ML20081B987
| ML20081B987 | |
| Person / Time | |
|---|---|
| Site: | Peach Bottom, 05000000 |
| Issue date: | 04/04/1977 |
| From: | Ullrich W PECO ENERGY CO., (FORMERLY PHILADELPHIA ELECTRIC |
| To: | |
| Shared Package | |
| ML20081B916 | List: |
| References | |
| FOIA-83-296 NUDOCS 8310310064 | |
| Download: ML20081B987 (109) | |
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PHILADELPHIA ELECTRIC COMPANY PHILADELPHI A PEACll BOTTOM ATOMIC POWER STATION i
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DOCKET NUMBER 50-278 ;
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.- REACTOR CONTAINMENT BUILDING }
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j i INTEGRATED LEAKAGE RATE TEST REPORT N
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i SUBMITTED TO s y
- THE UNITED STATES NUCLEAR REGULATORY COMMISSION t
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PURSUANT TO FACILITY OPERATING LICENSE NO. DPR-56
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9310310064 830706 PDR FOIA CONNORB3-296 PDR
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. , 1 Philadelphia Electric Company Peach Bottom Atomic Power Station Unit No. 3 Docket Number 50-278 REACTOR CONTAINMENT BUILDING 7
. .i INTEGRATED LEAK RATE TEST REPORT 4 APRIL 4, 1977 7
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4 p Submitted To J
h The United States Nuclear Regulatnry Commission I Pursuant To
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i5 Facility Operating License No. DPR-56 i
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A Preparation Directed by:
4 W. T. Ullrich, Superintendent 3 Peach Bottom Atomic Power Station b!
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k TABLE OF CONTENTS PAGE 1
I. INTRODUCTION 2
II. TEST SYNOPSIS l 4 6 III. TEST DATA
SUMMARY
.)
4
.f 3
( A. Plant - Information 1 3 D B. Technical Data Test Data - Type A Test 3 C. '
4 T D. Test Equipment - Type A Test b Test Results - Type B and Type C Tests 7 A E.
3 7 F. Information Retained at Jobsite 4:.
i! I' a ,
d ,; A-1
- APPENDIX A BECHTEL ILRT COMPUTER PROGRAM
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A-1
- I. DESCRIPTION
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? A-1 il ! II. EXPLANATION OF PROGRAM h
d A-3 III. COMPUTATIONS 1f E
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F F
G m M I
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TABLES PAGE 9
III.C.1 Summary Data III.C.2 Leakage Rate : Total Time Calculation 10 Constant Volume Leakage Rate: Total Time Calculation, 11 III.C.3 Trend Report - Constant Volume l
-l j Leakage Rate: Mass Point Analysis 12 III.C.4 Constant Volume Leakage Rate: Total Time Calculation 13
- III.C.5 Free Air Volume Varied l
Leakage Rate: Total Time Calculation, 14 III.C.6
' ' Trend Report - Free Air Volume Varied h
j III.C.7 Leakage Rate: Mass Point Analysis 15
- Free Air Volume Varied
\ Measured and Corrected Data Summary 16 - 48 l III.C.8 j (a) thru (gg)
Summary Data Verification Test 49 III.C.9 Leakage Rate Verification: Total 50 III.C.10 Time Calculatior.- Constant Volume Leakage Rate Verification: Total 51
- III.C.ll Time Calculation, Trend Report Constant Volume
(
h i
2 l -
+ . .
' TABLES (Cont'd.)
PAGE 52 III.C.12 Leakage Rate Verification:
Mass Point Analysis - Constant Volume 53 III.C.13 Leakage Rate Verification: Total i Time Calculation - Free Air Volume Varied 7
54 I
III.C.14 Leakage Rate Verification: Total l Time Calculation, Trend Report 3
" Free Air Volume Varied
- 55 III.C.15 Leakage Rate Verification:
v Mass Point Analysis - Free Air
.g Volume varied 4
Measured and Corrected Data Summary 56 = 81 h III.C.16 1 (a) thru (=) peakage Rate Verification
- f.
i
' Type "B" Test Summary 82 - 90
) III.E.1 l
(a) thru (i)
I 91 - 99 5 III.E.2 Type "C" Test Summary
{ (a) thru (i) 4 I
t FIGURE
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A-8 A-1 Computer Program Logic Diagram J
I c
-iii-
.. INTRODUCTION The Reactor Containment Building integrated leakage rate test is performed to ensure the leak tightness of the primaryand containment to vessel and attached piping up to the boundary valves, i
satisfy PBAPS Tech. Spec. 4.7.A.2 and Appendix J to 10CFR50.
l l Actual leakage is calculated from the measured pressure the peak decay rate with the containment vesselPressure, pre'ssurized temperature and dew point to Pa.,
accident pressure 49.1 psig.
data is computerl,rocessed p and reduced to a leakage rate expressed in percent of initially contained volume per day.
test,is reported, along with individual penetration test The results, in accordance with the requirements of 10CFR50 appendix J.
l 1
ST SYNOPSIS
. , 3 com-for the ILRT at Peach Bottom Unit yessurization of tne containment Peak test pressure was reached early unced late Saturday, April 2, 1977. During the local survey, anday. A local leak survey was conducted. d leakage rate from the con-
- na lyses of the contain=ent ILRT data indicateInvestigation of possible sources of
- ain=ent of about 10 scfm of air.;eakage continued by checking all system pip h i lightly (drop-
- t was also noted that reactor vessel water level was c ang ng sThe cooldown was causing ping) during cooldown from residual heat removal. lowering the reactor vessel water level to contract, It was
- he reactor coolant free air volume.
thereby causing a small change in the containment decided to determine what effect the changing free air l volume would would have d con-en the calculated leakage rate since an increasing free air vo um stant in the leakege rate calculations.
d that Based on calculations by PECo engineers at the jobsite it was 3 increase determine in con-
' a drop in reactor coolant tempe.rature of 10F caused a 5 f tThe water temperature in Also tainment free air volume due to water contraction. ture changes.
the operating recirculation loop was monitored for tempera reactor vessel water level was monitored for comparison.
The computer program was modified to compute leakage During therate assuming both a 8 hour9.259259e-5 days <br />0.00222 hours <br />1.322751e-5 weeks <br />3.044e-6 months <br /> constant free air volume and a variable free air volume. 3 The total free peak pressure ILRT the calculated 3 volume change was 24 ft .The calculated leakage r air volume was about.286,000 ft d within 1.8" constant free air vofume versus a variable free air volume agree (The constant -
h h the l of volume formula yielded,a leakage rate that was 0.005%/ofday each other based o'n the Total-Time Method calculations.
hig er t anSo
, variable volume formula.
Results from calculational methods are attached. fa The leak survey continued until the leak was discovered on the air side oThe torus water level instrument.The containment leakage valve.
rate then came into specificat (8) hours.
was successfully completed with a test duration of eight i t ly A verification test was then conducted (by imposing a leak rate approx ma eility to acc l
equal to La) which verified the ILRT measurement system's abThe containment was monitor and calculate the leakage rate. System.
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' with air exhausted directly to the Standby Gas Treatment i
1 i 1 l l
l 2
., TEST DATA
SUMMARY
A. PLANT - INFORMATION Cwner: Philadelphia Electric Company Plant: Peach Bottom Atmoc Power Station - Unit 3 Location: Delta, PA Type: Mark 1, Bk'R Jata Test Co=pleted: April 4, 1977 B. TECHNICAL DATA d 1. Containment net free air volume, 278,000 fc 3 including dryvell and torus. (FSAR) 56 psig
- 2. Design pressure 49.1 psig i
a
- 3. Calculated peak accident pressure
- 4. Containment te'mperature limits for ILRT 40-1350F j
C. TEST DATA - TYPE A TEST l '.
- 1. Test Method. Absolute Mass-Point and Leakage
- 2. Data Analy' sis Technique Rate (Total-Time) 49.1 psig
- 3. Test Pressure Maximum Allowable Leakage Rate (La) 0.5%/ day 4.
0.375%/ day
- 5. 75% of La Calculated Leakage Rate: Leakage Rate Upper 95%
- 6. Confidence Limit
(%/ Day)
- a. Free air volume assumed constant 0.296 0.322 i i) Mass Point Method 0.281 0.372
' 11) Leakage Race Point Method
- b. Variable free air volume assumed 0.278 0.304 i) Mass Point Method 0.276 0.352
- 11) Leakage Rate Point Method 1
3
L _ . _ . _ _ _ . _ _ _ _ _ -
Containment Free Air Volume C. TEST DATA - TYPE A TEST - Cont'd. Assumed Constant Variable Verification Test I= posed Leakage 0.483 / day 0.483%/ day 7.
Rate (corrected for temperature and pressure at the ficwmeter), Li
- 8. Verification Test Measured Leakage Rate, Lvm
- a. Mass Point Method 0.671 0.665
- b. Leakage Rate Point Method 0.669 0.661
- 9. Verification Test Limits
- a. Upper (L1 + Lam + 0.25 La)
- 1) Mass Point 0.904 0.886
- 11) Total Time 0.889 0.884
- b. Lower (Li + Lam - 0.25 La) i) Mass Point 0.654 0.636
- 11) Total Time 0.639 0.634 0
- 10. Report Printouts Attached are the Report Printouts for the ILRT and the ILRT verification test. Printouts are provided for the Mass-Point and Leakage Rate Point (Total-Time) Analyses for containment free air volume constant and containment free air volume assumed variable. Information provided on Report Printouts includes: containment average temperature and absolute air pressure for each data set; calculated leakage rate at the upper 95% confidence limit; and, measured lea,k age rates.
! D. TEST EQUIPMENT - TYPE A TEST
- 1. Pressure (1)
Texas Instruments Precision Pressure Gage Model 145-02, Range C
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Bourdon Tube Type 2 Range: 0 - 100 psia-Accuracy: 2 0.015% of reading Repeatability: 2 0.001% of full scale or 2 0.001 poia 4
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- . ~ . . . -
D. TEST EQUIPMENT - TYPE A TEST - Cont'd.
- 2. Temperature (12)
Leeds and Northrup Resistance Temperature Detectors Model 8197, 100 ohm copper Range: 32 - 250 F Limit of Error: 1 0.50F Calibrated Accuracy: 2 0.3 F or better Repeatability: 2 0.10 F
- 3. Vapor Pressure
-I a. Sensors '
(6)*
i( CTE Model 84P Dew Point and Dry Bulb Tmperature Sensor
) Dew Point Range Limits: -200F to 1300F i Dry Bulb Range Licits: -200F to 140 F j b. Analyzer Vap-Air 6-Channel Dewpoint Control and Readout Module for i Remote Readout on Item 4 below:
i h Range: 0 - 100 F Dewpoint Accuracy: 1 10F (Instrument ambient +600F to +1000F )
2 20F (Instrument ambient -200F to +1400F)
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ij Repeistability:
Output:
! 0.50F 0 to 10 mVDC for 0 -100 F Dewpoint t
- 4. Temperature and Vapor Pressure Readout Leeds and Northrup Numatron Digital Display Model 914-0001-999-1 i Range 1: 0.00-150.00 F Range 2:
Resolution:
0-10 mVDC 0.001 mVDC
} Resolution: 0.010F Conformity: 2 0.010F Accuracy: 1 0.005 mVDC t 1 digit
- 5. Overall System Figure of Merit (based on repeatability error):
! 0.03%/ day
- N3TE: One drywell temperature sensor malfunctioned. Therefore, only fiv'e readings were taken. Volume fractions were recomputed. Of the
- five dewpoint temperature sensors, three were in the dryvell and two were in the torus. Since the torus atmosphere was saturated (i.e., drybulb temperature, dewpoint temperature and wetbulb l temperature are equivalent) the torus air drybulb sensors were l' used to monitor dewpoint temperature to improve readout accuracy.
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3, TEST EQUIPMENT - TYPE A TEST _- Cont'd.
- 6. Temperature and Vapor Pressure Sensor Locations.
,1 VAPOR PRESSURE DEWPOINT i
Distance From Volu=e Elevation Azimuth
'(Deg.) Center (Ft) Fraction
',} _ (Ft)
- ] 45 16 0.130
- 1. Drywell 200 Q 0.180 162 225 20
- 2. Drywell 24 0.262 Drywell 150 328 L) 3.
240 66 0.214
- 4. Torus 115 0 66 0.214
- 5. Torus < 115 E. 1.000 t
' TEMPERATURE f
16 0.065
- 1. Drywell 200 45 0.065 200 225 16
- 2. Drywell
[ 90 20 0.073
- 3. Drywell 162 h 20 0.073
- 4. Drywell ,[ 162 270 24 0.085
- 5. Drywell .' 150 320 0.085 t
150 130 24
- 6. Drywell f 127 90 22 0.050
- 7. Drywell f
s1 8. Drywell 127 270 22 0.050 0 0 0.025
- 9. Dryvell 120 120 66 0.143
- 10. Torus 115 240 66 0.143
- 11. Torus 115 0 66 0.143
- 12. Torus 115 1.000 W
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- 7. Verification Flow (Superimposed Leakage Rate)
[ Brooks Hi-Accuracy Full View Rocameter N
Model 1110 FV 24 h Range: 0.7 - 7 scfm Accuracy: 1 1% of reading t
6
gST RESULTS - TYPE B and TYPE C TESTS is provided by Phila-A Su= mary of Results of Type B and Type C tests (Tables III.E.1,and III.E.2.)
delphia Electric Company.
I'iFORMATION RETAINED AT JOBSITE included in the summary but is retained The following information is not at the jobsite and available for review:
9
- 1. Data and Data Reduction
- a. Raw data sheets showing ILRT data as recorded from the i instrumentation and as entered in the computer.
b.
Computer printouts of rav. data reduction giving weighted average containment absolute air temperature and pressure suitably corrected for calibration, vapor pressure, and volume fractions.
c.
Formulas used by computer for calculation of leakage rate, regression analyses and confidence limits,
- d. Data to vdrify temperature stabilization.
c'
- 2. Systems Status (at time of ILRT) l A system line-up showing valve positions and status of 4
' a.
piping systems (drained, vented, etc.) for all plant systems associated with ILRT.
- b. Identification of normal plant instrumentation.
c.
Equipment protection list identifying action taken to h prevent equipment damage due to high containment atmosp ere pressure.
4
- 3. Event Log 4
A continuous log of ILRT events.
t
- 4. Instrumentation Documentation Calibration data and certificates.
- 5. Test Procedurel ffs.
The working copy of test procedure including signature sign o 4
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'. I ! TOR!mTIO:3 RETAIL 1ED AT JOBSITE - Cont'd.
- 6. Local Leakace Rate Tests The procedure and data to verify completion of penetrations and valves testing (Type B and C tests) including measured leakage rates, significant proble=s found, and applicable corrective action, and total, overall leakage rate.
- 7. Quality Assurance The Quality Assurance audit plan or checklist that was used to monitor the ILRT.
- 8. Local Leak Survey During ILRT Identification of any leakage (into or out of containment) i found during ILRT and corrective action taken.
- 9. System Restoration Checklist for restoration to normal status of non-standard i system or instrumenation conditions after completion of ' '
the ILRT. i i
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TABLE III.C.1.
SUMMARY
DATA
SUMMARY
DATA PEACHSOTTan UNIT 3 ILPT TIME DATE TEMP PEE 35URE VOLUME 1306 404 531.580 63.4720 265971.
1315 404 531.569 63.4675 285975.
1330 404 531.540 63.4607 285978.
1345 404 531.503 63.4532 2s5981.
I 140n 4 04 531.464 63.4439 265984 1415 404 531.420 63.4370 295967.
141u 404 531.360 63.4291 235999.
1445 4^4 531.354 63.4220 255986.
I 1500 404 531.325 63.4203 285981.
I 1515 4 04 531.307 63.4169 295993. .
1530 404 531.264 63.4114 295994 !
1545 464 531.256 63.4054 285984 (
1600 404 531.226 63.3999 235905. i I
1615 404 531.178 63.3935 285986.
1630 404 531.155 63.3869 265987.
63.3024 265907. !
p 1645 404 531. toe !
1700 404 531.205 43.3903 295997.
I' 1715 404 531.430 63.4199 265987. f
. ,1730 404 530.964 63.3530 285990.
1745 4 04 531.270 63.39?6 265790.
1900 404 5?1.727 63.4431 295990.
1815 404 532.176 63.4964 265999.
1930 404 532.577 63.5377 295991. .
1645 404 532.755 63.5443 295990.
1900 464 532.321 63.5011 285991.
1915 404 532.103 63.4911 265991.
1930 494 531.950 63.4620 265793.
1945 4n4 531.822 63.4453 195993.
2000 404 531.709 63.451? 245995.
2915 dr4 531.644 63.4204 235994.
2030 404 531.565 63.4693 295935.
2045 464 531.474 63.3992 295995.
2100 4u4 531.4?! 63.3975 2s5995.
O A 0. 0 u. 0 0. 0 ILRT STABIL. DATA GEACH BarTGM UNIT 3 ILRT TIME DATE TE"* 12I3k PRG33URE
. 0900 494 532.479 6 3. )( 4 ,
l
! 1200 4"4 531.645 63.813 l 1"60 494 531.530 63.804 I
i l 9 l
TABLE III.C.2.
LEAKAGE RATE: TOTAL TIME CALCULATION CONSTANT VOLUME PEACH 50TTOM UNIT 3 ILRT LEAKAGE RATE (WEIGHT PERCEMT/ DAY)
DASED ON TOTAL TIME CALCULAT!DNS TIME AND DATE AT START OF TESTt 1300 0404 ELAPSED TIMES 8.00 HOURS TIME TEMP. PRESSURE MEASURED (R) (PSIA) LEAKAGE RATE 1300 531.580 63.4720 1315 531.569 63.4675 0.482 1330 531.540 63.4607 0.493 1345 531.503 63.4532 0.484 1400 531.464 63.4438 0.543 1415 531.420 63.4370 0.481 1430 531.360 63.4291 0.419 1445 531.354 63.4220 0.497 1500 531.325 63.4203 0.402
- 1515 531.307 63.4169 0.378 1530 531.264 63.4114 0.346 1545 531.258 63.4054 0.387 1600 531.228 63.3988 0.393 1615 531.178 63.3935 0.355 1630 531.155 63.3869 0.371 5,- 1645 531.108 63.3824 0.335
. 1700 531.205 63.3903 0.349 1715 531.439 63.4199 0.314
< 1730 530.964 63.3530 0.382 1745 531.270 63.3936 0.330 1800 531.727 63.4431 0.351 1815 532.176 63.4964 0.336 ,
1830 532.577 63.5377 0.366 1845 532.755 63.5448 0.443 1900 532.321 63.5011 0.374 1915 532.103 63.4911 0.262 1930 531.950 63.4620 0.315 1945 531.822 63.4453 0.311 2000 531.708 63.4313 0.302 2015 531.644 63.4206 0.308 2030 531.565 63.4093 0.307 l 2045 531.474 63.3982 0.298 2100 531.431 63.3075 0.315 MEAN OF MEASURED LEAKR6E RATES = 0.376 STD. DEVIATION OF MEASURED LEAKA6E RATES = 0.071 Mex! MUM ALLDWADLE LERkAGE RATE = 0.500 75 *: OF MAXIMUM ALLDWABLE LEAKAGE RATE = 0.375 THE CALCULATED LEAKAGE RATE = 0.281 i THE CALC. LEAkRGE RATE AT 95*./ CONFIDENCE LEVEL = 0.201 2 0.091 CONSTANT YOLUME 10 l
)
i TABLE III.C.3.
TOTAL TIME CALCULATION, TREND REPORT LEAKAGE RATE:
CONSTANT VOLUME PEACHBOTTOM UNIT 3 ILRT TREND REPORT LERkAGE RATES WEIGHT PERCENT / DAY) :
BASED 0:1 TOTAL-TIME CALCULATIONS 1300 0404 i TIME AND DATE AT START OF 8.00TEST HOURS .
l ELAPSED TIME:
CH6 IN CALC LeR UFFER 95%
MEAN MEASURED CALCULATED NO. DATA ELAPSED POINTI TIME LEAkRGE RATE LEAkRGE RATE FROM LAST 0.527 POINT CONF LE 0.465 0.412 0.492 to 2.25 0.381 -0.031 E.50 0.453 -0.009 0.475 11 0.447 0.372 0.466 12 A.75 0.442 0.368 -0.004 0.447 13 0.354 -0.013
.'3.
3.2500 0.436 -0.006 0.438 14 0.431 0.349 0.420 15 3.50 0.336 -0.013 3.75 0.425 -0.007 0.411 16 0.420 0.329 0.394 17 4.00 0.316 -0.013 0 405 4.25 0.414 0.004 18 0.412 0.320 0.396 19 4.50 0.313 -0.007 4.75 0.408 -0.002 0.394 20 0.405 0.312 0.390 21 5.00 0.308 -0.004 22 5.25 0.402 0.002 0.395 0.400 0.310 0.429
' 23 5.50 0.325 0.014 24 5.75 0.402 0.002 0.430 0.401 0.326 0.415 25 6.00 0.311 -0.015 26 6.25 0.395 -0.005 0.407 0.392 0.306 0.400 27 6.50 0.301 -0.005 28 6.75 0.389 -0.006 0.392 0.386 0.295 0.396 29 7.00 0.191 -0.004 0.380 30 7.25 0.303 -0.004 0.381 0.287 0.374 31 7.50 0.283 -0.004 0.372 2
7.75 0.378 - 0. 0 02 32 0.376 0.281 33 8.00
= 0.281 THE CALCULATED LEAKAGE RATE CONSTANT VOLUME 11
TABLE III.C.4.
LEAKAGE RATE: MASS-POINT ANALYSIS CONSTANT VOLUME PEACHBOTTDM UNIT 3 ILRT LEAKAGE RATE (WEIGHT PERCENT / DAY)
MASS POINT ANALYSIS TIME AND DATE AT START OF TEST 1300 0404 ELAPSED TINE: 8.00 HOURS PRESSURE CTMT. AIR MASS LOSS TOT. AVG. MA~S TIME TEMP LDSS (LBM NP)
(R) (PSIA) MASS (LBM) (LBM) 1300 531.580 63.4720 92174 63.4675 92169 4.6 18.5 1315 531.569 4.8 18.9 1330 531.540 63.4607 92164 1345 531.503 63.4532 92160 4.5 18.6 63.4438 92153 6.9 20.8 1400 531.464 2.2 18.5 1415 531.420 63.4370 92150 63.4291 92149 1.1 16.1 1430 531.360 19.1 1445 531.354 63.4220 92140 9.3 1500 531.325 63.4203 92143 -2.6 15.4 1515 531.307 63.4169 92141 1.8 14.5 63.4114 92140 0.5 13.3 1530 531.264 7.7 14.9 1545 534.258 63.4054 92133 i 1600 531'.228 63.3988 92128 4.4 15.1 1615 531.178 63.3935 92129 -1.0 13.6 j 1630 531.155 63.3869 92124 5.6 14.3 12.9 i 1645 531.108 63.3824 92125 -1.6 1700 531.205 63.3903 92120 5.3 13.4 6 1715 531.439 63.4199 92122 -2.4 12.1 1730 530.964 63.3530 92107 14.9 14.7 !
1745 531.270 63.3936 92113 -5.9 12.7 l 1800 531.727 63.4431 92106 7.3 13.5 63.4964 92106 0.4 12.9 1815 532.176 14.1 1830 532.577 63.5377 92096 9.5 63.5448 92076 20.5 17.0 1845 532.755 14.4 1900 532.321 63.5011 92087 -11.7 63.4911 92111 -23.2 10.1 1915 532.103 92095 15.7 12.1 1930 531.950 63.4620 12.0 1945 531.822 63.4453 92093 2.1 2000 531.708 63.4313 92092 0. 6 11.6 2015 531.644 63.4206 92088 4.5 11.8 2030 531.565 63.4093 92085 2.7 11.8 2045 531.474 63.3982 92085 0.4 11.5 63.3875 92077 8.1 12.1 2100' 531.431 FREE AIR VOLUME USED (MILLIONS OF CU. FT.)
= 0.286 REGRE53!DN LINE INTEPCEPT (LBM)
= 92166
= -11.3 SLOPE (LBM/HR)
MAXIMUM ALLOWABLE LEAKAGE RATE
= 0.500
= 0.375 75 *. CF MAXIMUM ALLOWAPLE LEAKAGE RATE = 0. 2%
THE CALCULATED LEA > AGE RATE = 0.296 1 0.026 THE CALC. LEAKAGE PATE AT 95% CCNFIDENCE LEVEL CONSTANT VO!.UME 12
w TABLE III.C.S.
LEAKAGE RATE: TOTAL TIME CALCULAT ON FREE AIR VOLUME VARIED PEACHBOTTOM UNIT 3 ILAT a LEAKAGE RATE OdEIGHT PERCEMT/ DAY)
BASED ON TOTAL TIME CALCULATIONS TIME AND DATE AT START OF TESTS 1300 0404 ELAPSED TIME: 8.00 HOURS i
TIME TEMP. PRESSURE MEASURED (R) (PSIA) LEAKAGE RATE 1300 531.580 63.4720 4315 531.569 63.4675 0.348 1330 531.540 63.4607 0.376 1345 531.503 63.4532 0.372 1400 531.464 63.4438 0.434 1415 531.420 63.4370 0.374 1430 531.360 63.4291 0.319 1445 531.354 63.4220 0.416 1500 531.325 63.4203 0.360 1515 531.307 63.4169 0.334 531.264 63.4114 0.302 i.1530 1545 531.258 63.4054 0.348
.' 1600 531.228 63.3988 0.354 1615 531.178 63.3935 0.316 1630 531.155 63.3849 0.333 1645 531.108 63.3824 0.300 1700 531.205 63.3903 0.316 1715 531.439 63.4199 0.282 1730 530.964 63.3530 0.347 1745 531.270 63.3936 0. 2%
1800 531.727 63.4431 0.319
- 1815 532.176 63.4964 0.306 1830 532.577 63.5377 0.336 1845 532.755 63.5448 0.415 1900 532.321 63.5011 0.346 1915 532.103 63.4911 0.235 1930 531.950 63.4620 0.287 1945 531.822 63.4453 0.284 2000 531.708 63.4313 0.274 2015 531.644 63.4206 0.281 531.565 63.4093 0,280 2030 2045 531.474 63.3962 0.272 2100 531.431 63.3875 0.290 i
= 0.327 NEAN OF MEASURED LEhkAGE RATES = 0.046 3TD. DEVIATION OF MCASURED LEAKA6E RATES,
= 0.500 HAMINUN ALLOWABLE LEAKA6E RATE = 0.375 75 . OF MAXINUM ALLOWABLE LEAKAGE RATE = 0.276 I THE CALCULATED LEAKAGE RATE = 0.276 2 0.076 I THE CALC. LEAKAGE RATE AT 95*/. CONFIDENCE LEVEL l-l Free Air Volume Varied i
\
13
TABLE III.C.6.
LEAKAGE RATE: TOTAL TIME CALCULATION, TREND REPORT FREE AIR VOLUME VARIED PEACHBDVTDN UNIT 3 ILRT TREND REPORT LEAKAGE RATES GEIGHT PERCENT / DAY) i BASED ON TOTAL-TIME CALCULATIONS I TINE AND DATE AT START DF TEST 1300 0404 ELAPSED TINE: 8.00 HDURS 1
NERN NEASURED CALCULATED CHG IN CALC L/R UPPEP 953 1 ND. DATA ELAPSED
- l. PDINTS TIME LERKAGE RATE LERKAGE RATE FROM LAST PDINT CONF LEVEL 0.370 0.361 0.468 10 2.25 0.445 2.50 0.363 0.340 -0.022 11 0.436 12 2.75 0.362 0.339 -0.001 4
3.00 0.361 0.340 0.001 0.431' l 13 0.417 14 3.25 0.358 0.331 -0.009 3150 0.356 0.328 -0.003 0.409 15 0.396 16 375 0.352 0.318 -0.010 4.00 0.350 0.313 - 0. 004 0.338 17 0.375 1
18 4.25 0.346 0.303 -0.011 4.50 0.346 0.308 0.005 0.382 19 0.373 20 4.75 0.343 0.302 -0.006 0.342 0.301 -0.001 0.371 21 5.00 0.366 22 5.25 0.341 0.299 -0.003 5.50 0.340 0.301 0.003 0.369 23 0.401 24 5.75 0.344 0.317 0.015 6.0u 0.344 0.319 0.002 0.402 25 0 393 26 6.25 0.339 0.305 -0.014 6.50 0.337 0.300 -0.005 0.386 27 0.379 28 6.75 0.335 0.295 -0.005 0.333 0.289 -0.006 0.372 29 7.00 0.366
(
30 7.25 0.331 0.285 -0.004 0.330 0.202 -0.004 0.361 31 7.50 0.355 32 7.75 0.328 0.278 -0.004 8.00 0.327 0.276 -0.001 0.352 33 THE CALCULATED LEAKAGE RATE
= 0.276 1
i Free Air Volume Varied I
l 1
14
TABLE III.C.7.
LEAKAGE RATE: MASS-POINT ANALYSIS FREE AIR VOLUME VARIED PEACHECTTOM UNIT 3 ILRT LEAKAGE RATE (WEIGHT PERCENT / DAY)
MASS POINT ANALYSIS 1300 0404 TIME RND DATE AT START8.00 OFHOURS TEST:
ELAPSED TIME:
TOT. AVG. NHSS TEMP PRESSURE CTMT. RIR NASS LOSS LDSS (LBMeHR)
TIME MASS (LBM) (LBM)
(PSIR)
(R) ---------~~-----------~~~-----------~~---
720 1300 531.380 63.4 92164 92161 3.3 13.4 1315 531.569 63.4675 3. 9 14.4 63.4607 92157 14.3 1330 531.540 63 4532 92154 3.5 16.7 1345 531.503 63 4438 92148 5.9 14.3 1400 531.464 92147 1.3 1415 531.420 63.4370 0.4 12.2 63.4291 92146 16.0 1430 531.360 63.4220 92137 9.6 1445 531.354 92137 -0.3 13.8 1500 531.325 63.4203 1.2 12.8 63.4169 92136 11.6 1515 531.307 63.4114 92135 0.2 1530 531.264 92128 7.7 13.4 1545 531.258 63.4054 4.1 13.6 63.3988 92124 12.2 1600 53 L.228 63.3935 92125 -1.3 1615 531'il?8 92120 5.3 12.8 1630 53h 155 63.3869 -1.6 11.5 63.3824 92121 12.1 1645 531.108 63.3903 92116 5.3 1700 531.205 92118 -2.4 10.8 1715 531.439 63.4199 13.9 13.3 63.3530 92105 11.4 1730 530.964 63.3936 92110 -5.9 1745 531.270 92103 7.3 12.3 1800 531.727 63.4431 0.4 11.8 63.4964 92103 12.9 1815 532.176 92094 9.P 1830 532.577 63.5377 20.8 15.9 63.5448 92073 13.3 1845 532.755 63.5011 92085 -12.0 1900 532.321 -23.2 9.0 i 63.4911 92108 11.0 1915 532.103 63.4620 92093 15.1 6 1930 531.950 92091 2.1 10.9 1945 531.822 63.4453 -0.1 10.5 63.4313 92091 10.8 2000 531.708 63.4206 92086 4.8 10.8 2015 531.644 63.4093 92084 2.4 10.5 2030 531.565 63.3982 92083 0.4 2045 531.474 92075 0.1 11.1 2100 531.431 63.3875
= SEE SumARY DATA FREE RIR VOLUME USED (MILLIONS OF CU. FT.)
REGRESSION LINE = 92160 INTERCEPT (LBM) = -10.7 SLOPE (LBM/HR)
= 0.500 MAXIMUM ALLOWABLE LEAKAGE RATE = 0.375 75 *. OF MAXIMUM ALLOWABLE LEAKAGE RATE = 0.278 THE CALCULATED LEAKAGE RATE = 0.278 2 0.026 THE CALC. LEAKAGE RATE AT 95; CONFIDENCE LEVEL Free Air Volume Varied 15
- e*
TABLE III.C.8. (a)
MEASURED AND CORRECTED DATA
SUMMARY
1300 0404 IUMMARY OF MEASURED DATA AT TEMP 1 = 336.330 ( 76.73)
TEMP 2= 538.300 ( 78.70)
TEMP 3= 531.730 ( 72.13)
TEMP 4= 531.390 ( 71.79)
TEMP 5= 527.970 ( 68.37)
TEMP 6= 529.340 ( 69.74)
TEMP 7= 526.930 (.67.33) l TEMP 8= 526.390 ( 66.79)
TEMP 9= 522.220 ( 62.62)
TEMP 10 = 532.980 ( 73.38) t TEMP 11,= 532.540 ( 72.94)
TEMF 12 = 532.580 < 72.98)
PRES 1= 63.804 (63802.)
VPRSp 1 = 0.278 ( 62.30)
' VFRS.; 2 = 0.295 ( 64.00)
VPRS' 3= 0.272 ( 61.70)
VPRS' '4 = 0.401 ( 72.94)
VPRS' 5= 0.402- ( 72.98) f
SUMMARY
OF CORRECTED DATA TIME = 1300 '
I DATE = 0404 -
TEMPERATURE (DEGREES R.)
= 531.580 CORRECTED PRESSURE (PSIA)
= 63.4720 i e
16
~ _ _ _ _
TABLE III.C.8. (b)
MEASURED AND CORRECTED DATA SLHMARY
SUMMARY
OF MEASURED DATA AT 1315 0404 TEMP 1= 536.400 ( 76.80)
TEMP 2= 538.440 ( 78.84)
TEMP 3= 531.680 ( 72. 08)
TEMP 4= 531.350 ( 71.75)
TEMP 5= 527.980 ( 68.38)
TEMP 6= 529.230 ( 69.63) l TEMP 7= 526.940 ( 67.34)
TEMP 8= 526.360 ( 66.76) l TEMP 9= 522.170 ( 62.57)
TEMP 10 = 532.970 ( 73.37)
- TEMP 11 = 532.530 ( 72.93)
TEMP 12 = 532.550 ( 72.95)
PRES 1= 63.799 (63797.)
VPRSE 1= 0.277' ( 62.20)
VPRs' 2 = 0.295 ( 64.00)
[ VPRS 3= 0.271 ( 61.60)
I VPRS 4= 0.401 ( 72.93) .'
VPRS 5= 0.401 ( 72.95) k t
k,
SUMMARY
OF CORRECTED DATA TIME = 1315 DATE = 0404 TEMPERATURE (DEGREES R.) = 531.569 CORRECTED PRESSURE (PSIA) = 63.4675 17
TABLE III.C.8. (c)
MEASURED AND CORRECTED DATA
SUMMARY
CUMMARY OF MEASURED DATA AT 1330 0404 TEMP 1= 536.270 < 76.67)
TEMP 2= 538.380 < 78.78)
TEMP 3= 531.650 < 72.05)
TEMP 4= 531.370 < 71.77)
TEMP 5= 527.900 < 68.30)
TEMP 6= 529.290 < 69.69)
TEMP 7= 526.870 < 67.27)
TEMP 8= 526.360 < 66.76)
TEMP 9= 522.130 < 62.53)
TEMP 10 = 532.940 < 73.34)
TEMP 11.= 532.510 < 72.91)
TEMP 12 = 532.530 < 72.93) _
PRES 1= 63.792 (63790.)
VPRS \1 = 0.278 < 62.30)
VPRS p2 = 0.294 < 63.90)
VPRS l3 = 0.271 < 61.60) '
VPRS 4= 0.401 < 72.91)
VPRS 5= 0.401 < 72.93)
{
SUMMARY
OF CDPRECTED DATA TIME = 1330 DATE = 0404 ..
TEMPERATURE (DEGREES R.) = 531.540 CORRECTED PRESSURE (PSIA) = 63.4607 18 t
+ .
TABLE III.C.8. (d)
MEASURED AND CORRECTED DATA
SUMMARY
1345 0404
- UMMARY OF MEASURED DATA AT TEMP 1u 536.220 < 76.62)
TEMP 2= 538.250 < 78.65)
TEMP 3= 531.580 < 71.99)
TEMP 4= 531.320 < 71.72)
TEMP 5= 527.980 < 68.38)
TEMP 6= 529.150 < 69.55)
TEMP 7= 526.870 < 67.27)
TEMP 8= 526.310 < 66.71) ,
TEMP 9= 522.120 < 62.52)
TEMP 10 = 532.920 < 73.32)
TEMP 1'1 = 532.490 < 72.89) 72.91)
TEMP 12 = 532.510 PRES 1= 63.784 (63782.)
l VPR$ 1 = 0.277 ( 62.20)
VPR$ 2= 0.294 < 63.90)
VPRS 3 = 0.270 < 61.50)
VPRS 4= 0.400 < 72.89)
VPRS 5= 0.401 < 72.91)
SUMMARY
OF CORRECTED DATA TIME = 1345 DATE = 0404
= 531.503 i TEMPERATURE (DEGREES R.)
= 63.4532 CORRECTED PRESSURE (PSIA) f 1
t 19
)
TABLE III.C.8. (e)
MEASURED AND CORRECTED DATA
SUMMARY
1415 0404 IUMMARY OF MEASURED DATA AT TEMP 1= 536.030 < 76.43)
TEMP 2= 538.080 < 78.48)
TEMP 3= 531.460 < 71.86)
TEMP 4= 531.190 < 71.59)
TEMP 5= 527.780 < 68.18)
TEMP 6= 529.200 < 69.60)
TEMP 7= 526.820 < 67.22)
TEMP 8= 526.180 < 66.58)
TEMP 9= 522.040 < 62.44)
< 73.27)
TEMP 10 = 532.870 < 72.85)
TEMP 11 = 532.450 < 72.88)
TEMP 12 = 532.480 PRES 1= 63.767 (63765.)
VPRS 1= 0.274 < 61.90)
VPRS.. 2= 0.293 ( 63.80)
VPRC' 3 = 0.270 < 61.50) i VPR$' 4= 0.400 < 72.85) ,
VPRS 5 = 0.400 < 72.88) !
t
SUMMARY
OF CORRECTED DATA TIME = 1415 DATE = 0404
= 531.420 TEMPERATURE < DEGREES R.)
= 63.4370 CORRECTED PRESSURE (PSIA)
P 20
. s l
Table III.C.G. (f)
Measured and Corrected Data Summary IUMMARY OF MEASURED DATA AT 1400 0404 TEMP 1= 536.160 ( 76.56)
TEMP 2= 538.200 ( 78.60)
TEMP 3= 531.540 ( 71.94)
TEMP 4= 531.200 ( 71.60)
TEMP 5= 527.850 ( 68.25)
TEMP 6= 529.130 ( 69.53)
TEMP 7= 526.830 ( 67.23)
TEMP 8= 526.300 < 66.70)
TEMP 9= 522.090 ( 62.49)
TEMP 10 = 532.900 ( 73.30)
TEMP 11 = 532.480 ( 72.88)
TEMP 12 = 532.510 ( 72.91) ',
PRES 1= 63.775 (63773.) ;
VPRSU 1 = 0.277 ( 62.20)
VPRS 2 = 0.294 ( 63.90) ,
VPRS 3= 0.272 ( 61.70) !
VPRS '4 = 0.400 ( 72.88)
YPRS 5= 0.401 ( 72.91) ;
SUMMAPY OF CORRECTED DATA ,
t TIME = 1400 DATE = 0404 i
TEMPERATURE (DEGREES R.) = 531.464
, CORRECTED PRESSURE (PSIA) = 63.4438 i
21
l j
l Table III.C.8. (g)
Measured and Corrected Data Summary
SUMMARY
OF MEASURED DATA AT 1430 0404 h
l TEMP 1= 535.940 < 76.34)
!' TEMP 2= 537.960 < 78.36) 531.360 < 71.76) f TEMP TEMP 3=
4= 531.090 < 71.49) 527.730 < 68.13) 7 TEMP 5=
TEMP 6= 528.990 < 69.39) p 526.740 < 67.14) ri TEMP 7= '
TEMP 8= 526.180 < 66.58) f
+ TEMP 9= 522.020 < 62.42) j TEMP 10 = 532.860 < 73.26)
TEMP 11 = 532.440 < 72.84) g TEMP 12 = 532.460 < 72.86)
PRES,1 = 63.759 (63757.)
h !
s VPRSr.1 = 0.276 < 62.10)
VPRS. 2= 0.293 < 63.80)
VPRS 3= 0.269 ( 61.40) r VPRS 4= 0.400 < 72.84)
( VPRS 5= 0.400 < 72.86) b 3
4 4
SUMMARY
OF CORRECTED DATA TIME = 1430 k.
DATE = 0404
+ TEMPERATURE (DEGREES R.)
= 531.360 t
CORRECTED PRESSURE (PSIA)
= 63.4291 k
k, 1,
22 I
Table III.C.8. (h)
Measured and Corrected Data Summary EUMMARY OF MEASURED DATA AT 1445 0404 TEMP 1= 535.830 < 76.23)
TEMP 2= 537.860 < 78.26)
TEMP 3= 531.360 < 71.76)
TEMP 4= 531.100 < 71.50)
TEMP 5= 527.680 < 68.08)
TEMP 6= 529.100 < 69.50)
TEMP 7= 526.750 < 67.15)
TEMP 8= 526.220 < 66.62)
TEMP 9= 521.990 < 62.39)
TEMP 10 = 532.860 < 73.26)
TEMP 11 = 532.430 < 72.83)
TEMP 12 = 532.470 < 72.87)
PRES 1 = 63.752 (63750.)
VPRS 1= 0.278 < 62. 30)
VPRS. 2= 0.292 < 63.70)
VPRQ 3= 0.269 < 61.40)
VPRS 4= 0.400 < 72.83)
VPRS4 5= 0.400 < 72.87)
SUMMARY
OF CORRECTED DATA TIME = 1445 DATE = 0404 TEMPERATURE < DEGREES R.) = 531.354 CORRECTED PRESSURE (PSIA) = 63.4220 22 -
Table III.C.8 (i) reasured and Corrected Data Summary
SUMMARY
OF MERSURED DATA AT 1500 0404 TEMP 1 = 535.760 ( 76.16)
TEMP 2= 537.enn ( 78.20)
TEMP 3= 53?. 380 < 71.78)
TEMP 4= 531.050 < 71.45)
TEMP 5= 527.680 < 68. 08)
TEMP 6= 529.050 < 69.45) '
TEMP 7= 526.670 < 67. 07) j TEMP 8= 526.120 < 66.52)
TEMP 9= 521.930 < 62.33)
TEMP 10 = 532.850 < 73.25)
TEMP 11 = 532.430 < 72.83)
TEMP 12 = 532.460 < 72.86)
PRES 1= 63.750 (63748.)
[
I VPRSr. 1 = 0.274 ( 61.90)
VPRS; 2= 0.292 < 63.70)
VPRS 3= 0.270 < 61.50) h' 0.400 < 72.83)
' VPR$ '4 =
VPRS 5= 0.400 < 72.86) t t
'1 y
OUMMARY OF CORRECTED DATA TIME = 1500 DATE = 0404
= 531.325 TEMPERATURE < DEGREES R.)
t = 63.4203
- i. CORRECTED PRES $URE (PSI A)
- \
?}-
Table III.C.8. (j)
Measured and Corrected Data Summary
SUMMARY
OF MEASURED DATA AT 1515 0404 TEMP 1= 535.720 < 76.12)
TEMP 2= 537.830 < 78.23)
TEMP 3= 531.320 < 71.72)
TEMP 4= 531.050 < 71.45)
TEMP 5= 527.660 < 68. 06)
TEMP 6= 529.030 < 69.43)
TEMP 7= 526.630 < 67. 03)
TEMP 8= 526.050 < 66.45)
TEMP 9= 521.940 < 62.34)
TEMP 10 = 532.840 < 73.24)
TEMP 11 = 532.420 < 72.82)
TEMP 14 = 532.450 < 72.85)
PRES 1= 63.747 (63744.)
VPRS 1= 0.274 < 61.90)
VPRS. 2 = 0.292 < 63. 70)
VPRS 3= 0.268 < 61.30)
VPRS' 4= 0.400 < 72.82)
VPRS '5 = 0.400 < 72.85)
SUMMARY
OF CORRECTED DATA TIME = 1515 DATE = 0404 TEMPERATUPE < DEGREES R.) = 531.307 ,
CORRECTED PRESSURE (PSIA) = 63.4169 i
i l
l i
i "c
1 l
Table III.C.8. (k)
Measured and Corrected Data Summary IUMMARY OF MEASURED DATA AT 1530 0404 TEMP 1 = 535.550 ( 75.95)
TEMP 2= 537.810 ( 78.21)
TEMP 3= 531.300 ( 71.70)
TEMP 4= 531.000 ( 71.40)
TEMP 5= 527.590 ( 67.99)
TEMP 6= 528.930 ( 69.33)
TEMP 7= 526.630 ( 67. 03)
TEMP 8= 526.010 ( 66.41)
TEMP 9= 521.900 ( 62.30)
TEMP 10 = 532.820 ( 73.22)
TEMP 11 = 532.400 ( 72.80)
TEMP 12 = 532.430 ( 72.83)
PRES 1= 63.741 (63738.)
VPRS,,1 = 0.273 ( 61.80)
VPRSP 2 = 0.292 ( 63.70)
VPRQ' 3 = 0.267 ( 61.20)
VPRS ,4 = 0.399 ( 72.80)
VPRS 5= 0.400 ( 72.83)
SUMMARY
OF CORRECTED DATR TIME = 1530 DATE = 0404 TEMPERATURE (DEGREES R.) = 531.264 CORRECTED PRESSURE (PSIA) = 63.4114 0
0 n
'l ll
.i
- e e8 l
l Table III.C.8. (1)
Measured and Corrected Data Summary 1545 0404 IUMMARY OF MEASURED DATA AT
( 75.95)
TEMP 1 = 535.550 TEMP 2= 537.830 (( 78.23)
TEMP 3= 531.320 ( 71.72) 71.36)
TEMP 4= 530.960 527.600 ( 68.00)
TEMP 5= < 69.29)
TEMP 6= 528.890 ( 67.01)
TEMP 7= 526.610 TEMP 8= 525.990 ( 66.39)
( 62.29)
TEMP 9. = 521.890 ( 73.22) f TEMP 10 = 532.820 ( 72.80)
TEMP 11 = 532.400 ( 72.82)
TEMP 12 = 532.420 1
63.735 (63732.)
PREsp1 =
0.273 ( 61.80)
VPRS 1 = 0.291 ( 63.60)
'2 =
VPRS' 3= 0.268 ( 61.30) e q
VPRS 4= 0.399 ( 72.80)
VPRS 5= 0.400 ( 72.82)
' VPRS i
SUMMARY
OF CORRECTED DATA
?
TIME = 1545 DATE = 0404
= 531.258 TEMPERATURE (DEGREES R.)
= 63.4054 COPPECTED PRESSURE (PSI A) e 27
l e l
. . 1 l
Table III.C.8. (m)
Measured and Corrected Data Summary 1600 0404
SUMMARY
OF MEASURED DATA AT TEMP 1= 535.490 ( 75.89)
TEMP 2= 537.740 ( 78.14)
TEMP 3= 531.230 ( 71.63)
TEMP 4= 530.960 ( 71.36)
TEMP 5= 527.550 ( 67.95)
TEMP 6= 528.980 ( 69.38) f TEMP 7= 526.550 ( 66.95) 525.950 ( 66.35) t TEMP 8=
f TEMP 9= 521.830 ( 62.23)
TEMP 10 = 532.790 ( 72.78)
( 73.19) J r TEMP 11.= 532.380 ( 72.80) f l
I TEMP 12 = 532.400 i
PRES 1= 63.728 (63725.)
VPRS U1 = 0.271 ( 61.60) ;
VPRS; 2 = 0.291 ( 63.60)
VPRS.' 3 = 0.268 ( 61.30) 0.399 ( 72,78)
VPRS 4=
i VPRS 5= 0.399 ( 72.80) l L
[ SUMMAPY OF CORRECTED DATA i
TIME = 1600
! DATE = 0404 l
= 531.228 1
' TEMPERATURE (DEGREES R.)
I = 63 3988 l CORRECTED PRESSURE (PSIR) 2E
Table III.C.8. (n)
Measured and Corrected Data Summary 1615 0404 EUMMARY OF MEASURED DATA AT TEMP 1= 535.380 < 75.78)
TEMP 2= 537.650 < 78.05)
TEMP 3= 531.180 < 71.58)
TEMP 4= 530.850 < 71.25) i TEMP 5= 527.480 < 67.88)
TEMP 6= 528.810 < 69.21)
TEMP 7= 526.550 < 66.95)
TEMP 8= 525.980 < 66.38)
TEMP 9= 521.800 < 62.20)
TEMP 10 = 532.780 < 73.18)
TEMP 11 = 532.360 < 72.76)
TEMP 12'= 532.390 < 72.79)
PRES 1= 63.723 (63720.)
VPRS 1= 0.274 < 61.90)
VPRS U2 = 0.291 < 63.60) j VPRS :' 3 = 0.268 < 61.30)
VPRS. 4= 0.399 < 72.76)
VPRS 5= 0.399 < 72.79) I, I
/
SUMMARY
OF CORRECTED DATA TIME = 1615 l DATE = 0404 l TEMPERATURE (DEGREES R.)
= 531.178 CDPRECTED PRESSURE (PSIA)
= 63.3935 29
l e
4 Table III.C.S. (o)
Measured and Corrected Data Summary 1630 0404 IUMMAPY OF MEASURED DATA AT 535.300 < 75. 7 0)
TEMP 1 = < 78.00) 2= 537.600 TEMP 3= 531.150 < 71.55)
TEMP 4= 530.320 < 71.22)
TEMP 5= 527.440 < 67.84)
TEMP 6= 528.850 < 69.25)
TEMP 7= 526.500 ( 66.90)
TEMP < 66.33)
TEMP S= 525.930 521.780 < 62.18)
TEMP 9= < 73.17)
TEMP 10 == 532.770 < 72.75) l TEMP 11 532.350 < 72.78) i TEMP 12,= 532.380 1 = 63.716 (63713.)
PRES 1 = 0.273 ( 61.80)
VPRS < 63.50) 2= 0.290 VPRS 0.268 ( 61.30)
VPRS 03 = 0.399 < 72.75)
VPRSti4= 0.399 < 72.78)
VPRS.' 5 =
N
SUMMARY
OF CORRECTED DATA TIME = 1630 DATE = 0404
(
= 531.155 TEMPERATUPE (DEGREES R.)
= 63.3869
- f CORRECTED PRESSURE (PSI A)
I i
\
l l
l i
F 30
i l
)
Table III.C.8. (p)
Measured and Corrected Data Summary
SUMMARY
OF MEASURED DATA AT 1645 0404 TEMP 1= 535.280 < 75.68) 2= 537.440 < 77.84) j TEMP TEMP 3= 531.110 < 71.51) c TEMP 4= 530.760 < 71.16)
TEMP 5= 527.440 < 67.84)
TEMP 6= 528.700 < 69.10)
TEMP 7= 526.490 < 66.89) 8= 525.870 < 66.27) j
- TEMP TEMP 9= 521.750 < 62.15)
TEMP 10 = 532.740 < 73.14)
TEMP 11 = 532.330 < 72.73)
TEMP 12 = 532.350 < 72.75)
PRES 1= 63.711 (63708.)
VPRSp. 1 = 0.273 < 61.80)
VPRS, 2= 0.289 < 63.40)
VPR$ 3= 0.267 ( 61.20)
VPR$ '4 = 0.398 < 72.73)
VPRS 5= 0.399 < 72.75) i'
.4 V
SUMMARY
OF CORRECTED DATA TIME = 1645 DATE = 0404 TEMPERATURE < DEGREES R.)
= 531.108 CORRECTED PRESSURE (PSIA)
= 63.3824 i
k 31
A a Table III.C.8. (q)
Measured and Corrected Data Summary 1700 0404
SUMMARY
OF MEASURED DATA AT TEMP 1 = 535.400 < 75.80)
TEMP 2= 537.530 < 77.93)
TEMP 3= 531.200 < 71.60)
TEMP 4= 530.650 < 71.05)
TEMP 5= 527.840 < 68.24)
TEMP 6= 528.620 < 69.02)
TEMP 7= 526.780 < 67.18)
TEMP 8= 526.240 < 66.64)
TEMP 9= 522.500 < 62.90)
TEMP 10 = 532.760 < 73.16)
TEMP 11 = 532.330 < 72.73)
TEMP 12 m: 532.370 < 72.77)
PRES 1 = 63.723 (63720.)
VPRS 1= 0.281 < 62.60)
VPRS 12 = 0.293 ( 63.80) 0.276 < 62.10)
VPRS I,3 = 0.398 ( 72.73)
VPRS 4 =-
VPRS' 5 = 0.399 < 72.77)
SUMMARY
OF CDPRECTED DATA TIME = 1700 DATE = 0404 TEMPERATURE (DEGREES R.)
= 531.205 CORRECTED PRESSURE (PSI A)
= 63.3903
+m
r-Table III.C.8. (r)
Measured and Corrected Data Summary
SUMMARY
OF MEASURED DATA AT 1713 0404 TEMP 1= 535.730 ( 76.13)
TEMP 2= 537.840 < 78.24) u h TEMP 3= 531.560 < 71.96)
TEMP 4= 530.760 < 71.16)
TEMP 5= 528.250 < 68.65) j TEMP 6= 529.260 < 69.66)
TEMP 7= 527.210 ( 67.61) k TEMP 8= 526.860 < 67.26)
TEMP 9u 522.890 < 63.29)
TEMP 10 = 532.780 < 73.18)
TEMP 11 = 532.350 < 72.75)
TEMP 12,= 532./380 < 72.78)
PRES 1 = 63.753 (63751.)
VPRS 1= 0.283 < 62. 8 0)
VPRS 2= 0.301 < 64.60)
VPRS F3 = 0.274 < 61.90)
VPRS( 4 = 0.399 < 72.75)
VPRS. 5 = 0.399 < 72.78) s
SUMMARY
OF CORRECTED DATA TIME = 1715 DATE = 0404 TEMPERATURE (DEGREES R.)
= 531.439 CORRECTED PRESSURE (PSIR)
= 63.4199 h
]
33
. l l
Table III.C.8. (s)
Measured and Corrected Data Summary
SUMMARY
OF MERSURED DATA AT 1730 0404 TEMP 1 = 534.960 < 75.36)
TEMP 2= 537.310 < 77.71)
TEMP 3= 531.040 < 71.44)
TEMP 4= 530.690 < 71. 09)
TEMP 5= 527.040 < 67.44)
TEMP 6= 528.790 < 69.19) i TEMP 7= 526.140 < 66.54)
TEMP 8= 525.380 < 65.78)
TEMP 9= 521.140 < 61.54)
TEMP 10'= 532.690 < 73.09)
TEMP 11 = 532.280 < 72.68)
TEMP 12 = 532.300 < 72.70)
PRES 1 = 63.679 (63676.)
VPRS 1= 0.266 < 61.00)
YPRS'2 =
f 0.288 ( 63.30)
VPRS- 3= 0.264 ( 60.80)
VPRS 4= 0.398 < 72.68)
VPRS 5= 0.398 < 72. 7 0)
SUMMARY
OF CORRECTED DATA TIME = 1730 DATE = 0404 TEMPERATUPE (DEGREES R.)
= 530.964
= 63.3530 COPPECTED PRESOURE (PSIA) 34
Table III.C.8. (t)
Measured and Corrected Data Summary 1745 0404 LUMMARY OF MEASURED DATA AT TEMP 1 = 535.460 ( 75.86)
TEMP 2= 537.580 ( 77.98)
TEMP 3= 531.260 ( 71.66)
J TEMP 4 = 530.350
< 70.75) 1 TEMP 5= 528.250 < 68.65)
{ TEMP 6= 528.690 < 69.09) i TEMP 7= 526.970 ( 67.37)
) TEMP 8= 526.550 ( 66.95) 1 TEMP 9= 523.040 < 63.44)
TEMP 10 = 532.750 < 73.15) i i
/
( 72.72)
TEMP l i' = 532.320 < 72.76)
TEMP 12 = 532.360 l PRES 1= 63.729 (63726.)
VPRSU1 = 0.291 < 63. 6 0)
VPRSf' 2 = 0.298 ( 64.30) 2 VPRS. .3= 0.278 < 62.30) 7
- VPRS 4= 0.398 < 72.72)
VPRS 5= 0.399 ( 72.76) i a
a j
SUMMARY
OF CORRECTED DATA TIME = 1745 5 DATE = 0404 j
= 531.270 TEMPERATURE (DEGREES R.)
= 63.3936 CORRECTED PRESSURE (PSIA) 25
l i
1 Table III.C.8. (u)
Measured and Corrected Data Summary UMMARY OF MEASURED DATA AT 1800 0404 TEMP 1 = 536.140 < 76.54)
TEMP 2= 538.040 < 78.44)
TEMP 3= 531.770 < 72.17)
TEMP 4= 530.780 < 71.18)
TEMP 5= 529.460 < 69.86)
TEMP 6= 529.380 < 69.78)
TEMP 7= 527.700 < 68.10)
TEMP 8= 527.560 < 67.96)
TEMP 9= 524.710 < 65.11)
TEMP 10 = 532.810 < 73.21)
TEMP 11 = 532.370 < 72.77)
TEMP 12 = 532.420 < 72.82)
PPES l' = 63.788 (63786.)
VPRS 1= 0.309 < 65.30)
VPRS 2= 0.315 < 65.90)
VPRS. 3= 0.296 ( 64.10)
VPRS O 4= 0.399 ( 72.77)
VPRSf'5 = 0.400 < 72.82)
SUMMARY
OF CORRECTED DATA TIME = 1800 DATE = 0404 TEMPERATURE (DEGREES R.)
531.727 63.4431 CORRECTED PRESSURE (PSIA)
26
.7 1 *. .* l I
l f
7
's Table III.C.8. (v) f Measured and Corrected Data Summary i:
?i i 1815 0404 j
SUMMARY
OF MEASURED DATA AT
( 77.22) i TEMP 1 = 536.820 M
TEMP 2= 538.360 < 78.76) y TEMP 3= 532.350 < 72.75)
TEMP 4= 531.590 < 71.99) h TEMP 5= 530.460 < 70.86)
Y TEMP 6= 530.370 < 70.77) g TEMP 7= 528.290 < 68.69) t
<j TEMP 8= 528.140 < 68.54)
TEMP 9= 526.110 < 66.51)
< 73.27) ff TEMP 10 = 532.870 ( 72.81)
} TEMP 11 = 532.410 < 72.86)
TEMP 12 = 532.460
]U
) \ '.
63.848 (63846.)
' PRESp 1 =
'l= 0.320 < 66.30)
VPRS' 2= 0.329 ( 67.10)
VPRS ( 65.00)
VPRS 3= 0.306 4= 0.399 ( 72.81)
VPRS ( 72.86)
VPRS 5= 0.400 1 .
a b
s
.f
SUMMARY
OF CURRECTED DATA ld
't TIME = 1815 DATE = 0404
] = 532.176 TEMPERATURE < DEGREES R.)
4 = 63.4964
$ CORRECTED PRESSURE (PSIA) l 1
s Ik
'l
r ]
l l
Table III.C.8. (w)
Measured and Corrected Data Summary I
1830 0404
SUMMARY
OF MEASURED DATA AT 4
TEMP 1 = 537.450 < 77.85) 2 TEMP 2= 538.740 < 79.14) k TEMP 3= 533.020 < 73.42) k i' TEMP 4= 532.140 < 72.54)
TEMP 5= 531.410 < 71.81)
TEMP 6= 531.210 < 71.61)
TEMP 7= 528.830 < 69.23) t TEMP 8= 528.770 < 69.17)
TEMP 9= 527.200 < 67.60)
< 73.30)
TEMP 10 = 532.900 < 72.84) 4>
TEMP 11*= 532.440 < 72.86) f ,
TEMP 12 = 532.460 PRES 1= 63.895 (63893.)
VPRSl'1 = 0.329 < 67.10)
() VPPSr 2 = 0.340 < 68.10)
VPRS. 3= 0.314 ( 65.80)
G).
VPRS .4= 0.400 < 72.84) i VPRS 5= 0.400 < 72.86) 1 l
} r SUMMAPY OF CORRECTED DATA h TIME = 1830 t
i DATE = 0404
= 532.577 TEMPERATURE (DEGREES R.)
63.5377
=
Igf CORPECTED PPESSURE (PSIR)
I i
38
t
.. .. 1 I
1 Table III.C.8. (x) ,
Measured and Corrected Data Summary t
1 1845 0404 j IUMMARY OF MEASURED DATA AT j 1 = 537.650
( 78.05) ,
539.070 ( 79.47)
TEMP TEMP 2=
TEMP 3= 533.490 ( 73.89) l TEMP 4= 532.580 ( 72.98) !
s 531.500 ( 71.90) j:
TEMP 5=
TEMP 6=
7=
531.440 ( 71.84) 529.190 < 69. 59) l
[*
- j TEMP 8= 529.210 < 69.61)
TEMP 527.180 ( 67.58)
Q j TEMP 9= ( 73.33)
TEMP 10 = 532.930 ( 72.85) 4 TEMP 11 = 532.450 J4 532.490 ( 72.89)
TEMP 12 =
~! 1 = 63.904 (63902.)
PRES fj 1 = 0.330 ( 67.20)
VPRS. ( 68.50)
$ 2= 0.345
- VPRSi 3= 0.318 ( 66.10)
VPRS' 4= 0.400 ( 72.85)
- VPRS 5= 0.400 ( 72.89)
VPRS Lj 1
1 J
SUMr.ARY OF CORRECTED DATA
't i TIME = 1845
- DATE = 0404
= 532.755
~e TEMPERATURE (DEGREES R.)
(PSIA) = 63.5448 CORRECT'ED PRESSURE I
i 39
A Table III.C.8. (y)
Measured and Corrected Data Surr: nary 1900 0404 l.
IUMMARY OF MEASURED DATA AT 536.900 ( 77.30)
TEMP 1=
h.e TEMP 2= 538.710 ( 79.11)
(i TEMP 3= 532.910 ( 73.31) 531.800 ( 72.20) 4 TEMP 4=
530.350 ( 70.75) l.{ TEMP 5=
530.760 ( 71.16)
J TEMP 6= I
,-j TEMP 7= 528.810 ( 69.21) l 4
TEMP 8= 528.660 ( 69.06)
TEMP 9= 525.460 ( 65.86)
?
' TEMP 10 = 532.870 ( 72.82)
( 73.27)
TEMP 11 = 532.420 ( 72.86)
TEMP 12*= 532.460 53 PRES 1= 63.857 (63855.)
YPRS 1= 0.322 ( 66.50) kk VPRSy,2 = 0.341 ( 68.20) 4 VPRS,; 3 = 0.312 ( 65.60) j VPRSt 4= 0.400 ( 72.82) 4 VPRS' 5= 0.400 ( 72.86)
.j 1
SUMMARY
OF CORRECTED DATA TIME = 1900 DATE = 0404 4
_3 = 532.321 i TEMPERATURE (DEGREES R.)
f+ = 63.5011 CORRECTED PRESSURE (PSI A)
F/
s E
o,:
40
.. - j
- il
[
,d f !.
s i
r i Table III.C.8. (z)
~
[
' Measured and Corrected Data Summary .
?
O 1915 0404 l IUMMARY OF MEASURED DATA AT
( 76.83)
T TEMP 1 = 536.430 TEMP 2= 538.510 ( 78.91) 532.640 ( 73.04) 3=
531.590 ( 71.99)
TEf1P 4=
529.850 ( 70.25)
TEf1P 5=
530.340 (( 70.74) y TEMP TEMP 6= 68.96) k TEMP 7= 528.560 528.240 ( 68.64)
TEMP S=
'c 524.690 ( 65.09)
TEMP 9= ( 73.25) e TEMP 10 = 532.850 ( 72.80) k TEMP 11'= 532.400 ( 72.84)
O TEMP 12 = 532.440 63.830 (63828.)
s
' PRES 1=
k; VPRS El= 0.311 ( 65.50)
VPRS I2 = 0.334 ( 67.60)
VPRS'3 = 0.258 ( 60.20) 0.399 ( 72.80) 4=
VPRS VPPS 5= 0.400 ( 72.84)
SUMMARY
OF CORRECTED DATA TIME = 1915 DATE = 0404
= 532.103 TEMPERATURE (DEGREES R.)
= 63.4911 CORRECTED PRESSURE (PSI A) 1 41
~
t .. .
t Table III.C.8. (a-a)
Measured and Corrected Data Summary a
P 1930 0404
$ :UMMAPY OF MEASURED DATA AT ft TEMP 1= 536.160 < 76.56)
TEMP 2= 538.280 < 78.68) j 532.450 < 72.85)
TEMP 3=
l TEMP 4= 531.420 < 71.82) j TEMP 5= 529.440 < 69.84) i I TEMP 6= 530.160 < 70.56)
TEMP 7= 528.240 < 68.64) f TEMP 8= 527.910 < 68.31)
( TEMP 9= 524.160 < 64.56)
< 73.25) f- TEMP 10.= 532.850 < 72.81)
$1 TEMP 11 = 532.410 < 72.84)
' TEMP 12 = 532.440 3
1= 63.809 (63807.)
PRES f = 0.306 ( 65.00)
VPRS {1 < 66.90)
VPRS r2 = 0.326 3= 0.297 < 64.20)
VPRS < 72.81) d VPRS 4= 0.399 I
5= 0.400 < 72.84)
VPRS f
j J,
i .
s
SUMMARY
OF CORRECTED DATA
[a TIME = 1930 I DATE = 0404 I
= 531.950 TEMPERATURE (DEGREES R.)
(PSIR) = 63.4620 COPPECTED PRESSUPE 1
9; s
e
e Table III.C.8. (b-b)
Measured and Corrected Data Summary 1945 0404 IUMMARY OF MEASURED DATA AT
< 76.33)
TEMP 1 = 535.930 i TEMP 2= 538.160 < 78.56)
TEMP 3= 532.180 < 72.58)
TEMP 4= 531.340 < 71.74)
TEMP 5= 529.160 < 69.56)
TEMP 6= 529.950 < 70.35)
TEMP 7= 527.980 < 68.38)
TEMP S= 527.560 < 67.96)
TEMP 9= 523.700 ( 64.10)
TEMP 10 = 532.860 < 73.26)
TEMP 11 = 532.420
< 72.82)
TEMP 12 = 532.450 < 72.85)
! PRE $ 1 = 63.789 (63787.)
I' VPRS,1 = 0.298 ( 64.30)
VPRS 2= 0.321 < 66.40) f VPRS 3= 0.292 < 63.70)
L VPRS 4= 0.400 < 72.82)
VPRS 5= 0.400 < 72.85)
SUMMARY
OF CORRECTED DATA j
5 TIME = 1945 DATE = 0404 f
= 531.822 i TEMPERATURE RDEGREES R.)
) = 63.4453 4 CDPRECTED PRESSUPE (PSIA)
J t
)
i 43
- e ,e Table III.C.8. (c-c)
Measured and Corrected Data Sumary
- UMMARY OF MEASUPED DATA AT 2000 0404 TEMP 1 = 535.710 < 76.11)
TEMP 2= 537.890 < 78.29)
TEMP 3= 532.100 < 72.50)
TEMP 4= 531.350 ( 71.75) l TEMP 5= 528.870 < 69.27)
TEMP 6= 529.760 < 70.16)
TEMP 7= 527.740 < 68.14)
TEMP S= 527.210 < 67.61)
TEMP 9= 523.4E0 < 63.82)
TEMP 10 = 532.860 < 73.26)
TEMP 11 = 532.420 < 72.82) j TEMP 12 = 532.450 ( 72.85)
PRES 'l = 63.772 (63770.) .
I VPRS 1= 0.295 ( 64.00) '
[ 2= 0.314 ( 65.80)
VPRS VPRS 3= 0.287 < 63.20)
VPRS. 4= 0.400 < 72.82)
VPR,! 5= 0.400 < 72.85)
SUMMARY
OF CORRECTED DATA TIME = 2000 DATE = 0404 TEMPERATURE (DEGREES R.)
= 531.708
= 63.4313 CORRECTED PRESSUPE (PSIA) 44 i
f J
J Table III.C.8. (d-d) i Measured and Corrected Data Summary j
r 2015 0404 OUMMARY OF MEASURED DATA AT h' 1= 535.580 < 75.98)
TEMP 537.780 < 78.18) cf TEMP 2= < 72.37)
TEMP 3= 531.970 < 71.83) 9 a TEMP 4= 531.430 < 69.10)
Ji TEMP 5=
528.700 < 70.10)
TEMP 6= 529.700 < 67.91)
[d 7= 527.510 < 67.47) j:t TEMP TEMP 8=
9=
527.070 523.160 < 63.56)
TEMP < 73.26) j TEMP ,1,0 = 532.860 < 72.82)
, TEMP 11 = 532.420 532.450 < 72.85) rI TEMP (12 =
(63757.)
i= 63.759 PRES 1= 0.291 < 63.60)
VPRO 2= 0.310 < 65.40)
J VPRS 3= 0.283 < 62.80)
VPRS 0.400 < 72.82)
{ VPRS 4=
0.400 < 72.85)
- VPRS 5=
Y U
e 5
d b
e
SUMMARY
OF CORRECTED DATA TIME = 2015 DATE = 0404
$s' = 531.644
- 4 TEMPEPATURE (DEGREES R.)
{ COPRECTED PPESSUPE
<,PS I A) = 63.4206 y -
i 4
45
.. - i F
Table III.C.S. (e-e)
Measured and Corrected Data Summary l
IUMMARY OF MEASUPED DATA AT 2030 0404 ;
i TEf1P 1 = 535.480 < 75.88) '
TEMP 2= 537.650 < 78.05)
TEMP 3= 531.860 < 72.26) i TEMP 4 = 531.470
< 71.87) f TEMP 5= 528.490 < 68.89) ,
TEMP 6= 529.570 < 69.97) l TEMP 7= 527.380 ( 67.78)
TEMP 8= 526.810 < 67.21) -
TEMP 9= 522.970 < 63.37)
TEMP 10 = 532.840 < 73.24)
TEMP 11 = 532.410 < 72.81)
TEMP 12 = 532.440 72.84)
PRES 1 = 63.747 (63744.)
VPRS l'= 0.288 ( 63.30)
VPRSU 2 = 0.308 < 65.20) ,
VPRS6 3 = 0.280 < 62.50) lt VPRSl 4= 0.399 < 72.81) l VPRS '5 = 0.400 < 72.84) I;
,!i
' l,
'l
SUMMARY
OF CORRECTED DATA :$
TIME = 2030 DATE = 0404 t
= 531.565 TEMPERATURE (DEGREES R.)
= 63.4093 COPPECTED PRESSUPE- (PSI A) l' J
46
I .
~4
, 77s e a d
- } NN
- K,k J
l 69 3:3 O'
f*
Table III.C.S. (f-f) l t Measured and Corrected Data Summary f I
I 2045 0404 CUMMARY OF MEASURED DATA RT l 535.210 < 75.61)
TEMP 1= ',
2 TEMP 2= 537.520 < 77.92)
{ 3= 531.710 < 72.11) l t TEMP 4= 531.380 < 71.78) f j TEMP TEMP 5= 528.350 < 68.75) j TEMP 6= 529.350 < 69.75) f'
-g TEMP 7= 527.310 < 67.71)
. 8= 526.720 < 67.12) 522.780 < 63.18)
TEMP 3
TEMP 9= < 73.23)
TEMP 10 = 532.830 < 72.80) j 4 TEMP 11 = 532.400
.! TEMP 12 = 532.430 < 72.83) cf
.i 1= 63.734 (63731.) >
PRES ;
,1 s
Y VPRS, 1= 0.284 < 62.90) !
I 2
2= 0.305 < 64.90)
VPRS < 62.20) !
Y VPR$ '3 = 0.277 i 4= 0.399 < 72.80)
VPRS < 72.83)
.] VPRS 5= 0.400 l
h
't t 7* '-
b T I 1
SUMMARY
OF CORRECTED DATA t 2 f e TIME = 2045 l f
DATE = 0404 531.474 4 =
TEMPERATURE < DEGREES R.) j I (PSIA) = 63.3982 CDPRECTED PRESSURE D. ;
b 2 e o
1 r
I i.
47
~ - _- ___---------~--___.m_
e Table III.C.8. (g-g)
Measured and Corrected Data Summary 2100 0404
/
SUMMARY
OF MEASURED DATA AT
( 75.54) l TEMP 1 = 535.140 4
TEMP 2= 537.480 ( 77.88) i TEMP 3= 531.630 < (
- 72. 03) 71.70)
TEMP 4 = 531.300 528.220 (<68.62)
[ TEMP 5= 69.83) jl TEMP 6= 529.430 i ( 67.58) 527.180 ( 67.02)
TEMP 7=
J TEMP 8= 526.620 ( 63. 03) 9= 522.630 f'y TEMP TEMP 10 = 532.820 ( 73.22) 532.390 < 72.79)
TEMP 11 = ( 72.82) i
- TEMP 12 = 532.420 1
e 1= 63.722 (63719.)
PRES
/ ( 62.80) 1 0.283 J - 1 ( 64.60)
V S. 2:
3 .275 ( 62.00)
VPRS/
'4 : -
( 72.79)
VPRS < 72.82)
VPRS 5- 0.400 J
4 k.
3 4
SUMMARY
OF CORRECTED DATA TIME = 2100 Y DATE = 0404
= 531.431 TEMPERATURE (DEGREES R.)
= 63.3875 CORRECTED PRESSURE (PSIR) i s
i f
- aa i
?
48 i
, .. s t
b Table III.C.9 Su::: nary Data Verification Test
SUMMARY
DATR PEACH SOTTDM ONIT 3 ILRT VERIF 3
k TIME DATE TEMP PRESSURE YOLUME 30 405 531.595 63.4043 296001.
F 45 405 531.615 63.4024 286001.
100 405 531.647 63.4012 266001.
115 405 531.680 63.3986 286001.
, [. 130 .405 531.699 63.3953 296001.
,, 145 405 531.694 63.3936 286001.
5 200 405 531.706 63.3908 236002.
, 215 405 531.712 63.3973 286002.
230 405 531.720 63.3329 286002.
245 405 531.725 63.3817 2-66002.
300 405 531.739 63.3736 236003, 315 405 531.742 63.3725 246403.
330 405 531.744 63.3681 236003.
345 405 531.746 63.3629 296003.
400 4 05 531.766 63.3604 2960n3.
415 405 531.763 63.3553 286003.
430 405 531.756 63.3508 236004 445 405 531.790 63.3459 236004
- 500 405 531.778 63.3426 286004 515 405 531.790 63.3399 266064 530 405 531.775 63.3344 296004 4
545 405 531.766 63.3325 296004 600 405 531.769 63.3295 286004 615 405 531.778 63.3250 296005.
630 405 531.756 63.3205 286006.
) 645 405 531.602 63.3153 286006.
1 0 0 0. 0 0. 0 0. 0 1
i t
)
49 l
I'<'df 93 4g 3 )
u .
SI X'
Table III.C.10 !
Leakage Rate Verification: Total Tirne Calculation i Const. ant Volume
.31 PEACH EDTTOM UNIT 3 ILPT VEP!F f8 s
LEAAA6E PATE sWE16HT SERCENT DAY)
T PASED GN TOTAL TIME CALCULATIONS 30 04v5 TIME AND DATE AT START CF TEST:
6.25 HOURF
, ELAPSED TIME:
PPE; LURE MEA 0VEED TIME TEMP.
(R) *PSIR) LEAAAGE RATE 30 531.595 63.4043 45 531.615 63.4024 n.649 531.647 63.4012 0.704 100 0.799 115 531.600 63.3986 s 130 531.699 63.3953 0.810 L 531.694 63.3936 0.661 145 0.675 20n 531.704 63.3908 215 531.712 63.3873 0.669 23n 531.720 63.3529 0.687 245 531.725 63.3817 0.641 309 S31.739 63.3786 0.649 f
U 531.742 63.3725 0.679 315 0.661 33u 531.744 63.3661 345 531.746 63.3629 0.692 400 531.766 63.3604 0.695 415 531.763 63.;553 0.637 430 531.756 63.3508 0.663 445 531.780 63.3459 0.716 500 531.779 63.3426 0.702 515 531.700 63.339? 0.690 530 531.775 63.3344 0.6*1 531.766 63.3;25 0.665 545 0.657 600 531.769 63.3295 531.773 63.3250 0.665 615 0.650 63u 531.756 63.3205 531.902 63.315 O.626 645
= 0.699 NEAN GF MEA!UEED LEAKAGE FATE! = n.odo
!TD. DEVI ATION CF MEA 5UGED LEAAAGE PATE S
= o.869 VE91FICATICri TEtt LEAK A6E R ATE UPFER LIMIT n.639 VERIFICATIDr* TE:T LEAKAGE RATE 1.CWER LIMIT = = u.669
' TwE C ALCULATED LE** AGE PATE I
I
- , CONSTANT V0LundE L
t a
t q 50
4M:l
.. ,. %?tye ww.1 idif
'dd
.di @
Q-
!_7iET.f.
t
.$$l TableTotalIII.Tire collCalculation, Trend Report Leakage Rate Verification! Constant Volume PEACH SQTTCN UNIT 3 ILRT VERIF TREND REPCRT (WEIGHT PERCENT / DAY)
LEAKAGE RATES BASED CN TOTAL-TINE CALCULATICNS 30 0405 TINE AND DATE AT START CFHOURS 6.25 TEST ELAPSED TINE:
CALCULATED CHG IN CALC L/P NO. DATA ELAPSED NEAN NEASURED LEAKAGE RATE LEAKAGE RATE FRDN LAST POINT POINTS TINE 0.702 0.670 -0.012 10 2.25 0.657 11 2.50 0.696 0.658 0.001
.2.75 0.695 0.001 72 0.694 0.660 0.004 13 3.00 0.664 3.25 0.694 0.004 04 0.694 0.668 0.004 15 3.50 0.694 0.672 0.001 16 3.75 0.673 4.00 0.693 0.681 0.007 17 0.695 0.003 18 4.25 0.695 0.684 19 4.50 0.684 0.000 20 4.75 0.695 0.684 0.000 21 5.00 0.695 0.680 -0.004 5.25 0.693 0.675 -0.005 22 0.692 -0.003 23 5.50 0.691 0.672 :
24 5.75 0.667 -0.005 i 6.00 0.689 0.B69 0.002 25 0.689 26 6.25 1
= 0. 66ie THE CALCULATED LEAKAGE RATE J
CONSTANT VOLUME f
51
p Table III.C.12. Mass Point Analysis Leakage Rate Verification:
Constant Volurae PEACH BOTTOM UNIT 3 ILPT VEPIF LEF* AGE RATE < WEIGHT PEFCENT/ DAY)
MAOS POINT ANALYOIS TEST: 30 0405 TINE AND DATE AT START Of6.25 HOUPS ELAPOED TIME:
TOT.Av6. NA50 TEMP PPE!!UFE CTNT. AIF MATIiLENS LO' LOOS *LEM HG TIME MAS! <LBMs (R) W !A>
63.4043 92073 24.9 30 531.525 63.4024 92067 6.2 27.0 45 531.615 92059 7. 3 100 531.647 63.4012 9. 5 30.7 63.3996 92050 31.1 115 531.680 92042 9.1 26.1 130 531.699 63.3953 1.6 63.3916 92040 d'5. 9 145 531.694 92034 6.1 100 531.706 63.3908 92028 6.1 25.7 215 531.?l2 63.3073 7.8 26 4 43.3829 92020 24.6 2'30 531.720 92018 2.6 245 531 725 63.3817 92011 6.9 24.3
-i 300 531.739 63.3766 9.4 26.0 1
63.3725 92001 26.1 315 531.742 63.3661 91995 6.7 26.5 330 '*71.744 63.3629 91987 7. 9 26.7 345 532.746 91980 7.1 26.7 400 531.766 63.3604 6.9 63.3!53 91973 26.4 415 531.763 61.35v6 91967 5.3 430 531.756 11.3 27.5 63.?459 91956 26.9 445 531.750 91952 4.4 560 531.778 63.3456 91947 4.4 26.5 i15 531.720 A 3. 5 396 7. 9 26. "-
i3.3244 91'40 25.*
530 531.775 91939 1.2' 545 531.766 63.3.125 91934 4.9 25.2 600 531.769 63.3295 31926 3.1 25.5 615 531.77A 63.3250 91923 2. 7 24.9 630 ",31.754 63.3205 15.5 26,4 63.31 3 9190&
645 531.962 OF CU FT.s = 0.296 FREE AIR VOLUME U*ED (MILLION:
FEGPE*SION LINE a 92072 INTERCEPT < LENS = -25,7 SLOFE < LLn *
- 0.904 EFIFICATION TEST LE6k AGE PATE #JP6EP LIMIT =0.654 VERIFICATICN TEST LEAKAGE PATE LuwCP= LIMIT =0.671 M CALCOLATEI LEAkAGF PATE CONSTANT VOLUME i
. - T .
Table III.C.13.
Leakage Rate Verification: Total Time Calculation Free Air Volune Varied PERCH BOTTDM UNIT 3 ILRT VERIF LEAKAGE RATE GEIGHT PERCENT / DAY)
EASED ON TOTAL TIME CALCULATIONS
[ TIME AND DATE AT START OF TEST 30 0405 E
ELAPSED TIME 6.25 hJURS TEMP. PRESSURE MEASURED TIME (R) (PSIA) LEAKAGE RATE 30 531.595 63.4043 45 531.615 63.4024' O.649 100 531.647 63.4C12 0.704 115 531.680 63.3906 0.799 ISO 531.699 63.3953 0.810 145 531.694 63.3936 0.681 F 200 531.706 63.3908 0.669
' 215 531.712 63.3873 0.665 230 531.720 63.3829 0.683 cm ,
245 531.725 63.3817 0.637 300 531.739 63.3786 0.642 315 531.742 63.3725 0.673 330 531.744 63.3681 0.675
- 345 531.746 63.3629 0.687 400 531.766 63.3604- 0.690 415 531.763 63.3553 0.692 430 531.756 63.3500 0.681 445 531.780 63.3459 0.710 500 531.778 63.3426 0.697 515 531.700 63.3398 0.684 530 531.775 63.3344 0.686 545 531.766 63.3325 0.660 600 531.769 63.3295 0.653 615 531.778 63.3250 0.660 630 531.756 63.3205 0.643 645 531.8G2 63.315'3 0.682
= 0.685 MEAN CF MEASURED LEAKR62 RATES = 0.041 OTD. DEVIATION OF MERSURED (EAKAGE RATE:
0.884 VERIFICATION TEST LEAKAGE RATE UPPER LIMIT = 0.634 YERIFICATICM TEST LERKAGE RATE LDWER LIMIT == 0.661
) THE CALCULATED LEAKAGE RATE Free Air Volume Varied a
h 1
_ - ,- - , - . , - w., , , . -,
I
.. .. j i;
i i
i 1
Table TotalIII.C.14.
Time Calculation, Trend Report l r
Leakage Rate verification: Free Air Volume Varied i f !
e
- f 1 PEACH BOTTCM UNIT 3 ILRT VERIF !
ie TREND REPORT .
ij LEAK AGE RATES WEIGHT PERCENT / DAY)
BASED ON TOTAL-TIME CALCULATIONS 30 0405 3
TIME AND DATE AT ELAPSED TINE:
START OF TEST 6.25 HOURS T
W ;- CALCULATED CH6 IN CALC L/R f='
NO. DATR ELAPSED I NE POINTS ..__1._._A-NEAN MERSURED LERKAGE RATE FRON LAST POINT LEAKAGE RATE- .-...
0.665
._ _.__. 0.700 -0.014 10 2.25 0.694 0.451 0.000
!! 2.50 0.692 0.652 0.001 12 2 75 0.691 0 653 0.004 3 3 00 0.657 4
13 3.25 0.690 0.662 0.004 14 3.50 0.690 0.004 i 15 0.690 0.666 0.001 16 3.75 0.690 0.667 0.007 17 4.00 0.691 0.674 0.003 4.25 0.677 0.000 k.
18 19 4.50 0.691 0.677 0.001 4.75 0.691 0.677 20 0.691 -0.004 1 21 5.00 0.689 0.673 -0.005 22 5.25 0.688 0.668 -0.003 22 5.50 0.686 0.665 -0.005 24 5.75 0.685 0.660 0.001 25 6.00 0.685 0.661 26 6.25
= 0.661 THE CALCULATED LEAKAGE RATE
{-
r<
Free Air Volume Yarted
=
9 4
54
. s .
a Table III.C.15.
I.eakage Rate Verification: !! ass Point Analysis Free Air Volure Varied PEACH BOTTCM UNIT 3 ILRT VERIF LEAAA6E RATE (WEIGHT PERCENT / DAY)
MASS PulhT MNALYSIS TINE AND DATE AT START DF TEST: 30 0405 ELAPSED TIME: 6.25 NOURS TIME TEMP PRESSURE CTNT. AIR MASS LOSS TDT. AVG. MASS (R) (PSIA) MASS (LBM) sLBM) LOSS (LBMeHR)
___ - - - - = _ __ ____._ ..___..._---__ __
30 531.595 63.4043 92073 45 531.615 63.4024 92067 6.2 24.9 l
100 531.647 63.4012 92060 7.3 27.0 115 531.680 63.3986 92050 9.5 30.7 130 531.699 63.3953 92042 8.1 31.1 145 531.694 63.3936 92041 1.6 26.1 200 531.706 63.3908 92035 5.0 25.7 215 531.712 63.3873 92029 6.1 25.5 230 531.720 63.3829 92021 7.8 26.2 245 531.725 63.3817 92018 2.6 24.4 300 531.739 63.3786 92012 6.6 24.6 315 531 742 63.3725 92002 9.4 25.8 330 531.744 63.3681 91996 6.7 25.9 345 531.746 63.3629 91988 7.9 26.3 400 531.766 63.3604 91981 7.1 26.5 415 531.763 63.3553 91974 6.9 26.6 430 531.756 63.3508 91969 5.0 26.1 445 531.780 63.3459 91957 11.3 27.3 500 531.778 63.3426 91953 4.4 26.7 515 531.780 63.3398 91949 4.4 26.3 530 531.775 63.3344 91942 7. 0 26.3 545 531.766 63.3325 91940 1.2 25.3 600 531.769 63.3295 91935 4.9 25.0 615 531.778 63.3250 91928 7.8 25.3 630 531.?!6 63.3205 91925 2.4 24.7 645 531.802 63.3153 91910 15.5 26.1 FREE AIR VOLUME USED (MILLICNS OF CU. FT.) = SEE SI M ARY DATA REGRESSION LINE INTERCEPT (LBM) = 92072 SLDPE (LEMeHR) = -25.5 VERIFICATICN TEST LEAKAGE RATE UPPER LIMIT = 0.886 i
VERIFICATION TEST LEAKAGE RATE LOWER LIMIT = 0.636 I THE CALCULATED LEAKAGE PATE = 0.665 Free Air Vohree Varied 55 _,
.. .s ',I
- ?
- r Il
- b q
l Table III.C.16. (a) l l'easured and Corrected Data Summary f Leakace Rate Verification ~
A i
9 30 0405 6 IUMMARY OF MEASURED DATA AT TEMP 1= 535.220 < 75.62) '
TEMP 2= 537.370 < 77.77) 531.830 < 72.23)
TEMP 3=
TEMP 4 = 530.860 < 71.26) !
TEMP 5= 529.160 < 69.56) l TEMP 6= 529.510 < 69.91) .
TEMP 7= 527.910 < 68.31) !
TEMP 8- 527.640 < 68.04) l TEMP 9= 524.290 < 64.69)
TEMP 10 = 532.750 < <
73.15) 72.71)
~
TEMP 11 = 532.310 TEMP 12 = 532.340 < 72.74)
- PRES 1 = 63.751 (63749.)
VPRS 11 = 0.309 < 65. 3 0)
VPRS ,12 = 0.323 ( 66.60)
! VPRS ' 3 = 0.299 < 64.40) 0.398 < 72,71)
VPRS 4' =
VPRS 5= 0.398 < 72.74) c 4
(
I i
l
SUMMARY
OF COPPECTED DATA I-TIME = 30 f DATE = 0405 )
(
= 531.595 TEMPERATURE < DEGREES R.)
4
= 63.4043 CORPECTED PRESOUPE (PSIA)
}
h r 1
?
56
'I Table III.C.16 (b)
Measured and Corrected Data Surmary Leakage Rate Verification
$UMMARY OF MEASURED DATA AT 45 0405 ;
i TEMP 1 = 535.27 - ( 75.63)
TEMP 2= 537.350 ( 77.75)
TEf1P 3= 531.810 ( 72.21)
TEMP 4= 530.920 ( 71.32)
TEMP 5= 529.220 ( 69.62)
TEMP 6= 529.500 ( 69.90)
TEMP 7= 527.960 i 68.36>
TEMP S= 527.780 ( 68.18)
TEMP 9= 524.330 t 64.73)
TEMP 10 = 532.750 ( 73.15)
TEMP 11 = 532.320 ( 72.72)
TEMP 12 = 532.350 ( 72.75's PRES 1= 63.750 (63748.>
YPPI I l = 0.310 ' 45.46)
VPPI F 2= 0.324 56.70s VPPS 3= % 301 ( 64.60)
VPP; 4 = 0.098 ( 72.72)
VPP5 5= 0.399 ( 72.75) .
l IUMMARY OF COPPECTED DATA TIME = 45
< DATE = 0405 TEMPEPATUPE (DEGPEES R.) = 531.615 COPPECTED PPE55UPE (PS I A's
= 63.4024 57
.r .
s, ,e
( . .
Table III.C.16. (c)
?!easured and Corrected Data Summary Leakage Rate Verification
SUMMARY
OF MEASURED DATA AT 100 0405 TEMP 1 = 535.250 ( 75.65)
TEMP 2=
537.300 ( 77.70)
TEMP 3= 531.930 ( 72.33)
TEMP 4 = 530.990 ( 71.39) r TEMP 5= 529.250 ( 69.65) i TEMP 6= 529.630 ( 70.03)
TEMP 7= 528.010 ( 68.41) l TEMP 8= 527.760 ( 68.16) '
TEMP 9= 524.390 ( 64.79)
TEMP 10 = 532.760 ( 73.16)
TEMP 11 = 532.330 ( 72.73)
- TEMP 12 = 532.360 ( 72.76) .
1
$ PRES 1= 63.750 (63747.)
{
i VPRS Ii = 0.311 ( 65.50)
VPRS f2 = 0.324 ( 66.70)
, VPRS 3,= 0.301 ( 64.60)
VPRS 4= 0.398 ( 72.73) .
VPRS 5= 0.399 ( 72.76)
SUMMARY
OF CORRECTED DATA TIME = 100 DATE = 0405 TEMPERATURE (DEGPEES R.) = 531.647 COPPECTED PRESSUPE (PSIA) = 63.4012 en
h Table III.C.16. (d) ,
Measured and Corrected Data Summary Leakage Rate Verification ;
I, i
115 0405
SUMMARY
OF MEASURED DATA AT 1= 535.250 ( 75.65) 537.340 ( 77.74)
TEMP TEMP 2= ( 72.35.5 l 3= 531.950 TEMP 4 = $31.120 ( 71.52)
TEMP 5= 529.330 ( 69.73)
( 70.15)
TEMP 4 6= 529.750 '
TEMP 7= $29.030 ( 68.43)
TEMP ( 68.13) j TEMP 3= 527.730 524.430 ( 64.83)
TEMP 9= ( 73.17)
! TEMP 10 = 532.770 ( 72.73) i TEMP 11 = 532.330 ( 72.76)
I. TEMP 12.= 532.360
{ 63.748 (63745.)
PRES 1= '
[
p 1= 0.312 ( 65.60) 9 VPRS 0.325 ( 66.80)
VPRSp 2 = ( 64. /0) i VPRS.,3 = 0.302
-h 0.398 ( 72.??) ,
VPR3' 4 = 0.399 ( 72.76)
} #
-VPR3 'S = j
SUMMARY
OF CURRECTED DATA TIME = 115 LATE = 0405 531.680 i
TEMPERATURE (DEGREES R.5 =
e 63.3986 CURRECTED PRESSURE (PSIA) l w
L l't g 59
r Table III.C.16, (e )
"easured and Corrected Data Summary Leakace Rate Verification i
SUMMARY
OF MEAEURED DATA AT 130 0405 TEMP 1 = 535.260 < 75.66)
TEMP 2= 537.450 < 77.85)
TEMP 3= 531.980 < 72.38)
TEMP 4 = 531.050 < 71.45)
TEMP 5= 529.340 < 69.74) 529.720 < 70.12) 7 TEMP 6=
TEMP 7= 528.110 < 68.51)
- TEMP 8= 527.870 < 68.27)
', TEMP 9= 524.470 < 64.87)
TEMP 10 = 532.780 < 73.18)
TEMP 11 = 532.340 < 72.74)
TEMP 12 = 532.370 < 72.77)
?
PRES 1= 63.745 (63742.)
Y
- 1= 0.311 < 65.50)
J VPRR f VPR$ 2= 0.328 < 67.00)
VPRS 3= 0.302 < 64.70> '
VPRS 4= 0.398 < 72.74)
VPRS 5= 0.399 < 72.77) a h \
+
t
SUMMARY
OF CURRECTED DATA i TIME = 130 i
DATE = 0405 TEMPERATURE (DEGREES R.)
= 531.699
?
CDPRECTED PRES $UPE (PSI A>
= 63.3953 Y
60 l
l
D-Table III.C.16. (f)
Measured and Corrected Data Summary Leakage Rate Verification 145 0405
SUMMARY
OF MEASURED DATA AT t
TEMP 1= 535.230 ( 75.63) i 2= 537.360 ( 77.76) l TEMS TEMP 3= 531.950 ( 72.35)
'j TEMP 4 = 530.990 ( 71.39) 1, TEMP 5= 529.330 < 69.78)
TEMR, 6= 529.740 ( 70.14)
TEMP 7= 528.100 < 68.50) y TEMP 8= 527.860 ( 68.26) d TEMP 9= 524.500 ( 64.90) q l
( 73.19)
TEMP 10 = 532.790 ( 72.75)
TEMP 11 = 532.350 ( 72.78)
TEMP 12 = 532.380 PRES 1= 63.744 (63741.)
VPPS 1= 0.313 ( 65.70)
VPRS 2.= 0.328 ( 67.00)
J 0.304 ( 64.80)
] VPRS VPRS
'i =
4' = 0.399 0.399
( 72.75)
( 72.78)
VPRS 5=
2
SUMMARY
OF CURRECTED DATA TIME = 145 DATE = 0405
= 531.694 TEMPERATURE (DEGREES R.)
= 63.3936 CURRECTED PRESSURE (PSI A) 7 61
1 Table III.C.16. (g)
Measured and Corrected Data Summary Leakage Rate Verification
-i 200 0405 IUMMARY OF MEASURED DATA AT TEMP 1= 535.280 ( 75.68) i 2= 537.380 ( 77.78)
TEMP TEMP 3= 531.920 < 72.32>
{ TEMP 4 = 530.980 < 71.38) 1 j TEMP 5= 529.410 ( 69.81)
TEMP 6= 529.780 ( 70.18) 3 528.110 ( 68.51) 7.=
f TEMP TEMP 3= 527.940 ( 68.34) i TEMP 9= 524.510 ( 64.91)
}4 TEMP 10 = 532.780 ( 73.18) .
TEMP 11 = 532.360 ( 72.76
}o TEMP 112 = 532.380 ( 72.78)
PRES. 1= 63.741 (63738.)
VPRS 1= 0.312 < 65. 6 0) h VPRS 2= 0.328 ( 67.001 .
g VPRS 3= 0.304 ( 64.80)
I VPRS 4= 0.399 ( 72.76)
VPRS 5= 0.399 ( 72.78)
SUMMARY
OF CDPRECTED DATA TIME = 200 DATE = 0405 TEMPEPATURE (DEGREES R.)
= 531.706 l l
CDRRECTED PRES 1URE (PC1 A>
= 63.3908
' f 62
Table III.C.16. (h)
Measured and Corrected Data Summary Leakage Rate Verification 215 0405
SUMMARY
OF MEASUPED DATA AT TEMP 1= 535.260 < 75.66)
TEMP 2= 537.400 < 77.80) 532.010 < 72.41) s TEMP 3=
4 TEMP 4 = 531.030 < 71.43)
TEMP 5= 529.400 < 69.80) 529.770 < 70.17) i TEMP 6=
TEMP 7= 528.150 < 63.55) d i
TEMP 8= 527.960 < 68.36)
TEMP 9= 524.550 < 64.45)
TEMP 10 = 532.750 < 73.15')
j TEMP 11 = 532.350 < 72.75) i TEMP 12 = 532.370 < 72.77) j 1 PPES 1= 63.738 (63735.')
j
< 65.8 0)
I VPRS 1= 0.314 g VPRS 2= 0.328 < 67.00) i VPRS .* '3 = 0.305 < 64.90)
$ VPRS .4 = 0.399 ( 72.75)
VPR3 5' = 0.399 < 72.77:)
G b
30MMARY OF CDPRECTED DATR E8 TIME = 215 DATE = 0405 TEMPERATURE (DEGREES R.)
= 531.712
= 63.3873 CURRECTED PRESSURE (PSIA) 63
T k
lj *. .*
s
?
4 1
Table III.C.16. (i)
Measured and Corrected Data Sur. mary l*
Leakage Rate Verification t
't W
i o 230 0405 j IUMMAR/ OF MERLURED DATA RT TEMP 1 = 335.210 < 75.61)
TEMP 2= 537.250 < 77.65:)
TEMP 3= 532.060 < 72.46)
TEMP 4 = 531.020 < 71.42)
TEMP 3= 529.410 < 69.8D TEMP 6= 529.810 < 70.21)
TEMP 7= 528.180 < 68.58)
[ TEMP 8= 327.940 < 68.34)
TEMP 9 ,= 524.570 < 64.97')
TEMP 10 = 532.800 < 73.20) t TEMP 11 = 532.360 < 72.76) 1 TEMP 12 = 532.400 < 72.80) .
- PRES i.1 = 63.734 (63731.)
- ~
VPRS 1 = 0.314 ( 65.303 VPRT 2= 0.328 < 67.00)
VPP3 3= 0.306 < 65.00')
VPR5 4 = 0.399 < 72.76)
VPPS 5= 0.399 < 72.80)
SUMMARY
OF CURRECTED DATA TIME = 230 DATE = 0405
= 331.720 TEMPEPATUPE (DEGPEEE R.)
= 63.3829 CDPRECTED PRES?UPE (PSIR)
G4
Table III.C.16. (i)
"easured and Corrected Data Summary Leakage Rate Verification IUMMARY OF MEASURED DATA AT 245 0405 TEMP 1 = 535.210 < 75.61)
TEMP 2= 537.290 < 77.69)
TEMP 3= 532.010 < 72.41)
TEMP 4 = 531.060 < 71.46)
TEMP 5= 529.450 < 69.85)
TEMP 6= 529.800 < 70.20)
TEMP 7= 528.200 < 68.60)
TEMP G= 527.940 < 68.34)
TEMP 9= 524.570 < 64.97)
TEMP 10 = 532.800 < 73.20)
' TEMP 11 = 532.390 < 72.79)
- I TEMP 12 = 532.370 < 72.77)
PRES 1 = 63.732 (63729.) .
VPRSE 1 = 0.314 ( 65.80i VPR9' 2 = 0.329 < 67.00)
? VPRS 3= 0.302 < 64.70)
VPRS 4 = 0.399 < 72.79)
[ 0.399 < 72.77)
VPRS 5=
i
SUMMARY
OF CURRECTED DATA TIME = 245 DATE = 0405 TEMPERATURE < DEGREES R.)
= 331.725 CURRECTED PRESSURE (PSIA)
= 63.3817 i
t 65 b
99 . .
rt C
0 hl F1 i I
I
= (815d) 3dDS53dd G3103ddOO l f, 9828'E9 3,
6c2 icG = (. a s33ae3G, San. tea 3aW3.t .
e 5
60 t0 = 3.L60 !'
008 = 3WI.t e d
r 6.18G G3.103edD3 30 AeBWWD5 ;
3 i
i
! L 1
r k
<e2 e2 > 66E 0 =9 Sede.
c92'22 (02*t9
)
)
66E'
- 0 20E *0
=d
= 0 5ddA 5ed6 f
g t0T*29 ) 6EE*O = 2 Edda {
2-(08*G9 ) FIC*O = IJ ShdA I
.i k;
(
- 922E 9) 622*E9 = I S38d s-T (82*E2 > 08E*EEG = 21 dW3.1 [
(92 *E2 > 09C*2EG = II dW3L i-
- (.0E*E2 > 008*2EG =
- 01 dW3.L k 009'tCG = 6 dW3.L F (00*G9 )
(6E'89 ) 066*2EG = 8 dW3.L $
(C'*89 ) 082*826 = 4 dW3.L (02 '02 > 008*6EG = 9 dW3.1 (28*69 ) 02t*625 = G dW3.L I (Gr
- 12 > 090*IEG = t dW3.t !
(Gr
- E2 > 060*2EG = E dW3.L [
(92*22 > 09C*2EG = 8 dW3.L t (99*G2 > 09E*GEG = 1 dW3.L f i
i 60t0 00E .Le 8.LYG G380593W 3D AM4WWD5 r i
c uoyaecy;T2aA ages a5egeeg -
A2esans egeG paaca22o3 pue pa2nsea;3 (M) *9T*3*III aIgez e ,
3
.= *.
~
I Table III.C.16. (1)
Measured and Corrected Data Summary Leakage Rate Verification f.-
.?
IUMMAkV 0F MEASURED DATA PT 315 0405 TEMP 1 = 535.230 < 75.63) f j .
TEMS TEMP 2=
3=
537.360 532.090
< 77.76)
< 72.49) d TEMP 4 = 531.100 < 71.50) 3 TEMP 5= 529.460 < 69.86)
) TEMP 6= 529.760 < 70.16) i TEMP 7= 528.240 < 68.64)
TEMD 8= 527.990 < 68.39)
TEMP 9= 524.620 < 65.02) j TEMP 10 = 532.790 < 73.19)
- TEMP 11 = 532.370 < 72.77) k TEMP 12 = 532.390 < 72.79)
LRES 1= 63.723 (63720.)
T VPRS 1= 0.314 < 65.80)
- VPRS 2= 0.328 < 67.00)
VPR3) 9 = 0.304 < 64.80)
If VPRS:- 4 = 0.399 < 72.77)
VPRS 5= 0.399 < 72.79) w, 3
SUMMARY
OF CukREC1ED DATA n TIME = 315 ll' DATE = 0405 I TEMPERATURE (DEGREES R.:)
= 531.742 l = 63.8725 g : ORREC1ED PRES $UPE (PSIA)
I!
i, l
1 D,
v
':4 k
e ew
r -
(
.. .. 1 l
2 . . !.
h S :
~
Table III.C.16. (m) ll i 4 Measured and Corrected Data Summary i
Leakage Rate Verification 3 \
t i
- 5. I IUMMARY OF MEASURED DATA AT 330 0405 !
f, !
4 ;
J TEMP 1 = 535.140 < 75.54)
< 77.64') !
J* TEMP 2= 537.240 !
TEMP 3= 532.100 < 72.50) f TEMP 4 = 531.080 < 71.48)
TEMP 5= 529.520 < 69.92)
TEMP 6= 529.840 < 70.24)
TEMP 7= 528.220 < 68.62)
TEMP 8= 528.040 < 68.44)
TEMP 9= 524.630 < 65.03)
I TEMP 10 = 532.810 < 73.21)
TEMP 11 = 532.370 < 72.77)
TEMP 12'= 532.390 < 72.79)
PRES 1= 63.719 (63716.) .
3 4
1 VPRS 3 1= 0.313 ( 65.7D')
VPRS J2 = 0.329 < 67.10')
VPRS* 3 = 0.305 < 64.90') ,
VPRS 4 = 0.399 < 72.77)
VPRS 5'= 0.399 < 72.79)
EUMMARY OF CORRECTED DATA TIME = 330 DATE = 0405 TEMPERATURE (DEGREES R.) = 531.744 CORPECTED PRESSUPE < PSIA') = 63.3681 a -
68
~
f Table III.C.16. (n) i Measured and Corrected Data Summary Leakage Rate Verification
.UMMARY OF MEASURED DATA AT 345 0405 .
TEMP 1 = 535.130 ( 75.53.)
TEMP 2= 537.220 ( 77.62')
TEMP 3= 532.100 ( 72.50) f TEMP 4 = 531.110 ( 71.51')
4 TEMP 5= 529.470 ( 69.87)
I TEMP 6= 529.980 ( 70.28) ,
TEMP 7= 528.260 < 68.66) F TEMP 8= 528.050 < 68.45)
TEMP 9= 524.640 ( 65.04) ,
TEMP 10 = 532.810 ( 73.21) >
TEMP 11 = 532.370 ( 72.77) -
a TEMP 12 = 532.390 ( 72.79) l PRES 1 = 63.714 (63711.1 ,
VPRS 1= 0.313 ( 65.70) ,
I-* YPRS 2, = 0.330 ( 67.20)
VPRS 3= 0.305 ( 64.90)
VPRS 4= 0.399 ( 72.77) i VPRS 5= 'O.399 ( 72.79) l l- .
i EUMMARY OF CORRECTED DATA
, TIME = 345 DATE = 0405 l
< TEMPERATURE (DEGREES R.) = 531.746
'DRRECTED PRESSURE (PSIR)
= 63.3629 ,
I f
l 3
6 69
s v i &
. i t
I.
Table III.C.lG. (o) i Measured and Corrected Data Summary Leakage Rate 7erification IUMMARY OF MEAIURED DATA AT 400 0405 j TEMP 1= 535.200 < 75. 6 0')
7 TEMP 2= 537.270 < 77.67)
,i i TEMP 3= 532.070 < 72.47) f TEMP 4 = 531.200 < 71.60)
! TEMP 5= 529.530 ( 69.93)
{ TEMP 6= 529.920 < 70.32) 7' = 528.240 < 68.64:)
[
TEMP TEMP 8= 528.030 < 68.43)
TEMP 9= 524.640 ( 65.04')
[ TEMP 10 = 532.810 < 73.21)
~
TEMP 11 = 532.380 < 72.78) s TEMP 12 = 532.390 < 72.79)
PRES 1= 63.712 (6 37 09. ~)
~ <
Y .
-; VPRS. 1 = 0.315 < 65.90~)
. VPRS' 2= 0.330 < 67.20)
VPRS 3= 0.306 < 65.00)
VPRS 4 = 0.399 ( 72.78')
i VPRS 5= 0.399 ( 72.79)
EUMMARY OF CURRECTED LATA -l I
TIME = 400 DATE = 0405 TEMPERATURE (LEGREES R.) = 531.766 CURRECTED PRES $URE (PSIA) = 63.3604 I f:
a 70
.. .. (
Table III.C.16. (p)
!!easured and Corrected Data Summary Leakage Rate Verification IUMMARY OF MEASURED DATR AT 415 0405 .
TEMP 1 = 535.180 < 75.58)
TEMP 2= 537.250 < 77.65)
TEMP 3= 532.030 < 72.43) i TEMP 4= 531.190 < 71.59)
TEMP 5= 529.540 < 69.94)
TEMP 6= 529.890 < 70.29)
TEMP 7= 528.270 < 68.67)
TEMP 8= 528.030 < 68.43)
TEMP 9= 524.650 < 65.05)
TEMP 10 = 532.820 < 73.22)
TEMP 11 = 532.380 < 72.78)
TEMP 12 = 532.400 < 72.80)
PRES 1= 63.707 (63704.)
VPRS 1= 0.315 < 65.90)
VPRS 2= 0.330 < 67. 2 0)
VPRSr 3 = 0.306 < 65.00)
VPRS',4 = 0.399 < 72.78)
VPRS' 5= 0.399 < 72.80) i i
OUMMARY OF CORPECTED DATA TIME = 415 DATE = 0405 ,j
! TEMPERATURE < DEGREES R.) = 531.763 t CORRECTED PRESSURE (PSIA) = 63.3553 i ?'
i 1-I f
4 I,
71 L
- s' Table III.C.16. (q)
Measured and Corrected Data Summary Leakage Rate Verification
- UMMARY OF MEASURED DATA AT 430 0405 TEMP 1= 533.160 < 75.56)
TEMP 2= 537.280 < 77.68)
TEMP 3= 532.100 < 72.50) ,
TEMP 4= 531.050 < 71.45) r!
TEMP 5= 529.540 < 69.94) l:
TEMP 6= 529.870 < 70.27) !.
TEMP 7= 528.310 < 68.71) !!
TEMP 8= 528.020 < 68.42) l!
TEMP 9= 524.670 < 65. 07) l TEMP 10 = 532.810 < 73.21)
- TEMP 11 = 532.380 < 72.78) h TEMP 12 = 532.390 < 72.79)
[l PRES 1= 63.702 (63699.) Il VPRS I = 0.314 < 65.80) i. l VPRS ',2 = 0.330 < 67. 20) Mi VPRS
- 3 = 0.305 < 64.907 !
VPRS' 4= 0.399 < 72.78) ;
VPRS 5= 0.399 < 72.79) !,
R r
I i
SUMMARY
OF CORRECTED DATA TIME = 430 .
DATE = 0405 TEMPERATURE (DEGREES R.) = 531.756 63.3508 l CORRECTED PPESSURE < PSIA) = ,
l k
i
'l r
i i
72
- e e' l
I a
Table III.C.16. (r)
Measured and Corrected Data Summary Leakage Rate Verification EUMMARY OF MEASURED DATA RT 445 0405 I
TEMP 1 = 535.160 < 75.56) !
TEMP 2= 537.310 < 77.71)
TEMP 3= 532.140 < 72.54)
TEMP 4= 531.230 < 71.63)
TEMP 5= 529.530 < 69.93)
TEMP 6= 529.950 < 70.35)
TEMP 7= 528.270 < 68.67)
TEMP S= 528.020 < 68.42)
TEMP 9= 524.670 < 65. 07)
TEMP 10 = 532.820 < 73.22) i TEMP 11 = 532.380 < 72.78) i TEMP 12 = 532.400 < 72.80) ,
(63694.)
PRES .1
= 63.697 !
VPRS 1= 0.315 < 65.90)
VPRS 2. = 0.330 < 67.20)
VPRS 3= 0.304 < 64.80)
VPRS 4= 0.399 < 72.78)
VPRS 5= 0.399 < 72.80)
SUMMARY
OF CORRECTED DATA ,
TIME = 445 DATE = 0405 TEMPERATURE < DEGREES R.)
= 531.780 .
CDPRECTED PPESOURE (PSIA)
= 63.3459 i
73
s I
Table III.C.16. (s)
Measured and Corrected Data Summary Leakage Rate Verification
SUMMARY
OF MEASURED DATA AT 500 0405 TEMP 1 = 535.130 < 75.53)
TEMP 2= 537.270 < 77.67)
TEMP 3= 532.100 < 72.50) j TEMP 4= 531.220 < 71.62)
TEMP 5= 529.570 < 69.97)
- TEMP 6= 529.930 < 70.33)
TEMP 7= 528.270 < 68.67)
> TEMP 8= 528.080 < 68.48)
TEMP 9= 524.660 < 65.06) .
TEMP 10'= 532.820 < 73.22) :l TEMP 11 = 532.390 < 72.79)
TEMP 12 = 532.400 < 72.80)
< PRES 1= 63.694 (63691.)
- d. Y -
i i
VPRSc 1 = 0.315 ( 65.90) i VPRS. 2= 0.330 < 67.20) l VPRS 3= 0.305 < 64.90)
VPRS 4= 0.399 < 72.79)
VPRS 5= 0.399 ( 72.80)
SUMMAkY OF CORRECTED DATA .
TIME = 500 DATE = 0405 TEMPEPATURE (DEGREES R.) = 531.778 CORRECTED PRESS.URE (PSIA) = 63.3426 ,
I L
74
w -
f I
i Table III.C.16. (t)
I Measured and Corrected Data Summary 1 Leakage Rate Verification '
E
SUMMARY
OF MEASURED DATA AT 515 0405 TEMP 1= 535.160 < 75.56)
TEMP 2= 537.290 < 77.69)
TEMP 3= 532.080 < 72.48)
TEMP 4= 531.160 < 71.56)
TEMP 5= 529.550 < 69.95)
TEMP 6= 529.980 < 70.38)
TEMP 7= 528.290 < 68.69)
TEMP 8= 528.080 < 68.48)
TEMP 9= 524.680 < 65.08)
TEMP 10 = 532.820 < 73.22)
TEMP 11 = 532.390 < 72.79)
TEMP 12 = 532.400 < 72.80)
PRES 1= 63.691 (63688.)
VPRS r1 = 0.314 < 65. 8 0)
VPRS/.2 = 0.330 < 67.2n>
VPRS' 3= 0.305 < 64.90)
, VPRS' 4.= 0.399 < 72.79)
VPRS 5= 0.399 < 72.80) .
'a I
SUMMARY
OF CORRECTED DATA 1 TIME = 515 .
DATE = 0405 TEMPERATURE (DEGREES R.) = 531.780 CORRECTED PRESSURE (PSIA) = 63.3398 .l 75
7 l
.i '
- Table III.C.16. (u) !
4 Measured and Corrected Data Summary i Leakace Rate Verification E
2 9 l 4 IUMMARY OF MEASURED DATA AT 530 0405 TEMP 1= 535.070 ( 75.47) f TEMP 2= 537.220 ( 77.62)
O TEMP 3= 532.140 ( 72.54)
$ TEMP 4 = 531.170 ( 71.57)
- TEMP 5= 529.540 < 69.94) di TEMP 6= 529.990 ( 70.39) 9 6 TEMP 7= 528.290 ( 68.69)
Ij ! TEMP 8= 528.070 ( 68.47) 3 TEMP 9= 524.680 ( 65. 08) .
3 5 TEMP 10 = 532.830 ( 73.23) l i TEMP 11 = 532.390 ( 72.79)
- p TEMP 12 = 532.400 ( 72.80) .
SJ PRES 1= 63.686 (63683.)
i VPRS 1= 0.315 ( 65'.90)
VPRS 2= 0.331 ( 67.30)
VPRS 3 = 0.305 ( 64.90)
VPRS 4= 0.399 ( 72.79) '
- VPRS 5= 0.399 ( 72.80) ,
l
SUMMARY
OF CORRECTED DATA .i L TIME = 530 DATE = 0405
_ TEMPEPATURE (DEGREES R.) = 531.775 ,
b
[ CORPECTED PRESSURE (PSIA) = 63.3344 !
l I
i I
" l 76
1 i
e e' I
Table III.C.16. (v) y Peasured and Corrected Data Summary
, Leakace Rate Verification 1 i t
2
.Uf1 MARY OF f1EAIUFED DATA AT 545 0405 '
S TEMP 1 =
535.050 !
( 75.45)
) TEMP 2= 537.250 ( 77.65)
TEf1P 3= 532.120 < 72.52) :
/)' TEMP TEMP 4 = 531.200 < 71.60) )
~
5= 529.530 ( 69.93) l TEMP 6= 529.880 ( 70.28) '
i D TEMP 7= 523.280 < 68.68)
.~..
TEMP 8= 528.050 < 68.45)
TEMP 9= 524.680 < 65.08)
TEMP 10 = 532.830
.f TEMP 11 = 532.400
< 73.23)
< 72.80)
Jj TEMP 12 = 532.400 < 72.80) 4 PPES 1 = 63.683 (63620.) -
t,
!,- VPPS 1 = 0.314 ( 65.80) f VPPS 2 = 0.329 < 67.10)
VPRO1 3 = 0.302 < 64.70) tbj P; VPRO:'4 = 0.399 ( 72.80) g! VPRO- 5. = 0.399 < 72.80)
?
lbt i
g 1
2UMMAPY OF COPRECTED DATA 5 TIME = 545 '
f- DATE = 0405 TEMPERATURE (DEGREES R.) = 531.766
.COPPECTED PPESCUPE (PSIA) = 63.3325
- l i
i t
5 g
d) 77
Se *
, i
. I Table III.C.16. (w)
Measured and Corrected Data Summary Leakage Rate Verification
- i 4
I IUMMARY OF MEASURED DATA AT 600 0405 5
N TEMP 1 = 535.100, ( 75.50) ,
.h TEMP 2= 537.180 ( 77.58) -
} TET)P 3= 532.160 ( 72.56) i 3 TEMP 4= 531.220 ( 71.62)
} TEMP 5= 529.550 < 69.95) !
$ TEMP 6= 529.840 ( 70.24) d TEMP 7= 528.300 ( 68.70) f) TEMP 8= 528.060 ( 68.46) ;;
4 TEMP 9= 524.660 < 65.06) L
$ TEMP 10,= 532.830 < 73.23) ll 7 TEMP 11 = 532.400 ( 72.80) .
1; TEMP 12 = 532.400 < 72.80) i i
y PRES 1= 63.680 (63677.)
.. I VPRS li = 0.314 ( 65.80) l VPRS c2 = 0.329 < 67.10) 4 VPRS 3= 0.302 < 64.70) "
4 VPRS 4 - 0.399 < 72.80)
J VPRS 5= 0.399 < 72.80) h i 1
W. i
SUMMARY
OF CORRECTED DATA i.{ ( ,
TIME = 600 .i
- DATE = 0405 l t
TEMPERATURE (DEGREES R.) = 531.769 i e !
> COPPECTED PRESSUPE (PS I A) = 63.3295 i
- l 4
< ! 4 4 ' '
e T3 '
's.
78
l' f-l t
t Table III.C.16. (x)
~
Measured and Corrected Data Surmary
}
Leakage Rate Verification t
-\
615 0405 -
5 IUMMAPY OF MERSUPED DATA RT 535.030 < 75.43) 1 TEMP 1 =
1 TEMP 2= 537.180 < 77.58) i TEMP 3= 532.090 < 72.49) 531.330 < 71.73) 4 TEMP 4=
i TEMP 5= 529.540 < 69.94) i TEMP 6= 529.920 < 70.32)
] TEMP 7= 528.290 < 68.69) ; ,
5 TEMP 8= 528.070 < 68.47) - :
d TEMP 9= 524.670 < 65.07)
J4 TEMP 10 = 532.840 < 72.81)
< 73.24) ; l TEMP 11 = 532.410 ,
l TEMP r2 = 532.410
< 72.81) l g {
PRES 1 = 63.676 (63673.) , I 1i VPRS 1= 0.315 < 65. 90)
~
?
VPRS- 2= 0.329 < 67.10) ,
i VPRS 3= 0.304 < 64.80)
- VPRS 4= 0.399 < 72.81)
.3 0.399 < 72.81)
VPRS 5=
~{p
SUMMARY
OF CDPRECTED DATA TIME = 615 .l DATE = 0405 .!
i
= 531.778 TEMPERATURE (DEGREES R.)
= 63.3250 CORFECTED PRESSUPE (PSIA) .
1 i
d i if
~' 79
i
- . .- i j 1
l
. l 3 4 I
6 i
Table III.C.16. (y)
} Measured and Corrected Data Surrary l 4
Leakage Rate Verification l I
I 1
1 j IUMMARY OF MEASURED DATA AT 630 0405 TEMP 1= 535.010 < 75.41) j
- 1. TEMP 2= 537.160 < 77.56) i J TEMP 3= 532.110 < 72.51) i TtMP 4= 531.110 < 71.51)
TEMP 5= 529.550 < 69.95)
{ .
6= 529.950 < 70.35)
.i ! TEMP TEMP 7= 528.290 < 68.69) ;
TEMP 8= 528.060 < 68.46)
{
TEMP 9= 524.670 < 65.07)
- TEMP 10 = 532.820 < 73.22) '
TEMP if = 532.390 < 72.79)
TEMP 12 = 532.400 < 72.80)
[* PRES 1= 63.671 <63668.)
0.313 P VPRSF 1= ( 65.70) '
VPRS, 2= 0.330 < 67.20)
VPRS 3= 0.302 < 64.70)
VPRS '4= 0.399 ( 72.79)
VPRS 5= 0.399 < 72.80)
SUMMARY
OF CORRECTED DATA TIME = 630 DATE = 0405 t TEMPEPATURE < DEGREES R.) = 531.756 ;
= 63.3205 'I CORRECTED PRESSURE (PSIA) I>
i
> i t
a M t 30
t s
4 Table III.C.16. ()
Peasured and Corrected Data Summary t Leakage Rate verification !
i IUMMARY OF MEASURED DATA AT 645 0405 TEMP 1 = 535.060 < 75.46)
TEMP 2= 537.140 < 77.54) n TEMP 3= 532.130 < 72.53) ,
TENP 4= 531.370 < 71.77) .i, TEMP 5= 529.590 ( 69.99) '
TEMP 6= 529.940 < 70.34) i TEMP 7= 528.330 < 68.73) l TEMP 8= 528.090 < 68.49) .
TEMP 9= 524.700 < 65.10) l TEMP 10 = 532.860 < 73.26) l
< 72.83)
TEMP 11 = 532.430 TEMP 12 = 532.440 < 72.84) b l PRES 1= 63.666 (63663.) ,
I h
P VPRSr 1 = 0.312 < 65. 6 0) ,
VPRS,', 2 = 0.329 < 67.10) d VPRS' 3= 0.304 ( 64.80) ll VPRS 4= 0.400 < 72.83)
< 72.84) h VPRS' 5= 0.400 '!
f I
ib
((
OUMMARY OF CORRECTED DATA .r g TIME = 645 g DATE = 0405 !
TEMPERATURE (DEGREES R.)
= 531.802 ,
CORRECTED PRESSURE (PSIA)
= 63.3153 E I l
I
!l 81 ;
1
.. .- t Table III.E.1. (a) ,
l TYPE "!!" TEST
SUMMARY
i I
i l
PEN'T SY STEM CR PENETR ATICN DATE TOTAL TOTAL REKAR KS NO. NAME .
2-07 74 20 1 Equip. Access Match "0" 2-12-74 10 eing 10675 to >
10 10 ,
1-26-77 2-08-74 850 l!
l 2 Personnel Airlock 8 22-74 1051 6
,; 281 1
- 10-08-74 !,
10-25-7 610
- 418 li 1
11-03-74 11 20-74 420 4 j i 12-1674 3 96 o 0 4
9 24-75
' 12-27-75 0 i 20 9 i 2-0676 0 ll a 3-07-76 3 7 6 400 ('
5-05-76 of f Scale
) 0 Replaced inner door seal 5-1676 5-2676 20
.f 5-31-76 0 0 I 7-16-76 7-2676 0 j 9-21-76 0 4-02-77 1100 1
d M
Personnel Airlock 2-05-74 0 ,
Double "0" Ring 1-0675 0 !
2 26-75 550 1-26-77 to 1110 0
f.
2 1474 >
p 4 Head Access 1-09-75 0 to 10 l i 1-25-77 l
2-06-74 0 .{
6 CR0 Hatch 8-15-74 0 i~
10-01-75 0 10 10 6 01-77 2-14-74 0
- Ory Well Head Seal 8-21-7 4 0 ,
l.09-75 0 1-31-76 0 10 10 Fj 4-01-77 J
i i
l.,
t
[ 82
.C c.
L
.I) c i
I Table III.E.1. (b) r TY DE "B" TE ST S UMMAR Y i
i TEST TE ST PE st 'T I PEN'T SY STEM CR PE NETR ATICN REMARKS DATE TOTAL TCTAL l No. ut i Reactor Stabilizer 0 12-17-73 si Manways A thru H 0
' I-30-75 1-18-77 45 'S l
1 22-74 0 fg 7A "A" Main Steam Lin' eellows 7 23-75 0 20 9-01-76 20 7e "B" Main Steam LW 1-22-7 4 0 Bellows 7-23-75 1500 1 29-76 2705 ;
Repaired Bellows I" 7" -
i 7C "C" Mai n St* *' 'i"* 1-22-74 0 Bellows 0 7-23-75 '
j 9-01-76 , 20 20 i.
': 4
.5 70 '"0" Main St**m 'i"* 0 '
sellows 1-22-74 4
7-23-75 9-01-76 99 105 105
[
g 5
9A Feedwater Line
' Be ll
- 5 1-22 74 0 1-23-75 99
- i 9-01-76 105 105 2
I I! 99 Feedwater Line 0
+
Be l las 1-22 74 7-23-75 0 y-9-01-76 20 20 m 0 K 11 MPCI Steam Line 1 22-74 9-16-75 0 gi Bellow 5 10-14-76 20 20 s
d 12 R m Suction Line 1-22-7 4 0 u Bellows 0 9 16-75 10-14-76 10 10 f
e i k
L s t j 83 !
Table III.E.1. (c) f TYPE "B" TEST SunMARY l
~
PEN'T SYS'EM CR PE NETR ATION TE ST TE ST PE N 'T NO. NAME REMARKS DATE T OT AL TOT AL 13A RHR Injection Line Bellows 1-22-74 0 0
ij 9-16-75 10-14-76 240 240 14 RwCU Suction Line Bell =s 1-22-74 0 9-16-75 0 10 t'
10-14-76 10 ,
i 16A Core Spray Injectf(e Line Bellows 1.22-74 0 i' 9-16-75 0 10-14-76 10 10 il 17 Head Spray Line l 8* 3 3 *
- 11-22 74 0 }
9-16-75 0' !
10-1676 10 10 i
13B "A" RHR Injection Line Bellows 1
,) _ , ,
10-1676 145 145 16B Core Spray Injection t i i"* B* I I *
- 1 22-74 0 i l
9-30-75 0 10-04-76 10 10 201A Torus vent Bellows 3 -
3 - 1[5 9-07-76 58 58 g
i 201e Torus Vent Bellows 12- -3 6 9-07-76 20 20 t
201C Torus vent Bellows 0 1 j6- 3 _
9-02-76 20 20 2010 Torus vent Bellows l2j6 j 0- 5 i 9-02-76 20 20
,l ;
I i
84
ew - .
l
.. i I
i Table III.E.1. (d) .
I TYPE "B" TEST
SUMMARY
fi
,ll TE ST PEN'T PEN'T SYSTEM OR PE hETR ATICN TEST DATE TOTAL T CT AL
- f REMARKS t NO. NAME , ,
12-05-73 0 I
201 E Torus Vent Sellows 10 09-75 75 58 58 9-02-76 12-05-73 0 201F Torus Vent Bellows 10 -0 9-)3 0 20 20 ;
9-02-76 12-04-73 95 201G Torus Vent Be11nws 10-10-75 108 3
9-07-76 130 130 0 l 12-04-73 :
20!H Torus Vent Bellows 10-10-75 0 .
9-07 76 20 20 ll 205B A0-30502A Double 12-06-73 ,0 4
"0" Ring 1-31-74 0 260 l 11-11-75 10-07-76 256 l s
I-09-74 0 26A Double "0" Ring 10-13-76 to
< 266 4
2-02-74 217 .
205A A0-350 2s Double "C" 11-11-75 0 i Ring Replaced "0" Ring 20 10-07-76
( 1 a
i 1-09-74 0 s 26B couble "C" Ring i
10-13-76 10 30 1
A0-3505 Double "0" t
25 12-21-73 0 Ring 10-28-75 0 {>
10-08-76 20 12-26-73 0 A0-3519 Double "0" 10-28-75 0 Ring 10-08-76 to 12-21-73 0 A0-3520 Double"0" 1-18-74 0 Ring 10-28-75 0 1 10-08-76 10 40 f 1
- i i
} i 85
7_
.. l
. j
-l Table III.E.1 (e)
TY PE "B" TE ST S JM".AR Y l l
t k
PEN'T SYSTEM OR PENETRATION TEST TE ST PEN'T NO. NAME REMAPKS DATE TOTAL TUTAL f' 26 AC-3507 Ocuble "0" Ring 12-20-73 0 11-10-75 0 .
10-07-76 10 1 A0-3506 couble "0" "I"3 . 2-03-74 50 !
11-10-75 0 l 10-07-76 20 1 30 !
219 A0-3511 Double "0" l Ring 11-12-75 0 10-12-76 37 i
A0-3512 Double "0" Ring 11-12-75 10-12-76 10 0
[
47 2058 A0-3521 A couele "0" Ring 12 06-73 0 1- 26-7 4 0 1- 26 -76 0 10-07-76 10 A0-35123 Oouble "0" Ring 12-06-73 0 1- 26 -7 4 0 1-26-76 0 10-07-76 20 30 35A TIP couble "D Ring 12-15-73 0
~
1-22-76 0 10-25-76 10 10 l
)
T 35S TIP couble "0" Ring 1 5 0 !
4- 25-7 4 0 6-10-74 0 1-22-76 0 10-25-76 10 10 t
}
86 i l
l l
y n j
, 1 1
Table III.E.1. (f)
TYPE "5" TEST SMRY TE ST PEN'T TEST
-} TOTAL TOT AL _
DATE
^
PEN'T SYSTEM CR FENETR ATION REMARKS NO. NAME 0
12-15-73 4 24-74 0 35C TIP Double "0" Ring 4-25-74 0
'[. 0 ~
M 1 22-76 10 to
- @ 10 25-76
- ']
- $ 12-15-73 0 0 ~
4 4 30-74 TIP Double ,"0" Ring 0 I#4 350 6-11-7 4 0
7-01-74 j l I-22-76 10 25-76 0
10 to .
d 0 f 35E TIP Ocuble "0" Ring 12-15-73 4- 23-74 0 0
4- 25-7 4 l 0 f 1 22-76 10 to 11 6 10-25-76 7 '
0 lld! 12-15-73 0
TE TIP Double "0" R ing L 23-74 i 35F 6 25-74 0 c 0
- 1 22-76 10 10-25-76 to i
0 !
12-15-73 6-28-74 0 353 TIP Double "0" Ring 0 f
+ 7-01-74 0 I-22-76 10 10-25-76 _
to 0
2-07-7 4 tc_
150 Test Nozzle Couble "0" 10 Ring 8-31-76 2-1674 0 i 0
Torus F.anway 9 22-75 200A 12-12-75 650 0
1-28-76 10 l 10 3-17-77 0
7-02-74 0 Const. Drain 12-10-75 10 213A 10 9-23-76 7-01-74 28 lI
}
12-0675 0 213B Const. Drain 10 10_
10-19-76
! l l
L 2
Y e
87 44 w
t Table III.E.1.(9)
^ TYPE "S" TEST SUMMRY 1
4 TE ST PEN'T TEST 3 PEN'T SYSTEM OR PENETRATION TOTAL TOTAL REMARKS DATE NO. NAT _
$ 1-21-7 4 0 Y 1000 Electrical 9-26-75 0 f 10 10-20-76 10 _
}
- 1-21-74 0 Electrical
'} 100E 9 26-75 0
-- 10
(
x 10-20-76 0
10 ___
'$ 1-21-74 1010 Electrical 9-26-75 0 9'
10-20 -76 10 10 y ,
I-21-74 0 101C Electrical 9-26-75 0 f.; 10-20-76 10 10
.<^
1- 21-7 4 0
- $ 101E Electrical 9-26-75 0 .
} 10-=-76 to 10 1-21-74 0
[ 1038 -Electrical 9-26-75 0 10-20-76 10 10
[
b .
I-21-7 4 0 i F. 104E Electrical 9- 26-75 0 -
10-20 -76 10 10 .
1- 21-7 4 0 10LF Electrical 9 26-75 0
'- 10 10-20-76 10 l 1-21-74 0 ICLH Electrical 0 9-26-75 10-20-76 10 10 1-21-7 4 0 i 105C Electrical 9-26-75 0 e 10-20-76 to 10 l 1-21-74 0 105D Electrical 9-26-75 0 10-20-76 10 10 1- 21-7 4 0 l 106C Electrical 9-26-75 0 . I 10-20-76 to 10 ;
i i I
i III 88
[f m
ll . .
h p
O h Table III.E.1. (h)
TYPE "B" TEST SUMSRY k
i
? ~
'i -PEN'T SYSTEM OR PEhETR ATION TOTAL TOTAL, {
4 R E MR KS DATE NO. NA Z ._
l) 4 j 1C60 Electrical I- 21-7 4 9-26-75 0
0 1
to 10 10-20-76
~
1-22-74 0
}4 100A Electrical 9-25-75 0 10 10-20-76 to q
J@ ,
1-22-74 0
~
100C Electrical 9-25-75 0 10 10 20-76 10
, i 1
.i l 1-22 74 0 i 104A Electrical 9-25-75 0 10 10
? l 10 76 l l 1-22-74 0 ]
i' 104B Electrical 9-25-7 5 0 to 10 10-20-76 1-22-74 0
~- 104C Electrical 9- 25-7 5 0 l
10 10 10 20-76 1-22-74 0
' Electrical 0 i 1040 9-25-75 10 10-20-76 10 1-22-74 0 j 105A Electrical 9-25-75 0 i
~
10 20-76 to 10 I-22-74 0 105B Electrical 9-25-75 0 l' 10-20-76 10 to 1-22-7 4 0 106A Electrical 9-25-75 0 10 10 [
10 76 i 1-22 74 0 106B Electrical 9-25-75 0 .
I 10 to 10-20-76 i 1-22-74 0 lf i l 107 Electrical 9 25-75 0 e !
to to 10-20-76 +
I i
(
t I
2, 89
1 Table III.E.1. (i)
TY PE "2" TEST SUMWY SYSTEM 04 PENETRATICN TEST TE ST PE tt 'T PEN'T NO. NAME REMARKS DATE TOTAL TCT A L l'
R 8 220 Electrical 1-22-74 0 9-25-75 0 I
- 10 10 10-20-76 J{
te 1-22-74 0 ij's 101A Electrical 0 9-14-75 10-19-76 10 to i .
101B Electrical 1-22-74 0
~:
1 9-14-75 0 10-19-76 10 10 1-22-74 0 y, 101F Electrical 0 9-14-75 cy j 10-19 76 to 10 y ,
'it t 231A Electrical 2-07-74 175
@i' g
4-15-74 0 5 - 10-19-76 to '
10 I
2318 Electrical 2-04-74 325 k-15-74 0 ,
2- 10-19-76 10 10 j f-? :
Electrical 1-21-74 0 J 10LG 9-26-75 0 l 2if 10 20 76 10 10 l 3li
- 2002 Torus Manway 1-22 74 0 7-11-74 0 y 12-10-7 4 0 ,
3 1-31-76 0 N 5 28-76 0 E( 7-13-76 0
,'? 4-01-77 to 10 a
7 a
i f
I 1
3
]
l
?h M, _
' ' ',if Y 90 l ~t1
9 I
l
^
~ Table III.E.2. (a) l l
)
PEN'T SYSTEM 04 FE NETa ATION REMARK; DATE T OT AL T OT AL C No. Na *I a) 12-01-73 326 7A MsIV 8; A Off Scale
?,1 12-29-76
,y Lapped Valve 12-14-77 1 20 1'
'T.
1-02-74 2173 II MSIV 86A 12-29-76 1540
.jb 1560
.g MsIV 8;B 12-01-73 0 3s 7e 12-29-76 to m# 12-01-73 97 8 l c' MSIV 862 12-26-76 4850 i
^
kB53 1 03-74 B48
$ 7C MSIV 80C 12-26-76 off scale Lamped Valve 2 14-77 85 1% MSIV 86:
4-06-74 316 1240
12-26-76 1240 1 19-74 913 70 MSIV 800
- 12 26-76 Dffscale Lapped Valve 2-I4-77 t00 MSIV 86D 1-19 76 283
, 12-29-76 1520
- 1520 MSL Drain 2-06-74 115 8 0 L 2-01-75 MO 2-74 235 235 12-29-74 M0 2-77 I 1-31-74 200 9a ree water l 1-29-75 380 1-30-76 381 1-18-77 556 556 1-21-74 1200 9B F eeowater 0 1-30-76 1-08-77 Of f Scale 1-21-77 off scale 4200 4200 l r
Lapped 288 f, 96B 2-03-77 !
L i r- .
t I
l
)
($ '
91
Table III.E.O. (b) i TYPE "C" TE ST SJtMAR-<
+ NO. NA *I k 1-09-74 0 9 10 RCIC Steam Supply 2-02-75 127
} MO 13-15,16 5-18-75 1 90 T 2-14-77 8000 5
100 100 Lapped MO-13-15 3-14-77
.}
4 12-05-73 0 g
} 11 MPCI Steam Supply MD 23-15, 16 i-09-74 1 25-75 0
0 y 1-20 -77 off Scale e 2-15-77 60 60 Lapped MO-23-15 12-04-73 0 12 RHR Suction 0 MD-10-17, 18 5-03-74 it 12 19 75 144 400 34 3-18-77 400
- 1-07-74 6 90 f 13A RMR Injecti " 1-02-76 600 MO-258, 1548 '
4 y SV-5222 1 21-76 600 400 400 1-28-77
.3 4 12-10-73 0 13B RHR Injection 2-01-76 0
' MC-10-154 0 B-10-76 SV-5221 12-21-76 to q
]! 200 3-03-77 '
~- MO-25A 200
+
l '
12-31-73 0 ~
14 R 'CU Swetion 0 j MO-12-15, 18 2-02-75 N 1-21-77 10 10 t e
t I t3 Core Spray 12-04-73 37 16A MO-14-11B, SV 5224 1-30-75 Ic6 l Lapped 11B Valve I-21-75 45 3 12 29-76 35 l
10 l MO-14 128 1-23-77 ;
. 35 I
16B Core Spray 400 !
MD-14-11A, SV-5 225 12 11-73 '
Lapped 11 A Valve 2-C I-75 85 12-15-76 Boo .
i MD-14-12A l-25-77 10 l
800 ,
i l
g
- 92 I
l k
Table III.E.2. (c) i
- r. TYPE "C" TEST
SUMMARY
PEN'T SY 3 TEM CR PENETR ATION TE ST TE ST PEN'T l NO. NAME REMARKS DATE TOTAL T CT AL j
17 Head Spray 5-21-74 0
^'
MC-10-32, 33 1-13-76 0 SV-5223 2-14-77 950 950 18 OW Floor Drains 2-06-74 42 AC-20-82, 83 '
1-21-75 110 Lapped valves 2-24-75 39 l-14-77 15 15 19 OW Ecuip. Crains 2-06-74 450 A 0 9*,95 Lapped Valves 1-26-76 0
- 10-21-76 to 10
- 22 Inst . Nitrogen 12-15-73 78
, A0-3 965A
- I-08-76 42 Check valve 2-02-77 75 h 75 I!i; 25 Containrent Purge 2-07-74 200 1
Purge Sucply Valves Replaced Rubber Seat 10-16-74 0 l
i 10-15-75 0 10-23-75 192
, Replaced Rubber Seat 10 l Slow Purge 10-27-75 250 E Check Valves Lapped Torus Check Valve 10-28-76 47 P ,
p Slow Purge Valve 4.18-74 0 B A0-3523 10-28-75 325
{
j 10-28-76 130 l'0
+
26 Orywell Purge 12-14-73 40 Exhaust {
11-11-75 0 i AC-3506, 3507 2-26-76 22 j 9-02-76 35 ,
Drywell CAD. Exnaust I f 12-14-73 140 { i AC-350 9, 3510, 11-07-75 202 '
5235 9-07-76 235 Lepped A0-3509 l-26-77 90 PCAC Sample Rebuilt Valve 1-10-74 95 !
SV-36710 4-01-74 0 B-27-74 0 4-28-75 0 i t 9-02-76 10 1 10 l 2-25-77 i l l
l a
4 9
6 f
r, O
.,.2=
s
.d l Table III.E.2. (d) 4 2 TYPE "C"
SUMMARY
PEN'T SYSTEM CR PENETR ATICN TE ST 2 TE ST PE N 'T NO. N A =I R EMAR KS DATE TOTAL TOTAL d*
Y.
PCAC Samle 4-04-74 200 y sv-39783 Rebuilt valve 8-27-74 40 5-08-75 0
.$ 9-02-76 20
/{ 9-25-77 10 9:
f CAO Sam le SV-596C8/61B/668 5-25-76 to
' ILS
~
f 32C ILRT Test Tao i i 5-22-74 0
,4 5 21-76 0 10-22-76 10 10 fa
,5' 32D ILRT Test Tap 5-22-74 0 M 5-21-76 0 10-22-76 10 10
) 218C ILRT Test Tap 5-22-74 0 s t 5-21-76 38 j 10-22-76 135 135 36 CRD Return 1 22-74 400 Check Viv.13-110 Lapped Valve 2-08-77 10 Check V!v.13-113 6-28-74
'g 30
- 1-13-77 10 10 I
(' 39A Containment Spray
- mo-10 268, 31B 12- 10-73 0
'- 12-19-75 160 ,
Laoped 26B Valve 12-16-76 40 I I
CAO Injection 5-15-76 15 f
SV-5 948A, 49A 55 41 Recirc. Samle 1-04-74 0 A0-2-3 9, 40
- 1-27-75 0 k- 1 04-77 10 10 42 Stand-by Liquid Control 4-22-74 0 W -14A, 148 2-01-75 0 3-11-77 In Check V3v. 11-16 l -0 2-74 0 4-23-74 0 2 01-75 0 3-11-77 to 10 l
n; i .U N
.a
p ,
. I
)
L
.i e Table III.E.2. (e) 9
[ TYPE "C" TEST Sum.vaY
?
,e II
!$ PE N 'T SYSTEM CR PENETRATION
($ NO. TEST TE ST PE rd 'T kame R E MAR KS li, DATE TOTAL TCTAL a
.I 3 35 C ont ain.,e nt Sor ay r0-10-26A, 31A 12-11-73 150 12-19-75 370 "dI l 3-30-77 215 CAD Injection I
10-28-76 80 2 c5 ,
SIS PCAC samole' l f t Sv36710 l-8-74 0 l 4-7-74 0 1
- 4-30-75 0
, 10-19-76 43 .
i' 2 25-77 15 j SV 3978D 1-4-74 0 ll 4-4-74 40 T. i 5-7-75 0
' I 9 2 76 260 il 2-25-77 32 32 .
51 C
- PCAC sample l
SV 3671C i 4-7-74 0 8-24-74 0 i
2-19-75 0 5-2-75 75D Rebuilt valve 7-1-75 80 i
CAD samle I~
SV 5960 C/61C/66C 5-24-76 5 55 i-i SID PCAC samole return !
SV 4980 !
1-8-14 0 1
8-23-74 0 '
5-0-75 0 i 9 9-76 310
, j.
1-22 74 215 !
5-8-75 265 i Lapped Valve ;
3-10-77 20 j
3 10 i l
1 os
f Table III.E.2 (f)
TYPE "C" TEST SWuRY PEN'T SYSTEM OR PEhETRATION NO. NAMI TE ST TE ST PE N 'T
- REMARKS DATE
- TOTAL TCTAL SIA pggg 3*"PI' SV-3671 E Rebuilt Valve l-08 7 200 4-07-74 0 8-24 74 0 l 4-30-75 10-20-76 0
5 4
a
- 2 25-77 38 SV-3 978E
/
~
l-04-74 0 4-04-74 0 5-08-75 0 9-02 76 0 .
2-25 77 10 38 52F Inst. Nitrogen AC-3 969B 12-14-73 0 '
I 1 20-76 0 -
2-04-77 20 '
! Check valve Lamped Val" 2-02-74 925 )
I-20-76 0 j
2-04-77 25 e 25 57 Main Steam Sample A0-316- 317 3.c4,74 g ,
12-08-74 0
- i l-04-75 0 ,
i 12-30-76 25 25 ..
g 203 PCAC Sarnple -
4 g SV-36718 4-07-74 0 .
4-28-75 0 '
12-10-75 0 I-9-22-76 18 2-25-77 10 f
SV-3978s 4-05-74 0 5-07-75 0
, 8 31-76 48 i 2-25-77 55 CAO Suple SV-59600, 610, 660 5-24-76 to 65 '
205A Torus Vac areaker ,_
A0-35028 & VRV 9-268 1-18-74 30 f
' l-11-76 0 i 11-03-76 20 20 '
i 1
l t
t i
s 96
s i
1:
Table III.E.2. (g)
SUMMARY
a 5
$, PEN'T SYSTEM CR PENETRATION NO. TEST
} NA =E REMARKS TE ST PE N 'T DATE TOTAL TOTAL 205B Torus vac Breaker h A0-3502A t, vav 9-26A Replaced vav seal 2-02-74 240 t 1-15-76 65 F 11-02-76 10 10 h 211A Torus Spray t MO 34,33,399 1-26-74 200 g Lapped MO-398 1-26-76
. 25
- v. 12-29-76 L80 CAO Injection SV-5 95c s , 5951B 5-22-76 25 505 211B Torus Spray M0-10-34,38,3 94 1-30-74 50 -
1-27-76 210 j Lapped MO-3SA 12.20-76 off scale N 4-04-77 1425 y
CAO Injection sv-5 950A, 5951 A 5-20-76 20 I445 4 212 RCIC Exhawst 7 13-9. 50 1 21-74 50
'. I-08-76 475 -
.A 2-01-77 270
,1 Lapped 13-9 2-16-77 185*
AC-5240, 41 1-26-74 0 9-19-75 20 12-28-76 10 13-9 "0" R ing 1-0 N .6 M 20 5 4
214 NPCI Exhaust 23-12, 65 2-02-74 80 1-20-76 0 -
Lapped Both Valves 1-15-77 Off scale 2 15-77 to '
AC-5247, 48 1-22-74 0 1-13-76 0 12-29-76 off scale 2-22-77 450 23-12 "0" Ring ,
1-12-76 10 470 1
e e'
_ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - - - - - - - - ' - ' ~
I Table III.E.2. (h)
TYPE "C" TEST
SUMMARY
(
i
)
l PEN'T SYSTEM CR PENETRATICN l i
NO. MAKE TE ST TE ST ped'T REMAR KS DATE TOTAL TCTAL 217B MPCI Vac Breaker MC-5245 B-20-74 0 1-09-76 50 i 2-14-77 2000 g RCIC Vac Breaker E .
M0-5244 Lapped Manual Valve 5-02-74 250 t 8-30-74 40 h, 1-14-76 52 2-14-77 240 2240 21EA Inst. Nitrogen A0-3968 Lapped valve 1-30-74 100 6
1-29-75 0 L l-31-77 Off Scale I.
7 2-22-77 360 ,
,) Check Valve Lapsed valve 2-04-74 0 Laoped Valve 2-02-76 475 +
1-31-77 Off Scale 1 2-22-77 10 '
360 2188 PCAC Sample t SV-3671A 4 03-74 0 9-28-75 0 '
9-07-76 Of f scale
" Rebuilt valve 9-15-76 Rebuilt Valve 1700 .
9-22-76 10 SV-3 978 4-05-74 0 '
5-07-75 0 i 8-31-76 Of f Scale "
9-15-76 1700 !,
9 22-76 0 i-2 25-77 to !
10 219 T orus Exhaust A0-3511, 12 2-06-74 40 .
10-17-75 0 12-16-75 0
(
9-09-76 220 CAO Exhaust AC-3513, 14 2-02-74 28 !
11-14-75 0 i Lapped Valves 9-10-76 off scale i 3-11-77 1510 t,
i l i
I. k' t
I, i e
i l !
.c
t !
g l
Table III.E.2. (i)
TYPE "C" TEST
SUMMARY
FEN'T SYSTEM OR PENETR ATION TEST TEST PEN'T NO. NAME REMARKS DATE TOTAL TCTAL PC AC S amo le 2-04-77 225 SV-3671F Rebuilt Valve 8-27-74 0 4-30-75 0 10-21-76 0 2 25-77 10 Sv-3978F ' 2 7+ 0 _
i 4-03-74 0 8 27-74 0 5-08-75 0 9-02-76 0 2 25-77 to CAD Sample '
l SV-5960A, 61 A, 66A 5-25-76 10 1750 221 R CIC Vac Pui o 1-14 74 90 ,
1 Disenerge 1-13-76 50 13-10, 3B 12-29-76 250 250 ,
223 HPCI Exhaast Drain 12-13-73 310 23-13, 56 8-07-75 100 12-29 76 225 225 t 225 R C IC ' Sue ti on 2-01-74 0 {,
MO-13-3 9, 41 5-21-74 90 -
l 1-29-75 60 ;
l-14-77 off Scale !
2-11-77 50 I Torus Clean-Up 12-26-73 0 M0-14-70,71 i 7-18-75 190 +
9-01-76 10 l' 60 1 227 HPCI Suction 1-26-7 4 275 M0-23-37,58 4-08-74 0 1-30-75 0 i 1-18-77 Off Scale !
3-21-77 135 135 TC 'AL B fr C TESTS 20,290 6C' ; La CRITERIA 71,13( '
t 1
i i
l I
99 ',
_ . . .. . . . . . . . . . . . . . . _ . . . . _ a
APPENDIX A 0
E BECHTEL ILRT COMPUTER PROGRAM ;
DESCRIPTION A. The Contain=ent Integrated Leakage Rate Test (ILRT) Program calculates the leakage rate for a nuclear reactor contain=ent vessel. The program computes the leakage rate at a given time from input values of absolute pressure, drybulb temperature and dewpoint te=perature (water vapor pressure). Leakage rate is calculated by the Absolute Method as defined in ANSI N45.4-1972, " Leakage Rate Testing of Containment Structures for Nuclear Reactors".
B. The Containment Integrated Leakage Rate Test Program is designed to allow the user to evaluate containment leakage rate test results at the jobsite during containment leakage s rate testing. Interim leakage rate test reports may be obtained at any time during the testing period. Each interim j report can provide three prir.couts. The first printout, called the Total-Time Method, uses the initial and latest f input data to compute leakage rate s Each computed leakage rate is statistically averaged using a linear least-squares fit.
j C. The second printout is the Trend Report. This report is a ,
trend of Total-Time Method calculations and gives a more concise and. timely description of test results. In this printout the leakage rate is reported as a function of test -
duration. F
. D. The third printout, called the Mass Point Method, uses data at a given time and computes the mass of air within the contaic-ment. Each individually computed mass of air is statistically 3
i ~-
fit to a straight line using a linear least-squares fit. The .
, slope of the straight line is the leakage rate. The Mass - n Point Method is a recommended method in the ANS N274 draft ,
1
- standard which is being prepared to supercede ANSI N45.4. ,
i l'
E. The test results indicate that both methods are satisfactory ,
for computing containment integrated leakage rates. However, ;
the Total-Time Method is recommended by Appendix J to 10 CFR 50 r C
and is used, therefore, to report the containment leakage f ^!
rate.
!. E:JLANATION OF PROGRAM t:
A. The Containment Integrated Leakage Rate Program computes con- ,l tainment leakage rate using the Absolute Method given in
, !j
~
i< ANSI N45.4-1972, " Leakage Rate Testing of Containment Struc- -
E tures for Nuclear Reactors". ,
n .
f
'l
?1 i
A-1 .
.. , . -- ?--
- F i
- B. Prior to the start of the test basic data is entered, which consists of:
(1) Number of containment drybulb temperature points, dew-point temperature (vapor pressure) points and absolute pressure points, j
(2) Volume fractions assigned to each sensor.
(3) Calibration data, conversion factors, etc. I At the start of the test the following information is inserted
- t (1) Test title.
- l i
j (2) Test pressure. "
~
t f
4 (3) Maximum allowable leakage rate at peak test pressure. '
I (4) Containment free air volume.t '
, (5) Verification test imposed leakage rate.* .
} C. The recorded data, which is used to compute the leakage rate, t l is then entered. Recorded data consists of: ~ '
(1) Containment atmosphere drybulb temperature.
(2) ConEainment atmosphere absolute pressure.
O t' (3) Containment atmosphere dewpoint temperature.
(4) Containment free air volume S.
5 i
D. -Drybulb temperature, absolute pressure and dewpoint temperature ;-
f (water vapor pressure) values are entered as read from the L data sheets, 1Ee., each drybulb and dewpoint temperature is !-
]i entered in 'F and pressure is entered in counts. After all data for a given time step is entered, a printout Summary or the
, Measured Data is provided.
} ' E. If a drybulb temperature or dewpoint temperature (vapor pressure) !.
t sensor becomes inoperable during the course of the test, the t-sensor is eliminated and volume fractions recomputed. The nev
, volume fr, actions are then entered in the computer program of-j -
the' leakage rate computations.
i .
[
{or verification test and Mass Point Method only. .
or, varification test only. ,
f Iantainment free' air volume is changing (due to water level,chan'ges, p or exsuple) . ,
8
% g- '
.kW# 'x #
8.
~
.. / E
, ., r -
. n~
_v, _ _ . . _ _ _ _ _ . , _ _ . _ _ . . , , - - - _ . - _ _ , . __ .._ .. - . - , - -
j - -
,r, l ,
[ 7. In the Summary of the M2asured Data, each temperature entry is
, printed out in *F as entered. Each dewpoint temperature entry
- is corrected based on calibration data and on standard con-d version factors. Dewpoint temperature is printed out in *F as L entered, in *F corrected by calibration data, and in the l equivalent water vapor pressure in psia. Pressure is printed out in counts as entered and in psia as corrected by calibra- 4 tion data,
?
,t
. i
! G. At this point the user is given an opportunity to check the data and correct any errors. Following any corrections, if j !~
required, a Corrected Data Summary is printed out. This l summary consists of the date, time, one weighted average j containment drybulb temperature and one average containment a air pressure (corrected for water vapor pressure and water
} vapor pressure volume fractions). These corrected values of 3 temperat.ure and pressure are the values used in the contain- ,
mint leakage rate computations. Free air volume changes, if
[
f applicable, are recorded on the data file for use in the '
f leakage rate computations.
I I COMPUTATIONS 7 (A.
g Total-Time 1
- 1. The leakage rate is computed as follows: .
1,:
'5 E PV WyRTy (1) y7 r ,
(2)
PY2 2 " w 2RT2
~
w_w
% leakage , E 1 2 (100) (3) ! -
24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> t W 1
_. .[
Solving for W y and and substituting equations (1) and (2) into (3) yields.2 ,.
y 122 L = 2400 at 1
TPV (variable free air volume) -
2y l\
TPy2 L " 2400 gg 1 (constant free air volume) 'l TP 1
. 21 (
b E A-3
u-- . -
1
. . . 4.
i
. 4 6
l Where:
i Wi ,W 9 = Weight of containment air at time yt and t 7,
- ~ ,
- respectively. [
T y,T2 = Absolute temperature of containment volume at time tyand t2, respectively.
P ,P = Absolute containment air pressure (corrected for 2
water vapor pressure) at time yt and t 2' ;
respectively. t V ,V 2
= Containment internal free air volume at time ty and t2, respectively.
l At = t 2
~# 1, in hours. ._
L = Leakage rate (percent / day) .
[
R = Gas Constant (assumed constant). . -
- 2. Linear least-squares fitting is used to establish the value '
of leakage rate at any hour. The leakage rate as a linear function of time is: ,
I,
= y a + bt (4)
Where :' .
IL 1It g
- It gIt g1 L nit - (It )
NELggt - L gItg
! b =
2 nit -
(It )2 i L = Calculated leakage rate from equation (4) above at ,
cf.me t . j, N = Number of leakage rate calculations. i '
l-N I = I l
i=1 l
1 w - , , - - , - . . , - , , - - - - , - - - ,
t Where:
W ,W = Weight of containment air at time ty and t y 2 2' respectively.
T ,T 1 2
= solute temperature of containment volume at time t and t2, respectively.
P y,P2 = Absolute containment air pressure (corrected for f water vapor pressure) at time ty and t 2'
respectively.
V ,V = Containment internal free air volume at time t y 2
and t2, respectively. ,
- at = t 2
-t l, in hours. .
i 1 L = Leakage rate (percent / day) . [
R =
Gas Constant (assumed constant).
j 2. Linear least-squares fitting is used to establish the value !'
a of leakage rate at any hour. The leakage rate as a linear function of time is:
( L =i. a + bt ,
(4) r .
Where :'
2 ELgEtt - It gItggL
! a = .)
1 NZt[ - (It ) 2 -
NEL t -
L gEtg 2
nit -
(It g)2 ,
Lg = Calculated leakage rate from equation (4) above at ;
time t y.
N = Number of leakage rate calculations. -
s N
I = E i=1 .
4 i
t
' l A_4
i> l i
- 3. Considsring confidenes limits:
l
~
~
~
-2 2 1 p i~ i S = 1 + ;s=
+t0.025(s) 37 + I(tg-t)2 N-2 It t N t = Percentage point of the students-t distribution 0.025 at the 95% confidence level.
Formalizing the standard t-distribution table yields:
t = 1.96 + 2.37 ,2.82 0.025 N-2 (N-2) t = test duration -
P 1
~
and .
L g'5 Li i8 m
, l' .
B. Mass-Point Method
- 1. The leakage rate is computed as follows:
+
PV g
N " 144 i RT -
1
- 2. Linear least squares fitting: ,
W = b + mt (EW g )(Itg ) - (It W gg )(Ecg ) ! ,,
b = t-N(Itg) -
(Et )2 N(It Wg ) -
(IW )(Itf) - !
N(It ) -
(Et } )
i A-5 i
k, 3 lt
- N t L
1,
= { (2400)
? ,'
i 4 i
- 3. Considering confidence limits: l
) ~
l I(Wi-W 1 )2
! W2 S
m
-+c 0.025 g(g )2 and 2400 L "
(*I8) 95 b m
! i-Where: !
ti g = Mass of contained air at time t g. [
! Tg = Absolute temperature of containment atmosphere at '
- time t g.
P g
= Absolute pressure of containment atmosphere air at ,
time t g.
R = Gas constant for air. - -
l V = Containment internal free air volume. !
1 tg r= Time, in hours. j l
i ,
,' L 95
=. Leakage rate, percent / day at the 95% confidence j
- level.
W = Regression line value of mass of contained air at time t g. -
j D. Program Logic ,
- 1. The general flow of user's decisions for the Bechtel Time l Share System ILRT_ program is shown in the flow chart in
~
Figure A-1, Page A-8.
~ ~ '
l 2. Initially, the basic data (see paragraph II.B of page A 2) ~
is supplied to the system. After entering the basic ---
(
l data, values of drybulb temperature, absolute pressure, i dewpoint temperature, and containment free air volume (if l i changing) for each data set are entered. The Temperature !
( and Pressure Corrected Data Summary is then computed for each data set and this information is stored on a -
file. Therefore, when restarting the program it is -
l l
A-G
possible to enter averaged values of temperature and pressure from previous runs frem a stored file. After entry of data the user may select one of the following options: j Option !
Co =end Function I DATA Enables operator to enter additional raw data. When the system requests values of time, drybulb tempera-ture, pressure, dewpoint temperature (vapor pressure),
and free air volume (if applicable) the user enters '
data as directed by the program. After completing the data entry, a summary is printed out for the user's verification of data correctness. If there -
are errors detected, the user will be given the opportunity to correct the errors. After the user ,_
certifies that the data as entered is correct, a ~
Corrected Data Summary Report is printed.
TREND Terminal vill print out a Trend Report.
4 TOTAL Terminal will print out a Total-Time Report. ,
. [
- MASS "-
Terminal vill print out a Mass Point Report.
i , ,
j TERM Enables operator to sign-off temporarily or permanently.
' U ,
SAVE Enables operator to store the Temperature and ,
- Pressure Corrected Data Summary on a file thereby !
updating the previous file automatically. -
^
LIST When used with a given file name, the printer will print out a listing of the Corrected Summary Data stored on the file. ~
k r.
1 l .
l I n.
4 A-7
(SIGNON) l l
\
w 1
\ ENTER BASIC /
\INFORMATION/' NO / ENTERPREVIOUSh ,'
\ VALUES FROM FILE 7/
g YES (OPTIONSr j , i o
n i ,
(UiTERDATA> DATA * '
STORES CORRECTED u <- SAVE r
SUMMARY
DATA IN (ERROR 7)
PREVIOUS FILE -
YES W
<- 1 REND =j f' ER , TREND REPORT s / NO
\ CORRECTIONS /
o <
- TOTAL = TOTAL-TIME -
j '
( _
SUMMARY
OF REPORT
~
i '
RMEASURED DATA
.. 'V 1
i- MASS MASS POINT l 1
v REPORT I (ERROR 7)' l
- YES l' -
NO '
COREIG1w '
. 1 i
SUMMARY
DATA PRINTOUT ,
- TERM :(SIGNOFF) -
e .8 Y $.':_
i- i CONTAINMENT INTEGRATED LEAKAGE RATE TEST PROCEDURE l
i COMPUTER PROGRAM LOGIC DIAGRAM i
- 1 FigureA_1 l
i I'
l t
i ,
l I
A-8 i
~ v.,e, .,dihV v 27 -
o 2.@-@g g VJ93
- niff PHILADELPH!A ELECTRIC COMPANY usy
[jV 2301 MARKET STREET P.O. BOX 8699 P Hl' EA.D v . E,LP H IK P. . A. ',1.91Q1 (2151841-4000 June 23, 1977 "e*
D
~ %he t *"'8
~~
Regulatory Docket Fih g, _,, % .
- 'r. doon G. Ca r:.e
- QWWif .'y s \
/.c:*n~, Director Offire of Nuclear Leactor T.cgulaticn
/ (h a s< / b j ,g' p \
States Nuclecr Pe ;ulaterv Co=sicsion Ur.it e '?
l 8- 1 C ,
Unshin-ton, D. C. 20555 '
'.- 4 "
- y*
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' f SUIG CT: Feach Botto:n Unit 3 Eeactor Contain::wtnt Building Integrate'd ~ ~
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Lenk Rate Test Report -
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This letter accenpnnics 15 copies of the Reactor Containnent Building Integrated Lenk Rate Test T.eport for Peach Bottom Unit 3, pur -
cuant to Operating License DrR - 56 Thic rc'po rt is beine, submitted in coc.pliance with Section -- -
4.7.A.2 of the Tecimical Specifications of Appondix A to DPR-56 and Apendi: J to 10 CFR 30.
Very truly yours,
~ ~ ' ' '
' ~ ~ ~ ~ ~ ~ ~
W. M. Alden
' Engineer-In-Charge _. _ _ _
~ Nuclear ~Section . . _
L n . _ _ _ . _
~ ' Generation Division ---
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1 cc: Mr. William G. Mcdonald ~~~"
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Offica of Management Information and '
~~~7 3 Program Control ' "
! U.S. Nuclear Regulatory Co: nission --- -~
s .,ashington, DC 20555 - -
p vith enclosure (1 copies)
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