561 64 0.6783 1.2M9 1.6690 1.9977 2.3840 2.6549 63 0.6783 1.2M7 1.6646 1.9971 2.3451 2.6536 64 g 0.6782 .I.2M5 1.6443 1.99H 2.3842 2.6524 47 0.6782' 1.2943 1.6679 .1.9960 2.3433 2.6512 64' O.6781 1.2M1 1.6476 1.9955 2.3824 2.6501 69 4.6781 1.2939 1.6472 1.9M9 2.3816' 2.6490 70 '0;6780'- 1'.2934 1.6669 1.9944 2.3804 2.6479 71 'O.6780 1.2936 1.6666 1.9939 2.3800 2.H69 72 0.6779 1.2934 1.6663 1.9935 2.3793. 2.6439 1.2933 1.u60 1.9930 2.3785 2.6449 73 }9.6779 1.9925 2.3778 2.6439 74 -0.6778 1.2931 1.6657 73 0.6778 1.2929 1.6654 1.9921 2.3771 2.6430 76 0.6777 1.2928 1.6652 1.9917 2.3764 2.6421 77 0.6777 1.2926 1.H49 1.9913 2.3758 2.6412 78 0.6776 1.2925 1.6646 1.9908 2.3751 2.6403 79 0.6776 1.2924 1.6644 1.9905 2.3745 2.6395 80 0.6776 1.2922 1.6641 1.9901 2.3739 2.6387 81 0.6775 1.2921 3.6439 1.9897 2.3733 2.6379 82 0.6775 1.2920 1.6636 1.9893 2.3727 2.6371 83 0.6775 1.2914- 1.6634 1.9890 2.3721 2.63M 84 0.6774 1.2917 1.6632 1.9886 2.3716 2.6356 SS 0.6774 1.2916 1.6630 1.9883 2.3710 2.6349
- 86 0.6774 1.2915 1.6624 1.9879 2.3705 2.6342 87 0.6773 1.2914 1.6626 1.9876 2.3700 2.6335 88 0.6773 1.2912 1.6624 1.9873 2.3695 - 2.6329 89 0.6773 1.2911 1.6622 1.9870 2.3690 2.6322
- 90 0.6772 1.2910 1.6620 1.9867 2.3685 2.6316 e O D .
ws o . 2 1708 091 A-ll
m e APPENDIX B RAW AND PROCESSED DATA D e O e e B-1
\708 092
TABLE OF CONTENTS Sectlon I - Leak Rate Determination: 7:05 a.m., August 21, to 9:35Za.m., August 22 A. Leak Rate Report - 95% Confidence interval B. Leak Rate Analysis - Deviation of observations from predictions C. Normalized Air Weights - Containment and individual compartments D. Volume-weighted Instrument Data - Individual compartments E. Test Initialization - Compartment volume fractions and calibration curve coefficients for individual instruments F. Raw Data from Instrument Readings G. Calibrated Data from Instrument Readings H. Plot of Data about Regression Section II-Verification of Measured Leak Rate by Imposed Leak of .1986% Per Day: 9:35 a.m. to 8:55 p.m., August 22 A. Leak Rate Report B. Leak Rate Analysis C. Normalized Air Weights D. Volume-Weighted Instrument Data E. Test Initialization F. Raw Data from Instrument Readings G. Calibrated Data from Instrument Readings
~
H. Plot of Data about Regression _
$ G 1708 093 B-2
SECTION I 8-3 1708 094
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4.) eeoeeeoeeeeee eoe oeee eo eeoeeee y eeeeeeeeeoee 4 ee CCCCCCOCCCCCCCCCCCCCCCCCCCCCC CCCCCCCCCCCC CC 00 0B 6 000t O408 98 00 99g 8 80 W d e= == C C s= @ P" C C V k e t emf = e fb F C h > 4 fb er e= 4 C O W d @f%@ w @ e N C fL C C e @ ** 2 C C a= 4 O f4 P*e* @ F a= d @ CF 4 @ e= N e= 4 5 f% == @ C C C C 1 sm *= 4 f4 C == ft C 4 # C C I EC
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- C FP W 8% d > @ C o-C C e f\ E C == e ** C a pr e
== Derm @ o fbc c r pm @ e == C C F @ @ E == == C M4 @ f4 =F C fr O O F A O C ee eeeee eee e eoe ee e eeeo eo ee eee o eo ee ee Fe.P t.F Fef\eCe mdfLEteC F 4ftC O C O F 4 f4E e r C Mdit@@dC SP,4 ft a @ p= C pF 4 ft et @ W C l b r= > ft f% e r= > > tbit e P= P= > f4 f4 W" > > P= f% f4 = >> > ts f% # P= #m P= ft fg f4 N == 8% N ft f%
CCCCCCE C C C C C C P= CCCCCCr= C C C C C C P= C C C C C C P= CCCCCCP P pe C c ar d @ C A P= P= r @ s C .=C C r om r c CO ef fb C C C @FWVdEC C&4@CVC F e=e-V C C C F C e=4 @ fbC PP == o-d F # C F C o= C C W" C A C ==C C 4 C me C == C e= e= C eeoeoeo eee oeee e eeeoe o eoeeoee oeeoeee eo eeee o PEFO@CC fr a pPe C e c fr ec F O ct ft C PP 4 pr C P C C sesL fP C O e C ar st er @ @ C C e r= > A f4 6 P* > P= ft f4 E k k P= fk fk W5 > > > 8P fk *= P* P= P= P' fb # P= P* rm ft 4 ft it om fu #Q f% tb CCCCCCC C e C C C C P= CCCCCCPm CCCCCCC C C C C C C P= CCCCC C P=OMOaCC P= F r= 0 k C C pm 8e 0 e C e C E V P= > P= #P C P= C er 4 0 P= C > ft et r P. C eCC
, meC@@eC OP r= C e=F P C FPP= C O 4= M C PP M C e= C DP C F P= C C C & C 8F M C P= C @ c eeeoeee eoeo eee oeoeeee eeeeoee e eeoe oe e oeo eo e f4 e fLP= P= ft C fu O f% et P= F6 Pb O fk r= C W C ibe f4Cet d C fN g fte E == C rk p= et (
k Pm P= f% f4 m P= P=P= f% ftP.C P* e= r= fb ft e P Pm P= ft f4 C M em en f% ft V f% e. P= ft et .C e= P N
- A N A N CCCCCC@ CCCCCCE C C C C CiC E C C C C C C et CCCf.CCE CCCCCC@
Pm P E r* P= 4 4 C 44dEPPC WCVCVOC C 4 4 e= e C C e=r W" A C a= C e= r 4 == C D C d P= F V f4 9 C C P= 8P ( F W* C O P= P* d ( == C Cef*44&C EP=F4/FC pm e= 8P 4 4 A C eeeoeee eoeeeee eeeoeee eeo eeee eeeee ee eee eee e FP NW"f4 C d C PPitt ft Pm 4 C fr fb d fle= Pm C F it.F fL P= C C PP f\ # A mm e C or fi t ft em e= C P= P= P= E f%fb r* > Pm C tb P= Pm P* P= E fVF P* P= P= E fbC P= > P= E ft 4 P= P= P= C ft w N
- 4 N 4 A e-o e CCCCCCG CCCCCCC CCCCCCC CCCCCCC C C C C;C C C CCCCCCC I
> d C == == P" W" O fk f4 @ d P* e- 4 C o=0 F VfnF c @ f4 e= U P= =C E PP PP I:l* C C C em K @ e= w F SQ W P" E P* > @ C ft fe r* d P= C pr fu F M d P= PP ft f% f\ b r* P= @ C ft ft P= # N r P= A 8P e= 4 P= pP f5 f4 C ee eee e e oee oeee e e e ee e e oe o e eeo eeoe e e o ee e e o e e F f% d it e= 8P d le f%d tt C C 4 PPf% d fk t #4 4 fe f% d it > P= d fr ft s ft k r 4 ar f% d it et # 4 T P=P= p* W fb fb m Pm P= P= C f4pm 8F r= P= Pm C ft PP W* Pa k r= E F4 @ $P P*P= > C f\ *r *P ** ** P* C fk C fr+
l 4 A w N = A A a i CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC
> O C O C ftF ft 4 C ft fe rP@ f\ F P= C fr W' r @ == C 0 ==W" O f5 C W" e= == c 0 e fb d p= ft F f( e W9 l 2 F P= 4 == d V fb V E e e=E 4 ft W" E e ==d V tb V P= 4 e= P= ft f% (E e == # 4 ft # >= 5 o=O d e=
w eeoee e e eeeeeee eeeeoee aee e eeo eeoee oe oeeeoe e 2 AAFVace AAWV-dC AAtrede AAWFCPU AAC/Cee AAc/CCe g 3 >>kkFAm kkkkVdF >>>>FAr >>>>FFF >>>>FFF khkkFCm a fu - ft e- f% is 9;
- 2 CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC se W e=> @ d e= C 4 e= C W" pF ft e it @ ft V E e f4 fu e ftf\ e=O C P O PP C O 4 *= 4 0 ** C == se C P.
e g d e m er ric W d C E == r= C ff. d @ P= e= F == fe d F P= # C e= PP'd @r* efb C 8P 4 C C d == ==
=
W eo eee oe eee eeee ee eeeo e oee e oee eoeeo ee o eeoe e e P= f4faf\e C F F f% PPf4 8 C E ( ftmf( W C C @ fimfL 4 C4@ f4 0P f4 W C P= ( ft pf f\ W C fL( 4 p= P= > Pm F == *= > > P= P* st V == P= Pm P= *= #P e= == f* * = P= P* PF E e= P=P= > > 8e A a= Pn e= P= P= se e e= k ini e= ik *= ft o= i W 4 CCCCCCm CCCCCCW CCCCC'CP CCCCCCC C C C C C C o= CCCCCCO WM == O N C O f% P == C f= r W" d C C et t et( P= C f4 E = ft d C C ==C d e= e d @ 3s=@wrec
, J WWeEwFN WreEd?A ce=CFWA WWAEdra CW-E4AA *WerkFA , eeeeoee ee ee eoe eoe eeee oee oe ee eeeoe ee e o eeeee i e=fP. fP fe r == @ ==se pP PP C C e a=aP pe rP @ g @ esse pe pec fg on o=ar er F 3 y 7 .= se sP pe t g y , P=Pm k r= 4 C tb P= P=P= > f% e ft P= P= P= P= fL C fb b r= f* P= f4Pm fk P= P= k k 8% ==N f* P= P= P= f% P= fb WW == N == fb om e
CCCCCCC CCCCCCN CCCCCCfb CCCCCCC CCCCCCP* CCCCC N (Efb C W C fL E C f% r 0 4 th e= E # 8P P == d V r C C C a= == O C d em # e- E O P= == C om C == :r C E s VCem P= o C e d C f\ q t fu fud 4 > f%d t f% P d f C f%C o f% W=d d C e=f% Q f% C dW=em eP e # fu fud f pm f%PP W fs cee ee oe
- C eee** ee C ee e e ee o C *eeo eee ** * ****e o == e oe eee e e wAMCGChF =AFCTChe =AFCW@ke =AFCU@ke *AFCO2>@ =AFCUOkt ee f= P= Pm P= ft fW ft ** Pm P= P P= fbi %f4 se k Pm P= #m fbf% fu o* Pa > P= >= fk f% f% ** Pm P= P= f* ft f% f% ** P= P= r= P= fbfk et m m m M M pr m pm U" fP M P' fu fu fL- fb fu N
@CCCCCC@ @CCCCCCfb FCCCCCC@ FCCCCece eCeCCeese eeeeceet we P= d e= ==fb r4 C P= p= O a=8* 4 C F C k W" C C @ P= == P= M V C # F Pm E C f=MC C f4 e=ft C M 8P & C pm s d Pm C e CO fkO ft C W C O V C fW C O F F at P= ft C e C O f4 P= ft eeeeoee >eeeeee e es Ceeeoe F C et f4 4 fb C O C C e e- fb P= eeoeoee e f\ OR Ofr E E @
p= eoe e oee 4 f% P" O ft C P= @ t= eeeoeee t= ee 4 fbpP W ft C P= @ e f4 8^8M ft f P= P 4 f%fP W A E P* @ 4 f\ re e f( E P= O P= P= f*> ft tbib Pm P= P= P= f\ f%d% P= P= P= > fb fbf% F* Pa > > f4 f% fW k P* Pm P= f4 f% fb P= P= b p= f% f% N G O O @ C C 2 2 2 2 2 2 P. Ps e== > om a= o C O C C C e as as as e er ce b *=fb fP e f 4 P* We= 4M C P 4 P* b ==f% fP. O V 4 Pm We*f4 F W W d P= We*f% FP W @ d P* W e= ASP W W" d r= F3 & M M k 2 2 l > WWWWWWW WWwwMEW wwwwwww WWYWwWW WYwuwWW wzgwwww g 2 CZF22722 =2222Ei2 AZ722222 F2222222 #2222:22 #2227222
== p as as an an at er as e se es w as as am ar e am er ar ee < en er F se e e er as as er @ ar as er ac er e er @ as as e as e an er O EfECEEC R@CEEFE EssECE@
708 07 IL EsECfff ECCCCEE C E E E (DEC D 9 e e e e e e e e e e e e e o e
a e t t 6 l e t * ( += e *
. CCCCCCM CCCCCCM CCCCCCN CCCCCCM CCCCCCh CCCCCCM . C oe ft @ e P= C C C C @ P= C fr C C C C W.4 s= C @ ikO C & fk C @@dFdCC @ T k W If N C l w m>EMAdC M4CreWC m=@k=CO NAEECCC AwEn=(C AOCC==C g eeoee e o eeeeeee eeo eeee e e eeeee eoeeo e o e o eee ee s F4f%C@CC Be r= f% E C e= C pe k fk r= @ W C P" P= fb r* O at O pr P= fb a O em C pr E F%C @ F C p= P= Pm a f% @ kr= > f% fk @ f*P= > f4 Pb O >>P*44E > F= P= ft ft t > P= 8m f% fb E == e- N == a= em CCCCCCE CCCCCCk CCCCCCP. C C C C C C Pm CCCCCCom CCCCC @ C P= 4 76 W F C CCF&W#C E 4 fbF ibe=C >= d C P= aL Pm C d> fLrm a g C p= C f% ft. CCC P=
f% C ==r C C C #% C e=# C f% C fb C e=> C O C f4C==WC C C A C e= C C e= C f% C == 4 *=4f C eeeeoee oeeeoee eee** ee **eee eo eeeeoe e oeeeeee 8P C frE @ d C mC 8 Pet @ 4 C MCFC&CC fr C F E S #C mE FE @ ec pr E fr at @ C C g 9= en t= ft f%C Mf= > f4 f% E P= rm P= f4 fk r Pm P* r* ft % C b r= P= 4 ft E r= P= p* fk f4 k e= a= f% a= en on
. CCCCeet f=, C C C C C C CCCCCCC CCCCCCs= CCCCCCC C C C C C C P=
a E 4@COCFC 4CCeE4C 4@COMCC d C C W F ==C r @ -C a= @ C 4 / sr er C md C af'C C C fer= CEO F G P* d @ f* @ @ C P" r= C d e == C me d C If 3 C C PF Pm C 0-@ @ C ee oeeoe a eeoeee eeeeee o eeeeeee e oee e e o eeeee ee f% W f4 sm et ** C f4 8 f4t h e= C N W e*C Pm C C tb e fbE k C C' f% W f4 E P= h C F4 4 tbr= P= F G P= > > f% f% E > > k tk ft 4 k Pa r ik ik W P* > > fk f4 C Pa k Pm f\ % Pm M Ph #m ft f%M
== em f% a= e. em i
CCCCCCO CCCCCCC CCCCCCE CCCCCCC CCCCCCO CCCCCCE P= @ # W f4 Of% C C re pe ftF W C 4 W er W k O C f4 F W F P= E C If r f% 4 FL = C 4 f% ft C f4 W C dP=8r dP=@ C dr*F4VFC P=pm fr 4 e if C 4 r= 8r 4 e f% C d P= P" d e W C P= P= #e m d E C eeoeeoe oeee o e e eeeeo ee eeeoe ee eeeoe e o eeoeeoe er f% r A P= C C f* fk it fb > C C IP f%ir fk Pm W C F fk ir f% E C C F fk / ft 2 @ C P= r= #= st f4 C fr. P= fk p= W
> E!%f(PP= 4. C M P= e= C ft pr > > P= E A P. >= > P= E #4 Pm k e= P= C f4 4 ** em ft om a= es e CCCCCCC OCCCCCC CCCCCCO CCCCCCC CCCCCCC CCCCCCC == 4 @ @ ft s @ f4 ef' E nf f%E c et c P= W 4 C E ft WS p er C e a= C e P= e ft c & s= d 1r ==C O ft fk E e f%#m d PmE pfb f4 e= @ P= W @ f% f% P* d C # 4 f% f% F= 4 P= @ e= f% ftp= 4 >= 4 & *= ik D* 4 P= P= f% e=
C ee*e o** e e e
- eee aeee e e e ee e eeee eeee ee o e ee e e ee Pa fb d n et t e fr ft d rs st e d m f% d fL C C 4 F r% d f% C E d se fs d it @ C d F es d r. @ r d f==
2 > P= Pm C f%9m r p= r= Pm s, rk en e p= P= P= C ther m P= P= > t f4 4 m en P= P= E f% d 'e W h P= ar f% d r ,g at em ae fb es en em l E O2 CCCCCCC CCCCCCC CC CCCCCCC CCCCCCC CCCCCCC
> V 4 0 == W P= 4 O If eme= ar g soir 4gCCCCC g if C C tr s, C W W em C r C == = 4 e- C e = C or if fk 4 2 ( P= C a= 0 E = tr E W == P= C a= If Pm C e= tf r= o= V P= C ==( d fk if r= 4 a= P= P= == if E C a= C ** e=
laJ eeeoeee eeoeoee eeoeoee ee eeee eeeo ee e oeeeeee 3 f% ft e # C C W WVCOW A ft e v C C C f4,s .e veeW <s ts = < .= n e 4 ,% = ir ,4 s= O l3 k P= e= rm F o fe f4ftP=>
>P se d m p= > > P= fr f% #* P=P= P= #me d m P= p= P= > se o pa e *= > >= fr d er & o= e= fb e= e ==
e= f Z CCCCCCC CCCCCCC CCCOCCC CCCCCCC CCCCCCC CCCCCCD e= W C C C If r? @ V E fk @ d C f% 4 C e=E P= lf C W em s F P= O ft 8r 4 O C O C P= et # C C V tr C O' W # E P= dir f4 e d C P= 8c f% @ m d@P=P"e=P P"V @ P* d d @ fr tr @ m e= E E sr 4 C em en f%E b ee eee eo eeo eeee -eeee oe eeoe o ee eeee e o e o e o eeeo
> f4 8mf% W C O If. ft pr ft W C == W fb m fb er C == 4 f%mf% ar C C C f%serk e C g e ur % W C e e at P= Pm e=P=8r 4 == Pm P= P= P= 8P d es Pa r= P= P= st f% e= M P= f* Pm 8Pt f e= k p= P= #= pr / == ft. P= P= h r ( ==
P Q == em f% em es es at e CCCCCC@ C C C C C C P= CCCOeCC C C C= C C C e= CCCCCCC CCCCCCC th f6 O P= e-it'd Pm C @ E F f% d d em O # m e= 6f C F C if'@ PPf4 @ @ C 4 ft C F4 4 em rm J" C em g
- 7
=J P" W == E e == fk F c ==& ft e f4 F W *=C f4 P= ft P"W CetPr@ft P* e e=P. # w f( Pr C'k C O f%ft eeeeeoe eoeeeee oeoe oeo e eoee ee ee ee eo e o e eeoee e=ar se er g se g .= ,, y y g c @ emen pr eeg >= @ F or,F C @ @ e=yFPge@ e= c or e g fg g.
P= r= > > fb# fb k e= r= P= f% r tu > >m > P= f% C ru k e= #m P= f4 0 f% pm P= r p= f4 W ft r* *= > #* ft e f%
== em f% == - =
CCCCCCd* CCCCCC@ CCCCCC4 CCCCCCom CCCCCCd CCCCCCd N Wd OO E fiem er fL > 1r 0 tr e C C P=e= C O @ C # th er= #E O ar C e P. rme-d ftd P' P* m e=Odf%>=@W # P= == @ C fu C # d >= f% C re fU f% W @ r= E *= 8F fb 87 #ren 'r C ar ft C rif4 ertref.* e mprgC er h em f% es eeeeeoe e. e eeee ee f% eeo eo e e f% e e e eeee fu e o ee ee e fboeeeo e e
= ==f4 P" C W P o= @ e=f% Fr C W st P.@ e= f4 P" C W P r= P ef%FCW@m@ ==r(F C er @ pm @ efk ar C e @ P=O e* P= > Pn em it tk t% ee r= p= Pm P= fb it tu ee M > pm en ftf% f% e* > > Pm P= ft f%ft ** 9m f= P=P= ft f% ft o= > hr* P= ft f(fb d= M GP M M M= F M fe m M OR PP s N f% fU N f% h @CCCCCCC @CCCCCC4 p C C C C C C s= FCCCCCC@ ItCCCCCCC OCCCCCCPm I a= > F O d C F W E, f*w E Pr O d fr Pm M F E @ C P= a*h Pm W C C P"C W ** r=8Ph *= st a= C P= M8 ram 0 Cfk@e.
cmc O M4 f4 C fr C a . eL 4 N C rec @ C 4 f4 C pr O F w m f% C se p @ # @ f4 CW@@CCf%
> eeeeee e k eeeeeee >= eeeoeee t- eeeeeoe >= e e e o e e o k eeeee oe e O F W f4 E Pm @ e & SP W ftP= P= @ e Ibfr Pr d%S P= @ a8 f4 fr 9A f% E P= @ k kPP fe f4 C P= @
e aE ft Pr F f%E E @ k Pm
- P= ft fs et P ken e= fwfstb k = P= P= f% f% f% P= > P= P f4 fs f% e= > P= Ph is tk ft P=
- P= r f% ft ft O O O C C O 2 2 2 2 2 Z
** >e e >= o= >=
C C C C C C e as e as as as ee tes ==ft f# # @ d Ph laJ e= f% fP W F d em b e=f% MW @ d P. W **I\ BA W @d Pm be=f% F C V g > be=ftF el Vi4 pm F@ Q CE @ & &
> wwwtwww wwwwwww wwwwwww WWWwhyw wwwwmww wwwwwww 2 482 e= F e as22Le e as 22 >2222222 er e @ ar as as as as asC er 2 F2e 2 2.a2hse2 e er e .s @ er@2222222 d e e an os e c anO222222[ *2kZ2e 22 at as as as er e C e an e er e e as "--- -~~ --- --- - - ~ ~ ~ - - - -
1708 108.
> e o e e e o o e e a e e o e a e ,.=.e=.~.- - = . . = . = . . . . . = = , - . . . . . - ._ , .e.,
e e D**D # D T
- Dl . g j
_=
%=
e== CCCCCCP= CCCCCCP. CCCCCCP. C C C O C C et CCCCCCpm CCCCCC4 C FOFfrWDC C e t r e a= C E V E -r f4 C E P= K O == r c E F s' C @ C C d > V == @ p= C { m AVEhmmO AVES =FC AdCFerC AVCWwFC AECdCNC AEEFehC
, eeoe eee e oeeo eo ee e eeeo e e oe eee eoeo e o e e o eeeee g OP.d f%P C fr C Mditt@mC P' d fbk O W C Md f4 C O r* C fad fL E G A C ** d fL E : dc > > P= f4 f%e e= > P= f4 8% C b r= P= ft f4 7 P= P= rm f4 f4 V P= P= > P= f4 # P P= rm fk th d f% ** *= f% A f%
I CCCCCCP. CCCCCCP= CCCCCCP= CCCCCCE CCCCCC4 CCCCCCd [ F d E er O #4 e=C =D C e* C F 8% c ddCCe(C O C == == & st C W Pm a C V O C A"p= P= 0 == se c A F *=E *=d C fk c e= d C C C ft C e= r C e C f%C a= 4 7 fr C ftO C a C e C fL O C e C
- C eeeeoee eeeeoee eaee oee e oeoeo e eeeeoee oeoeeee F r= pr C & C C Br a PPO @ P= C fr E rr C O E C P"E F @ E fr C er P= pr E O V C mP= ar s' ' or C g & P= P= f\ f%fr P= > pm f4 f\Pm P= P= > 88" f% E p= > M ft ft V Po r= P= f. f% C P= P= g= .i fW 4 f%I == == 4 A 8%
e C C C O e; C P= CCCCCCet CCOCCCP CCCCCCE C C C C C C P= CCCCCC4
= ' t V O ereft f C mf* C O K V 9m c V C C w f%et t Ed@O80C ** w 9m r= = == C FVKOeVC M d C E @ r= C P9 Pm p W @ k C fr' d Cit C P C Md @ E C P= C FPdOECCC fr d r V 7 e=C ee eeoee eeeoe e e eo eo ee e e e ee oe e eeee ee e o eee eee ! db e fthem er C NWwCh@C f4 C f%E C eD C f . W e= >= E E C f4 W e= >= K C C f4 e ==h r* 4 C p= p= P= ft eter P= > P= f4 f% P= P= rm e= ft fk E P= M M ib ft C P= e= P= f\ ft pr P= P= > A f% e . N a= en f% A f%
CCCCCCF CCCCCCP CCCCCCC CCCCCCO CCCCCCE CCCCCCr= P= F Pr e=EC w@ C 4 f\ a= C == W S G rk C O fn ft C W e=C C C pm C VCOCC(C C D E A a= P= C d P= fe d P*p= C d rm eP P= em e=C de= pr d C Pr C d M F r= ft C C d e= ft P= fr P= C E 4 ft *= t e C
, eeeeeee eeeoe eo eeeeoee o eo eeoe eeeeeee e eoeeee AfbFfb E C C 8P fW f\ Pm F C F rkV f\ h C C F ft# PL P=fL C f4 h A C pr f\ # A >= C C pm em m et it f% M P= e= C f4 4 P= P= P= a f4 E P= em e= E f4 C PP fk #. et f\ ar P= >= p p= P= p g f( o f4 ** ** N fb A e CCCCCtc COCCCCC CCCCCCC OCCCCCC CCCCCCC CCCCCCC >d V e C *P 4 0 O 4 em e= e C C f\ (fL C V ft O eL e 8r 4 V f% e= E W>retF4 pr F d or e=
- F e AdVCFda AddCOWA ANothd= AhdENEw A4VC C O A AJVEACw @
C ee ee eee e ee oe e e eee eeeo e ee oeo e eee e oe o e e e e e oe sW F Nd fL E W 4 ** ft 4 fL E (= 4 8P Pb d fk et # d Pf4 d f%p= P= 4 P'ft d A rm 7 4 F f\ d f\ L F 4 l
- kkMCAAF Nh>CA4r phkrAMP >>>CAFF h>>t'A%F >>>tAFF M e N == == f4 ft
- f4 Ck CCCCCCC CCCCCCC CCLCCCC CCCCCCC CCCCCCC CCCCCCC
> O m W F Pr *= ==9 fr W S *P ( C C *= fr er P= f%C e=f% ft C P= P.C F f4 o a= 4 em T e C - 2 V P= F e=( t C V P= F em @ f\ C P*
( P=e= p* C
**fPF P= >4 e=V E 9F a= e 4 e- ( P= F em V ft e. # >= pr a= ( == C
- w eeeoeee eeeee oe eee eeee eoeeoe e eeeeeeo e eeoeoe 7 A f4 4 V P= E e d e # == t* C V C f4 W ft (L e f4f4 e V C e e tk f% c V C FL e p\P= pm yn g pe f4 ft pe.m F p se p= p= p. V C ft C t "= > P= > em fe .=ar 8%.
p pm P= p pr.or er y= pm > y= y fg se em p= p p.pr priar. g O A =
- A A A
' F et CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC *= W V V W C P= F e= V F C e ft C m E 7 e= E C C == 5 V @ a=C e= f\ e V ft p= F ft - Afr ft I / V N F' f 9 p= P' f g Or V O P= te d 7 Vf C 4 4 *m 9 ** f P= fs f% d Q F f E P= W i 7 Ft f 9mn d C C' , e, eo eoeeo eeeeee o eee eeeo e e eeeo e e eeeee e e eeeo ee J > 8% F fk e C,f4 @ f4 8P f% W C PP W fb8P ft e C W e fbP* f% e C d W f\F #4 e C d T f%se f% e C P= W '
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*= fb f% 4 fb tb CCCCCCP= CCCCCCem CCCCCCP. CCCCCOk CCCCCOM CCCCCC4 , C EkO4FFC CFCrdec Ctem-WC E W-C A W C M4FA(-C >>ced-C ft @@ C C e=C AOOCEMC fb(@4C(C A@@ (t e=C f4 W' O 4 E 4 C f\g @ g C @ C eeee ee e eeeee ee e ee e e e e e ee ee e e oeee e e e e ee e ee e i f\ W ==> P=( C fb 4 *=C M P= C fb e ==P= > @ C fb C e= Po *= 8P C fb e ==> >= == C f4 5 - ** P= fk C b r= > ib fb C k p= P= ft f4 PP P= h em f( fk r P= P= > A ft r P= P= P= ft f5 C Pm ** Pm f(ft S e= fV fW ik fk N 4
CCCCCCE CCCCCCC CCCCCCC CCCCCCP= CCCCOOK CCCCCCat Pm C W ( a= O @ C == 5 e f\ @ (C tbpr PP a= P*V" C F FF F ft P* e= C 4ft4ft= y c g er pr er (( C= 4 4 fbC C tbc C 4 f( C ft P= C 4 4 f( E ( @ C em 4 ft E @ @ C P= 4 f5 E f\ f\ C 4 4 % E Fr C C eoeeo ee eee oeeo eoe e oe e eeo eo e e oe eo ee e e e eeeee 8Pitr fLC -C fP f4 W" ft C fb C P*ftV ft P= 4 C F fbr fth C C pe rk t ft P= 4 C F%#ft>EC P= P= N E f5 C k k e= C NFP f= Pm P= K f\ m P= k r= K fber P= P= Pm E f\ "F P= k > et f(9P a= f% tb ft % fb e CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCOCC CCCCCCC
> 4 P=P"Vf47= C e= C r > Pb & F == P= fr U" 4 C - @ 4 @ 4 ( 4 4 e- W" C k C / = T P= C' T ft 4 P C 4 ==4(@e=Ce= fL @ @ @ h phe= e=4 W O @ fk C **d 4 @ e* == e= a= 4 f C V C C *= V C @ w f\C C eeeee ee o ee oeoe oee o e e e o e o e e *
- ee oe e o e e e o e o e e t en A 4fLt @ 4 se r%d ft C fb 4 **f\ tfLE V 4 0P FL 4 t\ n C 4 *Fh
> z f\ f\ m P= e= P= E ft PP w k P= P E fk f\ fr P. P= P= r % v w a ft F F 4 a= fb fb f% A ft a N I
CCCCCCC CCCCCnc CCCCCCC CCCCCCC CCCLCGC CCCCCCC C
> v 4 k mftF 4 et F .C ae -C e e (P* es tt e - r r e s* C ( F F v 4 -c t re ft C 4 e= fs 4 e fb I 2 4 4 fr+ e= P= == W 4 * == C C f. elr 4 Pr ==ft e fb er 4 F ==W ( ft a 4 F G C .* f\ C 4 * * # C f4 ww eoee eee oeeoeoe e oe o e ee eoe e e ee oe eo e e o e e e e e e e 1 f\ fb t @ e= C C f\ft C V A C C ft f( C ( e=P= c fbfL C V C ft U f(fb e ( C 4 1 f5 eme(Cae O >>WWFhM >>WMMAm >>NkFAF kkkkFAF >>>>"AF Wh>>FAm j @ W 4 4 4 A A . t=
e I (. 2 CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC
** U MEtb@-Ce P= @ C C # er ft 4 P= e 5 C C P. 4 E ft F --f2 (P.CCFA( # L* *L e >= ( **
A W k rm er e E ft e K P=cet C f( g P= 4 ( P= C f% C E Pa # -C ft O E P= 8= C C ft C et P= P6 E C 6 eeeeo ee e eoeo e e eoe o e e e e oe oe e e e e e e e e o ee o e e a e t k fkF ft W C @ W fbre f% e C M C f\fe fb c C @ c ft PP f4 4 C 4 & fbpP fb C C C W" f\ ar fg e c pep j , e a P= P= P= P= Pr= 4 == P= 8m P= P= V e= == fb P P=h em er ,==b . P= P= p r* *r == == fu Pm P= P= Pm
- fk -
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== 8P er er C er @ e=se m pe t Pm @ emeP F eP O P= O o=F or er e C @ em eP F ar ; y 3 er = or y e g P= P* P= P= f4( f4 p= P= k em fb C fb p= P= P= P= ft C tb P= P= P= P= ft C fi f= P P= > A C ft M *= > h f% e= ft *= fW fb N % 4 CCCCCCO CCCCCC@ CCCCCCe CCCCCCP' CCCCCCf( CCCCCCfV N Y P O ftf\F fL & et U*r c e= 4 F @ c C4 g g g g w.4 g r d er eP a on e Cae4(gg4 Conkreth C r @ e e@dE-@ C W' r A FoggmAgr eged-car eneggewA reefs Fr *e e*
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.* er E =f%E C ==4 k et fk C= C a=4 P= @ F 8e O == 4 P= ft ft C C ==C Pm en - @ C == 4 E P= ft % C eeeeeee eeee eee eeeee o e ee e e o e e ee e e e e e ee o eeee fr.4 fb5 @ @ C fr ,0ft N O 4 C fr.4 fA E O C Ce fr 4 f4 E O E C Pr 4 ft P= O rec i m4 p r= fkP=P= @P f4.C f= P= P= fbft h P= kem f\ fb P= P= P= P= A fL E P= P= fw ft eb C
> > P= ft fk C fbit e= e= f%
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@ M e=e= e- 4 C C f= r fk e 4 4 C 4 O == ==C == C @c C C P= ==C r e-or P= 4 et C 4.= ft g g ==C
==C C 4 C F C ==@ C V C V C .- @ C C C fk C ==@ C @ @ fe c e= 0 C fr C a C == & C ar C 4 C eeeeoe e e eeoe ee eee e oeo eo eee ee ee o e oe e oee o e ee fr E P* et O e C F P= F C O & C Pf P= fr C @ ==C f*P=le P= C #r C F P= F E O 4 C *e sm ar t & E C
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CCCCCCP= CCCCCC4 CCCCCC# CCCCCCW CCCCCC4 CCCCCC4 K P= f C F o E C 4 4 C o- fL 4 C 44CQC@c V C t f\ n P* C f fr e= = C C C 4 t h e-q fe c f4 W O *= E'4 C ftV@CE4C ftF E a=E ft C f4 7E fthC C ft( F C P= 4 C ft # C ( P. E C e oeo ee o e e oe e ee eoeee e o ee oe o ee oeeoe e o e e e oe e e g AWwCNEC NW=EWFC AWeChCC Ac=ChCC AC-EkFC Ace >>>C k P= M fbfk Pm P= r=P= fb fb 4 P* P* P= f4 fk Pm >= *= > ft a @
e= == P= P* > fk ik 4= e= f* P= P= ft f\ eC. ,=
I CCCCCCE C C C C C-C Pm CCCCCCP= CCCCCC4 CCCCCCN CCCCCCP=
k U ==m d Or te C- e= ft fk e tt 4 C fr a= fb e- C e C C o= e=f4 4 f% C 4CCCCCC > == == V e= W C C 4 ft a rec C P= 4 ft s tk & C V 4 f(E ft 4 C Pm 4 fb E ft 4 C 4 4 f( E P= fg G ar g g g g 4 C ee oeeeo eeeo eee eoe oe eo ee oe o ee ee oeoe o eoe e oee fr f%gf it P= a c F f\r f%fs F C fr f\v ft p f%C et t\f f\ Pm eL C fr ft f ft E 2 C v ft t h E er C b r= > E f\ P= P= > P= E ft 4 P= Pm P= C ft e em e= P= E f\ @ k r= P= C ft P= f* *= = E ft C*
a= ee a= em a= e-
, 4 CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC
> 4 W E F f\ @ e= 4 4 L == O sr e ft P=@ n ft t er c V E= @ Fm e= t t F EfLC e=C J t h t s # C f\
4 ==( # @ O E C e=r e C e=4 C ==(4@efC ==V' O fk C e @ ==# C C C T & == f C 7 4 == @
' C e eee o e e e eee eee ee oe e= e ** e
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b M CCCCCCC CCCCCCC CCCCCCC N CCCCCCC CCCCCCC CCCCCCC D= r M E C & C fi e= ft 4 == == C & C 97 7 CC e f% e= fr W @ fk ft P= F C" ft C C w ar ft f( ft 7 mr 4 @ E O 2 e 4 pr C 4 fr ft c 4 Pr == 4 c e= C 4 F e=pr f\ == T44=(4C P" 4 fr == C 3 em C 4 't == G f( @ E w e e oe oee oeoeeoe oe oeoe o ee eeeee ee e e oe o e e e e e oe
& iSAOVC@e ft fi c ( C r t' FLf4 UV C E o ftf%4 F C C e ft tk e # C == " ft f\ C # -c 8P O P= P= P= N F' 4
- P= P= > Pm F # F Pm P= f= P= fe r ta P= > fm P= Pr 4 fr Pm P= P= P= P P= P= fe" Pm Pm P= F E Fr O e= en we == e- we 9:
F CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC
*= O c o- V O P= f4 fb *P P= c ft O of f* fr c C 4 P= C c F k t ft et == # f( e=O e et O C ft == V F C 97 C f\ rP= 4 4 C C ik W P= P= V C @ fk c E P= W C E fk C 4
- fr C @ fb C P= e=t
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> ik F fbW C fb@ f4 F f\ U C ft @ ibF f4 C C P" W f\ Pr f\ S C # W f% PP f5 C C P= ( f(PP f\ C C C.C 4 P= b r= P= F 4 a= Pm P= > P= F r om P= f= P= P= pr # == P= P= P= P= fe r e= P= P= P= P= fr 4 e= P= Pm m e= pr E ==
& en e= em em em em M
4 CCCCCC= CCCCCCC C C C C C C ft- CCCCCCO CCCCCC# CCCCCC4 E fa @ F 8* *r f4 fr P* @ V C f4 P= ft > C mitft C 4 4 C Dr P= F *=@ 4 4f4NC#C8* C97C@O4 es fLfr C P= 0 C ft f( pr C P= mar fg pe fr C P= *= @ ft f\ P*C N fL P= ft f%Pr C P= rt 4 % fg er C P= C ar f(
e e oe eoe o e e e e oe eoeeoe o e o e e o e o ee e ee e o ee e e o e o e*F Fe Cr E F @ e= G9 W ** E h o e=ff Ff ff E F @ e=F Ff
- E E & == W fr 'Y E S T e**r W FP E h Q P= P= P= P= f4 ( I4 P P= P= Psit U f% P=P M P= f% C f% fm P*P= P= tb c ft k P= Pa P= ft V f4 P= P= k P* ft P= fb
== = ee ee == es CCCCCC@ C C C C C> C C= CCCCCC@ CCCCCCC CCCCCCft CCCCCCC
. f%' f 4 f% C FF Fm P= f C t o C O rt etc v 4 fe neV E E f C fe t C ft @ c h ff Pr er 4 @ C 4 C 4 4 L* K 7 C 4
! f4 V' O W 4.= P= pe f\ C U f 4 a= 4 fk f( f( O C 4 o=@ ibf( PP O W 4 f\ 4 f\ f% # C C 4 == 86 4 Ib F*
ceoeoeP W 4e fb@ 8'e oC e e eeeoe a= ee e ee e o == eo e e oe e == e o e e e e * == oe o ee e o
= f4 F C U F P= @ fbft PP C W E P= @ f% ft Pr.C C C P= @ fWitseC S & > O tbf0 *r C C F P. O' f%
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@CCCCCC@ 6CCCCCCP= @ C C C C C C P= @CCCCCCfb PCCCCCCf% @CCCCCCE
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OMEE4VA eoee eoe
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PAEWrNA ee oee ee >=@,AeE eM ee E EeA e > OAEECCA e e e ee o e 8 8"# b I P* @ 4 ** $P PP f% Sm P= @ e e=8r DP % P=P= @ 4 **fr F % C >= @ 4 e6 PP 8e f\ P* P= @ 4 Pfr 8# AP= E @
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== a= C P= C pr f% C ==(P=@Af(C a=P= > W ft C C e= 4 Pm C f\ C C se W P= f\ e- F C a= g P. e ft C C e e eeee e oeee e e e eoee eeo e o e eoe o ee oe e e e e e e e e e e
- P94 ft at O ft C F.4 ft P= 0 >= C Or ef\C O e=C OP 4 f4C @ p= C fe d f4 st O ( C M4ftt3(C k P* P= ft it fb P= > P= fbit t P= P= P= ft ik e= W P P= ft ft f% P= P=h A ft P= P= > P= ft ts C l' A - N A - -
CCCCCC4 CCCCCC4 CCCCCCP= CCCCCC4 CCCCCCE CCCCCCP.
@ 04WV40C s e tt C P= r C O ss fi e=eg C fl* C et P= C 4 C VF0VC4C Fr E > F F ft C
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- P= C eoe eoe o eeeoee o eeee eee eee eee e oe e eee e o eo e e ee F f5 W ft E C C se ftV fte= f4 C pr ft # ft P= m c F FL / ft P= P= C frfL(ft>8rC 8e ft# ft b r C P= P= P= C it - > > P C tb> e= P= P= C f% C P= P= P= C ft c P=P= e= C ft 4 P= h > E % P=
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9 z CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC j ** 4 fr ft 8* tb 4 8' C fr e # fr P= (4 fr fbft ft Ftd a ftpr E P= # E c fife 4 E % E pr == F .f C 4 c h 4 fb e c n em e @ fb e P= f* F e e fi o .c e= r e e ft e P= 4 e e C fse4440 fs a P= e= 4 e=
l 6 e o eoee e o eoe e oe eo eoe e o eeee e eo e ee oe e o e oe oe o e f M AFAUCCG CE Am4CCE4 AF4 Woc 7 AFAOCae AFArC3r
- P= P= > P= 8r C *= AP P. A U.
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- k P* P* P= fLP fb P= P= P= P= fk P* f\ Pm P= r= P= ik C fb M P= P= P= ft 3 ft N N P= P= fk T fV e em Sm P= P=P= . ft f.fb em .= es em CCCCCCC* C C C C C C s= C C C C C C er CCCCCCF CCCCCCW CCCCCC#
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> d O C C f5 fw e=P= C 4 C P= fL 4 P= k P* C F *P= Pr E Pr 4 P= wt > c et er F C 0 C 4 4C t ,C 4 tb
. C r e E P= f( a= C # U C @ PF w C if* F E V rk et C 7 ar P* w A ft C#CC4fte C c e == C == h f%
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>= f P= @ V t e= eP Y W e=4 @ f f%f f 4 t O ftVP= V C f t ,C e @ C O F t >= @ C t id* == C 2 9
- 3 ** V h C P= f ft V 4 f\ C C 4 fb pr v fL C 4 e f% *r f ft C it* O Ps PPV P. C P= r* % Pv d f% C= 3 P= fL'=
kJ e eeee e e e e ee eeo eeeoe ee ee eoe ee ee e e e e e e ee e e oe 3 fb f\ t V C C C ft ft 4 It" ==F e ibf( c V' C = c ft #4 e ( C C C f(ft C # C ft at ft A C ( == 4 W 2 P= P= p= P=pese m P= P. om P= m 4 pr. p= P= P= p= p= 4 se y= P.P= P= pe g er > P= p= P. F or se P.P=P=P=F d m
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e=F P= 4 V # ft ==# V P= == c fb == 8P ad* P= E == C *= P* P= P= # O C e= W fm 4 Pm f\ *= p M 4 T 4 P= O k eoea ee e e o eee oe oe e eeoe oe e oe e e o ee e oe o e ee e e e e f4 fe fb e C 4 nd* f\ F f\ e c 0+ @ fk P.fb e C 4 # f\prft O C # # f\PP f(4 C (# f(9P f4 C C =O t.a M h P= P= F fb e= P= P= P= P= F #. e= > > > > fr ( == P=M r* P= F lt' e= P= P= P= P 8P fk a P= P= P= P= 8r d e=
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=J fbfk E 4 V W ft f\ fbC 4 PP 4 f( ftibt 4 f(saf\ f5 f(C 4 C 4P N f( f5 T 4 C ft f( ft fL E 4 - 4 f(
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f\ VN C 4f wo o C 4 @ P= f\ 4 ,C r @4CCOV40 C 4f%V fO C V f.C 4 P= t @ P= Q C4C0 COCO I 8F F W ( ==C fbit W" M fr Id* ==lt* f( fb CF5e ( CetfkN ft M e @ one= sefb ser e @ f5 W" Fr fb # E 4 V* C fL C tb
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CEOCFwC CE@=EOC Ch@CENC CNOCc4C CCE P O cc CNE4CAC e e ee eee e ee ee ee eeeeeee eee eeee eeeee e e eeeeee e l F em ft @ C pm C f* P= fb 0 C C C FP P= f\ C C == C MP= fb C E ft C F N fbO E / C FkibEOCC k r= P= fb f4 F > > P= ft f% C p r= k re ft C P=m em fr ftP" P=> P= ft tk it P= P > fk f% C f% f% == f\ ft f%
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- C V Ft O f\ Ph e= C f erom e** f% C f 0* N o or f% Cf 0 C w4 ft C at'f* 4 Pm t f\ C C
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- h. 8" V V m2 ftC f C 4 f\ d 4 W (. 49m C # E O ed" F O P= 8r # # 4 e3 c @ e= @ ft / 8e ft F 0 C C U f it fbt F C W fM fb fb C 4 *= P" fV f4 ft E C ft C f% ik fkk 4 4 0 ft ft f% P= 4 4 a ft f\ ft P=( C FP ft eeoe oe e oee eoee oe eeoe o eeoe e ee o eeoe o e eo e o eo e
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) @ 4 e= P= C E 4 C O C 4 k P= # C 4 5 V C 9= C C (@ 4 PF(E C F fb 4 ? C ft c ( PF / 87 4
- C C Pm t ft 7 C C CCCe&ftC C Pa t @ C O C C 4 E==cP=C C Pm E fic e C C P= C 4 7 O C eeoeeee eeeee oe oeoe eee e oe eeee oe ee e e e o e eoe e e I Pr > fL C C 4 C P P= fL C E # C F r. fb t C 4 C P* f= 8% g E C C PP P= fL C C C C F P=f\ E E C C M P= P= ft ft == P= P= P= ft ft m P= P= P f\ f% e P= P= P= ft P. Pr k > P* f\ ft F P= P= k f(ib P=
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CCCCCCV CCCCCCf CCCCCCf CCCCCC't CCCCCCC CCCCCCes
@ r e d m e=> C rCdrC&C W M P* p= 4 ft C e **W==> V C P'.F ft Pr E P* C U P= ft 4 == s- C, Cr*E NCOC C P= E E 7 8F C C4CC@tC C P= C U C
- C C4EECEC C4E;COC eeeoeee oeeoe eo eeoeoeo eeee e o e eoee ee e e e e eee e OP P= ft a P E C fe P* ft C E C C mr= ft C E pm c poem fb& C PC, EeC w P= ft t E >= C P= P= P= ft it C P= P= P= ft it C P= f* P fb ft em P* P* P= ft it P* P P= ft.
P=P=P @fk fk C P= P= rm A ft C
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- C .= e 4 4 4 e eee eeee e eeeo ee oeee ee e eoeee ee ee e oe o e eoee e e e fV 4 == P= P= P= C ft C e=E P= c c fu e ==rm P= C C (b e eh h 3 C fb C -P= h O C P= M r= ft ft C P= P= P= ft Ft p* fb er=e-P=
pm P= ft fte=
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CCCCCC4 CCCCCC4 CCCCCC4 C C C C C C.P= CCCCCC# CCCCCCr*
P= P F pr C F C C ==C ft 'r V 4 C (P= =O e e C V N C -O 8r C - s* C ft C ar C F ** C - I ( C.
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>= 4 C 3 O a= f C O P' 4 C er Pr e- C ere. 4 r= y p= pe ft V C C C / P* fber c g g er / .- E r( g g ; r e C C P* e Fr 7 ft C Q ar C *s f eb CV fLC 4 m ft C C F o=0 4 e= C Q F P= 4 / *= C M ft 4 *J F= == O C ee oe oee e e e o ee e e o ee e e e o ee e e oe eoe oe e e e e e e o ee m 944F744 FALFE44 FA4FCnd FA4Fn>4 WA4Anf4 FA4C>nt g i MMFCAOF WNMCAAF >>>CA4F MMWEA7" Wh>CANF g og e= ft N h m C Ae4.e a= == e=
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>= O C= U C C ft V 7 == ==C P= ft p8 C f4 0 #=C ft e @CP4tF4 C & C*4erft/ E 8r 3 4 4 > C 7 pr F fb C e=E F. F F A C C P"Oo= fe7 == C s- E C ft r e= C ( ft ar' ftCe=CP # ft V
- C
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==ee ft se et C @ e= st a pe P= a p ,er ft F g og e.ce ft F g er g wer f(pr C p= *= v fi er :r # e l hh M P= f4P= fb f= P P= s ft C fb *= r= #m em ft # ft P= P= P=P PF P f\ P P= P= P= ft 4 f(
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** f* P= k r= ftet fV se P= p= > p= fb f% fb es e= P= P= ra ft et ts C es pA. P=MCP= U r=
EN ft ftSf6 ee fm P= r= P= ft tt N ** P= r= r* P= 4 ft fu
** C C C q er= @
80 P' fri fr. M P' N fb ft it' fu N OCCCCCCO 7CCCCCC@ FCCCCCCe OCCCCCCA QCCCCCCa OCCCCCCP h"*VA"CP
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== C @ ( P= pr C C C ir # fk f% 4 C C C ir fr =@ C C -V (fbit C C @ ir F -4 C e oeee eo e ee e o ee ee e ee o e e e e ee e e eeee e o e fr f4 f4 P= 0 PF f=, m 4 ft k a *= C fr 4 fS P= O -C pep = A P= & M C mP= f\ p= 0 P= C P= C > fif\ E P= M P= f4 ft P= P= P= P= ft ft e b e= P= ft ft C P Pm P= fb f4 P
- - N A 4 C C C C C C Pm C C Cc C C C 4 C C C C C C e= CCCCCCV CCCCCCC
@ ftir ==== P= C C ft F ==# C C C pr.4 C C fL C C f\ f% C C @ P C 9e r *= P *t C C C4WOEMC C4E4FwC C4KFEOC C 4 P= C F. C C CLEEOCC eo eoeee eoe oeoe oee e e oe eo e e o ee eoe o e o e fr P= fk E et P= C F h fL E & C C 8P P= f\ E F P= C feP= ft E T 4 C 9P P= A P= E U C k P= r* f4 ft f* P= P= P= ft it 4 P= > P= ft fL FP P=> P= ft f4 C P= P* P= fL fb e
** *= fb' fb fL t CCCCCCP= CCCCCC4 CCCCCCM CCCCCCU CCCCCC#
C erCOe(r*C C C 4 0 *r E C ( E et 4 == ft C F C P= f\ C C C C h C C P= r &
== C 4 fL 4 0 C ==C404CC ==fe 4 C L P G *= m 4 f\ f P= C == ft > 3 If F eoeeeeo e e e ee eo eee o e ea e e e a e e e ee e oe o e fb e == et P= 4 C ib e =P= P= g C fW e *= E P= c C f\ T == C P= == C fbe *=> P= O C i kWMAAN Wh>And >>>AAF MkhAAC Wh>AAA
== *= ik (b (b CCCCCCE CCCCCC4 CCCCCCW CCCCCC4 CCCC C C 4 P. fk e= E ft e- f( C == 4 C o-C V C P= 4 E rb4 7 C 4 # E D O e= C C 4 E f4 E K "
V C C C fr *= C tr 4 C C Ve-C W W C C ft pf" C C C C J C P= C 4WCCCaC eoe e eoe oeoeoee oeeo e oe oee oe oe oeoeeo e e rk V er em f4 C Pr tb # er e= C C Pr ft # Pr P= C C Pr FLV fL P= 0 C F f4 er Pr E / C k M P C f4 P= P= P= P= C ft 4 P= P=> C fier* k e= P= E f4 0 r* P= M C f\ fb e= == tb em f4 CCCCCCC CCCCCCC C C C C C= C C CCCCCCC CCCCCCC e.
P 4 f4 P= ==E C C Pr - P O C P' C 4 C C ft h C F P= C e=0 C E ft r. efe tr 8r J J =*
4 C @ fLir 4 P= - C O rk e C C C C W ft C F # C C e ft CP= e@ C C f(C C V 3 e-6 C, e e o e e e o e oe a e e e oe e e ee e o e e ee e e o e o e e o e m PF fu d C E @ d ** fV 4 F E 4 4 F fb4 F er @ 4 se fb 4 pr t ir tr er ft t ar S P == l F hm>Cade >>5TAVF >>>CAAM NNME47F M N N Z A m 'e g as ** == fb ** f4 h
CCCCCCC C C;C C C C C CCCCCCC CCCCCCC CCCCCCC t= If et O E C C C ar' P= C P= tf # P= fk m. C sL O 4 e= f4 44CC4# P= P= 0 4 e C e-l
, 2' f4 5 ==C F f4 fe f4 V == C C fr *r. A e e-c c e= fr. fg g == C g e.C f( fL g e- C == f(
uJ eee eeo e e oeee ee ee eee e e eoeee oe ee e e e e 3 f\ ft C V C 4 C f5 A C(C Pr sr ft4 4 tf Cir e fs f\ C ir = fs c is ft .e ir - O C
"': h Pm P= P= fr 4 pr P= P= P= > frer PP P= P=P P= pr fk m P= P= P= f= pr @ pr P= > > P= pr == *r 3 a= *= fb e= fk e=
th 2 CCCCCCC CCCCCCC CCCCCCC CCCCCCC CCCCCCC
- W O == O fr f4 4 4 P= Pm 4 er g g g p= P= g g c p= g g pse C Pr g gf p. e g > E pr e C reV P= 4 == C C f\ 4 P= C U 4 C fL U P= 88'fL 4 CPrdP=e=C@
o C ff 4 P= e= w $
4 e e oeoe o eeee e oe ee oe oe e e eo e o eo eoe e e o e e= f4 er fb e C E e f4 Pr f\ t C C o A87 f\ c C -e ft p f% C C P= O f%fr f4 C C if C 4 P= > > P= fr ( *e M P= h P= pr nr == P= P= P= P= F ft == WP=P=> F r - P P=P=pmer . ==
@ ** em fW e= f(
r as CCCCCCS CCCCCC8P CCCCCCe CCCCCCC CCCCCCC 6 M PF **P= fb K P= C Pr.C Pm 4 O C C C E Pm k P= 7 # P= P= == C E e- C C E 4 Lf T 1l* nr
=J ft N 4 V W E ft fl e= 4 ( e= 4 ft ====e= # 3 E ft fb e=P= ( W " %
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es sie fu se fb CCCCCCP= CCCCCCP= CCCCCCM C C C C C C P= CCCCCCC fL . fL / f O a=*P S V E e= # 7 == e9 m Cem C E f4 7 F SP 7 C fL P= C 4 O Pr F
F *"
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e r eee eoe e E e eeoee e @ oee e o e e 0 e eoeee e @ eee o e o e
. O f\ fr C 4 C e* O- C #t pr C C C 8= 0 Cf4*PCCEP=@ C f\ MC O E P* C C Pkfr C C E P= @
ee P= > f= P= fk ft tb es p- P P= P= f% ft tb ee P= P= P= P= fbft tb o* P= P= P= fm f% ft tb ee P= P= > P= fuit tk
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.= seeee ee .= ee e eees .= ee seee s -eee eeee .m Ceeeed ese if 4 E ft.
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7 3 4 5 6 7 8 9 to l $IPOIN733 1 i 90 DFADING A7 7973321005 73.118 73.177
- RANK 1 71.061 673 71.374 77.3%9 77.574 73.777 73.619 77.477 (< ?/
- 4) RANM 7 71.an? 77 51A 74 73.4a7 71.41% 77.A37 77 R1A 77.764 74.6%A 7A.66a 76.773 %
AANM 1 74,ntt 7n.%A1 73.97A 77.91A 78.46A 76.701 75.477 71.qA4 73.179 77.947 r, p>
107 73.A19 74.400 7%.0A0 A7.619 A7.%An 77.989 79.670 78.708 L RAku 4 74.107
% 71 514 PA. 79.0%A PA.7%1 1n.447 11.A93 27.9A0 PA.31T 77.A77 28.cn5 79.7nn CD i
] $) RANM BANM 6 78.n?A 77.4AA n. n. n. O. n. O. n. n.
1 RANW 7 70.779 79.?An 79.794 15.06n 14.76n 36.778 n. O. n. O.
91 OFADING AT 70233 InPn 117 f ($ RANK 1 71.941 77.614 71.374 3%9 77.%7a 73.747 71.7A9 77.a72 73.1na 73 76 741 RANN 7 402 73.9A4 74.457 77 5G% 77 A67 77.70A 77.746 74.696 7A.014 RANK 3 73.n%1 74 70.574 71.978 73 77 774 74 n%# 76.6%) 7%.467 71.9A4 71.159 77.947 RANK 4 73.e47 74.217 73.469 74.M7n 7%.009 A7.619 A7.590 7A.1A9 79.74n 7A.9tA , ,
! ($ RANK 5 7A.794 74.AQ7 2A.717 in.197 31.937 PA.n40 77.477 77.9a7 78.93% 79.17n
. RAnn 6 77.9nA 27.424 n. n. n. O. n. n. n. n. [gg c9 i 9 ANN 7 79.?A7 70.7Ac 79.7A4 1%.070 3a,73n 16 ?no n. n. n. O.
!; GD 97 RE ADItJG AT 79243 3n3% 317 7g RANN j 71.9%4 77.673 71.16A 72 77.964 71.717 73.A69 77.477 74.79A 73 76 971
. 9 ANN 7 73.197 74.%nA 74.437 71.%AS 319 77.847 77.79A 77.74A 74.696 7A.n64 3 7a.n73 7n.903 73.96A 72.477 7a.4%A 76.A71 75.4%7 77.nne 71.169 77.9%?
C) RANK PANK 4 71.n?7 78.717 74.840 74.A7n 7%.119 A7.6t9 A7.610 77.919 79.74n 7A.Ata ,
l 31.731 78.350 77.63n 77.937 7A.01% 70.176 U i AANK 5 PA.AA9 79.t?6 79.at? 3n.717
- n. n.
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i RAnn 7 29.279 29.?A7 79.789 15.17a 14.710 16.7an n. n. n. n.
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. 93 DEADING AT 79733: In%n j RANK 71 72.%93 71.184 77.139 77.974 73.717 73.779 4A2 73.7A8 73.317 7 74 953 19? 71 %74 73.417 73.96% 77.A17 778 77.74A 72 74 716 78.054 76.674
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- NN 3 74 not 70.501 ya.ntA 7p.An7 74.n3A 77 76 791 75.467 71.084 71.170 77.9%7 RANK 4 74.n17 74.147 73.At9 74.750 75.110 A7.679 A7.6?n PA.169 in 9ao Po,pyR 9AN4 5 7A.067 70.776 70.777 in.667 i n . A ,t e PA.nnn 77.739 PA.nn? 7A.945 79.1%n RANF 6 77.755 77.479 n. n. O. n. n. n. n. n.
, Ep 8ANx 7 29.74o 79.77A 79.?An t%.19n 34. Pan 36. pan n. n. n. n.
94 RFADING T 7973381105 71.719 77.477 71.774 747 1 7 933 ,77.6ni 71.378 77.139 77.948 71.707 73,943 7[ g
- ll RANN 7 RANK 7 197 73.494 71.437 73.57% 77.A%7 77.718 77.716 74.AA6 77.994 7A.
8 R A'4M 3 7a.071 70.574 71.96A 77.877 74.43M 7A.671 79.457 71.9%4 71.179 77.917 RAM 4 4 71.nn? 79.372 75,A79 74.Ain 7%,100 A7.6 40 A7.610 78.n59 in. tan 78.8%8
% PA ine 79.4pA 788.107 in.717 t h . A '4 4 77 A19 77.5A1 7A n?? Po.nr% pc.?qn
<> RAN4 RANx A 77.s95 77.quA n. n, a. n. n. n. n. n.
9ANK 7 79.7Al 79.777 79.791 15.h6n 14.776 46.74n n. G. O, n.
95 Rf ADING AT 70733:117n 74.A19 74.7AA
($ RANK t 71.435 77. Ant 71.4%A 77.gte 77.554 74.777 F7.n7p 71.797 RANN 7 73.4A7 74.5nA 74.477 ft.%F5 F7.AIF 17.774 77.7tA F4.APA 7 A . t*% 4 76.774 RANW 4 74.071 7n.SA4 71,99A 77.An7 74.41A 76.671 75.4AF Fl.9ta 71.179 77.947 f 4 77.0%7 74.247 71.A%9 74.Asn 7%.099 A7.A7e A7.Aan 77.770 Po.1A1 pA.518
. () RANW RANM % 74.474 79.416 74.797 in.707 in.964 PA.44n 27.759 DA.nn? PO.n4% 79.360 t RAYN 6 77.A19 77.ata n, n. n n. n. n. n. n, t RANK 7 79.778 70.??7 79.289 1%.37n 34)15n 16,71n n. n. O, n.
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Ch kh LEAK 9 ATE TMSTRU"ENT CAllRRATED DATA 1 7 3 4 5 6 7 A 9 to f$> POINTS i 96 9 FADING AT 702332113%
I RANW t 71.013 7 7.f. n 4 71.1%R 77.349 77,554 74.717 73.619 72,4A1 73.76A 73.297
) () RAN4 7 73,1A2 73.StA 73,477 71.54% 77,A47 77,796 77.73A 74.A%6 7A.034 76,7%3 >
RANK 3 74,0Al 70.514 73,917 77.807 74.449 76,611 75.447 71.914 73.149 77.971 RANT 4 77 74,797 73,869 74.700 ,79,109 A7.669 A7,A10 77,5P9 2A.661 7A.39A 5 PA.947 474 79,236 PA.573 10,737 31.014 74.970 77.774 P7.932 78 08% 79.P50
() RAN4 BANw 6 77.Ais 77,47A o, O. A. O. O. D. O. O.
I RA%M 7 79,740 29.276 29.7A9 1% 750 14,150 16.750 0 O, 0, 0, 97 READING A7 7973331350 71,764
$) RAN4 1 71.933 77.5A3 71.4%A 77.379 77.544 73.707 71.579 72.461 74,666 73.247 77,614 RANK ? 73,477 71,49A 74.417 73,565 77,A%7 77.7%A 77.71A 78.044 I RANK 3 74.0%1 70.50e 71.947 77.A17 74.444 7A,611 75.437 71.914 74.119 77.971 RANW 4 77.977 74.17? 73,449 74,900 75.0G0 A7 A69 A7.630 PR.159 7A.AA1 7R.34A GD RANK 5 77,94% 70,006 PP.374 10,177 34.7A4 PA.440 77.611 27.*17 7A.9A5 79.170 g RANK 6 77.60% 77.134 0, O. O, 0, 0, O. O. O. C23 RANN 7 24.776 29,275 79,777 14.960 14.150 56.740 6 O. O. O.
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77,583 ri.=5A 77.579 77.ss4 75 i97 vi.sa9 77.45: vi.76A 73.2A7
- vi. ass 77,776 111 RANN 7 73.377 73.C44 71,407 74.%%% 77.877 77,74M 74.656 7A.073 77,947 RANK 3 74,011 70,%74 74,417 77.007 74.41R 76,6%) 75.M47 71,M94 71,100 77,
() RANM 4 72,997 74,217 74,A79 74,A10 7%,109 A7.649 A7,650 78.14e PA. API 77.76P GANN 5 79,376 PA 333 10.472 30,504 70.610 77.%51 ?7.907 PM,969 P4.140 RANN 6 74,544165 77, 77.344 6 D. O. O. P. O. O. O.
j RANK 7 79,77A 29.276 29,790 14.940 34.100 36.750 0, O. O. O, j
9 99 # FADING AT 7973321??O RANK 1 71.es3 77,5A3 71,34A 77 139 77.944 73.102 71,%49 72.461 71.7%g 71,p?p i, 9 ANN 7 7t.377 73.%0A 71.407 71,.57% 77.A27 77.7%A 77.716 74,6A6 78.07% 77.7%3
() RANW 3 74.003 70.574 71.497 77,847 74.47A 76,593 7%.437 71.414 71.nA9 77.971 RANK 4 73.017 74.3n? 71,P49 74.A10 7% 100 A7.A79 M7.660 PA.Ata 7A,561 77.9nA RANK 5 78,344 79,146 PA. tat 30.767 30.544 78.940 2i.551 77.M92 po,n?% p9,070 RANN 6 77.715 77.774 0, O. 4 O. O. D. O. O.
49 RAN< 7 79.77a 79.777 re.79i i4.ain =0.700 5A.740 6 D. D. D.
,1 100 READING A7 797333173%
1 71,,933 e77,571 71.34A 77,109 77,544 71.147 73.579 72,451 73.74A 73.277 7] g ll RANF RANM 7 71,167 73.50A 71,417 73.51% 77 A47 77.74A 77.716 74.696 7A,034 77,773 RANN 1 73.491 70.574 71,477 77.477 74,4TA 76.611 7%.477 71.034 71.109 77,A91
- RANK 4 74,667 74,757 71,749 74.A10 7%,644 M7.670 R7.A70 74,400 PP.961 78,7%A S 78.A03 79 *16 7P,597 40,77? 31,741 79.611 29,197 77,A77 70.075 70.140
. c) RANK aAN< A 77 a76 77,77A 0 n. 4 O. O. O, n. O.
RAN4 7 79.774 79.776 70.773 14,490 44.100 16.160 6 O, 0, 0, 101 9FA0!Nr. 77 7923331750 1 71,911 77.554 78.51A 77.790 77.%18 71.707 74.A49 77.481 73.7%m 7=,77p
! () RAN4 HANK ? 71,167 74.49A 73.407 74,00M 71.Sn%
77,77A 77.A%7 77.7tA 77.706 7%,477 74.A7A 71.974 7/.QAM 73,100 7A.477 77.901 i AANK 1 74,011 70,544 74.n/m 76.541 pp,nsa 3ANW 4 77,ngy yg,pMy 71,Apg ya,ygn 7%,nqq A7,A79 ap,7go 77,qqo pm,73g 79.Sul th.hpl 47.nnd /4.FS1 ph.6mn 77.367 Pa.0SS 79,1 to
() R A N4 % PM.tt% 74.476 0,
. RAhM A 7A.066 77,44M 0, O. O. O. 4 O. O, eAN< 7 Pa.777 Pa.pr6 Pa.7a0 i4.A90 34.160 is.iAO 0 O. O. D.
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N kh 4 (FAK RATE INSTRUMFNT CALIRRATFO DATA d> POINTS 2 1 7 3 4 5 6 7 8 9 10 107 PEADING AT 79233 130% 71.579 72.4%1 73.74R 73.272 71.074 77.573 71.3%A 77.799 7?.574 73,177 l> AANK AAMK ?
1 71.1%7 73.49A 73.407 73.49% 77.7P7 77.648 77.7tA 74.696 77.041 76.674 77.971
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77.A67 74.41A 7%.417 71.974 73.119 i
RANK 3 RANK 4 74.011 77.977 70.574 74.172 73.937 71.Ac9 74.P00 099 75.%51 17 76.snt A7.714 78.390 A7.A90 78.3P7 77.869 77.862 78.9At 70.n65 77.74A 79.170
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9ANK 7 74.777 79.276 29.2A0 14.910 34.090 36.100 0 O. G. G.
103 READING AT 70213:1320 77.451 73.74A 73.767 l> RANK 1 71.911 77.571 71.368 77.799 77.574 71.147 73.589 73.357 73.46p 73.495 77.787 77.67A 77.706 74.6A6 77.Q63 76.574 RANK 7 RANK 3 74.011 70.514 71.197 71.gom 77.A67 74.7AO 74.41A 7%.049 76.603 97.779 79,417 A7.710 71.gra 78.479 71.049 70.770 77.911 PA.4AA
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l 4 77.9A7 74.097 73.A59 78.410 77.7R9 77. SAP 79.03% 70.170 cgj RANK % PP 794 78.947 7P.534 14.107 11.097 s
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PANK A 77.41A 0 O, O. 6 77.906 O. O. O.
! RANK 7 79.774 79.775 79.7P6 14.930 1n.0A0 16.270 C.
() 144 DFADING A7 79233:1345 b:9 th RANK 1 71.914 77.513 71.319 789 77.%74 73.177 74.%74 7?.4%1 73.74A 73.767 i i e
' RANW 7 73.357 74.49A 75.197 77 71 535 77.757 77.778 77.706 74.646 7P.023 76.643 3 71.001 70.%I4 71.9 A A 77.71A 74.40A 76.591 75, 407 71.014 73.049 77.011 l l> RANK eA~K 4 77.oir 74.777 7s.A09 14.170 7%.099 A7.719 A 700 Pa.269 so.4A9 77.9,e j RANK 5 pm,%%3 j9,066 po, pap 30,472 30.814 78.750 77.507 77.0%? 7R.945 20.130 RANK 6 77.795 77.49A 0 G. D. G. O. 4 4 O.
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; R A ta K 7 74.777 29.275 29.2AA 14.410 14.110 16.1A0 0 O. h 105 RFADING AT 74733:1150 73.569 77.441 71.71R R7NK 1 71.973 77.543 79.31A 77.7A9 77.574 73.167 73.767 RANK 7 147 73.4M8 73.187 73.405 77.877 77.73R 77.646 74.676 77.963 76.604 5 CD R A *JK 3 73 73 941 70.514 73.897 77.716 74.M9A 76.651 75.407 71.944 71.099 77.411
- RANK 4 71 74.177 73.799 74.7%0 7%.0Ao A7.719 A7.710 77.880 74.700 74,475 7R.96A RANK 5 74 .A41 077 79.416 79.747 30.777 10.44% 77.749 77.174 77.977 74.044 O. O. O. O. p. O. 4 O.
6 77.79% 77. 4%m
- n. O. O. D.
RANK 7 79.773 79.774 29.767 14.970 34.170 4A.lR0 ll>944K
; 106 READING AT 19733:1405 73.1A7 74.579 77.411 73.774 ffl 1 74.903 e77,543 73.144 77.7A9 77.414 73.?67
! l> AANA RANK ? 73.147 71.4AA 73.187 71.49% 77 M77 72.67A 77.AP6 74.696 77.941 76.863
] HANK 3 71.811 70.514 71.027 77.716 74.t"A 76.571 7%.107 78.A84 73.0A9 77.011 5 RAMK 4 77.477 74.097 7 4.H 70 74.M10 74.0M9 Rd.779 A7.710 77.470 PM.A01 78.61A
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75.?A7 71.714 77.691 RANK 1 74.761 70.355 71.A77 77.696 7a.76A 7A.161 77.914 i RANN 4 77.747 74.n97 7T.674 74.770 75.n%D R7.769 A7.040 77.040 PM.A91 77.90s I () HANN 5 7A.593 79.n46 70.377 31.141 (n.45% PA.4no 71.74n 77.6%7 7A.9%% 70.140 RANF 6 77 %A4 77.746 n. O. O, O. D. O. p. O.
9 RANM 7 79.749 79.767 15.140 14.110 16.150 0, 0, 0, 0, 79.?55 1
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$> Pn f N 7 3 'l i 2 1 4 % A 7 4 9 to 156 READING A7 79714:0739 73.n17 73.439 72.311 73.06A 71.117 l RANN 1 71.793 77.164 71.749 77.119 77.364 77.A73 79.161 (D R A *!M 7 75.191 71.114 71.777 73.115 77.5A7 72.508 77.536 74.476 77.6P1 74.778 76.191 7%.7A7 72.P99 71.647 77.6A5 h )
RANK 1 71.7Al 70.14% 71.714 PANK 4 77.7A7 74.102 71.659 74.710 7%.056 A7.769 A7.990 2A.0A9 PR m71 77.47A RANK % 7A,174 79.016 79.597 10.647 10.754 7A.750 77.70% 77.617 7A.975 79.140
(> nANK 6 77.574 77.75A n. n. n. a. o. a. n. a. Q__;)
RANN 7 29.2%S 79.749 24.751 15.760 14.730 36.170 0 O. p. O.
I 157 READING AT 79234207%n 73.599 72.311 73.06A 73.107 i G) RANN 1 71.793 77.354 71.778 71,p17 77.109 73,33g 77.144 yp,6g7 73.012 77,56A 77.51A 74.446 77.471 An.411 i R AtIW 7 73.1Rt 74.*nA PN RANM 4 71.871 70.35% 74.677 77.474 74.74A 76.491 7%.7A7 71.714 77.910 77.671 e 4 77.717 7c.077 71.6%9 74.77o 75,06n Al.7%9 87.970 78.059 7A.741 77.76A
() RANK RANM S PP 794 7 A . A 17 PP.191 30.767 31.044 28.9%n 27.444 77.612 78.97% 79.32n j RAN4 6 77.77A n, n. n. p. P. G. D A.
. eAN. 7 ,77.574 9.253 79.e64 19.75 1%.750 34.,50 3e.i70 e. o. y... O.
0C fd) 15A READING AT 797343030%
94NN 1 71.7A3 77.354 71.7tA 72.109 77.444 77.997 73.%79 72.301 71.079 71.107 RANK 7 73.1Al 71.118 73.717 71.11% 77.607 77.578 77.54A 74.446 77.761 80.401 3 73.771 70.365 74.677 77.914 74.769 Th.4A* 75.787 71.714 77.919 77.691
() RRANN APIK4 7?.7 17 71.097 73.A%9 74.7A0 7%.n60 91.714 A7.9An 77.549 78.nA7 77.61A nA6K % Pa.i7s Pa.977 pa.555 30.477 =n.664 74.%40 PA.ips 27.6aa 7A.9A% 79.i70 BAMM 6 77.574 77.77A n. G. 6 O. O. G. n. O.
19.06n 34.770 sh. pin n. D. O. D. h e 159 READING29.751 9ANK 7 t 29.749 24.751 AT 792342nT7n 109 77.144 73.002 73.149 77.311 71.nAA 73.097 RANM 1 71.7A3 77.354 71.734 77.51A 77.7A3 RANK 7 1R1 71.41A 73.717 77 73 13% 77.%A7 77.536 74.446 A1.100
() RANN 1 71 73 7M1 70.31% 71. A 4 7 77.675 74.77A 76.551 75.777 71.714 77.909 77.701 AANK 4 77.767 74.10? 71.659 74.R00 75.0%n A1.760 A1.000 77 R79 77.777 77.97A BANK % PP lR4 70.766 7A.493 10.%77 in.A04 79.191 74.%%D 77.567 7A.90% 79.79n RANF 6 77.66% 77.76A n, n. O. O. D. O. D. O.
E3 BANS 7 29.e57 79.2%) 79.763 1%.nao 34.79n 36.700 n. n. O. n.
16n READING AT 792342013% 73.519 72.301 71.678 73.097 AAN4 1 7f.773 77.194 71.74A 77.n99 77.134 71.0np A7.059 [ l
$) RANK 7 71.tAl ,73.378 74.777 74.3%% 77.5A7 77.548 77.51A 74.446 77.744 R A t?M 1 71.871 70.455 73.677 77.A7% 74.75A 76.471 7%.7A7 71.774 77.879 77.A41 MAFK 4 77.717 74.747 71.659 74.71n 7%.nsn 9n.ono A7.9an PA.np9 77.967 77.714
% PP.714 74.6A6 pa.441 to.707 g o . 8' t h 79.771 ?>.774 77.497 PM.95% 79.190
() 9tNK aANn A 77.an% 77.<ia o. n. n. n. n. D. c. a.
AAN4 7 70.7%3 79.749 79.767 1%.114 44.799 16.16n n. O. 6 D.
I 161 UEADINC AT 79714to1%n 71,p64 7p.040 7p,414 77,9mp 71,%40 77.7M1 74.46A 71.nR7 E G) RANK 1 71.744 7p,1%g 77.%97 77.4M9 77.%3A 74.4th 77.AR1 A7.770 RANK 7 71.941 71.11M 74.717 71.49%
R A ke t i 71.791 70.47% 71.647 77.579 74.71A 76.441 7%.7%7 71.7%4 77.949 77.7nt RANN 4 77.767 71.092 71.649 74.440 7%.n%9 al.n70 A7.99n 77. tan pp.1A1 77.97A
() RANK % 78.774 79.166 PR.1A1 10.7%7 18.113 79.001 78.154 77.4M7 78.03% 79.170 RAN4 A PR nP6 77.4AA n. n. p. n. n. o. n, O.
3 s 6ANK 7 74.750 29.747 29.750 15.070 14.770 36.770 4 n. c. o.
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LF4x RATF INStoquEP7 CALIRRATFD DATA I (poo!NTS: I ? 3 4 5 6 7 8 9 in 162 RFanthG AT 79734:na0% 77.291 73.0%R 71.n72 C3 RANE I 71.771 77.344 71.PIR 77.n49 77.37a 77.997 71.a69 l $$ RAAM 7 71.961 71.11 A 73.707 71.145 77.%77 77.91A 77.%?A 7a.416 77.771 A4.049 RANM i 71.731 7n.17% 71.617 77.494 74.7%A 76.171 75.757 71.60A 77.mA0 77.A71 I 9ANM 4 77.747 74.787 71,609 74. Mon 75.n40 79.Aln A7.490 77.410 79.111 77.a78 RANN % 28.175 79.n16 2A.nM1 3n.6np 11.A47 ps.7An 27.84A 77.572 78.8R5 79.750 C 23 g (p sANx 6 77.996 77.iin n. n. n. p. n. O. n. n.
- BANA 7 20.25n 70.734 29.751 15.07n 14.376 16.180 0. O. O. n. C3 q 163 RFADING AT 7923a n4pn 1 l$ BANK 1 71.761 77.174 71.7nA 77.n99 77.374 77.907 71 %70 72.701 73.n6A 73.nRP J RANK 2 71.17A 71.717 71.14% 77.677 72 %%A 77.516 74.a%6 77.AP1 87.679 C223 RANM 3 73 71 771171 7n.19% 71.677 72.615 74.794 76.1%l 75.767 71.744 77.On9 77.609 J 71.A79 7%.n70 An.n70 77.87a 79,7pg pp,n%A
- RANK 4 77.817 74.007 7a. man n?.970 7A.p?A 79.770 8
RAMW % 78.173 78.777 70.777 30.1m? 17,gsp 7A,gan p7. cap 77.947 c ::3 1 ll =ANw 6 77.R7% 77. inn n. n p. n. n. O. n. n.
, eANx 7 pa.7%i 79.7%n Pa.754 15.n30 34.14n 16.ain n. o. O. O. gjyjg l @ 164 READING AT 79714:nals C
- BANN 1 71.741 77.174 71.77A 77.nA9 77,174 77.907 71.494 72.793 71,n%R 71.nA2 AANM 7 71.1A1 73.17R 71.??7 71.17% 77.%97 77.578 77.576 74.416 77.751 Rt.470 g 9ANK 1 71.761 70.17% 71.6n7 77.61% 74.7%P 76.171 7%.767 71.714 77.890 77 A41 CP"
? (I PANK 4 77.787 74.167 71.669 74.M40 75.n60 A1.170 81.07a 77.719 30 n90 78.5%M RANK % pm.a64 2m.847 70.1g7 in.467 31.a11 74.4%0 77.161 77.617 PA.77A 79.?6A l BANT 6 77.71% 77.77A n. n. n. n. n. n. n. n.
7 29.pa9 29.247 29.251 15.040 14.79n 36.21n n. n. O. n.
2
(> BAN 4
- 16% READING AT 79714:n4%n
; RAMM f 71.773 77.T74 71.714 77.0A9 77.114 77.947 71.6%9 77.741 71.n%R 73.nA7
; RANK ? 75.158 73.748 71.197 71.1n% 77.567 7p.518 77.a96 74.4p6 77.711 at,5%n GD RANM 1 71.711 7n.11% 71.576 77.59% 74.?an 76.191 75.747 71.644 77 RM9 77.A71 RANN a 77.7A7 74.7a7 7 4. A 49 74.84n 7%.n4n R/ 999 A1.n?n 77.M79 in.1%n 77.9AA RANK % 7P.74a 7A.967 70.712 in.1R7 in.554 24.19n 77.175 77.647 PR.P7% 79.?%n
; nANx 6 77.66% 77.74s n. n. n. n. n. n. n. n.
7 29.748 79.24% 79.760 15.070 14.16n 36.24n n. O. n, n.
J (I RANK 1A6 9FADTNG 47 79234:090% 77.9A7 71.499 77.771 71.n14 73.0%7 ffg l R AfJK 1 71,. 7 T3 a77.344 71,7am 77.n69 77.104 77.761 74.477 (h RANK 7 71.1%l 71.7%M 71.147 71.1n9 77.An7 77.518 77.446 74.an6 77.611 g
BANN 1 71.761 in.11% 71.%o7 77.606 74.744 7A.791 75.7%7 71.Ama 77.879 RANN 4 77.777 73.9A2 71.670 76.7A0 75. nan 47.5%9 ni,onn 77.496 po.apn 76 t nA
% 7P.a14 74.716 79.757 18.777 19.1A% 77.770 77.7%% #7.657 78.OnE 74.97n
() RANM nan < 6 77.An% n. n. n. n. n. n. n. n.
. =ANM 7 Pa. Pas 7 7 . 7 a n.
7 .74 79.7%= i%. nan to.=7n 16.7:n n. n. n. A.
167 RFADING AT 79?14:n%70
, () aann RANM 7 i ri.753 148 77.ii4 71.i9a 77.n7a 17%
77.ina 77.%77 77.aa?
77 aMA 71.apa 77.486 77.Pai 74.en6 ri.nta 77.771
- 71. n A.-
77.171 t 71.74A 71.177
, RANK 1 71 71 791 7n.7%% 71.59A 71 77 574 7a.p3s 76,17g 7%.747 71.664 77.pt9 77 A11 pm, nap RANN 4 77,AA7 74,11@ 74.669 74.7An 7% nnn m7,Ae9 m7,90n 77,j1n pp,771
() RANN % pn.Ani 79.776 Pa. top in #,5 7 54. 47% da.ogn 77.a21 7 7.6 =7 78.9a% 74.p?n g
SAMK 6 77.%44 77.778 n. n. n. n. n. n. n. H.
- n. n.
. BANK 7 24.7a8 20.744 70.247 t%.len 38.17n 16.2%n O. O.
4 O B-46 40
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en I LEAM RATF INSTpHwENT CALTRRATFD DATA 2 3 4 5 6 7 8 9 to l $ POINTS: 1 144 PEADING AT 7923430%34 7P.7At 73.6%7 77.957 73.304 AANK 1 71.743 77.164 71.718 77.669 77.314 71.naA l 77.e96 4 j$ 9ANK 7 71.tal 71.75A 73.147 73.315 77.957 77.508 74.466 77.671 77.373 RAN4 3 71.741 70.2A% 73.576 77.615 74.778 76.141 75.747 71.654 77.8%o 77.611
- AANK 4 77.677 74.102 73.559 7a.790 79.n7n 07.An9 87.900 77.710 7A.791 77.7A8 9ANM 5 174 79.0A6 PA 573 in. net in.46s 78.460 77.191 77.547 28.975 ?*.710
-l Ep RAN< 6 7A.sna 77 77.2an O. O. n. O. n. O. O. O.
n.
l RANK 7 79.746 79.742 29.256 15.240 34.T90 16.730 n. O. G.
lA9 RE40TNG A7 79214:0550 77.271 73.03R
() RANN t 71.743 77.114 71.714 77.069 77.Tne 77,977 71.599 73.057 PANN 7 111 71.718 71.177 73.115 77.537 77.578 77.476 74.a?6 77.761 7A.943 g
RANN 3 73 751 74 70.745 74.976 77.431 7a.778 76.7A1 75.717 71.614 77 Mao 77.661 g77-3 i 4 77.667 74.067 71.619 716 7%.n3a R7.499 R7.0Pn 77.979 78 %ht 77.51A .
ll RAPM RAN4 5 7A.065 7A.597 78.701 74 30 512 3n.455 78.480 77.77% 77.537 28.*t5 79.770 RAH 4 6 444 77.71A 0 O, n. n. A. O, D. O. M BANM 7 77 745 79 79.742 29.744 15. Pan 34.160 1A.270 C. O. n. n.
! $ 170 RFADING A7 707142060% 77.9%7 77.771 73.n?R 71.n47
} AANK 1 71.753 72.244 71.1AA 77.049 77.7A4 71.569 l RAND 7 73.111 71.114 73.167 71.13% 77.577 77.518 77.4A6 74.406 77.701 76.A73 g RANK 3 73.731 70.7A5 71.516 77.411 74.77A 76.471 75.717 71.614 77.A30 77.6))
*3 () 9AN4 4 77.707 74.0%7 71.999 74. Ann 7%.046 A7.069 83.070 77.919 PA.441 77.0AM RANK 5 77.475 78.577 78.141 in.417 30.745 7A.9A4 77.193 77.572 78.816 79.280 j RANK A 77.a64 77.199 n. O. O. D. O. O. O. O.
RANM 7 79.747 79.743 79.756 ja 710 3a.140 16.7A0 n. n, n. n,
, El 173 READING AT 7973430670 73.570 77.771 73.057 RAN4 1 71.7%3 ??.3na 71.7pA 77.079 77.4n4 77.967 73.014 RAN4 7 111 71.268 74.167 71.305 77.%47 77.%7P 77.44A 7a.476 77.A53 7A.66a
.I () RAN4 3 13 771 71 7b.795 71.%16 77.5e4 78.73A 76.761 7%.74? 71.6a4 77.pa9 72.641 l 9tNM 4 ??.Jo7 78.117 73.579 74,P16 75.04n A7.9P9 A1.n50 74.0%9 7A 771 77.49A QANN 5 77.4%5 79.1J6 77.441 10.%37 in. jus 78. Fan 27. ant 77.%77 78.AQ% 79.1%0 RANN 6 77.4ha 77.17A 4 O. n. O. n. O. n. n.
{ () RANK 7 74.pah 29.244 29.759 14.970 18.16n 1A.740 n. O. O. n.
177 READING LT 7923420645 77,704 77,957 73,A19 77,771 73 n3A 73 RANN t 71 713 ,77.114 71.19A 77.n%0 77 0%7
(( g 3 $ RANK ? 7l.131 71.77A 71.157 73.1n5 77.%97 77.498 77.486 74.476 77.643 171 j RANK 3 71. Mat 70.795 71.607 77.514 74.774 76,1nt 75.777 71.664 77.A49 77.611 1 RANK A 77.777 74.017 74.619 74.670 7%.n%n A7.079 $1.070 78.779 74.1A1 7A.ntA RANM % 74.474 70.436 78.1%t 16.767 in.a15 74.743 7A.11C 77.%17 78.03% 70.016 j) RANK A 27.64% 77.19A o, n. n. n. p. n. n. n.
9 A P'M 7 74.74u 79.7%4 t%.14n in.ptn (f. 7nn n, o, q, 0, 70.74h 171 RFADING AT 7973420694 73.41R 71.n%7
- 4) SAN 4 1 71.753 77.504 71.19A 77.059 77.1n4 77.957 73.730 77.771 RANN 7 74.111 73.788 71.tA7 7 't . 7 4 % 77.5%7 77.4AA 77.4A6 7a.366 77.A91 7P.757 HAMM 3 71.641 70.405 71.%A6 77.Al% 74.71M 76.749 7%.777 71.664 77.P 49 77.671 RAHA a 77.707 74.147 74.%79 74.796 7%.can at.n?9 AS.ppo 77.6A4 7p 771 77.798 I () RANW 5 7M.4A4 70.776 7A.771 19.77? to.ana Pa.%61 7A.Anq 77 %17 74.90% 79.070 0 RANK 6 77.77% 77.79A n. n. O, n. c. O, n. O.
1 RAN4 7 70.747 79.745 29.757 15.000 14.190 36.260 6 D. O. G.
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CCCCCCC CCCCCCC C C C C' C C C CCCCCCC CCCCLCC CCCCCCC
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AANM p 77,o41 71,n77 71 77 9e7 71.1n% 7p,aA7 77.17A 77.17A 7a,7%4 77,a%1 mi.774 77,41A PANK 1 71.A71 76.nmA 71.144 77.191 7a.pMA 76,001 7%.na7 71.453 77.449
! R A ff 4 4 77,a47 74.017 74.368 74.77n 74.91n AD.1%n A7.7An 77.770 78.7At 77.6%A
; AANn 5 pa.1:a 7A.a77 79.iA7 in.4%7 in.7As 7A.nta 77.cor 77.sa? Pa.79A pa.n?n
. (I RANK 6 77.1a1 77.04A 6 4 6 n. p. n. 6 D.
8Aun 7 79.i9i 79.isA 79.i91 i4.7tn in.7sn 16.ian n. D. p. n. q___3 I 77A READING A7 79714!?n1% C3 4 () RANK 1 71,671 77.11e 71.n%m 71 A49 77,114 77,7m? 71.4S9 77.17n 77,8A9 77,887
{ RANM 7 77,4%t 74.077 77,907 71.09% 77.147 77.70A 77,1#A 74.776 77.e51 7A.A71 I RANN 1 71,A11 70.09A 71.7A6 77.149 74,964 76,191 7% n77 71.411 77.679 77.aon i MANK a ??.%e7 74,nna 71,s?A 74,Amo 7 4 o n t. M7.619 RP.71n 77,4>9 Pn.4%1 77.438 i () MAWM % 77,4A% 72.%97 79.701 10.a97 in,17% 77,A%9 77,tna 77.%07 78.pnA 79.n6A ,
HANK 6 77. int 77.nGA n, p. 6, n, n, p. O, n, j RANN 7 7n.190 79.tM5 74,107 14.616 14,7tn 1A.7An 6 O. n. D. )P5/(
l d) 779 RFAOING A7 74714 70%D RANK 1 79, Ant 77.174 73.n99 71,970 77,114 77.7n7 71,149 77.179 77.aA4 77,87p J, RANK 7 77.411 71 n47 77.9R7 71 e4% 77,497 77,t%8 77,1n6 74.746 77,aji 77,671 g, 7a,nAA 7A.111 7%.nt? 71.ett 77,614 77,aan U RaffW 1 74,6n1 7n.996 71 4%A 77,191
() A Af tM 4 77.417 71.917 71.17A 74.690 74.unn qp,Apg m7.770 77.6A9 78.7%1 76.94A g
RANN 5 77.6t6 7H.177 77.011 in.507 30.715 77.749 76.998 77.a72 78.74A 79.07n
;, AAHW A 77,771 77.0%m n, o, n. n, p. A. n, o, D.
e RANM 7 79,189 79.1A1 79.194 14.560 14.736 16. ten A. O. 6 8 h 1
73n RFADING A7 70714!710%
I R A PIM 1 71.611 77.144 71.n14 71.AA9 77.tte 77.777 71,149 77.14A 77.M70 77,867 i RANN 7 77,941 71,0A7 77.987 71.DAS 77,107 77.tlA 77.4nA 74,7%4 77.441 AD.Rin j () .
RANK 1 RANN 4 71.Att 77,a%7 70,n7%
71 ufp 71.116 74,199 77.377 7a 7n0 74 nem
- 74. mon 76.091 pt,An0 74.007 47,Agn 71.ett 77,729 77.614 77 A97 77.190 77.048 70,e80 j RANK'% 77.AeA 7A.147 77.801 an.7ep 10.14% 77,844 77,n77 77,as? pm,696 RANM 6 77.7%1 7A.97A n. n. n. n, n. 0 n. n.
() RANN 7 Po.tAA 79.191 79.10e to.610 in.710 16.100 n. i. n. n.
I h ', s i tr i 4
lO 1
1 Io a
e B-73
". (3
( PLOT OF f!RE* MSS Ptti SF fint*fui STEBOL Ult 0 Il e STRIOL UlES 15 0
*( TIA4
- 673 * *O
( 449 + e 0 643
- e 8
( te 430 e
( 4tl
- O e ett
- Go
( I
; as * . t e - sie .
. O 135 *
- O
( mm m see 0 .
9 y -
( 523
- 0 e
@@ w .. n g
110
- O e
( 0 49s
- 8 e
- 4te
- e 8 f 465
- Oe 454
- O e 435
- 0 e 429 * *e 445 *
- O ltt
- Go 175
- 0 e 348
- e 0 345
- 8 e 338 + e 0
. 315
- O e 4 h
- n.
- Os a 285
- Se 270 *
- 8 235 *
- 0 248
- e 0 22S
- 0 e 2:0
- e 693
- 0 e 189
- e 0 tel
- Os 150 *
- 0 133
- 0e
, 120
- e 0 .
143 *
- 0 99 *
- 0 73
- e 0 et
- e 43
- 0 e 30 + 0 e r-1708 169
(
0.9996 0.9908 0.9999 9.9992 0.9994 0.9994 9.ft90 f.6004 0.0002 f.0004
m APPENDIX C CHRONOLOGY OF MAJOR TEST EVENTS e
e E 1708 166
APPENDIX C Minutes of Major Test Events DATE / TIME -
m.
i 1/23/79 0800 Decision was made to perform ILRT with$'ut ice on the Ice Condenser. Present schedule called for the test to be conducted on the second week of August 1979.
7/25/79 0900 Began preparing for ILRT per TP/1/A/1200/06.
Organize team to assure 24-hour coverage for test activities. Assign personnel for eatn specific activity during the test.
7/27/79 1600 TP/1/A/1200/06 procedure got final approval from Station Review Committee. Sent one copy to NRC Inspector.
7/30/79 0800 Sent all test personnel assigned to enter building under pressure to have physical checkup to ensure physical fitness as required by safety procedure.
7/31/79 1000 Performed Isolation Valve Verification. All isolation valves were checked to ensure they were operable.
7/31/79 1300 Verified an outstanding Work Request and shutdown request form to ensure all isolation valves were free of any outstanding work which might affect valve operation.
8/02/79 0800 Completed test instrument installation and check-out. Work on computer terminal was in progress.
8/03/79 1200 Maintenance crew identified major deficiencies existed on normal and emergency personnel air lock that prevented the Class "C" leak test be perfo rmed. Decision was made to isolate both hatches. Hatches were temporarily fixed and a temporary leak test (TT/1/A/9100/It) will be performed to ensure that hatches could provide a temporary leak-tight barrier for the ILRT.
[ '
Commitments were made to perform Class _"C" leak test after hatch deficiencies were corrected.
The test difference between this test and TT/1/A/9100/14 test will be added to th,e ILRT result.
1708 167 C-1
DATE / TIME 8/07/79 1800 Completed isolating and performir g temporary leak test on personnel hatches. (TT/1/A/9100/14 proce-dure). Normal batch leak rate was 1300 scem.
Emergency was 900 secm. This was evaltrated as acceptable for ILRT test.
{ 3 S/14/79 0830 Solid state protection system was de-energized to ensure that plant equipment was not activated by high containment pressure.
8/14/79 0935 Final check on test instrument completed.
8/14/79 0935 Closed both normal and emergency hatches. Paged all personnel to clear the building.
8/14/79 0945 Began pressurizing the building.
8/14/79 1115 Reached 1 psig. Detected pressure line of pressure sensor inside the Ice Condenser froze.
8/14/79 1200 Sent personnel in to fix and clear pressure tubing.
8/14/79 1345 Completed fixing pressure sensor. Resumed pressuriz-ing.
8/15/79 0440 Reached 10 psig.
8/15/79 0530 Started visual inspection to detect obvious leak.
8/15/79 0945 Detected significant leak around the joint where concrete base and steel vessel joins.
8/15/79 1100 Sent men in to inspect the cathodic penetration which penetrates the steel base liner. Suspected the plug in the cathodic penetration was left opened which provided a leak path to the concrete base and secped out the joint.
8/15/79 1200 Men confirmed that prediction was right.
8/15/79 1350 Temporarily plugged the penetration to verify leak stopped.
8/15/79 1451 All leaks stopped. Decided to permanently seal weld g the plug. ,
8/15/79 1900 Completed seal welding the plug. -
8/15/79 1910 Resumed pressurizing the building to t'h'e structural integrity test pressure.
1708 168 C-2
DATE / TIME 8/16/79 0705 Reached 16.875 psig (gauge read 32.22 psia).
Began 10-minute holding periods.
8/16/79 0828 Started depressurizing to 13.5 psig for
{ inspection. ;
8/16/79 1105 Reached 13.5 psig.
8/16/79 1235 Started structural integri.cy inspection.
8/16/79 1400 Ended structural integrity inspection.
8/16/79 1420 Pegan bringing pressure to 14.8 psig.
8/16/79 1936 Reached 14.8 psig.
8/16/79 2204 Completed soap bubble test of hot penetrations.
No leak detected.
8/16/79 2400 NRC Inspector requested that air penetrations, which were still not isolated and vented, to be vented to avoid inleakage to the building.
He also requested all RTD's weighed volume fraction value to be changed to reflect no ice condition which increased the net-free volume of the building.
He also requested that the test be performed at higher than 14.8 psig to ensure that at the end of the test, test pressure did not drop below 14.8 psig.
8/17/79 0400 Temperature profile indicated that temperature was stable. ILRT test was not initiated until all inquiries of the NRC inspectors were satisfied.
Identified various problems in computer program.
Corrections were carried out and benchmarking the program was under way.
8/17/79 0840 Sent men in the building to:
- remove all RTD's in the upper plenum of the Ice Condenser away from the AHU's to avoid the latent heat in defrost cycle.
- Inspect tubing on door seal for leaks. -
8/17/79 1130 Completed removal of RTD's to new location.
Detect M h aks on door seal air tubing'.'
1708 169
!i-3
DATE / TIME 8/18/79 0800 Generated new RTD's volume weighted value for Ice Condenser RTD.
8/18/79 0900 Benchmark computer program continued. -
3/19/79 0300 Began to vent the air penetration which was used to pressurize the Ice Condenser to prevent air frort entering building.
8/19/79 1145 Began to vent the air penetration which was used to pressurize the lower containment to prevent air from entering the building.
8/19/79 1520 Depressurized building to <14.8, and sent personnel in to stop leak on door seal and fix 1 RTD.
8/19/79 1640 Men entered building.
8/19/79 2319 Work completed. Men exited building.
8/20/79 0115 Began to pressurize building to 14.98 psig. .
8/20/79 0500 Reached test pressure of 29.400 psia. Isolated all air penetrations.
8/20/79 0700 Seals of Reactor side door of normal personnel air lock deflated. Used Aux. Building side door as pressure boundary.
Pressure dropped to 14.8 psig because of this leak.
8/20/79 0855 Repressurized building to 14,90 psig.
8/20/79 1110 Reached 14.98 psig.
8/20/79 1120 Restarted the test; began at Step 12.21b to TP/1/A/1200/06.
8/20/79 1550 Completed 4 hour stabilization.
8/20/79 1600 Began 24 hour test.
8/20/79 2300 The inner seal of normal air lock deflated. Used
; Aux. Bldg. door as test boundary.
$/21/70 0700 The inner seal of Emergency Door leaked. Shift personnel report to vent door every 15-minutes.
8/21/79 0705 Ordered not to vent door any more. DeIided to restart 24-hour test at this time to ensure a reliable start for 24-hour test.
c., 1708 170
DATE / TIME 8/22/79 0705 Completed 24 hour test. Pressure dropped to 14.89 PSIG. Leak rate recorded .1070897%/ day, with 95% confidence value at .1136596%/ day.
8/22/79 0940 Began imposed leak test 7,
-8/22/79 2115 Leak rate registered at LT = .2824652%/ day.
Calculated value L T ~b am and saw that it meets the Acceptance Criteria. Also investigated the trend of the leak rate and saw that it stabilized.
8/22/79 2146 Discussed the result with NRC Inspector and en-sured that there were not any disagreements on the interpretation of the results.
Decided that ILRT has been satisfactorily completed.
8/22/79 2205 Depressurized the building 8/23/79 1230 Opened the building for NRC Inspector to inspect Reactor side valve line up.
8/23/79 1500 Completed inspection of Containment Vessel and no visual damage was noticed.
8/23/79 1515 NRC Inspectors identified two discrepancies in valve line up. 1KC331 and 1NC103 were found in closed position, and they should have been open.
Decided to perform Class "C" leak test on these two penetrations and add to ILRT test results.
? -
1708 17i C-5
.A 6
6 APPENDIX D TEST PROCEDURE 6
m e
~
1708 172
~
Sb TP/1/A/f" /06 DUKE POWER COMPANY McGUIRE NUCLEAR STATION THE CONTAINMENT INITIAL INTEGRATED LEAK RATE TEST AND STRUCTURAL INTEGRITY TEST 1 50 Purpose ((
E The purposes of the Containment Vessel Integrated Leak Rate'and
~
Structural Integrity Test are:
1.1 To verify the structural integrity of the containment vessel.
1.2 To verify the Integrated Leakage Rate of the Containment Vessel does not exceed the maximum allowable leakage specified in the McGuire Unit 1 Technical Specifications.
2.0 References 2.1 McGuire Unit 1 FSAR Section 6.2, Table 14.1.3-1 (Rev. 37) 2.2 Description of the Leak Rate Test Instrumentation System (Rev. 1) 2.3 MC-1499.03-08 (Rev. 'l N
+ ~
MC-1499.03-9.02 (Rev. 40 a.
MC-1499.03-9.01 (Rev.-G7 2.4 Letter of M.D. Hopkins to ".A. Haller. Ice Condenser Integrated Leak Rate Test, File MC-1201.17 (May 10, 1978)
Letter of R.O. Sharpe to J.E. Snyder, ILRT Method, File MC-802-01, (August 11, 1976) 2.5 McGuire Technical Specifications of Unit 1 Section 4.6.1.1.
3.0 Time Required 3.1 Time 168 hours 3.2 Mau Power:
2 Test Coordinators (in charge of test activity in the assigned shift) 8 Technicians (2 of Engineering Services + 2 of I&E + 2 of Performance) 1st Shift 2nd Shift Coordinator Coordinator
[ - DATA TAKER (2) - DATA TAKER (2)
- Instrument Supporters (2) - Instrument Supporters (2) e
*e 1708 173
Initial /Date 4.0 Prerequisite Test
-/ 4.1 Fuel Transfer Tube Leak Rate Test (TP/1/A/1200/17) g#g
/ 4.2 l%ff..Y_..F *Dreadd m w ouc %.'Y m uuo. . -ML#-o__.
_ - - _ W L. M rb.,.,
E. .,nn.n8)
/ 4.3 Leuer Ovu.u nmert Personnel Air Lock Leak Kate Ae=w (T"/1/A/1200/19)
/ -
4.4 Equipment Hatch Leak Rate Test (TP/1/A/1200/20) ,3,y { eg , fM)
/ -
4.5 Electrical Penetrations Leak Rate Test (TP/1/A/4M0/20
/ -
4.6 Isolation Valve Leak Rate Test (TP/1/A/1200/16) 5.0 Test Eauipment 5.1 52 RTD and spares (Leed & Northrup) 5.2 3 Digital pressure gauges (RUSKA) 5.3 3 General Eastern (1200 series) Condensation Dew Point Hydrometers 5.4 1 Digital Data Surveillance System (L&N) 5.5 1 Air operated pressure relief valve (Grinnel) 5.6 1 Turbine Flowmeter (Flow Technology) 5.7 1 Data Terminal 5.8 Soap Bubbling Liquid Solution -
5.9 Personnel hatch pressurization fixture 6.0 Limits and Precautions 6.1 To assure favorable test condition, the test schedule should be planned in so far as possible with advance weather prediction. The ideal weather condition is the one that minimi e barometric pressure variation, temperature fluctuation and windless.
6.2 Only personnel that have medical examination as per Safety Health Procedure #4 can enter the containment vessel under pressure.
6.3 Exposure to containment test pressure shall be limited to not greater.
than 200 min. When entering or leaving air lock, the time for pressure equalization shall not be less than 30 seconds.
6.4 If any alarms activated due to high pressure in the containment, notify test coordinator prior to taking any action that can affect the test pressure.
7M Recuired Station Status
/
7.1 Verify that Instrument Air System (VI) is operable and capable of providing o
~
35 F dew point air to the lower and upper containment compartment.
/ 7.1.1 Verify that air is oil free. (Sample Analysis).
/ 7.2 Verify Ice Condenser Inlet doors have been blocked cliised.
1708 174
- r. -
- 7. ,
(.) \s' Initial /Date 7.3 Verify k" pipe plug on the Ice Condenser equipment access door has been removed to equalize the internal door pressure.
/ 7.4 Verify the Station Air System (VS) is operable to serve as the backup pressurization system. .
All flam=able and explosive materials under pressure must be removed
/ -
7.5 from the containment vessel (i.e. oxygen bottles, ligBt bulbs with-out pressure shell etc.).
/ 7.6 Verify all tanks inside the containment vessel have been drained and vented (i.e. the pressurizer relief tank, the Reactor Coelant Drain Tank, Reactor Coolant Pump Motor Oil Drain Tanks).
/ 7.7 Verify all free water in the containment sumps and open tanks have been removed to the greatest extent possible to avoid conden-sation and change in the vessel volume.
/ 7.8 Verify that all personnel who are assigned to enter the containment vessel under pressure (at 10 psig and 14.8 psig) had physical check-up as per Safety Health Procedure #4. .
/ 7.9 Verify all penetrations and valves on the Enclosure 13.1 have been drained of fluids.
7.10 Verify valve checklist of Enclosure 13.2 has been completed to seal the containment vessel. Enclosure 13.2 is also aligned to vent all penetrations specified in Enclosure 13.1. Valve closure is accomplished by the normal mode of operation without exercise or adjustment for seating the valve.
/- - 7.11 Deenergize all electrical Innds 4-=4Aa cha ennem4e-ant vessel not
~
this test or ocner plauw v u al a w ras.
/ 7.12 Remove two NC Pump Hatches on opposite side to allow pressure co=munication between the lower and the upper containment vessel compartments.
/ 7.13 Verify the two penetration M394, M395 (Ice Condenser Ice Blowing Air In and Returned) are flanged.
/ - 7.14 Verify all bellows of the mechanical penetrations listed on Enclosure 13.3 are vented (Tech Spec requirements).
p -
m NO 1708 175
~
r :
Initial /Date 7.15 Verify the following valves are operable to serve as the vacuum breaker for the containment vessel:
/ VQ3, Cont. Air Addition Inlet from Aux. Bldg. Isol.
/ VQ5, Cont. Air Addition Outside Isolation
/ s VQ6, Cont. AirAdditionInsideIsolat{on j
/
^
7.16 Set VI200, Test Header to Unit 1 through WL pressure dontroller at
~
85 PSIG decreasing.
8.0 Prereaufsite System Conditions
/ 8.1 Verify all instrument cables for the leak rate test (ICE) have been checked for continuity and their relative location co= pared with the multiplexer have been verified.
/ 8.2 Verify the Digital Data Surveillance Facility (DDSF) has been installed and field operation check completed.
/ 8.3 Verify containment vessel air operated relief valve has been installed and the valve closed.
~
/ 8.4 Verify blind flanges on the containment pressurization and depressurization lines have been removed.
/ blind flange of the ice condenser pressurization line
/ blind flange of the lower containment compartment pressurization line
/ blind flange of the Annulus Ventilation Depressurization line
/ 8.5 Verify personnel training to use the DDSF have been conducted.
/ 8.6 Verify all RTD, Dew Point, pressure sensors have been installed.
/ 8.7 Verify the flow turbine meter has been installed.
/ 8.8 Verify the equipment hatch has been installed.
/ 8.9 Verify that the system under test has been turned over to Steam Production and all exceptions and their effect on the test procedure have been evaluated and documented in the test log.
/ 8.10 Install AP Cage (0 + 20 PSID) across lVIFE5210 ( +3/4" accuracy)
/ 8.11 Verify that preliminary inspection of the Containment Building per Enclosure 13.11 has been completed to establish base line datas for
! the structural integrity visual inspection. h%7g
/ Q 8.12 Verify that error analysi Type C Loi Rate Tests have
~. been nelosure 13.12 and their accee oucc crit e h s are met.
/ 8.13 Verify that all test instruments listed in Section 5.0 are calibrated and a copy of the calibration data sheet is attached.
1708 176
9.0 Test Method The containment vessel will be closed up and pressurized to 10 PSIG.
After the entry is made to detect any major leak at this pressure, the pressurization is continued to bring the pressure up to 16.875
- PSIG. The containment structural integrity test is conducted by c -
- holding the vessel at 16.875 PSIG for 10 minutes. Pressure is reduced to 13.5 psig (4/5 of 16.875) and inspection on the outside of the vessel is performed to detect any structure defor=ation. The pressure then is increased to 14.8 PSIG and the leak rate test is conducted for 24 hours af ter the adequate stabilization period. Soap bubble test of all hot pipe penetrations will be conducted during the stabilization period. Once the acceptable result is attained, an imposed leak test is performed to determine the test system error.
The test is considered completed when all acceptance criterias are met.
10.0 Data Required 10.1 Containment temperature, pressure, dew point temperature will b'e recorded on the cassette tape every 15 minutes. The contents of the tape is verified with the DDSF printer prior to feeding to the computer.
10.2 The following graph will be plotted regularly during the test:
10.2.1 The normalized containment vessel air mass (W1 ) versus the test run.
10.2.2 The upper containment vessel, lower containment vessel, Ice Condenser pressure versus the test run.
10.2.3 The upper containment vessel, lower containment vessel and Ice Condenser vapor pressure versus the test run.
10.2.4 The average temperature of the upper containment vessel, lower containment vessel and Tce Condenser versus the test run.
10.3 The computer print outs of all test runs will be documented.
10.4 All test data is processed by the Integrated Leak Rate Computer progr.un., Enclosure 13.8 outlines the formulas used to develop the program. ,
11.0 Acceptance Criteria 11.1 The Structural Integrity Test is acceptable if a pressdre of 16.875 PSI is maintained for 10 minutes. All abnormal findings not resolved by the team leader during the test will be resolved by Design Engiseering.
11.2 No bubble allowed in all hot penetratioh soap bubble test.
1708 177
i 11.3 The Total Containment Vessel Leak Rate (L ) is less than or equal T
to fifteen hundredth of one percent (LT < .15%/ day) of the contain-ment vessel air weight per day
~
p where LT= Lam (95%) + L aux. ,-
L,,(95%) = 95% confidence value of calculated feak rate L = leak rate of all penetrations, valves, flanges which aux cannot te exposed to test pressure due to system operation (see Enclosure 13.9) 11.4 The- ifference between the measured -(Lam) prior to imposing t own leak and tharTitam) after imposing the' known leak is within undred of one percent of the Contain-ment Vessel Air Weight (ILam - La _ 5%/ day) per day, pq) -aw ~=. WL W5 ab & a 2 % W fC t.rel Lr =
k ' ' 'i - F 5 m
& L~pa t = L
'r - L,, 2(t ,2 r Lct e
1708 178
~7~ -
mo o '
g
[,' .~) O O O \-
Initial /Date s oc c ,$..'m 12.0 Procedure
^
12.1 Verify all pretest requirements in Section 7.0 and 8.0 are met.
/ 12.2 Place the VI System in service per OP/0/A/6450/05.
/ 12.3 Complete valve check list 13.4 to route air to the containment vessel.
/ 12.3.1 Slowly open lWL363, Instrument Air to the Containment I
for Leak Test and physically r verify air is rduted to the
- lower containment compartment through the op'hning in the pipe chase area.
/ Close lWL363, Instrument Air to the Containment for Leak Test
/ 12.3.2 Open IVIl96, Test Air Dryer E Discharge Throttle to Test Header and physically verify air is routed to the Ice Condenser through the opening on the side of the intermediate and upper deck door of the ice condenser.
/ Close lVI196B, Test Air Dryer E Discharge Throttle to Test Header
/ 12.4 Place all 3 VI compressors in BASE LOAD
/ 12.'. 1 Verify that all air dryers and filters are in servich
/ 12.5 Adjust all the Ice Condenser Air Handling Unit timers per Enclosure 13.10.
-1 12.6 Notify all personnel through the page system that the containment vessel will be closed up for testing. Order all personnel to leave the containment building.
/ 12.7 Perform the final check over the whole project prior to closing up the containment vessel. The following specific items need to be rechecked.
/ a. All test instruments are operational.
/ b. Depressurization blind firsnge has been removed.
/ c. Ice condenser inlet doors have been blocked closed.
/ d. The containment vessel pressure relief valve has been installed.
/ e. Pressurization blind flange has been removed.
/ f. All personnel have left the containment building. ,
/ 12.8 Close the upper and the lower containment vessel personnel air locks.
/ -
12.9 Begin pressurization by:
~
/ Opening 1WL363, Instrument Air to the Containment for Leak Test.
e - _
/
. Throttling IVIl96, Test Air Dryer E Discharge Throttle to Test g Header unti' 1"ITC5210 (Ta n #$*a me M* <"ppi; Flce) indicetes no REcom M ae,uy ec- wF e G es 12 r o -
isP N220 ccfu. (C * *D "s"ea e 1 L O4 PSTD < AP < 1^_'5 fSID.)
(Ar ek4 r cettLg ica conda~ar d e press"rized 2t-e-highcr retc euu the leccr centei - u6 uv o==use enac no moisture air int utraces into --
tha 4~ cen:!ca w L the Ovnteinmcat41-l< ling.)
AcrN.ug ogsetpccq. pac.rc,g Le w pr s.At2 q - ( C406n L EMdEC pewa,teO AIGEfr VA LVC A wa.,) t 1c% X 2%
derJ 1%C ra , co c H2 patrc "t
,,.l a cpew'C GA, w - % pxct w
~ * >" & dG A.mv o.g o; m k m J$
.x m .
c ac stow j
l f
k_* .'
Initial /Date 12.10 Record the following data to calculate the rate of pressurization to facilitate planning information.
/ Initiation time
/ Containment pressure hour after initiation (A) PSIG
/ ; Rate of pressurization = (A) x 2 = PSIG/hrr c
- 12.11 When the pressure reaches 10 PSIG, cease the pressuritation by:
/ -
Close lWL363 for Leak Test L c u te= iwu mJ, Instrument com vu..a Air to thecw ccs.ac Containmen nce . z. ) w
/ Close IV1196 Test Air Dryer E Discharge Throttle to Test Header caes; aw u 32r A, cw; v. a . o '~ C oe m: 2.r o t- .
/ 12.12 a. Enter the Annulus area and visually inspect the vicinity of penetrations to detect any obvious leak.
/ b. Visually inspect the outside portion (Aux. Building side) of all penetrations. Drain and vent valves of all penatration which are exposed to test pressure per Enclosure 13.1 shall be inspected carefully for leakage. If air gust out or can be felt by hand through vent valve, notify Test Coordinator.
/ c. Document any leak found in b in test log. Follow one of the following solutions to resume testing.
/ Fix the leak found (this option requires report to the NRC).
Isolate the leak (this option requires the local leak test performed after the test)
/ 12.13 Perform the following steps to equalize personnel hatch to enter the containment vessel.
/ a. Install the pressurization test rig to the 3" emergency air penetration on t kt right side of the hatch. Connect rig to VI header.
/ b. Establish com=unication between personnel inside the hatch and one outside.
/ c. Enter lock, close door and inflate seals.
/ d. Slowly pressurize the lock at the rate of =3 PSIG/ Minute until 1).
gage indicate 10.0 psig (+_ ,1
- NOTE: Personnel pressurizing the door shall continuously
- cod $unicate with personnel inside the hatch to control the
+ -
7 presnurization process. Only assigned personnel who have been medi. ally examined per Safety Health Procedure #4 can enter the
~'
cont ainment vessel).
- e. Af ter pressure equalization is established, open the inner
_4 door to enter the vessel.
/ f. Reclose the inner door. .
f, . ~?.
)
- nitial/Da te
/ 12.14 a. Perform visual inspection inside the vessel. Pay attention to the followings:
- 1. Any obvious damage, dislocation to equipment due to pressure change.
- 2. Any obvious leak.
i 3. Collect any undesirable items fi.e. tools,fla5able
; containers, etc.) left in the vessel.
~
- 4. Inspect all Ice Condenser AHU. If coils are generally unobstructed proceed without change. If most coils (other than those defrostin at /
the time) AN,are choked N*'*F:n-y with frost, c4=- &)WP MC'f_YfR..*.
t__ __ _ 3____. ,' ^_."W3 P mm .a 3 ouw mm. m muu AH& . Rete n r + 43armr4an a n n 4 ,, sm e en apa*=*4aa - -h cr.
"DT prc; eor; ;f l' . 8 PSIC ir ebtaincL-
/ b. If any obvious leak existed, follow guidelines set in 12.12.c.
12.15 Exit from the Containment
/ a. Verify the Containment vessel pressure and the hatch pressure are equalized.
/ 5. Open the inner door and enter the hatch.
__ ] c. Close inner door and inflate seals.
j d. Slrvly open the depressurization valve of the test rig to equalize pressure with the auxiliary building (=3 PSIG/ minute).
/ e. Open outer door to exit the hatch and reclose the outer door.
/ I'.16 a. Resume press p % ra 32ibrization , m.T b :vN.O ou rMi W Mol.
/ Opening 1WL363, Instrument Air to the Containment for I.eak Test c w v.a. o supoc. c a. .nsc..
op a w ,1o A
/ Throttling iVIl96B, Test Air Dryer E Discharge Throttle to Test Header until AP gauge of IVIFE5210 indicates the value set in 12.9 to bring pressure up to 16.5 < P < 17.25 PSIG for the containment structure and integrity test.
/ __
- b. Reclose IWL363, and IVIl96B when pressure reaches 16.5 < P < 17.25 PSIG.
/ 12.17 Hold the containment vessel at this pressure for ten minutes.
/ 12.18 After the 10 minute holding period, reduce the containment pressure down to 4/5 P (4/5 of the value set at 12.16b) by: ,
/ } Opening IVESA, Cont. H2 purge to Annulus Inside Cont. Isolation _
~
/ .
Opening IVE6B, Cont. H2 purge to Annulus Outside Cont. Isolation ,
/ Regulating IVE9, Cont. H2 purge t Annulus Control to reduce pressure at the rate of 5 PSIG/hr.
- a. Reclose IVESA, IVE6B, IVE9 when pressure reaches 4/5 of Press. set at 12.16b
{-
s f.
Initial /Date
/ 12.19 Perfom Structural Integrity Inspection for the Containment Vessel per Enclosure 13.11.
/ 12.20 Whe g t is completed, bring the containment pressure up to l'.S P IG as per 12.9. ,
97 Q, f
/ a. Close lWL363, and IVIl96B when the pressure reaches -WSO. PSIG i (+.02), c g~
. .02
- b. Vent the pressurization penetration M221 (WL) by:
/ Close WL321A, Cont. Vent Unit Drains Inside Cont. Isol.
/ 3 Close WL322B, Cont. Vent Unit Drains Outside Cont. Isol.
/ L 2.1M h[WL881, Vent Unic Drain Tank High Vent ca.4J wI i99 Au 3 -ru; eq g; . ,a 2 e , pceeq feen, v .,; c5 hd Mc/P
/ 12.21 Record the containment vessel pressure of 3 coepartments every 15 c .-e i minutes and perform the calculation on Enclosure 13 C to determine
\, [f}'*f((> when the temperature stabilization is established.
/ a. Perform soap hubble test for all hot penetrations listed on i0.2 #. c c,oe s n r tW, &!
cc s A; :n: .c r: b.
Enclosure 13 ,.5.
cgog ,cy4 , g3 g a. appy e w 7 cart ce o rce , n) c,39 2 (cd)M
/ 12.22 At the end of 4 hour stabilization period begin the 24 hour leak rate test: ,
/ a. Record the initiation time /hr.
_ -/ b. Record temperature, dew point, and pressure on the cassette tape at 15 minute intervals (set the DDSF at 15 minute interval).
/ c. Perform data analysis as soon as the adequate data accumulated,
- d. Perform the following plottings:
/ Average temperature, pressure, vapor pressure of each compartment versus test run.
/ dverage containment vessel air = ass (Wg ).
/ 12.23 Record the time when the acceptance criteria is me" /hr. g
/ 12.24 At the end of the 24th hour, determine the imposed leak / CFM per Enclosure 13.7.
/ 12.25 If the le g at4 s4 still favorable, begin the imposed leak test by
/ Opening -lWb347, Cont. Leak Rate Test Instrument Isol.
F' V )
/ Throttlingdm.fesWL321, Cont. Leak Rate Test Instrument Calibration needle until the turbine flow meter readout indicates the values calculated e in 12.24. _
/ 12.26 Begin recording data and perform analysis as in 12.22.
/ 12.27 The test is considered completed as soon as the accepj:,ance criteria 11.4 is met.
12.28 Depressurize the building to O PSIC at the rate of <5 PSIG/hr as in step 12.18. ,
1708 182
- U C
In4'ial/Date (For the periodic test, air sample should be analyzed and the depressurization rate is set accordingly with the magnitude of air contamination). -
f 12.29 Conduct a thorough inspection of the containment vessel to detect
- -_ any visual damage to equipment due to test pressure. '
/
12.30 Return all valves on Enclosure 13.2 to their as found position.
/ 12.31 Replace all blind me ofladn es, cr removed 8
o p- Trrr igu.4.
vwf ve%- _ M W55 t Wg6 'c4a f ,- )
- g. a p r n-f e
/ 12.32 Recap all vent lines removed in 7.14. (Except M262, M153, M308, M440 of CF System and M393, M261, M154, M441 of SM System which outer bellows are normally vent to the annulus).
/ 12.33 Disconnect the pressure relief valve installed in 8.3.
/ 21 43.1 Raylace me Il.nge. b W ) ,
/ 12.'AfesetallIceCondenserAirHandlingUnittot c wph ^c<_ C%23 ,t wtyn 4 T of original ntC v T@settine gt r l' 13.0 Enc osures u p n3e y emo3y 13.i g()Ap 13.1 Checklist of valves and penetrations required to be drained.
13.2 Valve checklist to close up the containment vessel.
13.3 Checklist of penetration bellows required to be vented.
13.4 Valve checklist to lineup V1 System.
13.5 Checklist of penetrations undergone soap bubble test.
13.6 Te=perature stabilization calculation.
13.7 Imposed leak calculation.
13.8 The Containment Vessel Leak Rate Test Calculation.
13.9 ~.ist of Penetrations not Exposed to Test Pressure.
13.l( Ice Condenser Air Handling Timer Defrost Pattern.
13.11 Containment Vessel Structural Integrity Inspection Checklist.
13.12 Error Analysis of Type B and Type C Leak Rate Test.
13, 6 MC i /G TT<'O ALEA* 3 ff-o g N e
m e
1708 183
(\ .
Page 1 of 3 ENCLOSURE 13.1 TP/1/A/1200/16 Pipe Ection between and on both sides of the follow 4ng valves are '-dyined of all fluids Valves Penetrations W4 M377 W5 WL321A M221 WL322B WL385 Vll29B M220 VI40 VE10A M331 VEll VQlA M243 VQ2B VQ6A M384 VQSB NC195 M361 NC196 NC254 RF823 M353 RF821 KC322 M376 KC320A KC333A M355 KC332B KC280 .
KC3383 M327 KC340 KC425A M320 KC424B
~
KC279 VP8B - M456 VP9A , _
VP10A M368
~
VP113 l'
VP12A M455 VP13B 1708 184
('.:;.(' ' f. ~
Pye 2 of 3 Valves , Penetrations VP15A M119 VP16B YM116 M337 _.
? YM115B r J 0
R(32A RV33 RV130 RV101A M390 RV102B g Q th[
RV79A M385 RV803 RV76A M279 RV77B R
VB49B M215 VB50 VS12B M219 VS13 ,
VX34 M378 VX33B VX31A VX30 M325 VX40 FWil M358 FW13 FW67 WE13 M356 WE23 h53A M235 hT6A hT67 h37B NM26B M309 h525A hH22A h368
_- NM72B " M280
# hT75B _ _
NM78B h381B --
hT69 ~~
NM82A 9
1708 185
O -
C -
Page 3 of 3 Valves Penetrations KC47 M322 KC429B KC430A RN252B M307 Y Z RN253A RN277B M315 RN276A VPl7A M213 VP18B VP19A M138 VP20B VPlB M367 VP2A VP3B M454 VP4A VP6B M357 -
VP7A NC57 M216 NC56B NC54A M212 NC53B NCl41 M326 NC142 NC256 NI48 M330 NI47A NI95A M321 NI96B nil 20B NI436 NB260B M259 NB262 .
NI266A M348 NI267A
_ NI264B
- NI336 ,
a WL65B M374 _ _
I WL64B .
WL264 WL39A M360 WL41B WL2A M375 WLlB WL24 .
1708 186
O -
C A 1 0F g JKE POWE' COMPANY
[ " V L N > $
D D [ fkp h !
M}D Q 6 ib -
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@ h 5
EVE NO. ? VALVE NAME i- J~ z5
.NC103 PRESS. RELIEF TANK #1 SPRAY CONT. ISOL. TEST CONNECTION OPEN M216*
PF5SS. RELIEF TANK #1 SPRAY CONT. ISOL. TEST CONNECTION CLOSED M216
.NC120 PZR RELIEF TANK #1 SPRAY HIGH POINT VENT OPEN M216
.NC242 CLOSED M216
.NC56B PRESS. RELIEF TANK #1 SPRAY CONT. ISOL. OUTSIDE NITROGEN TO PRESS. RELIEF TANK #1 CONT. ISOL. INSIDE CLOSED M212 *
.NC54A CLOSED M212
.NC5 3 B. NITROGEN TO PRESS. RELIEF TANK #1 CONT. ISOL. OUTSIDE NITROGEN TO PRESS. RELIEF TANK #1 CONT. ISOL. TEST CONN. M212
.NC102 OPEN l NITROGEN TO PRESS. RELIEF TANK #1 CONT. ISOL. TEST CONN. OPEN M212
.NC101 CL & CP M343
.NV445 NC PUMP 1D SEAL SUPPLY CONT. ISOL. TEST VENT CLOSED M343
.NV446 NC PUMP 1D SEAL SUPPLY CONT. ISOL. TEST VENT ,
CLOSED M343
'NV76
. NC PUMP 1D SEAL WATER MANUAL CONTROL NC LETDOWN LINE HIGH POINT VENT CL. & CP M347 5 1 NC LETDOWN TO REGEN. HEAT EXCH. HIGH P01NT VENT CL. & CP M347 na3 NC LETDOWN TO REGEN. HEAT EXCH. HIGH POINI VENT CL & CP M347
'.NV4 64 CL & CP M347 LNv893 NC LETDOWN TO REGEN. HEAT EXCH. VENT ISOL.
CL & CP M347 LNV829 NC LETDOWN MODE CONT. TEST DRAIN lNV854 NC LETDOWN MODE CONT. HIGH POINT VENT ri A ro M347 LETDOWN CONT. ISOL. OUTSIDE' CLOSED M34 7-LNV7B LETDOWN ORIFICE lA OUTLET CONT. ISOL. CLOSED M347 INV459A LETDOWN ORIFICE IB OUTLET CONT. ISOL. CLOSED M347 INV458A .
CLOSED M347 LNV457A LETDOWN ORIFICE 1C OUTLET CONT. ISOL.
CL & CP M329 1NV441 NV SUPPLY TO NC CONT. ISOL. TEST VENT CL & CP M329 LNV442 NV SUPPLY TO NC CONT. ISOL. TEST VENT CLOSED M329 INV245 CHARGING LINE CONT. ISOL. OUTSIDE CL & CP M329 INV8@,' NVhETURNTONCINSIDECONT.VENTISOL.
~
CLOSED M228 LNV840' e ND 3TMP DISCH. TO PZR AUX. SPRAY CONTROL CL & CP M228 1NV933 ND ' PUMP DISCH. TO PZR AUX. SPRAY HIGH POINT VENT 1NV922 ND PUMP DISCH. TO PZR AUX. SPRAY HIGH POINT VENT CI .6 CP M228.
INV/ '9 NC PUMP SEALS RETURN CONT. ISOL. PRESS. TEST DRAIN CL & CP lM256 IN NC PUMP SEALS RETURN CONT. ISOL. INSIDE CLOSED lM256 INV95B NC PUMP SEALS RETURN CONT. ISOL. OUTSIDE ,
CLOSED l lM256
- PENETRATION VENTED TO MEET REQUIRE}ENTS l l l CL & CP = CLOSED AND CAPPED g j}f
OSURE 13.2 PAGE 9 0F g JKE POWER COMPANY
^ V i
N > E 8C DCD Nb 3
%ddML I
D a ;: a !!
r o g G
M SE.C. "I'"'.FZ LINE CGliT. ISOL. MSFAME hD# g, En M2i6
.NV436 NC _ PUMP 1C SEAL SUPPLY CONT. ISOL. TEST VENT SED M256
.NV60 NC7 UMP 1C SEAL WATER MANUAL CONTROL CLOSED 4339 NV437 NC PUMP 1C SEAL SUPPLY FROM STANDBY MAKEUP PUMP CLOSED 4339
'.NV4 34 NC PUMP 1B SEAL SUPPLY CONT. ISOL. TEST VENT CL & CP M339 tNV44 NC FUMP 1B SEAL WATER MANUAL CONTROL CLOSED M339 LNV432 NC PUMP 1A SEAL SUPPLY CONT. ISOL. TEST VENT CL & CP M350 LNV28 NC PUMP 1A SEAL WATER MANUAL CONTROL CLOSED M350 LNB260B PENT. M-259 OUTSIDE ISOLATION CLOSED M259i PENT. M-259 INSIDE TEST VENT CLOSED M259 LNB261 OPEN M259 LNB259 l PENT. M-259-0UTSIDE TEST VENT OPEN M259 LNB263 PENT. M-259 OUTSIDE TEST VENT CLOSED M300 LBB1B STM. GEN. lA BLOWDOWN CONT. OUTSIDE ISOL.
STM. GEN. lA BLOWDOWN CONT. INSIDE ISOL. CLOSED M300 IBB5A M300 STM. GEN. lA CONT. Ou1 SIDE ISOL. TEST VENT CL & CP CL & CP M300 13B13 STM. GEN. lA CONT. INSIDE ISOL. TEST VENT CL & CP M300 13B179 STM. GEN. lA CONT. INSIDE ISOL. TEST VENT CL & CP M300 IBB178 STM. GEN. lA CONT. INSIDE ISOL. TEST VENT CL & CP M300 1BB177 I STM. GEN. lA CONT. INSIDE ISOL. TEST VENT STM. GEN. 1B BLOWDOWN CONT. OUTSIDE ISOL. CLOSED M301 IBB2B f CLOSED M301 1BB6A STM. GEN.1B BLOWDOWN CONT. INSIDE ISOL.
STM. GEN.11' BLC';DOWN CONT. OUTSIDE ISOL. TEST VENT CL & CP M301 1BB10 CL & CP M301 13314 STM. GEN. 1B CONT. INSIDE ISOL. TEST VENT STM. GEN. 1C BLOWDOWN CONT. OUTSIDE ISOL. CLOSED K303 1BB3B CLOSED M303 1BB7A- STM. GEN. 1C BLOWDOWN CONT. INSIDE ISOL.
CL & CP M303 1BB11 STM. GEN.1C CONT. OUTSIDE ISOL. TEST VENT M303 13B15.. ' STR_. GEN. 1C CONT. INSIDE ISOL. TEST VE E CL & CP CLOSED M304 1B343 ST5. GEN.1D BLOWDOWN CONT. OUTSIDE ISOL. _ _
CLOSED M304 1BB8A STk. GEN.1D BLOWDOWN CONT. INSIDE ISOL.
CL'& CP M304 1BB12 STM. GEN.1D CONT. OUTSIDE ISOL. TEST VENT 1BB16 STM. GEN. 1D CONT. INSIDE ISOL. TEST VENT CL & CP lM304 1N BORON INJ. LINE CONT. ISOL. VALVE TEST VENT CL & CP lM351 INI19A BIT DISCHARGE ISOL. ,
CLOSED l lM351 INIl0B BIT DISCHARGE ISOL. CLOSED l l lM351 PENETRATIONS VENTED TO IEET REQUIREMENTT.7 CL & CP = CLOSED AND CAPPED
ENCI'OSURE 13.2 PAGE 3 0F y1 UKE POWER COMPANY gy"".c't^^St^=" vE s'f$ C E
D**$D
.. *$D
. T
- a. lk- -
s g
,4 c
e s"
g ALVE NO. - VALVE NAME -- -r 5
1NI327 , BOTt0N INJ. CONT. ISOL. TEST VENT CL & 'P M351 INI401 CCP DISCH. TO NC COLD LEGS HIGH POINT VENT CL & CP M351 INI47A ACCUM. N, SUPPLY OUTSIDE CONT. ISOL. CLOSED M330:
1 nil 07 ACCUM. N SUPPLY CONT. ISOL. VALVE TEST VENT CLOSED M330 INI202 ACCUM. N SUPPLY CONT. ISOL. VALVE OUTSIDE TEST DRAIN OPEN M330 ACCUM. N, SUPPLY CONT. ISOL. VALVE INSIDE TEST DRAIN OPEN M330 1NI204 TEST HDR INSIDE CONT. ISOL. CLOSED M321 INIf95A OPEN M321 INI205 TEST HDR. CONT. ISOL. VALVE TEST VENT TEST HDR. CONT. ISOL. VALVE TEST VENT CL & CF M321 INI46 TEST HDR. SAMPLE OPEN M321 1NI97 OPEN M321 INI435 TEST unR. <'ONT . T ent VATVE TF9T VvNT CLOSED M321 INI96B TEST HDR. OUTSIDE CONT. ISOL.
CLOSED M316
_lFT371A SAF. INJ. PUMP 1A HOT LEG INJ. HEADER ISOL. dub 1 ,9 ISOLATION VALVE 1 nil 21A TEST VENT CL 6 LF CLOSED M316 1 3 SAF. INJ. PUMP 1A HOT LEG INJ. HEADER ISOL.
SAF. INJ. PUMP 1A TO NC HOT LEG LOOP 2 & 3 HIGH POINT VENT CL & CI M316 INI422 SAF. INJ. PUMP 1B HOT LEG INJ. HEADER ISOL. CLOSED M319 INI152B ISOL. VALVE 1NI152B TEST VENT I cab ' ) IfvP CL & CP M319 1NI211 "
.. ~ -
hef 210 ' ISC'.ATICN '/Ahv9-MI15 2 0 !;JI /E.,I C'1 C "& 'CP M319 INI416 l SAF. INJ. PLHP IB to NC HOT LEG LOOP 1 & 4 HIGH POINT VENT CL & CP M319 1NI420 lSAF. INJ. PUMP IB TO NC HOT LEG LOOP 1 & 4 HIGH POINT VENT CL & CP M319 1NT389 SAF. INJ. PUMP 1B TO NC HOT LEG LOOP A & D LOW POINT DRAIN CL & CP l M319 1NI390 SAF. INJ. PUMP IB TO NC HOT LEG LOOP A & D HIGH POINT VENT CL & CP M352
~1NI213 ISOLATION VALVE INI162A TEST VENT CL & CP M352 1NI384 ISOLATION VALVE 1NI162A LOW POINT DRAIN CL & CP M352 INI385 l ISOLATION VALVE 1NI162A HIGH POINT DRAIN CLOSLJ M352 INI162A ACCUM. IB VENT LINE ISOL.
' ~
SAE. INJ, PUMP TO COLD LEG LOOP A HIGH POINT VENT CL & CP M352 INI 3 Er7-CL & CP M352 INI3EI6 SAF. INJ. PUMP TO COLD LEG LOOP A LOW POINT VENT CL & CP M352 1NI405 SAT. INJ. PUMP TO NC COLD LEG LOOP 2 HIGH POINT VENT CIJ & CP M352 INI406 SAF. INJ. PUMP TO NC COLD LEG LOOP 3 HIGH POINT VENT INI408 SAF. INJ. PUMP TO NC COLD LEG LOOP 4 HIGH POINT VENT CL & CP l M352 ISOL. VALVE INIl78B TEST VENT CL & CP l M336 2 5 INI381 ND PUMP IB NC LOOP B & C LOW POINT DRAIN ,
CL & CPl l M336 INI375 ND PUMP IB NC LOOP 3 & 4 HIGH POINT VENT fCL&CPf ! fM336 PEliET3AIIONS VICiTED TO MEET REQUIRDINTS CL 4 CI= CLOSID AND CAPPED 1708 189
~ ,-
. A g ENCLOSURE 13.2 - PACE 4 0F W JKE POWER COMPANY
- GUIRE NUCLEAR STATION TP/1/A/1200/06 g VALVE CHECKLIST IIT # 1 E -
,D - e wc o n
- 3 g dj m - $ $ i3 d e6 e , . a O
u.VE NO. ; VALVE NAME h
-r
~
INI374 ND JUMP 1B NC LOOP 3 LOW POINT VENT l1 & CP M336 INI377 ND7 UMP 1B NC LOOP 4 HIGH POINT VENT CL & CP M336 INI378 ND PUMP 13 NC LOOP 4 LOW POINT VENT CL & CP M336 INI376 ND PUMP 1B NC LOOP 4 LOW POINT VENT CL & LP M336 INIl78B ND HDR. TO NC COLD LECS LOOPS 1C & 1D CLOSED M336 INIl73A ND HDR. TO NC COLD LEGS LOOPS 1A & 1B CLOSED M306 LNI214 ISOL. VALVE 1 nil?3A TEST VENT CL & CP M306 LNI372 ND PUMP 1A TO NC LOOPS 1 LOW POINT DRAIN CL & CP M306 LNI373 ND PUMP 1A TO NC LOOP 2 LOW POINT DRAIN CL & CP M306 LNIIS4B CONT. SUMP LINE 1B ISOL. (, g , 3 A/P CLOSED
~
M278 1ND55 ISOL. . id V 1:;Il0iE TIST VE;;T CL ; CF M278 1NB7R 1 NG1 R ffe 97pla,;' LOW p;;;;T Opg!;; c1, g, gy ,Q 7 5 -
LNI'A5A CONT. SUMP LINE lA ISOL. CLOSED M302 5 mt!.TICl? V/.LVE 1FIl 05 ^ TEST 'T"? -
% 6 t.r .GO2 inn 79 'v?-191 L'"ETP19: 'HOU POI::T V;;;T CL E CP M302-LNI216 ISOL. VALVE 1NI183B TEST VENT CL & CP M277 1NII83B ND HDR. TO NC HOT LEGS ISOL. CLOSED M277 W N N l 39 19 E9 E9I .lE9 .Lgg{ 3 NIg,y {gINI ygyI _ ,,,,,_,, CL & CP
~
M277 M&a (NI,37,0 lNDTONCs5itist55P2HiGHPOINTviNT s23 l'NI2'69 UHI CHECK VALVE TEST LINE DRAIN $6N .N LNI266A UHI CHECK VALVE TEST LINE ISOL. CLOSED M348 LNI245A UHI ACCUM. DISCH. ISOL. CLOSED M33 4 LNI268 UHI CHECK VALVE TEST LINE TEST DRAIN CL & CP M348 1NI267A UHI CHECK VALVE TEST LINE ISOL. CLOSED h349 LNI398 UHI ACCUM. DISCH. HIGH POINT VENT CL & CP M349.
LNI2F)A' UHT ACCUM. DISCH. ISOL. CL & CP M36.
INI254B CLOSED '
M348 UH{CHECKVALVETESTLINEOUTSIDECONT.ISOL. _
INI266A [ UH5 CHECK VALVE TEST LINE ISOL. CLOSED M348
/ -
i .
1NI424 UHI CHECK VALVE TEST LINE HIGH POINT VENT OPEN y lM348 15 UHI CHECK VALVE TEST LINE TEST DRAIN <
g g, lM348 lIIS66 NS PUMP 1A DISCH. CONT. ISOL. TEST CONNECT. CL & CP l lM362 INS 65 NS PUMP 1A DISCH. CONT. ISOL. TEST CONNECT. lCL&CPl l lM362
*1'ENETRATIONS NINTED TO MEET REQUIREMENTS CL L CP = CLOSED AND CAPPED 1708 190
ENCLOSURE 13.2 PAGE 5 0F m Pom CON TP/1/A/1200/06 cGUIRE NUCLEAR STATION VALVE CHECKLIST NIT # 18 H 'e om 7 3 I E $ E D s z s ,,, a Ae w .S- ". ;s d g !:'
N k e d o
a
- ALVE NO. ; VALVE NAME 'i y 1NS34d
^
SP' RAY N0ZZLE SUPPLY LOCK OPEN fW 10 SED twsED M3_62_
w oi NSY2A NS PUMP 1A DISCH. CONT. ISOL. OUTSIDE :LOSED M362 INS 63 NS PLHP 1A DISCH. CONT. ISOL. TEST CONNECT. :L & CP M370 INS 62 NS PUMP 1A DISCH. CONT. ISOL. TEST CONNECT. CL & CP M370 1NS31 SPRAY N0ZZLE SUPPLY LOCK OPEN 10 SED l M370 1.131:3 STRA. JGZ;L: JIGH TOI:iT ?;NT :L 0 Cr "270 INS 29A KS PUMP 1A DISCH. CONT. ISOL. OUTSIDE CLOSED M370 1NS59 NS PUMP 1B DISCH. CONT. ISOL. TEST CONN. CL & CP M380 1NC100 CPPJ.Y N0ZZL: !!!C:: 20!NT 'J NT TL E CP "3R0 INS 15B NS PUMP 1B DISCH. CONT. ISOL. OUTSIDE LOSED M380 INS 17 SPRAY N0ZZLE SUPPLY LOCK OPEN CLOSED M380 1NS48 NS PUMP 1B DISCHARGE CONT. ISOL. TEST CONN. CL & CP M380 1NS40 NS PUMP 1B DISCHARGE CONT. ISOL. TEST CONN. CL & CP M387
{
S?J.Y "0::LE 'UCH ?OINT 'J:r' L ; Cr ";S7 1NS14 '
SPRAY N0ZZLE SUPPLY LOCK OPEN CLOSED M387 1NS37 NS PUMP DISCH. CONT. ISOL. TEST CONN. CL & CP M387 1NS12B NS PUMP 1B DISCH. CONT. ISOL. OUTSIDE CLOSED M387 1NS72 ND PUMP 1A DISCH. TO NS N0ZZLES CONT. ISOL. TEST CONN. ct 3 cp M38 1NS03 l ND .w.s. CONT. 02.AT UDR. la "ICH POINT 'CNT O_ E e M369 1NS47 SPRAY N0ZZLE SUPPLY FROM ND PUMP 1A (LOCK OPEN) CLOSED M369 1NS71 ND PUMP 1A DISCH TO NS N0ZZLES CONT. ISOL. TEST CONN. ct g cp M369 1NS43A ND PUMP 1A DISCH. TO NS N0ZZLES CONT. ISOL. OUTSIDE CLOSED M369 1NS42 SPRAY N0ZZLE SUPPLY FROM ND PUMP 1B (LOCK OPEN) CLOSED M381 INS 68 - ND PUMP 1B DISCH. TO NS N0ZZLES CONT. ISOL. TEST CONN. CL & CP M381 INS 69 ND PUMP 1B DISCH. TO NS N0ZZLES CONT. ISOL. TEST CONN. CL & CP M381 1FS91, ' 6_my cd7_ gmv imp 13 t!Igu poiv7 t7v7 ct &_CP -- M381 INS 3SB' lND) UMP 1BDISCH.TONSN0ZZLESCONT.ISOL.OUTSIDE CLOSED M381 lWL65B l REACTOR BUILDING SUMP PUMP DISCH. OUTSIDE CONT. ISOL. C CLOSED M374
- lWL64A REACTOR BUILDING SUMP PUMP DISCH. INSIDE CONT. ISOL. CLOSED M374 lWL390 REACTOR BUILDING SUMP PUMP CONT. ISOL. OUTSIDE TEST VENT CLOSED lM374 lWI LAUN. & HOT SHOWER SEC. FILTER TO W.M.T.A. OPEN lM374 lWLLa REACTOR BUILDING SUMP PUMP CONT. ISOL. INSIDE HIGH POINT VENT OPEN l lM374
~#
1 39A T E NS E O khb.. ,
CL Fhl l .l 360
- i'ENE TRATONS VE.iTED TO IICCT REQUIREMENTS CL & CP = CLOSED A'ID CAPPED 1708 191 -
ENCLOSURE 13.2 PAGE 6 0F #f M POWER CO N TP/1/A/1200/06
.cGUIRE NUCLEAR STATION I4 VALVE CHECKLIST HIT # 1 N > E a G M D
h 6b L hL #
- 4 h
5 N
'ALVE NO. . VALVE NAME i --
y lWL41B NCDT VENT OUTSIDE CONT. ISOL. CLOSED M36(f lWL40 NCDT VENT CONT. ISOL. TEST VENT JPEN PJ60 1WL42 NCDT VENT LOW POINT DRAIN 2 PEN M360 lWL389 NCDT VENT CONT. ISOL. OUTSIDE TEST VENT CLOSED M360 lWL2A NCDT PUMPS DISCH. INSIDE CONT. ISOL.
Y 3 [ CLOSED M375*
lWL25 NCDT PUMPS DISCH. CONT. ISOL. TEST VENT (C OPEN M375 1WL77 :: COT L;V:L CO:: COL LYTASC 0FL .;375 lWL28 NCDT PUMPS DISCH. FROM CONT. LOW POINT DRAIN OPEN M375 lWL859 NCDT PUMP DISCH OUTSIDE CLOSED M375 IW123 WE PUMP DISCH. TO REACTOR VESSEL HEAD SPRAY ASSEM. #1 CONT. 2.~_ CLOSED M356 '
~
IWLIB NCDT PUMPS DISCH. OUTS. CONT. ISOL, CLOSED M375 lWE13 WE PUMP DISCH TO REACTOR VES. HD. SPRAY ASSEM. #1 CONI. ISOL.- CLOSED M356 IWE15 ISOL. VALVE IWE23 TEST VENT OPEN M356
[ ISOL. VALVE lWE23 HIGH POINT VENT OPEN M356 UM4 lISOL.VALVElWE13HIGHPOINTDRAIN CLOSED M356 IN~ 13A lPZRLIQUIDSAMPLELINEINSIDECONT.ISOL, CLOSED 4 -
M235' liCf6A PZR STM. SAMPLE LINE INSIDE CONT. ISOL. CLOSED M235 1%!2 l CONT.ISOL.VALVEINM3ATESTVENT OPEN M235 LT t5 CONT. ISOL. VALVE INM6A TEST VENT OPEN M235 1N117B P2R SAMPLE HEADER OUTSIDE CONT. ISOL. CLOSED M235 IN1!8 CONT. ISOL. VALVE INM7B TEST VENT OPEN l M235 JNU26B NC HOT LEGS SAMPLE HDR. OUTSIDE CONT. ISOL. CLOSED M309' LT!25 A NC HOT LECS #4 SAMPLE LINE INSIDE CONT. ISOL. CLOSED
- M309*
1S'.12 2A. NC HOT LEGS #1 SAMPLE LINE INSIDE CONT. ISOL. CLOSED M309 B'M 2 7 CONT. ISOL. VALVE INM26B TEST VENT OPEN M309 lEM2t , ' CONT. ISOL. VALVE INM25A TEST VENT OPEN M309 1NM217 l CONT. ISOL. VALVE INM22A TEST VENT OPEN M309 1NM72B l NI~,ACCUM. lA SAMPLE LINE INSIDE CONT. ISOL. CLOSED M280i 1NM75B lNIACCUM.1BSAMPLELINEINSIDECONT.ISOL. CLOSED M280 lV!:78B lNIACCUM.1CSAMPLELINEINSIDECONT.ISOL. CLOSED l M280 Ir * #^ '. NI ACCUM.1D SAMPLE LINE INSIDE CONT. ISOL. CLOSED l M280
- h. a NI ACCUM. SAMPLE HDR. OUTSIDE CONT. ISOL. CLOSED l l l M280 liiM83 CONT. ISOL. VALVE INM82A TEST VENT .
OPEN l l lM280
- M; T:'.ATI0dS VENTED CL & CP = CLOSED AITD CAPPED }h2
ENCLOSURE 13.2 PAGE 7 0F g UKE POWER COMPANY V C BM D CD WT h 6 N ? Ia I
D gJMR s a
5 e
g c
- da $ e o
d
'ALVE NO. -
VALVE NAME g 1NM71 COUT. ISOL. VALVE LNM72B TEST VENT OPEN M2804 lhh74 C0 lit. ISOL. VALVE 1hT75B TEST VENT OPEN M280 INM77 CONT. ISOL. VALVE lhM78B TEST VENT OPEN M280 INM80 CONT. ISOL. VALVE INM81B TEST VENT OPEN M280 lhT280 NI ACC SAMPLE HDR LOW POINT DRAIN CLOSED M280 lhM187A S/G 1A UPPER SHELL SAMPLE CONT. ISOL. INSIDE CLOSED M335 lhT186 CONT. ISOL. VALVE INM187A TEST VENT CL & CP M335 lh3190A S/G 1A BLOWDOWN LINE SAMPLE CONT. ISOL. INSIDE CLOSED M335 lh3189 CONT. ISOL. VALVE lhM190A TEST VENT g CL & CP M335 1NM191B S/G 1A SAMPLE HDR. CONT. ISOL. OUTSIDE g y,hf CLOSED M335
( ~
1"v'Q7 rnNT. 7907. V AT VF 1 W1019 Tr9T VFNT ct,e c7 M335 1h3195 CONT. ISOL. VALVE INM197B TEST VENT CL & CP M338 1hM199 CONT. ISOL. VALVE lhM200B TEST VENT CL & CP M338 5 7B S/G 1B UPPER SHELL SAMPLE CONT. ISOL. INSIDE CLOSED M338 CLOSED M338
[NM2003 l S/G 1B BLOWDOWN LINE SAMPLE CONT. ISOL. INSIDE 1NM201A S/G 1B SAMPLE HDR. CONT. ISOL. OUTSIDE CLOSED M338
, cp M338 INM202 l CONT. 1501.. "ALVE IL5201A TEST V:NT CLOSED M340 1NM207A l S/G 1C UPPER SHELL SAMPLE CONT. ISOL. INSIDE CLOSED M340 INM210A l S/G 1C BLOWDOWN LINE SAMPLE CONT. ISOL. INSIDE CL & CP M340 INM206 l CONT. ISOL. VALVE INM207A TEST VENT CL & CP i M340 INM209 l CONT. ISOL. VALVE INM210A TEST VENT INM211B S/G 1C SAMPLE HDR. CONT. ISOL. OUTSIDE CLOSED M340 1rM212 cor_ ven[ VAT UF 1W711 R Tr9T VENT ct s cp M340 1NM216 CONT. ISOL. VALVE INM217B TEST VENT CL & CP M341 CL & CP M341 1NM219 CONT. ISOL. VALVE INM220B TEST VENT lhH2I.7.B ' CLOSED M341 S/~G 1D UPPER SHELL. SAMPLE CONT. ISOL. INSIDE CLOSED M341 INM210B l S/[G lb BLOWDOWN LINE SAMPLE CONT. ISOL. INSIDE CLOSED M341 INM221A l S[G 1D SAMPLE HDR. CONT. ISOL. OUTSIDE 1n050 CON 19m1- VAT vr 1w??1 A TrqT VTNT cv . i. cp _M341 1KC320A NCDT HX SUPPLY HDR. PENT. ISOL. (OUTSIDE) CLOSED yM3W 1K 9 NCDT HX SUPPLY HDR. PENT. TEST VENT (OUTSIDE) OPEN lM376 1K w S KC SUPPLY TO NCDT HX VENT OPEN l ,
lM376 1KC321 NCDT HX SUPPLY HDR. PENT. TEST VENT (INSIDE) CLOSED l l lM376 PENETRATIONS VENTED CL & CP= CLOSED AND CAPPED
.- 1708 193
.JKE POWER COMPANY ENCLOSURE 13,2 0 06 h PAGE 8 0F M lb
- IRE NUCLEAR STATION y c e 2 m
i a d
a c
g We c 3 w
- s d o
.4 U.VE NO. . VALVE NAME 5
~. _
LKC842. PENT. M376 OUTSIDE CONT. DRAIN CLOSED M376*
LKC332B NCDT HX RETURN HDR. PENT. ISOL, CLOSED M355#
LKC333A NCDT HX RETURN HDR. PENT. ISOL. (OUTSIDE) CLOSED M355 NCDT HX RETURN HDR. PENT. TEST DRAIN (INSIDE) OPEN M355 IKC331 OPEN M355 IKC334 NCDT HX RETURN HDR. PENT. TEST VENT (OUTSIDE)
CLOSED M355 IKC852 NCDT HX RETURN HDR. PENT. TEST VENT INSIDE OPEN M327*'
1XC341 NC PUMP SUPPLY HDR. PENT. TEST DRAIN (INSIDE)
CLOSED M327 1KC338B NC PUMP SUPPLY HDR. PENT. ISOLATION (OUTSIDE)
NC PUMP SUPPLY HDR, PENT. TEST VENT INSIDE CLOSED M327 LKC339 OPEN M327 IKC337 NC PUMP SUPPLY HDR. TEST VENT OUTSIDE
~
NC PUMPS RETURN HDR. PENT. OUTSIDE ISOL. CLOSED M320f 1KC425A CLOSED M320 1KC424B NC PUMPS RETURN HDR. PENT. INSIDE ISOL.
OPEN M320 1XC843 NC PUMPS RETURN HDR. PENT. INSIDE VENT OPEN M320 IF NC PUMPS RETURN HDR. PENT. TEST VENT (OUTSIDE)
CLOSED M322*~
TKC429B RX BUILDING DRAIN HDR. INSIDE CONT. ISOL.
CLOSED M322 1KC430A RX BUILDING DRAIN HDR. OUTSIDE CONT. ISOL.
OPEN M322 1XC428 RX BUILDING DRAIN HDR. PENT. INSIDE TEST VENT OPEN M322 1KC431 l RX BUILDING DRAIN HDR. PENT. OUTSIDE TEST VENT NON ESSENTIAL SUPPLY TO RB PENETRATION INSIDE ISOL. CLOSED M3074 1RN253A CLOSED M307 1RN252B NON ESSENTIAL SUPPLY TO RB PENETRATION OUTSIDE ISOL.
OPEN l M307 1RN75 CONT. ISOL. VALVE 1RN253A TEST VENT CONT. ISOL. VALVE 1RN252B TEST VENT OPEN M307 1RN74 1RN276A NON ESSENTIAL RETURN FROM RB PENETRATION INSIDE ISOL. CLOSED M315*
CLOSED M315 1RN277Bl NON ESSENTIAL RETURN FROM RB PENETRATION OUTSIDE ISOL.
OPEN M315 1RN76 CONT. ISOL. VALVE 1RN276A TEST VENT OPEN M315 1RNIC4.' CORT. ISOL. VALVE 1RN277B TEST VENT OPEN M213'*
lIIPI-DIl INCORE INSTRUMENT PURGE SUPPLY OPEN M138; lIIPE-Dl IN' CORE INSTRUMENT PURGE EXHAUST CLOSED ,M213 IVPl7A INCORE INSTR. ROOM PURGE SUPPLY INSIDE ISOL.
1VP18B INCORE INSTR. ROOM PURGE SUPPLY OUTSIDE ISOL. CLOSED lM213 CLOSED lM138 D 7 INCORE INSTR. ROOM PURGE EXHAUST OUTSIDE ISOL.
N2 a INCORE INSTR. ROOM PURGE EXHAUST INSIDE ISOL. CLOSED l l M138 TVP2A UPPER CON). PURGE SUPPLY #1 INSIDE ISOL. CLOSED l l l M3671
- ICETRATIONS VE;T;D CL 6r* CP = CLOSED AUD CAPPED 1708 194
> UKE POWER COMPANY ENCLOSURE 13.2 TP/1/A/1200/06 h PAGE 9 0F W 4
tcGUIRE NUCLEAR STATION VALVE CHECKLIST
, NIT #
v ~ D
" 5 " U
- T D a e g c em e . V "A..tQ= . = g , e O
'ALVE NO. - VALVE NAME IVPlB UPPER CONT. PURGF. SUPPLY #1 OUTSIDE ISOL. CLOSED M 367*
IVP3B UFPER CONT. PURG'd SUPPLY J2 OUTSIDE ISOL. CLOSED M454*
IVP4A UPPER CONT. PURCE SUPPLY #2 INSIDE ISOL. CLOSED M454 OPEN' M454 1RBPS-D-1 REACTOR BUILDING PURGE SUPPLY CLOSED M35 7*
1VP7A LOWER CONT. PURGE SUPPLY #1 INSIDE ISOL.
LOWER CONT. PURGE SUPPLY #1 OUTSIDE ISOL, CLOSED M357 IVP6B CLOSED M456*
IVP8B LOWER CONT. PURGE SUPPLY #2 OUTSIDE ISOL.
CLOSED 'M45 6 ~
IVP9A LOWER CONT. PURCE SUPPLY #2 INSIDE ISOL.
CLOSED M368*
IVP10A UPPER CONT. PURGE EXHAUST #1 INSIDE ISOL.
CLOSED M368 IVP11B UPPER CONT. PURGE EXHAUST #1 OUTSIDE 130L.
UPPER CONT. PURGE EXHAUST #2 INSIDE ISOL. CLOSED ,M455*
IVP12A CLOSED 'M455 IVP13B UPPER CONT. PURGE EXHAUST #2 OUTSIDE ISOL.
LOWER CONT, PURGE EXHAUST #1 INSIDE ISOL. CLOSED M119*
IVP15A LOWER CONT. PURGE EXHAUST #1 OUTSIDE ISOL. CLOSED Mil 9 l' 3 OPEN M119 1RBPE-D-kREACTORBUILDINGPURGEEMUSTDAMPER#1 STM. GEN. Id FDW CONT. ISOL. CLOSED MD 1CF2Dr43 ,
1CF137A h 1D FDW CONT. ISOL. BYPASS CLOSED / M440 1CF90 S/G b ET DRAIN CL&CP ,[ M440 1CF2&A&Bl S/G IC FDW ISOLATION g CMD M308 1CF136A S/G IC FDW CONT. BYPASS 3 h / CLOSED M308 1CF89 S/C IC INLET DRAIN \ fpMiU [ CL & CP M308 1CF30A S/G 1B FDW CONT. ISOL. \ \' [ CLOSED M262 1CF135A S/G 13 FDW CONT. ISOL. BYPASS CLOSED M262 1CF88
- S/C 1B INLET DRAIN [ \ CL & CP M262 1CF35 S/G 1A FDW CONT. ISOL. [ \ CLOSED M153 1CF154A S/G 1A FDW CONT. ISOL. M SS \ CLOSED M153 M153 1CF8I f S/G 1A INLET DRA_ Q CP.
~
CLOSt!L M153 ISM 102 l S/C 1D HIC NT VENT
' M153 CLOSED \
ISM 104 l S/G M GH POINT VENT
[ CLOSED M153 ISM 106 1B HIGH POINT VENT IS S/D 1A HIGH POINT VENT CLOSED i l Mlh A- s6 CONT. ISOL. VALVE SUPPLY PENT. TEST CL&CPl l lM218 1KC893 PENT. M218 OUTSIDE CONT. DRAIN CL&CP.j l lM218
' PCIET",ATI0dS VENTED CL & CP = CLOSED AND CAPPED j[Q@ j}}
UKE POVER COMPANY ENCLOSURE 13.2 TP/1/A/1200/06 h PAGE 10 OF ~Jr*
4 cGUIRE NUCLEAR STATION VALVE CHECKLIST HIT # 1 5 -
D** T 8 5 E b s r* o -
DD D ~
'ALVE NO. bALVENAME i m :-
lKC305A EXbESSLETDOWNHXSUPPLYPENT.ISOL. f- r sM( CLOSED M218 1MCO' EEESS LE0"" F2 SL??LY PEFT. SS? SFT s C N, c; ; cr M21E 1KC314 EXCESS LETDOWN HX RETURN HDR. PENT. TEST DRAIN CL & CP M217 1KC892 PENT. M217 OUTSIDE CONT. DRAIN ' CL & CP M217 1KC315B EXCESS LETDOWN HX RETURN HDR. PENT. ISOL. CLOSED M217 1XC310 EXCECC LETOO"" "2 RE'?? =? PEFT _ TE" "" ct s cp M217 ISMt& STM. GEN. lA HIGH POINT VENT CL & CP M154 ISM 106 STM. GEN. 1B HIGH ruir '"'3T tL & CP M261 1SM104 STM. GEN. 1C HIGH POT" i:ENT CL & CP M393 ISM DIM. GEN. HIGH POINT VENT CL & 5 44Y1 LYMll5B CONT. OUTSIDE ISOL. CLOSED ,
M337 1.YM127 CONT. ISOL. LEAK TEST VENT OPEN M337 1.YM82 CONT. INSIDE TEST DRAIN OPEN M337 CTIT. INSIDE TEST VENT OPEN M337 J1Yu4 CLOSED
- M24C l_ lLOWERCONT. VENT.UNITSUPPLYCONT.ISOL. (INSIDE)
CLOSED. M240 1RV32A MOWER CONT. VENT. UNIT SUPPLY CONT. ISOL. (OUTSIDE)
OPEh M240 1RV129 L k CONT. VENT. UNIT SUPPLY CONT. ISOL. (INSIDE) TEST VENT ,
OPENj / M24C 1RV316 l RV SYST k NT. PENT. M250 TEST VENT 1RV79A l UPPER CONT. VE UNIT SUPPLY CONT. ISOL. (OUTSIDE) gSED v M385 1RV80B l UPPER CONT. VENT. k SUPPLY CONT. ISOL. (INSIDE) [ CLOSED M385 CLOSED M385 1RV365 UPPER CONT. VENT. UNIT Sk CONT. ISOL PRES. TAP 1% l 1RV133 M385 UPPER CONT. VENT UNIT SUPPLY k ISOL. TEST V [ ISOL (INSID1:)0 PEN 1RV135 UPPER CONT. VENT UNIT SUPPLY CONT. k [ VENT ISOL. (OUTS,:DE)0 PEN M385 1RV10rA UPPER CONT. VENT UNIT DISCH. CONT. I IDE) CLOSED l J39C 1RV102B CLOSED M390 UPPER CONT. VENT UNIT DISCH. CO [ ISOL. (OUTS k M390 1RV113 UPPER CONT. VENT UNIT DIS [ CONT. ISOL. TEST VENT I INSIDf)OPEN M390
~
1RV120 UPPER CONT VENT UNI M SCH. CONT. ISOL. TEST VENT ISOL (O E)OPEN ED ^ ,. ' 2 7 9 1RV77B l LONER CONT. VE IT DISCH. CONT. ISOL. (OUTSIDE) .
1RV76A ENT UNIT DISCH. CONT. ISOL. (INSIDE) CLOSE} M279 LOWER C0h \ l 1RV124 lok NT. VENT UNIT DISCH. CONT. ISOL. TEST VENT ISOL. OPEN \ l M279 1RV317 WER CONT. VENT UNIT DISCH. CONT. ISOL. TEST VENT ISOL. CLOSED l M279
/
1F LOWER CONT. VENT UNIT RETURN PEN. ISOL. TEST VENT OPEN l l M279 p1129B A I!EADER CONT. ISOL. OUTSIDE , CLOSEIj l l T 20 O ENETRATIONS VENTED CL & CP = CLOSED AND CAPPED 1708 196
. . . . . . _ . . _ . . - . . _ . ._._ . ~
.'KE POWER COMPANY '
l .2 h PAGE 11 0F 8 _
yIRENUCLEARSMION VALVE EC N > E 4 e 5
* '3 Y 4 4 5 D** S y E 9s cc o V
.L a -
y F c g ALVE NO. . VALVE NAME 5 A HEADER CONT. OUTSIDE 733'6" TEST VENT CLOSED M220 let 284 n1.285 A HEADER CONT. INSIDE 733'6" TEST VENT OPEN M220 A HEADER C0dI. INSIDE 733'6 TEST VENT OPEN M220 LV1379
~
UNIT 1 CONT. STATION AIR OUTSIDE ISOL. CLOSED M219
~1VS12B UNIT 1 CONT. STATION AIR HEADER TEST VENT CLOSED M219 1VS25
~
UNIT 1 CONT. STATION AIR TEST VENT OPEN M219 1VS21 UNIT 1 CONT. STATION AIR HEADER ISOL. OPEN M219 IVS23
# M215 IVB49B UNIT 1 CONT. ISOL. CLOSED UNIT 1 CONT. HDR. TEST VENT CLOSED M215 IVB51 OPEN M215 IVB52 UNIT 1 CONT. HDR. TEST VENT OPEN M215 n153 UNIT 1 CONT. HDR. TEST VENT CONT. SAMPLE RETURN CONT. TEST DRAIN OPEN M325o IVX41 CLOSED M325 IV'" ^ CONT. SAMPLE RETURN CONT. ISOL. OUTSIDE
. 3 CONT. SAMPLE SUPPLY CONT. ISOL. INSIDE CLOSED A378'a CLOSED M378 IVX31A CONT. SAMPLE SUPPLY CONT. ISOL. INSIDE y OPEN M378 IVX34 l CONT.SAMPLESUPPLYCONT.ISOL.OUTSIDE 16410L S/G1AMAINFEEDWATERTOAUX.FEEDWATERN0ZZLEISOL[,,h))b CLOSED M378 ICF127t l S/G 1B MAIN FErow,u a TO AW.__ FEEDWATER N0ZZLE ISOL( tu uu n.u M378 NO t. u v1. . CLOSED M378 1CF12SB l S/G IC MAIN FEEDWATE _
~~
CLCSED M378 1CE.L2 WM AIN FEEDWATER TO AUX. FEEDWATER N0ZZLE ISOL.
1FW13 REFUELING CAVITY #1 TO FW PUMP #1 CONTAINMENT ISOL. OUTSIDE CLOSED M358; OPEN M358 IW14 REFUELING CAVITY #1 TO FW PUMP #1 LOW P'0 INT DRAIN CLOSED M358 IFWil l REFUELING CAVITY #1 TO FW PUMP #1 CONTAINMENT ISOL. INSIDE 0?EN M358 1F43 _I REFUELING CAVITY #1 TO FW PUMP #1 CONTAINMENT ISOL. OUTSIDr IFW12 f REFUELING CAVITY #1 TO W PUMP #1 CONTAINMENT ISOL. INSIDE CLOSED M358 1FW4E- WST TO REFUELING CAVITY #1 CONT. ISOL. OUTSIDE CLOSED M3772 IFW3d FW5T TO REFUELING CAVITY #1 CONT. ISOL. TEST CONN. _ CLOSED M377 IW6 FWST TO REFUELING CAVITY #1 INSIDE CHECK TEST CONN. OPEN M377 FWST TO REFUELING CAVITY #1 LOW POINT DRAIN OPEN M377 IFW3 CLOSED "! M331" lE10A CONT. H_ PURGE BLOWER OUTLET CONT. ISOL. OUTSIDE CLOSED lM331 11 CONT. H3 PURGE BLOWER OUTLET CONT. ISOL. TEST CONN.
CONT. H PURGE BLOWER OUTLET CONT. ISOL. TEST CONN. OPEN M331 IVE13 PT oCrTV i I V 9t i fs 1TA PONT. M_ Pf fDf'T' To AMTT f f C TYCTnt f'fW'T _ T e nt l
- PENETRATIONS VENTED CL 6 CP = CLOSED AND CAPPED 1708 197
N M SURI 13.2 PAGE 12 0F W UKE POVF.R COMPANY 1/A/1200/06 4
- GUIRE NUCLEAR STATION NIT # 1 M >
a e M
- 3 D** T TD o
- 1
- g 5 WW W - {1 a . E $ G d o
a ALVE NO. . VALVE NAME g
CLOSED M346 IVE6B CONT. H, PURGE TO ANNULUS OUTSIDE CONT. ISOL.
CLOSED M346 LVE9 CONT. H, PURCE TO ANNULUS CONTROL CLOSED M3261 INCL 41 NC PUMP MOTOR DRAIN TANK PUMP DISCH. LINE CONT. ISOL. INSIDE CLOSED M326 INCL 42 NC PUMP MOTOR DRAIN TANK PUMP DISCH. LINE CONT. ISOL. OUTSIDE CLOSED M326 INC154 NC PUMP MOTOR DRAIN TANK PUMP DISCH. LINE TEST DRAIN OPEN M326 INC153 NC PUMP MOTOR DRAIN TANK PUMP DISCH. LINE TEST VE!TI CLOSED 4 M243; lVQlA CONT. AIR RELEASE INSIDE ISOL.
CLOSED M243 IVQ2B CONT. AIR RELEASE OUTSIDE ISOL.
OPEN M243 lVQ13 CONT. AIR RELEASE OUTSIDE VENT CLOSED M384 IVQ6A CONT. AIR ADDITION INSIDE ISOL.
CLOSED M334 lVQSB CONT. AIR ADDITION OUTSIDE ISOL.
CLOSED M384 N ..
,lVQ1 p . s ,1, ,C,O.m.T A_IR RELEASE ADDITION PENT. TEST ISOL.
..- IVOSB
^NC~ YUE$0'TN I)I'L CONT'.iOINTJTSIDE ddSED * -
.3614 IN SB bu,6A NC PLW MOTOR OIL CONT. ISOL. INSIDE CLOSED M361 OPEN M361 INC210 NC PUMP MOTOR OIL FILTER LINE TEST VENT CLOSED
- M3 ~,3 7 1RF821 CONT. ISOL. OUTSIDE UNIT 1 OPEN M353 1RF824 CONT. ISOL. CHECK VALVE TEST VENT UNIT 1 OPEN M353 1RF820 CONT. SUPPLY ISOL. TEST VENT UNIT 1 CLOSED M353 1RF822 CONT. ISOL. TEST VENf UNIT 1 CL & CP M314 1ND55 NC LOOP 3'To ND SYSTEM CONT. ISOL. TEST CONN.
CLOSED M314 bD2A NC LOOP 3 DISCH TO ND SYSTEM CONT. ISOL.
CL & CP M314 IND54 NC LOOP 3 TO ND SYSTEM CONT. ISOL. TEST CONN.
1/ CC:'. ISOL. OC SIDE CLOSED M314 1N019/ "C 100" 1C TC "O 'r""
"O 1.00? 3 !O NO r"'.;' li, C;..!. ;5vs. v u a w:. CLodr.u M314 IN0'E
- PENTRATIONS VENTED L.' CL F CP = CLOSED AND CAPPED (m 3
.~
- "} (p, j NC194 l REACTOR COOLANT PUMP MOTOR OIL FILL TANK DISCHARGE ISOT ATTON v3 61*
(ACE' "'1,VE CLOS 0, P2'0" PL;r. "00: TO VENT INCL ^50).
VII MB INSTRUMENT ATR LOWER CONTAINMENT Ol'T9TBF T907 ATTON TF9T VFNT lI CLOSED 'M317 1 TN9TRf NFNT ATR TOW CONT. TP9T VrNT. OPEN lM317 VI393 M317 PENETRATION ISOLATION r,09rn M317 VI394 INSTRUkENT AIR LOWER CONTAINMENT TEST VrNT OPEN ) l M317 1708 198
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TP/1/A'2200/06 13
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. 1708 199
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.CLOSi-I 13.2 ACE.g0F j,
* ,UIRE SUCLIAR STA110N A 06 f9 f4 VALVI CFICVLIST SIT f /
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1708 200
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;).E :-D' ER CCM? A?;Y
-GUIRE NUCL E.!J. ST A1105 1/A VALVE Cd!CV!.IST 00/06 g f4 _
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y- 1 ,;5 g c r.-31 s,3 C w Y.H 13.2 A% f M f
-bike !;UCLEAR STATION
/1/ , /06 VALVE C:-:IC). LIST ff gg
. 1T f /
s E
- s 4 D
me m 's- g m
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w 3 *4 c@ . .. .
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. 1708 202 S 9 O
Pag 1 of 2 ENCLOSURE 13.3 TP/1/A/1200/06 All bellows of the following penetrations are vented to the annulus:
PF.NETRATION I INITIAL PENETRATION INITIAL PENETFATION INITIAL M212 M301 . M340 M215 M302 M341 M216 M303 M342 M217 M304 M343 M218 M305 M344 M219 M306 M346 M220 M307 M347 M221 M309 M348 M228 M314 M349 M229 M315 M350 M234 M316 M351 M235 M317 M352 M240 M318 M353 M243 M319 C354 M253 M320 M355 M254 M321 M356 M255 M322 M358 .
M256 M323. M359 M257 M324 M360 M258 M325 M361 M259 M326 M362 M260 M327 M369 u?74 M329 M370
"?75 M330 M371 .
M276 M331 M372 .
M277 M332 M373 M334 M374 M278 M335 M375 M279 M336 M376 M280 _
M337 M377 M281 M286 M338 M378 M300 M339 M379 i 1708 20'3
Page 2 of g
()
,) ,
ENCLOSURE 13.3 TP/1/A/120046 PENETRATION INITIAL FENETRATION INITIALI PENETRATION ' INITIAL M380 .
M381 r
M382 M383 M384 M385 M386
/
M387 M388 M390 i_ _ M394 .
M3100 M262 M153 M308 M440 M393 M261 M154 M441 e
1708 204
1 u . :.:, COM* ANT ENCLOSURE 13.4 ? AGE I 0F L I RE NUCLEAR STATION TP/1/A/1200/06 I! # I VALVE CHECKLIST r
VALVE NAME POSITION INITIAL
~_VE NO.
CLOSED JIl27 REAACTOR BUILDING HEADER ISOLATION TEST HEADER TO UNIT 1 CONT. HEADER ISOLATION OPEN
/Il97 VIl93 TEST AIR DRYERS ISOL. OPEN JIl96 TEST AIR DRYERS E DISCHARGE THROTTLE TO TEST HEADERS C10SPD JIl99 TEST HEADERS TO UNI 1 CONT. THRU WL SYST. ISOL. OPEN JI294 B AIR FILTER INLET OPEN
.I295 B AIR FILTER OUTLET OPEN
*L363 INSTRDfENT AIR TO CONTAIDfENT FOR LEAK TEST - ROS A CONT. VENT. UNIT DRAINS OUTSIDE CONT. ISOL. OPEN
{i s'L3 62 CONT. VENT UNIT DRAINS TO VUCDT ISOL. CLOSED 4L321A CONT. VENT UNIT DRAINS INSIDE CONT. ISOL. OPEN i'L361 VUCDT INLET CLOSED VIl48B INSTRDfENT AIR UPPER CONT. OUTSIDE ISOLATION OPEN VI201 TEST HEADER TO ICE CONDENSER AREA ISOL. OPEN VI24 D AIR FILTER INLET OPEN V125 D AIR FILTER OUTLET OPEN 1708 205
F88 _1. f _L .
(; ,
^
ENCLOSURE 13.5 TP/1/A/1200/ 06 SOAP BUBBLE TEST ALL OF THE FOLLOWING HOT PENETRATIONS PENETRATION INITIAL PENETRATION INITIAL PENETRATION '1NITIAL h2:5- M329 , .
, n F2 3 ' - M330
' \
k M#
M235 ruu
- n2 5 % M334 M256 M335 4C7 M336 h255 - M338
_ u, c n - M339 lH d M M @h6 }g-f M340 2.M262 /cs c by M341 M274 g f M275 M343 v277 M344 M278 M347
_,,,_M280 M348
% M349 M286 M350 M300 M351 M301 M352 M302 M360 M303 M375 M304 M393 M M3100 v106 M440 Eurm<
v10R i M441 %( -
pt a 6 v1nQ t i 19,occ m-M314 I'i D M316 tu 5 a -
M319 M321 1708 206
O -
O ENCLOSURE 13.6 TP/1/A/1200/16 The combined air temperature is considered stabilized when the value of C is less than 0.5 F/hr A B C Average T change Average T change C=A-B TIME TEMF Last 3 Hours Last Hour
# ~
( hr) F/hr t(hr) T( F) k n-3 -T n -
n-1 n t
g gw m Et+1 Xmm Eg+2 XXXXXX. h .AAXAXX Ut+3 Et+4 t .s t
t t+6 Et+7 E
't+8
*t+9 Et +10 Et+11
*t+12 1708 207
hh, (' (j Soc.edure Goa3e#
12.
Re3 a of a
.,d E NCL o su R.E 13.7 TP/#/4 /i 2.oo/o(.a
~l mPo s E b LE R A RRTE C ALC MLRT Io N In orker ko Sck. Yke forbi n e,. fow mei. t r d'o hde. rQ. a.c ek imposek led of .2o% per h3 , & voJu.e of a4per da3 neeh fo be converfeb fo C FIA o.t f he. fi me the. flow ender is being real.. TAe follour.n3 l ogic. was usek .w bderm,n3
+his convers,on :
Q. Wha $ iS -fl>e expression For .2.0% of he orf *no I enacs ?
A. .zoVM, = . 20% R V. /R, T,'
O.6)4d volume of 4Ae 4,me. & rneier is be,r3 reak does f Ac.s mass represend?
R. 2c% RV, /R,T, = Py /R,T, t ,Aere 'a ~ derofes & f,me 4/se meter .s se.n3 real.
~
y . 7o4 k M EtT,t '
2.0% 8 Tt%
2- '~ R J, Pt 5 T, Q. Neo man y CF M are_ IosY' if .?_o%/da3 of fAe origina.l rnau is lost
- 9. v,/k.n = 0 ze A3 )(P,Tt V.[PJT,)( G 24b)(IAr/ h .n) 3
(/en3n = [.zoV/da3 )(Pg2./PT) t h,2,3 9,497 R [(44o )
V, cm = (f)(eh f8 '")
Wh ttre 'l*represed5 C o ftb', YIott 5 Of ib t. orig.ne l ma s5 ank
7
- egpreSeft 5 CodiY.ons oY iht, tsme. Yhe Ilow meter
, 2
6 -
o -
ENCLOSURE 13.7 TP/1/A/1200h6 IMPOSED LEAK RATE CALCULATION In order to set the turbine flow meter to the~ required imposed leak (Limposed) of 0.15% per day, the value of %/ day needs to be epnvert to SCFM as follows:
e V I 12NVO V = -1,193, t -f t 3 Mass of air inside the containment at time t = R Tt (c
P P = 14.7 psia b ss of I scf of air =
RT T = 68 F - 528 R s s T
in terms of %/ day of the containment y,f ,
t s x 24 x 60 x 100 %/ day air mass , V P t s The required imposed leak (Limposed)
/ f .15%/ day is converted to SCFM by:
[ 0.15x P t L/kposed 3.35233 x 10-3T g P
L imposed
=44. 745 x 10 I f SCFM
/
T = erage temperature of the conteineent at time t when the imposed Isak test is initiated ( R)
P = Average pressure of the containment at time t when the imposed leak test is initiated (PSIA)
Cl,WN N e b W-
=
~
1708 209
O
~
6 -
TP/1/A/1200/06 ENCLOSURE 13.8 THE CONTAINMENT VESSEL LEAK RATE TEST CALCULATION A.1 DEFINITION OF SYMBOLS P = Absolute pressure in the Containment Vessel (PSIA)
T = Weighed average absolute temperature of the Containment Vessel cir compartment ( R)
Wg = Normalized mass of containment vessel air at i data point (dimension -less)
P = Partial pressure of water vapor (PSIA) lapsed the (hr) ti=
V = assigned volume fraction of k* sensor (Fraction of volume)
T = recorded temperature of k sensor ( R) .
k hg= estimated value of Wg in the least square fit calculation b = slope of the least square fit line (fraction /hr) ,
L = 95 confidence value of L , (%/ day) am(95%)
L = measured containment leakage rate (%/ day) a = y intercept of the least square fit line (dimension less) 2 S
y = the variance of W g 2
S b
= the variance of b A.2 SUBSCRIPTS u = upper containment compartment L
= lower containment compartment I = Ice Condenser compartment v = vapor 1 = data point at start of test i = 1* data point (i = 1 to N)
N = Final data point of a given set th k = k sensor 1708 210
E) -
O A.3 .
r ILRT cen.put er The following are the essential equations u. sed in developing program:
(tg 46 )
741
# f s 1 )(tr
- 1 f
0.M0 (P-P )g i+ 0. 3G& i (P-P )': + . M2 l(P-P ) '.
" lu "I L (s T" /Il T / \ T /
v= qpf t
'f i p., .
+ . M '(F-P )q 0.560.(?-P )', + 0.048,T (P-Py ) i y,
( T ,/" T' \ T/
T = IT;,Vk 5' = b t +a b= net +Wi - (EWi l IEty) nit f
2 _ (It,)2 IW1 (Itg) - (Itg) (It gWg)
*~ 2 nit - (It g)2 f
Las =-b. M Lam (95%) = Lam i tS b t
value is on enciesed table corresponding to f = N-2 and 0.975 S- . I(Wg - a - btg)
N-2 32 3,2 3,2 I(t -t) Itg -(Itg) , Itg 2-tit N
gwD WD W3 h 1708 211 dAr L,
gg g
) '
(,".% -
ENCLOSURE 13.9 TP/1/A/1200/06 The following penetrations, flanges and valves are n t exposed to test pressure due to system operation or test alignment. Type "C" preoperational result leak test shall be assigned to these penetrations and the total value (L, ,,) is added to the ILRT test results.
PENETRATIONS SYSTEM VALUE (% DAY)
M373 Glycol Supply for Ice Condenser M372 Glycol Supply for Ice Condenser M386 Air Supply to Ice Condenser Door Seal and Ice Condenser Pressurization Line M359 Air Supply to Personnel
- Hatch Door Seal i g2 u. O i
(t }G G g 7 [ p' Total (L, )=
u l') #} .
O e
=
1708 212
~
O C ENCLOSURE 13.10 TP/1/A/1200/06 CE CONDENSER AIR HAhTLING TIMER DEFROST PATTERN ups of Air Handling Units Def r6sted one at a time for one hour vals. r _
- R HANDLING UNIT AS FOUhT TIMER SETTING INITIAL 1A1A 1A4A 1A7A 1A10A 1A13A IB2A 1BSA 1BSA .
1BilA ,
IB14A 3A 1A6A 1A9A LA12A 1A15A 1314 134A 1B7A 1310A .
1B13A 1A2A .
lASA lASA lAllA 1A14A 1B3A 1B6A
'?9A sl2A 1B15A ,
1708 213
~
h -
(~ ~1 ENCLOSURE 13.10 (cont)
GROUP AIR HANDLING UNIT AS FOUND TIMER SETTING INITIAL lA1B 1A4B r 7 1A7B 1A10B 1A13B 1B2B 1B5B 8 1B8B 1B11B 1B14B 1A3B 1A6B ,
9 1A9B .
lA12B 1A15B 1B1B 134B 10 137B 1B10B 1313B 1A2B 1A5B 11 1A8B ,
lA11B 1A14B 1B3B 1B63 12 1B9B 1B12B -
1B15B 1708 214
() ENCLOSURE 13.11 TP/1/A/1200/06 Page 1 of 3 McGuire Containment Structural Integrity Test Visual Inspection
~
r In addition to the inspection during the structural integrity test, a prelim-inary inspection shall be made to familiarize the inspectors with the as-built appearance of Containment and establish a base line for the test inspection.
During the preliminary inspection particular attention should be given to local inperfections due to weld distortion in addition to the areas identified below.
Areas where noticeable distortion is found shall be identified for future reference.
The inspection tuam shall include a Structural Engineer from Design Engineer-ing who is familiar with design of Containment to act as team leader and an Engineer from Construction familiar with erection of Containment.
A valk-through inspection shall cover all accessible areas outside Contain:a'nt.
The inspectors should lock for the follesing:
- 1) Unusual or excessive local deformation, crAed paint could indicate large load deformations.
- 2. Twisted or warped vertical or horizontal stiffeners.
- 3. Cracked welds particularly fillet welds to attachments.
- 4) Cracked concret'e at the base of Containment.
- 5) Any location where the clearance between Containment and platforms, hangers, piping or other equipment rigidly attached to the shell wall is less than 13/4" in any direction.
1708 215~
Page 2 of 3
() .
(' N
- 6) Any location where the clearance between the shell wall and any plat-forms, hangers, piping or other equipment rigidly attached to Contain-ment is less than 13/4" in any direction.
r The following areas should be given special attention during the inspection:
- 1) Fillet welds near the ends of vertical stiffeners.
- 2) Attachments for platforms or hangers.
- 3) Intersection of cylinder and concrete foundation.
- 4) Intersection of cylinder and dome. -
The Containment Vessel will be divided into 4 areas:
Area 1 El. 725 - 746+5 Area 2 El. 746+5 - 766+5 Area 3 El. 766+5 - 796+5 Area 4 El. 796+5 - 894+3 Inspector will inspect an assigned area and document the findings on en-closure 13.11. The Inspection Team Leader will review all abnormalities identified on enclosure 13.11 and note the resolution for those he finds accepta ble. All abnormal inspection findings not resolved by the team leader during the test will be resolved by Design Engineering.
w
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{ Page 3 of 3 ENCLOSURE 13.11 TP/1/A/1200/06 .
Containment Structural Integrity Test V,isual Inspection Area Elevations All inspection findings shall be listed below:
Resolution of Location Comments Abnormal Findings Inspector Date Inspection Team Leader Date
!i;)8 217
O- O r81<1 ENCLOSURE 13.12 TP/1/A/1200/06 Test Procedure Test Result Instrument Conservative Type of Leak Final Test Result Error Rate Test B TP/1/A/1350/24 Electrical Penetration 0 Ring Leak Rate Test r B TP/1/A/1200/17 Fuel Transfer Tube Leak Rate Test .
B f
- TP/1/A/1200/18, Upper l
; Containment Personnel Lock Leak Rate Test B TP/1/A/1200/19, Lower Containment Personnel Lock Leak Rate Test B TP/1/A/1200/20, Equipment !
Hatch Leak Rate Test ,
C TP/1/A/1200/16 Isolation i Valves Leak Rate Test ,
TOTAL Initial /Date
/ Verify that the total value of BANDC test is less than or equal 54.267 SCCM (0,12% per day of the containment air weight. Conversion from % to SCCM is made at 800F)
Data Recorded by Date 1708 218
m E '
Page a of (,
9 YY '05" 6 '3 0
oe ,X. W'lA/'l
- l* , ip , y TEST In srt:amE uTS Pag e /of.3 T M Sveu M E MT MobEL MO: M 4 Ma WRc Tu RE k 7h Mo e
Nu modro n 914 Leed s feJertkrap S Y2 Ac-Il3 8 0
~
b.3,4a f Ir fec e caple c 2,30 Le&s ( % %p svzac -uset D,3ifal Cloc.k toI99 O Leelt / Mo-tbap 5 VI A c - 115 8 2.
Scan Conteo liec 70 o 7 2. Leels / No hp sv2 Ac - n 383 zuo Leels f No hp s Ylec - 1,28 4-b 3. fat Nster Dewpo,d Nyg romder- !EooAP 6enera l Easter n S PIRC - III 7 4-Dewpe.nt H73 romder 1200 AP 6eneral Eosha $P.I AC - /// 76 bewpo.ni 9;,3 re rr.ete r l'Eco A P Gen eral Eas1ce n SYI6c - /// //
77c - C<S -G 3 5 f~ low M der PEI -cu,61L P !cua Te'chne/o3 y $ yIPC. - " 3 3 4-btR-Oooo Pu s % SV P R.F - // c 0 3 Pressace 6s3e.
I're s r u c e. 6 a a e. b tRc6 oo o Eu s 'cos 5FPe F - I'0 0 4 a
Pressure Sage. but -c oc o Eusko srFRF-e/ cod
%ltwder 2000 Rs-2 New poe4 5 K[Ac - l'US 4 Vc I4 meter 2000 RS-2 Mea:Forf S P.T. FC - // Eb'.
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APPENDIX E LOCAL LEAK TEST
SUMMARY
1708 222
A. Type B Test: Type B Local Leak Rate Test is required for the following penetrations:
- 1. Air locks
- 2. Electrical
- 3. Fuel transfer tube flange
- 4. Equipment Hatch
- 5. Bellows on mechanical penetrations All were tested except bellows on mechanical penetrations prior to the conducting of ILRT.
Two methods were used to perform Type B tests: Make-up air flow measure-ment and pressure decay. The make-up air flow measurement method consisted of a digital air flow indicator which was used to indicate the volume rate of air required to maintain tested volume at constant pressure. This method was used for air locks, fuel transfer tube flange, equipment batch. Table 1 lists test results. The pressure decay method consisted of monitor pressure decay rate of tested volume and used ideal gas law to determine leak rate. This method was applied for electrical penetrations and bellows on mechanical penetra-tion. Table 1 lists test results. All tests were performed under approved preoperational test procedure. B. Type C Test: All isolation valves identified in McGuire FSAR Table 6.2.4-2 were tested using the make-up air flow measurement method. Tests were performed prior to the conducting of ILRT test. Table 2 lists test results. C. Any penetration modifications after the ILRT which affect the leak tight characteristic of the Containment Building will be local-leak tested. E-1 1708 223
TABLE 1 Type B Test Results PENETRATIONS PROCEDURE TEST DATE RESULT (SCCM*) Normal Air Locks TT/1/A/9100/14 1300 SCCM Emergency Air Locks (Note 1) 920 SCCM Fuel Transfer Tube Flange TP/1/A/1200/17 4/23/79 3.2 SCCM Electrical Penetration TP/1/A/1200/13 3/17/79 - 3/27/79 3.9 SCCM Equipment Hatch TP/1/A/1200/20 9/11/79 74 SCCM Bellows on Mechanical Pene. TP/1/A/12te,15 Note 2 Note 2 (Note 2) Note 1: Tests were performed on temporary procedure. See Test Log (Appendix C) for reasons. Note 2: Test will be performed before plant startup.
- SCCM = Standard Cubic Centimeter per Minute 1708 224 E-2
TABLE 2 Isolation Valve Leak Test Result PENETRATION VALVE NL'MBER VALVE TYPE TEST DATE RESULT (SCCM)* VALVE PENETRATION M216 NC57 Check 5/19/79 0 0.2 NC56B Diaphragm 0 M212 NC54A Globe 7/19/79 0 0.2 NC53B Globe O M326 NC141 Diaphragm 7/28/79 0 0.2 NC142 Diaphragm 7/21/79 0 NC261 Check 7/28/79 0 M330 NI48 Check 3/21/79 0 6.4 NI47A Globe 6.2 M321 NI95A Globe 5/06/79 18.1 18.3 NI196B Globe 18.1 NI120B Globe 18.1 NI436 Check 1.5 M259 NB260B Globe 10/27/79 20.6 22.6 NB262 Check 0.4 M373 NF228A Diaphragm 3/13/79 4.49 4.69 NF229 Check 6/01/79 2.0 M372 NF234A Diaphragm 3/13/79 0.05 0.25 NF233B Diaphragm 0.05 M348 NI266A Globe 7/19/79 0 0.20 NI267A Globe O NI264B Globe O NI336 Relief 0 M374 WL65B Diaphragm 12/11/79 0.13 0.23 WL64B Diaphragm 0.13 WL264 Relief 0.13 M360 WL39A Diaphragm 7/03/79 0 0.20 WL41B Diaphragm 0 M375 WL2A Diaphragm 3/13/79 0.6 4.6 WLIB Diaphragm 4.4 WL24 Check 0.6
*SCCM - Standard Cubic Centimeter per Minute E-3
TABLE 2 Isolation Valve Leak Test Result PENETRATION VALVE NUMBER VALVE TYPE TEST DATE RESULT (SCCM)* VALVE PENETRATION M356 WE13 Globe 10/27/79 9.8 10 WE23 Globe 9.8 M235 NM3A Globe 11/14/78 0.20 194 NM6A Globe 192 NM67 Relief 0 NM7B Globe 0 M309 NM26B Globe 10/29/79 0 0.21 NM25A Globe 0.1 NM22A Globe 0 NM68 Relief 0 M280 NM72B Globe 7/14/79 0.8 2.0 NM75B Globe 0.6 NM78B Globe 1.8 NM81B Globe 1.4 NM69 Relief 0 NM82A Globe 0 M322 KC47 Check 3/20/79 0 4.4 KC429B Globe 4.2 KC430A Globe 4.2 M307 RN252B Diaphragm 11/03/78 1.25 1.45 RN253A Diaphragm 1.25 M315 RN277B Diaphragm 11/17/78 0 0.2 RN276A Diaphragm 0 M213 VP17A Butterfly 6/04/79 0 0.2 VP18B Butterfly 0 M318 VP19A Butterfly 6/04/79 28 30 VP20B Butterfly 28 M367 VPIB Butterfly 4/06/79 50 52 VP2A Butterfly 50 M454 VP3B Butterfly 4/09/79 90 92 VP4A Butterfly 90 M357 VP6B Butterfly 4/09/79 30 32 VP7A Butterfly 30
- SCCM = Standard Cubic Centimeter per Minute E-4 1708 226
TABLE 2 Isolation Valve Leak Test Result PENETRATION VALVE NUMBER VALVE TYPE TEST DATE RESULT (SCCM)* VALVE PENETRATION M456 VP8B Butterfly 4/10/79 70 72 VP9A Butterfly 70 M368 VP10A Butterfly 4/16/79 30 32 VP11B Butterfly 30 M455 VP12A Butterfly 4/19/79 95 97 VP13B Butterfly 95 M119 VP15A Butterfly 4/19/79 61 63 VP16B Butterfly 61 M337 YM116 Check 10/28/78 4.0 10.6 YM115B Globe 10.4 M240 RV32A Butterfly 9/21/79 15 52 RV33B Butterfly 50 RV130 Check 50 M390 RV101A Diaphragm 11/6/78 0.9 1.1 RV102B Diaphragm 0.9 M385 RV79A Diaphragm 3/16/79 24 26 RV80B Diaphragm 24 M279 RV76A Butterfly 7/08/79 6 80 RV77B Butterfly 60 RV126 Check 6 M215 VB49B Gate 4/20/79 0 6.2 VB50 Check 6 M219 VS12B Globe 11/01/78 .05 0.25 VS13 Check .03 M378 VX34 Diaphragm 4/06/79 2.1 2.3 VX33B Diaphragm 1.9 VX31A Diaphragm 0 M325 VX30 Check 3/26/79 0.7 0.9 VX40 Diaphragm 0 M358 FW11 Diaphra gm 7/06/79 0 0.4 FW13 Diaphragm 0.2 FW67 Check 0
- SCCM = Jtandard Cubic Centimeter per Minute E-5 1708 227
TABLE 2 Isolation Valve Leak Test Result PENETRATION VALVE NUMBER VALVE TYPE TEST DATE RESULT (SCCM)* VALVE PENETRATION M377 FW4 Gate 6/05/79 0 0.2 FW5 Check 0 M221 WL321A Butterfly 12/08/78 4.6 48 WL322B Butterfly 49.2 WL385 Check 4.6 M359 VI161 Check 4/01/79 1.35 1.55 VI160B Globe O M386 VI149 Check 3/16/79 0.7 2.6 VI148B Globe 2.4 VI362A Globe 2.4 M317 VI124 Check 4/15/79 4.0 42 VI150B Globe 11 M220 VI129B Globe 10/28/78 4.9 5.1 VI40 Check 2.4 M331 VE10A Diaphragm 7/05/79 0.2 0.4 VEll Check 0 M243 VQ1A Diaphragm 11/22/78 3.72 3.92 VQ2B Diaphragm 3.26 M384 VQ6A Diaphragm 11/23/78 0 0.2 VQSB Diaphragm 0 M361 NC195 Globe 8/01/79 12 12.2 NC196 Globe 8 NC259 Check 8 M353 RF823 Check 7/15/79 0 0.2 RF821 Diaphragm 0 M376 KC322 Check 6/02/79 0 0.2 KC320A Diaphragm 0 M355 KC333A Diaphragm 5/01/79 .25 1.2 KC332B Diaphragm 1 KC280 Check 1 M327 KC338B Diaphragm 7/01/79 70 90 KC340 Check 0 M320 KC425A Diaphragm 5/14/79 30 42 KC424B Diaphragm 40 KC279 Check 40
*SCCM = Standard Cubic Centimeter per Minute 1708 228 E-6}}