ML18227D919
| ML18227D919 | |
| Person / Time | |
|---|---|
| Site: | Turkey Point  |
| Issue date: | 02/14/1976 |
| From: | Roman W Ebasco Services, Florida Power & Light Co |
| To: | Office of Nuclear Reactor Regulation |
| References | |
| Download: ML18227D919 (274) | |
Text
FLORIDA POWER & LIGHT COMPANY TURKEY POINT NUCLEAR POWER PLANT UNIT NO. 3 REACTOR CONTAINi~IENT BUILDING INTEGRATED LEAK RATE TEST
SUMMARY
TECHNICAL REPORT Prepared for".
FLORIDA POMER & LIGHT COMPANY
.Prepared by:
. William D. Roman EBASCO SERVICES INCORPORATED Plant Operations & Betterment Department FebrUary 14, 1976 h II I
IV I h h I P 3 I, 3 I e
llh I 33h'v I hkv I'
TABLE OF CONTENTS X. INTRODUCTION............................. ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 1 II ~ S Pru'fA RY ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 2 IXX. TEST DISCUSSION A. Descrip tion o f Containment......................... 3 B, Descrip tion o f Xns trumen ta tion........ ~ ~ ~ ~ ~ ~ ~ ~ 0 ~ 5
- 1. Temperature Xns trumentation. ~ ~ ~ ~ ~ 6
- 2. Humidity Instrumentation.... ~ e ~ ~ ~ 6
- 3. Pressure Instrumentation.... ~ ~ ~ ~ e6
- 4. Numatron (Digital Voltmeter) ~ ~ ~ ~ ~ 6 C. Description of Computer Program. ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 0 7 D, Error Analysis.................. ~ ~ ~ ~ ~ 8 E. Description of Tests............ ~ ~ ~ ~ ~ ~ t ~ ~ t ~ ~ ~ ~ ~ ~ ~ ~ ~ 8 IV. RESULTS AND VER'IFICATION....... ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 11 V. CONCLUS XONS ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 12 VI. F XGURES ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ t~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ ~ 14 APPENDICES A. Computer - Generated Report
- 1. Integrated Leak Rate Test (XLRT)
- 2. Controlled Leak Rate Test (CLRT)
B. Operating Procedure No. 13100.1 Integrated Leak Rate Test
- l. Ram Data
- 2. Test Log C. Periodic Type B and Type C Test Reports
I. INTRODUCTION A periodic Type A integrated leakage rate test was performed on the containment structure of the Plorida Power & Light: Company, Turkey Point Nuclear Power Plant - Unit No. 3 pressurized water reactor in November and December of 1975 utilizing the "Absolute Method" of testing.
This test was performed at the reduced pressure test (Pt) which is defined r
as not less than 50% of the calculated peak accident pressure.
This report describes and presents the results of this periodic Type A leakage rate test including the supplemental test method'tilized for verification.
All Type "B" and "C" tests were satisfactorily performed and repairs and corrections were made where necessary. At the start of the test, all valves were to be in their normal position for accident conditions. Excep-tions to this valve lineup were noted during this test and are listed in Appendix B. The measured total-time simple leakage rate was 0.040%lday at 41.89 psia (total containment pressure at start of test). The measured total-time least squares statistical fit leakage rate was 0.058%/day at 41.89 psia.
IIX. TEST DISCUSSION A. Descri tion of Containment The containment structure completely encloses the reactor coolant system and provides adequate biological shielding for both normal and hypothetical accident conditions. The structure is a post-tensioned reinforced concrete cylinder with a shallow dome and is connected to and supported by a reinforced concrete foundation slab. The inside surface of the structure is lined with >" thick welded steel plate to insure a high degree of leak tightness.
Principal dimensions of the containment structure are .as follows:
Inside
à diameter..........................ll6 feet Xnside height.................... . ..169 ieet (including dome but excluding reactor cavity)
Xnside depth of reactor cavity...........29 feet 8 inches Vertical wall thickness...................3 feet 9 inches Dome thickness...........................3 feet 3 inches Foundation slab thickness................10 feet 6 inches Xntexnal free volume....... ....... ....1,550,000 cubic feet Access to the interior of the containment structure is through a personnel lock located on the west side, at an elevation of 25'-10". An emergency escape lock is located on the east side at elevation 52'-9".
A 3.4'-0" diameter equipment hatch is located on the north side at eleva-tion 30'-6".
The interior of the containment consists of three levels; base floor at elevation 14'-0", mezzanine floor at elevation 30'-6", and operating floor at elevation 58'-0". Two stairways and an elevator have been provided in the containment with landings at elevations 17'i'~ 25il0"~ 58'10" and 73<8"
The polar crane can be reached via a stairway to the top of the elevator shaft, and then a ladder to the platform at elevation 113'-10".
A stai.rway is pxovided irom the personnel access platform to the base floor and from the emergency escape lock to the operating floor.
A ladder access is also available from the base floor to the emexgency escape platform at 52'-9".
The reactor vessel is located in the reactor cavity at the center of the containment. The three primary coolant loops including the steam generatoxs and the pumps are located in separate compartments around the reactor vessel. The primary shield wall (7'-0" thick and circular in shape) and the secondary shield walls (2'-6" thick) form boundaries of the com-partmerits and also provide radiation shielding. The mezzanine floor is a 2'-6" thick slab and'the operating floor is 2'-6" thick slab. On the
~
'eriphexy of the operating floor there is a galvanized steel grating plat-form which supports the containment noxmal and emergency coolers and filters and permits air circulation and flow path for water from the containment sprays.
The reactor refueling canal to the east of the reactor cavity is lined with a stainless steel plate. A stainless steel ring seals the reactor cavity during refueling. The canal walls are of reinforced concrete con-struction and extend from elevation 18'-0" to the operating floor at 58'-0".
The canal is illuminated by underwater lights and contains the reactor in-ternals storage stands, refueling tool racks, 'control rod unlatching tools and fuel'ransfer tube and mechanism. During refueling, the canal is filled with borated water which provides shielding and cooling for the spent fuel elements. The reactor refueling crane (manipulator crane) spans across the canal and travels longitudinally over rail tracks.
The reactor vessel is supported on its six nozzels, each of which sits on three structuxal steel beams cantilevering from the primary shield wall into the xeactor cavity. The steam generators and pumps axe supported on r
columns and embedded plates and anchor bolts. The'supports allow thermal growth but restrain the equipment during earthquakes or pipe rupture.
The polar crane supported on structural steel brackets at elevation 125'-9" with a capacity of 135T/35T services the reactor building during refueling and maintenance operations.
There are eighteen (18) dome trusses which weze designed to support the dome liner during constxuction. These trusses were then lowered and tied to the supporting brackets. They carry'he hangers for the containment spray piping.
=B. Descri tion of Instrumentation The containment system was equipped with instrumentation to permit leakage rate determination by the "Absolute Method". Utilizing this method, the actual mass of dry air within the containment is calculated.
The leakage rate becomes the time rate of change of this value. The mass of air (Q) is calculated according to the Perfect Gas Law as follows (reference Section 3.1.2 of Appendix B for additional information):
Q =PaV RT where: Pa = air partial pressure V = free volume R ~ gas constant T = temperature The parameters required are temperature, humidity and pressure. The location of the instrumentation is shown in Figures 1 and 2.
- 1. Tem erature Instrumentation The containment was equipped with 20 precision RTD's plus a
2 .spares.
The accuracy of these detectors is within + 0.2F. The maximum probable temperature error is equivalent to + 0.054F.
- 2. Humidit Instrumentation The, containment was equipped with 6 RHD's plus 2 spares. The accuracy of these detectors is + 2.5% relative humidity for a 0-100% relative humidity excursion. The maximum probable humidity error is equivalent to + 0.296%.
- 3. Pressure Instrumentation The containment was equipped with 01 precision readout unit plus 01 spare with a calibration accuracy of 0.015% of reading, resolution of 0.001%
of full scale and readout of 100,000 counts = full scale. The absolute pressure capsule had a range of 0-49 psi. The maximum probable pressure loop error is equivalent to + 0.001 psia.
- 4. Nvmatroa Di ital Volt~meter a
A L&N digital voltmeter (Numatron) was utilized to obtain direct readout humidity data. This instrument has an accuracy of + 0.01 millivolt which is insignificant.
Consequently, the maximum probable total instrument loop error is equi-valent to + 0.015% per day at a confidence level of 99.87%.
Additional information concerning all the above instrumentation may be found in section 5.1 oi Appendix 3.
C. ~Dcscri tiou oE Com uter Pro rcm Throughout the test, temperatures, humidities and pressure were monitored. These data were used to compute-the leak rate from the perfect gas law using either the point-to-point or total-time method. Leak rate predictions and estimates of error were provided by first order linear regression over the test duration of 24 hours. Furthermore,the sensitivity to sensor accuracy was computed to demonstrate that the test had met the minimum allowable leakage rates within statistical error bounds.
All data vere manually entered using a Texas Instrument 700 terminal at 15 minute intervals. A weighted average temperature was computed according to the fraction of the total free containment volume each RTD sensed. A weighted average partial pressure was also computed according to the fraction oi the total free containment volume each RHD sensed by utilizing "built-in" computer saturation tables. Data were verified by xequesting a tabular listing with actual sensor values and other computed values listed in tables or plotted as requested. At 2030 12-2-75, RTD $N was deleted as a result of this sensor malfunctioning. When r
this sensor was deleted, the volumetric fraction was updated by the computer and future calculations deleted this sensor. As a result, it was no longer necessary to input a value for this deleted instrument.
Information on the progress of the test was retrieved and listed in tables or graphical form upon request. Raw sensor data and computed variables, such as simple leak rates, average temperatures, vapor pressures, point-to-point, and total-time statistical leak rates were evaluated in these forms. Appendix A contains graphs of major variables, statistical and simple leak rate results, instrument error analysis, tabular listings "7-
of both major variables and raw input data, and certain appropriate notes which fully describe the ILRT and CLRT.
It should also be noted that this program has been verified extensively with and against previously performed ILRT's as well as concurrently, during actual test performance, by utilizing a desk calculator. All data have been in exact agreement.
D. Error Anal sis Although maximum instrument loop errors are determined prior to the ILRT to ensure the reliability of the measured data, the effect of instrument in-accuracies is computed following the ILRT and CLRT to reflect actual test conditions. Total instrument error reported is established by the likelihood that additive errors will not exceed 95% confidence limits. Contribution to the reported instrument error is an additive function of the loop errors for temperature, humidity and pressure sensors, and the initial test average variables for the first set of data recorded by either the ILRT or CLRT. In addition, a statistical measure of the goodness of fit of the first order regression is reported as a function of test duration in particular, this provides regression errors which diminish significantly as the amount of collected data increases.
E. Descri tion of Tests Interpretation and final analysis of test data show results well within the speciiied limits for this containment as delineated in section V of this report.
The containment was made ready for the integrated leak rate test with pressurization commencing at 2150 11-28-75 following final inspection and "correction" of relative humidity detector (RHD) problems encountered.
Pressurization was accomplished by utilizing seven (7) mobile oil-free air compressors with a total capacity of 6750 scfm. These units were connected to the containment as shown in Figure 3. Additional information concerning this equipment may be found in section 5.7 of Appendix B. At 0455 11-29-75 at approximately 41.47 psia pressurization was secured with data acquisition commencing at 0515. However, due to malfunctioning RHD's and excessive leakage, the ILRT was aborted at 1845. During the test period, foux (4)
RHDs had to be deleted with numerous leaks detected and repaired. At 0028 11-30-75, containment blowdown to atmosphere commenced following contain-ment air sampling. This sampling (utilizing a Tracerlab Model MD-12C beta-gamma GM tube and Eberline Model AMS-2 detectors) was continuous during this period. No detectable gaseous or particulate activity was observed. At 1030 the containment was at atmospheric pressure. An in-spection team then entered following satisfactory containment atmosphere air sampling.
During the following period, minor leaks were repaired where previously observed or suspected as well as re-verification of the valve line-up. The containment inspection revealed FT-474 on the steam line from "A" steam generator was removed with all associated valves in their open position, steam line high point vent on "C" steam generator was open with an empty packing gland and the level indicator and all associated vents open to containment. These discrepancies were corrected.
'Evaluation of the RHD problem indicated that the system was mal-functioning with no repeatability. As a result, a "new" RHD system was obtained from the St. Lucie Nuclear Plant who recently completed a preoperational XLRT. These sensors were then installed in the same
location as the previously discussed instruments and the system was function-4 ally tested. Upon achieving satisfactory results, pressurization again commenced at 0923 12-1-75 following containment inspection at 0810. At 1620 at approximately 42.55 psia, pressurization was secured with data acquisition commencing at 1630. Leak survey teams were then instituted with leaks de-tected and repaired in the ILRT panel sensing lines and associated instru-ment valves. Time zero was established as 0900 12-2-75 following a 16.5 hour5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> stabilization period. The ILRT was successfully completed at 0900 12-3-75 followed by a 4.5 hour5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> CLRT at an average flow rate of 3.4 scfm.
4 This discharge was also monitored with no detectable gaseous or particulate activity observed, At 1330 the CLRT was satisfactorily completed with blowdown commencing at 1449. Continuous monitoring during blowdown again revealed no detectable gaseous or particulate activities (see Appendix'B-Test Log) with atmosphcr" c prcssur achieved at 0116 1?-'4-75. Following satisfactory containment air sampling, an internal inspection was performed from 0149 to 0228 with no discrepancies observed.
Prior to performing the ILRT, a Local Leakage Rate Test (LLRT) was per-formed by Florida Power & Light personnel to verify" containment integrity.
Type B and C local leakage rate tests were performed on containment electrical penetrations, mechanical penetrations, piping system isolation valves which become part of the containment boundary under accident conditions, the fuel transfer tube, the personnel access lock, the emergency escape lock, and the equipment hatch. The acceptance criteria for this LLRT is that the total leakage from all local leakage rate tests shall not exceed 60/ of the maximum allowable leakage (La) at test conditions. The total leakage from these Type B and C tests was within these limits and is presented in Appendix C.
IV. RESULTS AND VERIFICATION The reduced pressure test (Pt) was conducted for a period of 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> starting at 41.89 psia with a total of 97 samples or data sets taken. This test followed a stabilization period of approximately 16.5 hours5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br />. The re-suits of a computed total-time least squares statistical fit of all data revealed a leakage rate of 0.058%/day by weight or a total-time simple leakage rate of 0,040%/day by weight. For the purposes of this test, the total-time simple leakage rate shall be utilized due to comparison to the CLRT data which are of much shorter duration. Since the least squares statistical fit of the first order regression is a function of test dura-tion, the regression errors during the CLRT are high. Consequently', for comparison during the verification phase, the total-time simple leakage rate shall be u 'ilized. This leakage rate corresponds to an initial con-tainment air weight of 318,834.2 pounds and a final containment air weight of 318,704.3 pounds or a loss of 129.9 pounds. tfaximum probable instrument error for this test contributes + 0.015%/day.
Following satisfactory completion of the ILRT at Pt,' 4.5 hour5.787037e-5 days <br />0.00139 hours <br />8.267196e-6 weeks <br />1.9025e-6 months <br /> veri-fication test or CLRT was performed. This tes't'was conducted by super-imposing a known lealc of 3.37 scfm at 39.696 psia which corresponds to a leakage rate of 0.123%/day by weight. Consequently, Ltm plus the super-imposed leak equal 0.163%/day by weight. The measured total=time,simple leak was 0.144%/day by weight (0.027 x 24 hrs. = 0.144, reference Appendix 4.50 h'rs A, section 2). This corresponds to an initial containment air weight of 318,709.3 pounds and a final containment air weight of 318,624.2 pounds or a loss of 85.1 pounds. Maximum probable instrument error for this test contributes + 0.015%/day.
V. CONCLUSIONS The 25.0 psig integrated leakage rate test provided acceptable results as evidenced by the computer printout and graphs in Appendix A of this report. These leakage rates are well within the specified limits. These limits are as follows:
- 1. The maximum design leakage rate (La) shall not exceed 0.25%/day.
- 2. The maximum allowable reduced pressure leakage rate (Lt) shall be the lesser of:
Lt = La Ltm or Lt = La Pt 1/2 Lam where, L = measured leakage rate Pt =- retest pressure, 25.0 psig Pa'= peak accident pressure, 50.0 psig
- 3. The maximum allowable operational leak rate (Lto) shall not exceed 0.75 Lt.
Preoperational test have provided the following results:
"
- 1. Lt = 0.0667
'. L~= 0.1020 As a result, Lt shall be equal to the lesser of:
- 1. Lt =La Ltm = 0,25 0.0667 = 0.1635 Lam 0.1020
- 2. Lt =La Pt 1/2 = 0.25 25.0 1/2 = 0.1768 50.0
In this case, since Ltm ~ 0.6539 or ~0.70, Lt =-
La Ltm = 0.1635 Lam ~ Lam As a result, for future periodic testing at the reduced test pressure:
Ltm < 0.75 Lt = 0.75 (0.1635) = 0.123%/day by weight.
The verification tests discussed in section IV contain the test results and 'verify the accuracy of the ILRT measurement system. The close correlation between the ILRT and supplemental test. provides sufficient data to validate the ILRT results. ~ The minor difierences between'these tests and the ILRT results are attributed to rotameter accuracy which is + 1.0% of full scale or less than the accuracy of the ILRT measurement system,
7LMP.: I)=VI.
- QDICA7OI CELL LQC ATIlohL RTC- I PHD-7 IOF O~ C~hi' RTD PAD Ii N ~ N IR7D <'-:C-'L IO'9 CP 6 V. GRh!.
%70-'L I. I\ II R
'Z7D- 5
'
II.I D- 4 2l ZT D
'QQ ZID & ~
/ . lu &.Oo Zl D 7 ZTD-6 zI D 9
.Ob 3 OG ZaD IO ZHD d TERY C A CC"V,.
2 IXI22 Z7D- ll
. 271 ?)=Tie.'=W 2 O4 r
~
'
H'." 2iD I I'TD-I j
Zilch -v L'MIlWZ 'C F
H..~&.OOI Zi0 - I5 ~M & M.
- "EL'. 'B IRI.OO.I El .&3.00
~
ZTD- ICn EI: G3.00 ZTD 16 17 5" 8 l r4l-- 4... Co 7 Q
RTD 2I V-i!.O IG Z 1C & I'I'D~"4 2.C P EL M,OO XEMOTE AH'D-8 SPA z=.F-z RHg-2
~z
/ :: EL. IS~.CIO 0!4: .,:...+0 lo II 12 !6 14
@HO-7 SMAZE-r TID-ll SPAZE- n".2 ZiD- l Ri D-2'L Pkz"= FOZ 2:III 2.WO-l 037 . ISQ EL.2o.oo':
l7, 'E Qs. ' 4@ :.
20;. 013 IS lCo l9 20 O!9 .
0 IS 0 l2
. EL.20. OO EL. 3G.OO PLA W5 0= LTD (20+ 2 5PAZ"-5) UECTlOW Fi ure 1
~= R,HO{:6 + '2 'SPA Z-5) ~= TUIZKEY REMI PLANi - UYtl I ~O RE b CTIOZ Co~ V ' II I VI-4' JOCK;!OMSC.= Zi'D'5 CT'HD'5
R-'l
--L-f. L-IA L-2. L.2A TE57 7-C 55'igure 2
'ZLR I PZ.&BUZZ ~wslMC, h.v.'2 CO JTRQj-L=D LK4'PhC~~ <<5) P84EL
~L&Y,. COMM:-CT.
('5T~'Elt4I-cIZc~O Hos~)
FOST FILTER 3
COW h lI iQ-LI "S.'H
'CD CD F= FlLic.R CD i CIIILL""Z~>OA DRY&.
C > CCV!PRE II = IRMA'. TMOICI'TOa Wi~ PZ Sam, Two!Ck<OR.
SVJ~ WMVICC WD i'd%.
... Svl U 0 I STUFZ 6-
<EP (< YP)
AFIiiZCOQLETO
~ I 7 igUZQ 3 IURY-=Y POLJ I PLANT - UNli 3 TLRI PZRSIIP17llIC, W4I ID 4 PZe55'IZI2lk!C. c>TAIIOQ
~ APPENDIX A Computer-Generated Report
l.
INTEGRATED LEAK RATH TEST (XLRT)
LEAK RATE COMPUTED USING TOTAL TIME METHOD AS RECOMMENDED BY APPENDIX J FOR 10 CFR 50 (REACTOR CONTAINMENT LEAKAGE TESTING FOR WATER COOLED POWER REACTORS)
TEST PERIOD STARTED AT 0900 HOURS ON DECEMBER 2, 1975 A LEAST SQUARES FIRST ORDER FIT OF LEAK RATE TO TIME SHOULD YIELD A SLOPE OF ZERO AND AN INTERCEPT EQUAL TO THE LEAK RATE AS COMPUTED AT THE INITIALSTART TIME THE EQUATION HAS THE FORM L=ST + R WHERE L CORRELATED LEAK RATE S SLOPE OF CORRELATION T TIME IN HOURS R INTERCEPT LEAK RATE LEAK RATE = 0.001 HOURS + 0.013 PER CENT MEAN = 0.036 PER CENT
'ERROR COEFFICIENT '
0.226 WHERE COEFFICIENT OF 1.0 MEANS A PERFECT FIT k COEFFICIENT OF 0.0 MEANS NO CORRELATION.
INITIALCONTAINMENT AIR WEIGHT = 318834.2 LBS.
FINAL CONTAINMENT AIR WEIGHT 318704.3 LBS.
LEAK RATE FOR 24.00 HOUR PERIOD IS 0.040 PER CENT BY WEIGHT.
MAXIMUMNRC LEAK RATE OF 0.128 PER CENT PER DAY GIVEN FOR LOW PRESSURE TEST AT 41.890 PSIA MAXIMUMPROBABLE TEMPERATURE LOOP ERROR = 0.054 DEGREES F.
MAXIMUMPROBABLE PRESSURE LOOP ERROR = 0.001 PSIA.
MAXIMUMPROBABLE HUMIDITYLOOP ERROR = 0.296 PERCENT.
INSTRUMENT ERROR CONTRIBUTES 0.015 PERCENT PER DAY TO ESTABLISH 99.87 PERCENT CONFIDENCE BOUND
0
- NOTE FOR GRAPHS ***
BOTH SAMPLE NUMBERS 'AND TIME ARE SHOWN.
~~~ NOTE FOR TABULAR DATA <<~~
TABLE VALUES OF ZERO SIGNIFY EITHER
- 1. DATA IS NOT APPLICABLE TO THE CALCULATION OR
- 2. SENSOR HAS BEEN DELETED FROM MONITORING
- ~~ DESCRIPI'ION OF VARIABLES ~**
AVG TEM VOLUMETRICALLYWEIGHTED TEMPERATURE AVG PRE AVERAGE PRESSURE VAP PRE VOLUMETRICALLYWEIGHTED VAPOR PRESSURE.
LEA COM FIRST ORDER COMPUTED LEAK RATE LEA TRA STATISTICAL TOTAL TIME LEAK RATE LEA SIM SIMPLE TOTAL TIME LEAK RATE ERROR STATISTICAL TOTAL TIME LEAK RATE ERROR
OBSERVRTION NUMBER 10 19 28 37 46 55 64 73 82 91 5.430 CONPUTED LEAK RRTES RELRT I VE TQ L I III TS X X STATISTICAL TOTAL TINE LEAK RATE 3.783 MAXIMUM DESIGH LEAK RATE HRC TECHHICAL SPECIFICATIOH LIMIT IHSTRUNEHT ERROR LIMIT REDUCTION COMPUTED FIRST ORDER EQUATIOH FIT 2.136 x
XX XXXX xxxxx 0.489 XXXX
>- -1 . 158 CC C3
-2.805 Q
I
-4.452 Q
-6.099
-7.746
-9.393
-11.040 120 240 360 480 600 720 840 960 1080 1200 132D 1440 TIME IN MINUTES
OBSERVRTION NUMBER 19 - 28 37 46 55 64 73 82 91 O.68OO COI1PUTED LERK RRTE F IT. RELRT I VE TO
~ MRXIMUM DESIGN LEAN RATE LIMITS 0.. 6120 NRC TECHNICRL SPECIFICRTION LIMIT INSTRUMENT ERROR. LIMIT REDUCTION COMPUTED FIRST ORDER EQUATION FIT o.544o UJ 0 4760
>- 0.4080
'0.3400 Oe2720 0.2040 0 1360 0.0680 r a a a a a a a a 'r a a a a a a s a a r r a a a a a a a rrsaaaaarraaraaasaa rrs ra ra rrs a a a r a a r a a a r a a ararasarraaaasaaraaaaaaaaaa aa o.oooo 0 120 240 360 480 600 720 840 960 1080 1200 1320 1440 TIME IN MINUTES
OBSERVRTION NUMBER 10 19 28 37 46 64 73 82 91 0.1800
. COMPUTED FIT RELRTI VE TQ CRITICRL LIMIT X X SIMPLE TOTAL TIME LERK RRTE.
0.1480 INSTRUMENT ERROR LIMIT REOUCTIOH COMPUTEO FIRST OROER EQUATION FIT 0.1160 0 '840 0.0520 x " xxxx arraaraaaaa x x x x x x xxxxxxx x x xxxx xx XX xxx)ggfggExyj~axax O araaaaaa x x xx xxxxxx xxxx xxxx X
x arear
~
aaaaaa 0.0200 raraaaa I x x x
-0.0120
-0.0440
-0.0760
-0.1080
-0.1400 120 240 360 480 600 720 840 960 1080 1200 1320 1440 TIME IN MINUTES
10 19 37 46 55 64 73 82 91 84 70 VQLUMETR I CRLLY HEI BHTED CQNTRI NMENT TEMPERRTURE 84.67 84.64 84.61 84.58 k k 84.SS k r x
'ra aa rr r xx kx k
a rr a
k k rr k 'k k~
r r rkr 'k r r 'k r r k k a
a x a
k k r r x r a 84.52 'k ka a
'k x 84.49 84.46 84.43 84.40 0 120 240 360 480 '00 720 840 960 1080 1200 1320 1440 TIME IN MINUTES
OBSERVATION NUNBER 10 28 37 46 SS 64 73 82 gi 41.894 RVERRBE CONTR I NUGENT PRESSURE 41.891 R
1 41.888 41.886 1
'1 (0 1 rr 1 0
z 41.883 a ra a
aaa RR aa 41.880 a ra 1 '1'1 1 Rra ararrar ra 'r '1 RRRR 1 arr 41.877 raa 1
rara 'r 11 rra aaa 41.874 1 rr a rara 1
1'1 1 41.872 1 '1 '1
'r '1 r R
'
41.869 41.866 120 240 360 480 600 720 840 960 1080 1200 1320 1440 TINE IN NI NUTES
085ERVRTION NUMBER 0.4200 10 19 28 '7 46 SS 64 73 82 91 VOLUNETR I CRLLY WE I BHTED VRPOR PRESSURE 0.4180 0.4160 CZ
'O 0 ~ 4140 0-4120 M aa aaaar ar a
<<aa ar r'a aa rarra r r xr r r r rara rrrar (0
o.41ao aa r ra Q rr a r a rrxrra rrr CL xa 0.4080 ar aa ra a raa xrarr arar o.4osa 0.4040 0.4020 0.4000
-120 240 360 480 . 600 720 840 960 1080 1200 1320 1440 TIME IN MINUTES
VARIABLE TABLE
SUMMARY
SAMPLE DELTA AVG. TEM AVG. PRE VAP. PRE LEAK COM LEAK TRA ERROR(T)
NUMBER MINS DEG. F PSIA PSIA PER CENT PER CENT PER CENT 1 0 84.615 41.891 0.408 0.014 0.000 0.000 2 15 84.606 41.890 0.408 0.014 -0.020 0.000 3 30 84.588 41.890 0.408 0.015 -9.914 -0.072 4 45 84.582 41.889 0.407 0.015 -3.449 ~ 0.036 5 60 84.573 41.889 0.407 0.016 ~ 0.773 -0.003 6 75 84.577 41.888 0.408 0.016 0.993 -0.007 7 90 84.567 41.888 0.408 0.017 1.211 -0.013 8 105 84.569 41.887 0.408 0.017 1.449 -0.017 9
'20 84.554 41.887 0.408 0.018 1.204 -0.015 10 135 84.552 41.886 0.408 0.018 1.164 -0.015 11 150 84.559 41.885 0.408 0.018 1.200 -0.013 12 165 84.545 41.885 0.408 0.019 1.097 -0.011 13 180 84.525 41.884 0.407 0.019 0.886 -0.008 14 195 84.535 41.884 0.408 0.020 0.796 -0.007 15 210 84.532 41.884 0.408 0.020 0.716 -0.006 16 225 84.530 41.883 0.408 0.021 0.674 ~ 0.004 17 240 84.524 41.881 0.408 0.021 0.670 -0.003 18 255 84.518 41.882 0.408 0.022 0.603 -0.002 19 270 84.529 41.882 0.408 0.022 0.564 -0.000 20 285 84'.525 41.882 0.408 0.023 0.520 0.000 21 300 84.534 41.882 0.408 0.023 0.498 0.002 22 315 84.529 41.881 0.408 0,024 0.473 0.003 23 330 84.533 41.881 0.408 0.024 0.453 0.004 24 '45 84.528 41.881 0.408 0.024 0.427 0.005 25 360 84.526 41.881 0.408 0.025 0.404 0.005 26 375 84.530 41.881 0.409 0.025 0.385 0.006 27 390 84.531 41.880 0.409 0.026 0.369 0.007 28 405 84.528 41.880 0.409 0.026 0.350 0.008 29 420 84.526 41.880 0.408 0.027 0.333 0.008 30 435 84.523 41.880 0.409 0.027 0.316 0.009
'1 450 84.529 41.880 0.409 0.028 0.302 0.009 32 465 84.525 41.879 0.409 0.028 0.289 0.010 33 480 84.520 41.879 0.409 0.029 0.274 0.010 34 495 84.530 41.879 0.409 0.029 0.263 0.010 35 510 84.517 41.879 0.409 0.030 0.251 0.010 36 525 84.526 41.879 0.409 0.030 0.241 0.011 37 540 84.530 41.879 0.409 0.030 0.233 0.011 38 555 84.526 41.878 0.409 0.031 0.224 0.011 39 570 84.510 41.878 0.409 0.031 0.213 0.011 40 585 84.502 41.878 0.409 0.032 0.201 0.011 41 600 84.519 41.878 0.409 0.032 0.192 0.011 42 615 84.548 41.879 0.410 0.033 0.188 0.011 43 630 84.538 41.879 0.410 0.033 0.182 0.012 44 645 84.552 41.879 0.410 0.034 0.178 0.012 45 660 84.553 41.879 0.410 0.034 0.173 0.012 46 675 84.543 41.879 0.410 0.035 0.168 0.012 47 690 84.549 41.879 0.410 0.035 0.163 0.013 48 705 84.552 41.879 0.410 0.036 0.159 0.013 49 720 84.558 41.879 0.411 0.036 0.154 0.013 50 735 84.554 41.879 0.411 0.036 0.150 0.013
>I VARIABLE TABLE
SUMMARY
(CONTINUED)
SAMPLE DELTA AVG. TEM AVG. PRE VAP. PRE LEAK COM LEAK TRA ERROR(T)
NUMBER MINS DEG. F PSIA PSIA PER CENT PER CENT PER CENT 51 750 84.550 41.879 0.410 0.037 0.145 0.013 52 765 84.550 41.878 0.410 0.037 0.141 0.013 53 780 84.542 41.878 0.411 0.038 0.137 0.013 54 795 84.547 41.878 0.411 0.038 0.133 0.013 55 810 84.549 41.878 0.411 0.039 0.129 0.013 56 825 84.548 41.878 0.411 0.039 0.126 0.013 57 840 84.556 41.878 0.411 0.040 0.123 0.013 58 855 84.538 41.877 0.410 0.040 0.119 0.013 59 870 84.533 41.877 0.410 0.041 0.115 0.013 60 885 84.550 41.877 0.411 0.041 0.112 0.012 61 900 84.549 41.877 '0.411 0.042 0.110 0.012 62 915 84.554 41.876 0.411 0.042 0.108 0.013 63 930 84.546 41.876 0.411 0.042 0.105 0.013 64 945 84.552 41.876 0.411 0.043 0.103 0.013 65 960 84.550 41.876 0.411 0.043 0.101 0.013 66 975 84.545 41.876 0.411 0.044 0.099 0.013 67 990 84.545 41.876 0.411 0.044 0.097 0.012 68 1005 84.549 41.876 0.411 0.045 0.095 0.012 69 1020 84.549 41.875 0.411 0.045 0.093 0.012 70 1035 84.539 41.875 0.411 0.046 0.091 0.012 71 1050 84.540 41.875 0.411 0.046 0.089 0.012 72 1065 84.556 41.875 0.411 0.047 0.088 0.012 73 1080 84.550 41.875 0.411 0.047 0.086 0.012 74 1095 84.548 41.875 0.411 0.047 0.085 0.012 75 1110 84.547 41.874 0.411 0.048 0.083 0.012 76 1125 84.543 41.874 0.411 0.048 0.082 0.012 77 1140 84,523 41.874 0.411 0.049 0.080 0.012 78 1155 84.530 41.873 0.411 0.049 0.079 0.011 79 1170 84.525 41.873 0.411 0.050 0.077 0.011 80 1185 84.530 '41.873 0.411 0.050 0.076 0.011
, 81 1200 84.525 41.873 0.411 0.051 0.074 0.011 82 1215 84.531 41.873 0.411 0.051 0.073 0.011 83 1230 84.521 41.873 0.411 0.052 0.072 0.011 84 1245 84.519 41.872 0.411 0.052 0.071 0.010 85 1260 84.519 41.872 0.411 0.053 0.069 0.010 86 1275 84.523 41.872 0.411 0.053 0.068 0.010 87 1290 84.517 41.872 0.412 0.053 0.067 0.010 88 1305 84.526 41.871 0.412 0.054 0.066 0.010 89 1320 84.519 41.871 0.412 0.054 0.065 0.010 90 1335 84.523 41.871 0.412 0.055 0.064 0.010 91 1350 84.511 41.871 0.412 0.055 0.064 0.009 92 1365 84.509 41.871 0.411 0.056 0.063 0.009 93 1380 84.503 41.871 0.411 0.056 0.062 0.009 94 1395 84.499 41.871 0.411 0.057 0.061 0.009 95 1410 84.491 41.870 0.412 0.057 0.060 0.009 96 1425 84.493 41.870 0.412 0.058 0.059 0.008 97 1440 84.490 41.869 0.412 0.058 0.058 0.008 END OF TABLE
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 1 TEMP 2 TEMP 3 TEMP 4 TEMP 5 TEMP 6 NUMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 0 84.360 84.740 84.880 84.850 84.540 84.840 2 15 84.350 84.730 84.870 84.830 84.540 84.860 3 30 84.300 84.730 84.870 84.850 84.520 84.840 4 45 84.280 84.730 84.870 84.850 84.530 84.850 5 60 84.290 84.700 84.870 84.840 84.530 84.840 6 75 84.300 84.710 84.870 84.820 84.520 84.810 7 90 84.290 84.690 84.860 84.840 84.510 84.810 8 105 84.290 84.700 84.860 84.820 84.490 84.780 120 84.260 84.690 84.850 84.820 84.500 84.800 10 135 84.250 84.690 84.840 84.810 84.500 84.860 11 150 84.290 84.680 84.830 84.830 84.490 84.780 12 165 84.240 84.690 84.830 84.790 84.480 84.800 13 180 84.200 84.670 84.820 84.820 84.490 84.810 14 195 84.220 84.680 84.820 84.810 84.490 84.800 15 210 84.240 84.660 84.820 84.800 84.480 84.740 16 225 84.250 84.650 84.810 84.810 84.460 84.780 17 240 84.270 84.630 84.800 84.790 84.450 84.720 18 255 84.210 84.650 84.800 84.810 84.460 84.810 19 270 84.220 84.670 84.810 84.790 84.470 84.790 20 285 84.230 84.650 84.800 84.790 84.470 84.780 21 300 84.250 84.660 84.800 84.780 84 460 84.780 22 315 84.230 84.660 84.790 84.810 84.470 84.800 23 330 84.230 84.670 84.790 84.810 84.480 84.810 24 345 84.240 84.650 84.800 84.820 84.470 84.780 25 360 84.220 84.660 84.800 84.810 84.470 84.770 26 375 84.230 84.660 84.780 84.850 84.480 84.780 27 390 84.250 84.650 84.780 84.800 84.470 84.760 28 405 84.230 84.660 84.790 84.790 84.460 84.760 29 420 84.230 84.650 84.790 84.810 84.470 84.790 30 435 84.220 84.650 84.790 84.810 84.460 84.770 31 450 84.240 84.650 84.780 84.800 84.460 84.780 32 465 84.230 84.650 84.780 84.800 84.460 84.780 33 480 84.220 84.640 84.800 84.840 84.480 84.760 34 495 84.260 84.640 84.780 84.810 ,84.450 84.760 35 510 84.210 84.640 84.780 84.870 84.470 84.790 36 525 84.230 84.650 84.780 84.810 84.470 84.840 37 540 84.240 84.650 84.770 84.830 84 480 84.750 38 555 84.230 84.650 84.760 84.820 84.440 84.740 39 570 84.220 84.630 84.770 0.000 84.450 84.750 40 585 84.210 84.610 84.780 0.000 84.470 84.780 41 600 84.230 84.630 84.770 0.000 84.460 84.740 42 615 84.280 84.660 84.780 0.000 84.480 84.790 43 630 84.240 84.660 84.780 0.000 84.480 84.840 44 645 84.270 84.670 84.790 0.000 84.480 84.780 45 660 84.260 84.680 84.790 0.000 84.480 84.780 46 675 84.250 84.660 84.790 0.000 84.470 84.780 47 690 84.230 84.690 84.790 0.000 84.490 84.810 48 705 , 84.250 84.680 84.780 0.000 84.460 84.820 49 720 84.260 84.680 84.790 0.000 84.510 84.840 50 735 84.270 84.670 84.780 0.000 84.480 84.780
i I
VARIABLE TABLE
SUMMARY
(CONTINUED)
SAMPLE DELTA TEMP 1 TEMP 2 TEMP 3 TEMP 4 TEMP 5 TEMP 6 NUMBER MINS DEG. F DEG. DEG. F DEG. F DEG. F DEG. F 51 750 84.250 F'4.670 84.790 0.000 84.490 84.800 52 765 84.250 84.670 84.780 0.000 84.490 84.780 53 780 84.250 84.650 84.790 0.000 84.490 84.810 54 795 84.240 84.670 84.780 0.000 84.490 84.820 55 810 84.250 84.670 84.770 0.000 84.490 84.soo 56 825 84.250 84.670 84.780 0.000 84.490 84.820 57 840 84.260 84.680 84.780 0.000 84.470 84.850 58 855 84.240 84.650 84.790 0.000 84.470 84.810 59 870 84.250 84.630 84.780 0.000 84.480 84.790 60 885 84.270 84.650 84.780 0.000 84.500 84.810 61 900 84.270 84.650 84.790 0.000 84.480 84.800 62 915 84.270 84.660 84.790 0.000 84.470 84.810 63 930 84.250 84.660 84.780 0.000 84.490 84.780 64 945 84.260 84.670 84.770 0.000 84.500 84.810 65 960 84.260 84.660 84.780 0.000 84 480 84.800 66 975 84.250 84.660 84.790 0.000 84.490 84.800 67 990 84.250 84.660 84.780 0.000 84.460 84.780 68 1005 84.260 84.660 84.780 0.000 84.490 84.800 69 1020 84.250 84.670 84.780 0.000 84.470 84.830 70 1035 84.250 84.640 84.770 0.000 84.500 84.810 71 1050 84.220 84.670 84.790>> 0.000 84.490 84.810 72 1065 84.270 84.670 84.780 0.000 84.490 84.790 73 1080 84.240 84.680 84.780 0.000 84.480 84.800 74 1095 84.260 84.660 84.780 0.000 84.490 84.800 75 1110 84.250 84.670 84.780 0.000 84.460 84.800 76 1125 84.230 84.670 84.770 0.000 84.470 84.820 77 1140 84.220 84.630 84.780 0.000 84.480 84.780 78 1155 84.240 84.630 84.780 0.000 84.460 84.810 79 1170 84.210 84.650 84.760 0.000 84.450 84.750 80 1185 84.230 84.650 84.760 0.000 84.440 84.770 81 1200 84.210 84.650 84.760 0.000 84.460 84.770 82 1215 84.230 84.650 84.770 0.000 84.460 84.770 83 1230 84.220 84.640 84.760 0.000 84.460 84.770 84 1245 84.210 84.640 84.750 0.000 84.470 84.790 85 1260 84.210 84.640 84.750 0.000 84.460 84.780 86 1275 84.230 84.640 84.760 0.000 84.450 84.750 87 1290 84.200 84.650 84.760 0.000 84 460 84.780 88 1305 84.240 84.640 84.760 0.000 84.460 84.770
, 89 1320 84.220 84.640 84.750 0.000 84.450 84.780 90 1335 84.220 84.650 84.750 0.000 84.440 84.750 91 1350 84.200 84.630 84.750 0.000 84.440 84.780 92 1365 84.200 84.630 84.750 0.000 84.450 84.780 93 1380 84.200 84.620 84.760 0.000 84.460 84.770 94 1395 84 180
~ 84.630 84.740 0.000 84.440 84.720 95 1410 84.170 84.620 84.730 0.000 84.430 84.740 96 1425 84.190 84.610 84.730 0.000 84.430 84.780 97 1440 84.190 84.610 84.720 0.000 84.420 84.750 END OF TABLE
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 TEMP 12 NUMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 0 85.010 84.840 85.330 85.050 84.710 84.330 2 15 84.950 84.830 85.330 85.030 84.690 84.330 3 30 84.950 84.800 85.320 85.020 84.710 84.330 45 84.920 84.820 85.320 85.010 84.690 84.340 5 60 84.920 84.800 85.340 85.020 84.690 84.320 6 75 84.930 84.800 85.330 85.030 84.690 84.310 7 90 84.910 84.780 85.320 85.030 84.690 84.310 8 105 84.910 84.790 85.310 85.010 84.700 84.320 9 120 s4.e7o 84.780 85.300 84.990 84.690 84.310 10 135 84.890 84.780 85.300 85.010 84.680 84.310 11 150 84.890 84.750 85,310 85.010 84.670 84.300 12 165 84.900 84.760 85.300 85.000 84.690 84.290 13 180 84.890 84.760 85.300 84.990 84.670 84.280 14 195 84.890 84.750 85.310 84.990 84.690 84.290 15 210 84.910 84.760 85.300 84.990 84.670 84.300 16 225 84.880 84.740 85.300 85.010 84.660 84.280 17 240 84.880 84.740 85.260 84.980 84.670 84.270 18 255 84.920 84.740 85.300 84.960 84.660 84.270 19 270 84.870 84.740 85.300 84.980 84.680 84.310 20 285 84.910 84.740 85,320 84.960 84.660 84.290 21 300 84.880 84.740 85.320 84.970 84.660 84.300 22 315 84.910 84.740 85.300 84.970 84.660 84.280 23 330 84.880 84.750 85.290 84.980 84.670 84.290 24 345 84.860 84.740 85.300 84.990 84.650 84.270 25 360 84.900 84.730 85.310 84.970 84.670 84.290 26 375 84.870 84.740 85.310 84.980 84.660 84.290 27 390 84.880 84.740 85.300 84.960 84.670 84.280 28 405 84.860 84.750 85.300 84.970 84.690 84.300 29 420 s4.eeo 84.750 85.300 84.990 84.670 84.290 30 435 84.920 84.740 85.310 84.980 84.660 84.310 31 450 84.860 84.740 85.310 84.990 84.670 84.310
"
32 465 84.890 84.750 85.320 84.970 84.670 84.300 33 480 84.880 84.740 85.310 84.980 84.660 84.290 34 495 84.870 84.750 85.320 84.970 84.660 84.280 35 510 84.870 84.740 85.310 84.980 84.670 84.300 36 525 84.860 84.740 85.300 84.970 84.660 84.290 37 540 84.890 84.750 85.320 84.970 84.670 84.280 38 555 S4.890 84.760 85.320 84.980 84.670 84.300 39 570 84.860 84.740 85.300 84.970 84.670 84.300 40 585 84.860 84.740 85.310 84.970 84.670 84.310, 41 600 84.890 84.750 85.330 85.010 84.700 84.360 42 615 84.890 84.750 85.320 85.040 84.720 84.340 43 630 84.910 84.760 .85.320 85.040 84.740 84.370 44 645 84.910 84.760 85.340 85.060 84.730 84.380 45 660 84.880 84.770 85.330 85.070 84.730 84.370 46 675 84.920 84.760 85.330 85.070 84.740 84.390 47 690 84.870 84.760 S5.340 85.080 84.770 84 400 48 705 84.870 84.770 85.350 85.070 84.750 84.400 49 720 84.930 84.780 85.340 85.070 84.760 84.370 50 735 84.890 84.770 85.330 85.080 84.730 84.390
VARIABLE TABLE
SUMMARY
(CONTINUED)
SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 TEMP 12 NUMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 51 750 84.900 84.760 85.350 85.080 84.750 84.380 52 765 84.920 84.770 85.340 85.090 84.770 84.390 53 780 84.910 84.770 85.330 85.080 84.750 84.380 54 795 84.940 84.770 85.340 85.060 84.770 84.400 55 810 84.890 84.780 85.350 85.070 84.750 84.380 56 825 84.890 84.770 85.340 85.060 84.760 84.360 57 840 84.880 84.770 85.330 85.080 84.760 84.390 58 855 84.890 84.770 85.340 85.070 84.770 84.390 59 870 84.870 84.750 85.350 85.080 84.780 84.370 60 885 84.920 84.770 85.360 85.080 84.740 84.370 61 900 84.910 84.770 85.360 85.090 84.750 84.390 62 915 84.940 84.760 85.340 85.090 84.750 84.390 63 930 84.900 84.770 85.340 85.090 84.770 84.380 64 945 84.880 84.770 85.350,, 85.080 84.770 84.370 65 960 84.900'4.900 84.770 85.340 85.100 84.760 84.400 66 975 84.760 85.350 85.090 84.770 84.390 67 990 84.930 84.770 85.330 85.090 84.780 84.410 68 1005 84,940 84.760 85.350 85.090 84.770 84.380 69 1020 84.930 84.750 85.330 85.080 84.770 84.400 70 1035 84.950 84.760 85.340 85.090 84.780 84.370 71 1050 84.860 84.770 85.340 85.080 84.780 84.390 72 1065 84.880 84.750 85.340 85.100 84.770 84.390 73 1080 84.910 84.760 85.350 85.090 84.770 84.410 74 1095 84.890 84.750 85.350 85.080 84.770 84.380 75 1110 84.890 84.760 85.340 85.070 84.770 84.390 76 1125 84.930 84.770 85.320 85.090 84.780 84.400 77 1140 84.890 84.750 ~
85.320 85.100 84.770 84.380 78 1155 84.890 84.750 85.340 85.090 84.780 84.410 79 1170 84.870 84.770 85.310 85.070 84.770 84.400 80 1185 84.860 84.750 85.330 85.070 84.760 84.390
, 81 1200 84.910 84.750 85.330 85.080 84.750 84.390 82 1215 84.890 84.740 85.320 85.070 84.770 84.380 83 1230 84.860 84.730 85.310 85.060 84.770 84.360
- 84 1245 84.900 84.720 85.330 85.070 84.760 84.350 85 1260 84.920 84.730 85.310 85.070 84.750 84.360 86 1275 84.870 84.740 85.290 85.060 84.760 84.380 87 1290 84.830 84.740 85.300 85.050 84.770 84.360'4.370 88 1305 84.870 84.720 85.320 85.050 84.760 89 1320 84.860 84.730 85.310 85.050 84.770 84.380 90 1335 84.860 84.710 85.320 85.060 84.770 84.350 91 1350 84.880 84.720 85.310 85.060 84.760 84.390 92 1365 84.870 84.720 ,
85.300 85.060 84.770 84.350 93 1380 84.840 84.720 85.310 85.050 84.750 84.320 94 1395 84.850 84.710 85.310 85.050 84.770 '4.350 95 1410 84.840 84.710 85.270 85.040 84.760 84.340 96 1425 84.820 84.710 85.260 85.040 84.740 84.330 97 1440 84.810 84.700 85.270 85.030 84.740 84.310 END OF TABLE
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 13 TEMP 14 TEMP 15 TEMP 16 TEMP 17 TEMP 18 NUMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F , DEG. F 1 0 84.590 84.500 84.910 84.160 84.190 85.110 2 15 84.590 84.500 84.900 84.170 84.210 85.110 3 30 84.550 84.490 84.890 84.160 84.220 85.120 45 84.560 84.500 84.890 84.150 84.220 85.120 6, 60 84.580 84.500 84.890 84.150 84.200 85.110 6 75 84.580 84.480 e4.eoo 84.140 84.190 85.110 7 90 84.580 84.480 84,890 84.140 ~ 84.210 85.110 8 105 84.570 84.490 84.880 84.140 84.190 85.100 9 120 84.570 84.490 84.880 84.140 84.180 85.100 10 135 84.550 84.480 84.880 84.140 84.180 85.100 ll 150 S4.650 84.480 84.870 84.140 84.200 85.100 12 165 84.540 84.480 84.870 84.140 84.170 85.090 13 180 84.560 84.470 84.870 84.160 84 180
~ 85.090 14 195 84.650 84.460 84.870 84.140 84.200 85.090 15 210 84.640 e4.4eo e4.eeo 84.140 84.170 85.080 16 226 84.630 84.460 84.870 84.130 84.180 85.070 17 240 84.610 84.430 84.860 84.100 84 160
~ 85.080 18 255 84.640 84.470 84.860 84.130 84.170 85.080 19 270 84.660 84.480 84.860 84.120 84.170 e5.oeo 20 285 e4.64o 84 480 84.870 84.120 84.200 85.080
'21 300 84.540 84.480 84.870 84.120 84.180 85.090 22 315 84.550 84.480 84.870 84.120 84.160 85.090 23 330 84.540 84.490 84.870 84.120 84.180 85.090 24 345 84.550 84.490 e4.evo 84.140 84.170 85.090 25 360 84.550 84.490 84.860 84,120 84.190 85.090 26 375 84.550 84.500 84.870 84.140 84.200 85.090 27 390 84.550 84.500 84,870 84.130'4.130 84.180 85.090 28 405 84.550 , 84.490 84.870 84.180 85.090 29 420 84.540 84.490 84.870 84.130 84.190 85.100
'30 435 84.540 84.490 84.870 84.130 84.170 85.090 31 450 84.540 84.500 84.870 84.120 84.200 85.100 32 465 84.550 84.480 84.870 84.130 84.180 85.100 33 480 84.560 84.510 84.870 84.140 84.180 85.090 34 495 84.540 84.490 84.870 84.140 84.190 85.100 35 510 84.540 84.500 84.870 84.130 84.210 85.100 36 525 84.560 84 490 84.870 84.130 84.180 85.100 37 540 84580 84.490 84.870 84.140 84.180 85.090 38 555 84.550 84.500 84.870 84.150 84.190 85.110 39 570 84.530 84.520 84.870 84.150 84.190 85.100 40 585 84.570 84.500 84.880 84.140 84.190 85.110 41 600 84.540 84.510 84.890 84.150 84.220 85.110 42 615 84.580 84.510 84.890 84.140 84.220 85.120 43 630 84.590 84.520 84.880 84.150 84.230 85.120 44 645 84.570 84.500 84.900 84.150 84.240 85.130 45 660 84.580 84.530 84.900 84.170 84.250 85.130 46 675 84.680 84.540 84.910 84.150 84.240 85.130 47 690 84.580 84.520 84.910 84.160 84.240 85.140 48 705 84.580 84.550 84.910 84.170 84.250 85.140 49 720 84.590 84.540 84,910 84.180 84.250 85.140 50 735 84.580 84.530 84.910 84.180 84.260 85.140
VARIABLE TABLE
SUMMARY
(CONTINUED)
SAMPLE DELTA TEMP 13 TEMP 14 TEMP 15 TEMP 16 TEMP 17 TEMP 18 NUMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 51 750 84.600 84.520 84.920 84.190 84.250 85.140 52 765 84.590 84.540 84.910 84.180 84.250 85.140 53 780 84.580 84.520 84.920 84.170 84.240 85.150 54 795 84.570 84.530 84.910 84.170 84.230 85.140 55 810 84.590 84.530 84.920 84.170 84.260 85.140 56 825 84.580 84.520 84.910 84.170 84.250 85.130 57'8 840 84.580 84.530 84.920 84.180 84.260 85.150 855 84.580 84.530 84.920 84.180 84.250 85.140 59 870 84.570 84.510 84.910 84.170 84.250 85.140 60 885 84.600 84.520 84.920 84.190 84.260 85.140 61 900 84.590 84.510 84.920 84.190 84.230 85.140 62 915 84.580 84.520 84.920 84.210 84.250 85.150 63 930 84.590 84.530 84.920 84.190 84.240 85.140 64 945 84.610 84.520 84.930 84.170 84.220 85.150 65 960 84.600 84.530 84.920 84.180 84.240 85.140 66 975 84.580 84.520 84.920 84.170 84.250 85.140 67 990 84.580 84.520 84.930 84.170 84.230 85.150 68 1005 84.sso 84.510 84.930 84.170 84.220 85.140 69 1020 84.570 84.520 84.930 84.190 84.230 85.150 70 1035 84.610 84.510 84.920 84.180 84.230 85.140 71 1050 84.61O 84.510 84.930 84.190 84.220 85.140 72 1065 84.600 84.520 84.930 84.190 84.240 85.140 73 1080 84.590 s4.coo 84.930 84.180 84.220 85.140 74 1095 84.600 84.500 84.930 84.180 84.220 85.150 75 1110 84.570 84.500 84.930 84.180 84.230 85.150 76 1125 84.580 84.500 84.930 84.180 84.240 85.140 77 1140 84.600 84.510 84.920 84.190 84.220 85.140 78 1155 84.560 84.500 84.920 84.180 84.240 85.140 79 1170 84.570 84.500 84.920 84.180 84.230 85.140 80 1185 84.570 84.490 84.920 84.170 84.210 85.140 81 1200 84.570 84.470 84.920 84.180 84.220 85.140 82 1215 84.560 84.500 84.920 84.170- 84.220 85.140 83 1230 84.550 84.470 84.910 84.170 84.230 85.130 84 1245 84.570 84.480 84.920 84.160 84.210 85.130 85 1260 84.570 84.470 84.920 84.180 84.200 85.130 86 1275 84.560 84.470 84.910 84.170 84.210 85.130 87 1290 84.560 84.460 84.910 84.170 84.190 85.120 88 1305 84.560 84.480 84.900 84.170 84.180 85.120 89 1320 84.550 84.470 84.900 84.160 84.200 85.120 90 1335 84.550 84.460 84.900 84.170 84.220 85.120 91 1350 84.540 84.480 84.910 84.170 84.210 85.130 92 1365 84.540 84.480 84.900 84.170 84.210 85.130 93 1380 84.550 84 460 84.890 84.150 84.200 85.120 94 1395 84.530 84.470 84.900 84.150 84.190 85.110 95 1410 84.520 84.450 84.890 84.150 84.210 85.110 96 1425 84.540 84.460 84.890 84.140 84.190 85.100 97 1440 84.510 84.440 84.890 84 140
~ 84.180 85.110 END OF TABLE
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 19 TEMP 20 PRES 1 HUM 1 HUM 2 HUM 3 NUMBER MINS DEG. F DEG. F PSIA FRACTION FRACTION FRACTION 1 0 84.700 84.460 41.891 0.721 0.672 0.669 2 15 84.690 84.470 41.890 0.722 0.672 0.669 3 30 84.710 84.440 41.890 0.722 0.672 0.669 4 45 84.700 84.450 41.889 0.721 0.672 0.669 5 60 84.700 84.450 41.889 0.722 0.672 0.669 6 75 84.700 84.450 41.888 0.722 0.673 0.670 7 90 84.660 84.460 41.888 0.722 0.673 0.670 8 105 84.690 84.470 41.887 0.723 0.673 0.670 9 120 84.690 84.450 41.887 0.723 0.673 0.670 10 135 84.700 84.440 41.886 0.723 0.674 0.670 11 150 84.690 84.450 41.885 0.723 0.674 0.670 12 165 84.690 84.440 41.885 0.723 0.674 0.671 13 180 84.690 84.430 41.884 0.723 0.674 0.671 14 195 84.700 84.450 41.884 0.724 0.674 0.671 15 210 84.680 84.430 41.884 0.724 0.674 0.671 16 225 84.670 84.430 41.883 0.724 0.674 0.671 17 240 84.670 84.420 41.881 0.724 0.674 0.671 18 255 84.670 84.450 41.882 0.724 0.674 0.671 19 270 84.690 84.430 41.882 0.725 0.674 0.671 20 285 84.680 84.450 41.882 0.724 0.675 0.671 21 300 84.700 84.450 41.882 0.725 0.675 0.671 22 315 84.710 84.440 41.881 0.725 0.675 0.672 23 330 84.700 84.460 41.881 0.725 0.675 0.672 24 345 '4.710 84.440 41.881 0.725 0.675 0.672 25 360 84.700 84 450 41.881 0.725 0.675 0.672 26 375 84.680 84.450 41.881 0.725 0.676 0.672 27 390 84.700 84 460 41.880 0.725 0.676 0.672 28 405 84.710 84.450 41.880 0.725 0.676 0.672 29 420 84.710 84.450 41.880 0.726 0.675 0.673 30 435 84.690 84.460 41.880 0.725 0.676 0.673 31 450 84.710 84.460 41.880 0.726 0.676 0.673 32 465 84.690 84.450 41.879 0.726 0.676 0.673 33 480 84.700 84.460 41.879 0.726 0.676 0.673 34 495 84.700 84.450 41.879 0.726 0.676 0.673 35 510 84.710 84.450 41.879 0.726 0.676 0.674 36 525 84.710 84.450 41.879 0.727 0.677 0.674 37 540 84.700 84.480 41.879 0.727 0.677 0.674 38 555 84.710 84.460 41.878 0.726 0.677 0.674 39 570 84.710 84.450 41.878 0.727 0.677 0.674 40 585 '4.720 84.450 41.878 0.727 0.677 0.674 41 600 84.720 84.460 41.878 0.727 0.677 0.674 42 615 84.710 84.460 41.879 0.727 0.677 0.674 43 630 84.700 84.470 41.879 0.728 0.678 0.675 44 645 84.710 84.470 41.879 0.728 0.678 0.675 45 660 84.720 84.460 41.879 0.728 0.678 0.675 46 675 84.720 84.470 41.879 0.728 0.678 0.675 47 690 84.720 84.480 41.879 0.728 0.678 0.675 48 705 84.710 84.470 41.879 0.728 0.678 0.675 49 720 84.730 84.470 41.879 0.728 0.678 0.675 50 735 84.730 84.470 41.879 0.729 0.679 0.675
~ ~
~ '
VARIABLE TABLE
SUMMARY
(CONTINUED)
SAMPLE DELTA TEMP 19 TEMP 20 PRES 1 HUM 1 HUM 2 HUM 3 NUMBER MI NS DEG. F DEG. F PSIA FRACTION FRACTION FRACTION 51 750 84.740 84.490 41.879 0.728 0.678 0.675 52 765 84.730 84.480 41.878 0.728 0.678 0.675 53 780 84.740 84.470 41.878 0.729 0.679 0.676 54 795 84.750 84.480 41.878 0.728 0.679 0.675 55 810 84.730 84.470 41.878 0.728 0.679 0.676 56 825 84.730 84.480 41.878 0.728 0.679 0.676 57 840 84.730 84.480 41.878 0.728 0.678 0.676 58 855 84,720 84.480 41.877 0.729 0.678 0.676 59 870 84.730 84.470 41.877 0.729 0.678 0.676 60 885 84.740 84 480 41.877 0.729 0.679 0.676 61 900 84.740 84.470 41.877 0.729 0.679 0.676 62 915 84.750 84.480 41.876 0.729 0.679 0.676 63 930 84.730 84.500 41.876 0.729 0.679 0.677 64 945 84.720 84.490 41.876 0.729 0.679 0.677 65 960 84.740 84.490 41.876 0.730 0.679 0.677 66 975 84.720 84.460 41.876 0.730 0.679 0.677 67 990 84.740 84.460 41.876 0.729 0.679 0.677 68 1005 84.730 84.480 41.876 0.729 0.679 0.677 69 1020 84.730 84.470 41.875 0.730 0.679 0.677 70 1035 84.730 84.470 41.875 0.730 0.679 0.677 71 1050 84.730 84 480 41.875 0.729 0.679 0.677 72 1065 84.740 84.470 41.875 0.730 0.679 0.677 73 1080 84.740 84.510 41.875 0.730 0.679 0.677 74 '095 84.720 84.500 41.875 0.729 0.680 0.677 75 1110 84.730 84.470 41.874 0.730 0.679 0.677 76 1125 84.730 84.500 41.874 0.730 0.679 0.677 77 1140 84.720 84.460 41.874 0.730 0.680 0.678 78 1155 84.730 84.470 41.873 0.730 0.680 0.677 79 1170 84.730 84.460 41.873 0.730 0.680 0.678 80 1185 84.740 84.470 41.873 0.730 0.680 0.678 81 1200 84.730 84 460 41.873 0.730 0.680 0.678 82 1215 84.730 84.460 41.873 0.731 0.680 0.678 83 1230 84.730 84.450 41.873 0.731 0.680 0.678 84 1245 84.730 84.440 41.872 0.731 0.679 0.678 85 1260 84.720 84.440 41.872 0.731 0.680 0.678 86 1275 84.710 84.430 41.872 0.731 0.680 0.678 87 1290 84.730 84.440 41.872 0.731 0.680 0.678 88 1305 84.720 84.420 41.871 0.731 0.680 0.679 89 1320 84.710 84.430 41.871 0.731 0.681 0.679 90 1335 84.730 84.430 41.871 0.731 0.681 0.679 91 1350 84.730 84.450 41.871 0.731 0.681 0.679 92 1365 84.700 84.440 41.871 0.731 0.680 0.679 93 1380 84.700 84.410 41.871 0.732 0.680 0.679 94 1395 84.700 84.440 41.871 0.732 0.681 0.679 95 1410 84.710 84.430 41.870 0.731 0.681 0.679 96 1425 84.700 84.440 41.870 0.732 0.681 0.679 97 1440 84.710 84.430 41.869 0.732 0.681 0.679 END OF TABLE
0 VARIABLETABLE
SUMMARY
SAM FLE DELTA HUM 4 HUM 5 HUM 6 NUMBER MINS FRACTION FRACTION FRACTION 1 0 0.699 0.700 0.715 2 15 0.699 0.700 0.715 3 30 0.699 0.701 0.716 45 0.699 0.700 0.716 5 60 0.700 0.701 0.716 6 75 0.700 0.701 0.716 7 90 0.700 0.701 0.716 8 105 0.700 0.701 0.716 9 120 0.700 0.701 0.716 10 135 0.700 0.701 0.716 ll 150 0.700 0.702 0.716 12 165 0.701 0.702 0.716 13 180 0.701 0.702 0.716 14 195 0.700 0.702 0.716 15 210 0.700 0.702 0.717 16 225 0.700 0.702 0.716 17 240 0.701 0.703 0.717 18 255 0.701 0.702 0.716 19 '0 270 0.701 0.702 0.716 285 0.701 0.702 0.717 21 300 0.701 0.703 0.717 22 315 0.701 0.703 0.717 23 330 0.701 0.703 0.717 24 345 0.701 0.703 0.717 25 360 0.701 0.703 0.717 26 375 0.701 0.703 0.717 27 390 0.701 0,703 0.717 28 405 0.701 0.703 0.717 29 420 0.701 0.704 0.717 30 435 0.701 0.704 0.717 31 450 0.701 0.704 0.717 32 465 0.702 0.704 0.717 33 480 0.702 0.704 0.717 34 495 0.702 0.704 0.718 35 S10 0.703 0.704 0.718 36 525 0.703 0.704 0.718 37 540 0.703 0.704 0.718 38 555 0.703 0.705 0.719 39 570 0.703 0.705 0.719 40 585 0.702 0.704 0.718 41 600 0.702 0.704 0.719 42 615 0.702 0.705 0.719 43 630 0.703 0.705 0.719 44 645 0,703 0.705 0.719 45 660 0.703 0.705 0.719 46 675 0.702 0.706 0.719 47 690 0.703 0.705 0.719 48 705 0.702 0.705 0.719 49 720 0.702 0.705 0.719 50 735 0.703 0.705 0.719
VARIABLE TABLE
SUMMARY
(CONTINUED)
SAMPLE DELTA 'UM 4 HUM 5 HUM 6 NUMBER MINS FRACTION FRACTION FRACTION 51 750 0.702'.703 0.705 0.719 52 765 0.705 0.719 53 780 0.703 0.706 0.720 54 795 0.703 0.706 0.720 55 810 0.703 0,706 0.719 56 825 0.703 0.706 0.719 57 840 0.703 0.706 0.720 58 855 0.703 0.706 0.720 .
59 870 0.703 0.706 0.720 60 ee5 0.703 0.706 0.720 61 900 0.703 0.707 0.720 62 915 0.703 0,706 0.720 63 930 0.704 0,707 0.721 64 945 0.704 0.707 0.721 65 960 0.704 0.708 0.720 66 975 0.704 0.707 0.721 67 990 0.704 0.707 0.721 68 1005 0.704 0.706 0.720 69 1020- 0.703 0.707 0.720 70 1035 0.703 0.707 0.720 71 1050 0.703 0.707 0.720 72 1065 0.704 0.707 0.720 73 1080 0.703 0.707 0.720 74 1095 0.704 0.707 0.720 75 lllP 0.704 0.707 0.721 76 1125 0.704 0.707 0.720 77 1140 0.704 0.707 0.721 78 1155 0.704 0.708 0.721 79 1170 0.704 0.708 0.721 80 1185 0.704 0.708 0.721 81 1200 0.704 0.707 0.721 82 1215 0.704 0.708 0.721 83 1230 0.704 0.708 0.721 84 1245 0.704 0.708 0.721 85 1260 0.704 0.708 0.721 86 1275 0.705 0.708 0.721 87 1290 0.705 0.709 0.721 88 1305 0.705 0.709 0.721 89 1320 0.705 0.708 0.721 90 1335 0.705 0.708 0.722 91 1350 0.705 0.709 0.721 92 1365 0.705 '.709 0.722 93 1380 0.705 0.709 0.722 94 1395 0.705 0.709 0.722 95 1410 0.705 0.709 0.722 96 1425 0.705 0.709 0.722 97 1440 0.706 0.709 0.722 END OF TABLE END OF COMPUTER REPORT ON CONTAINMENT LEAK RATE TEST TO NRC
2.
CONTROLLED LEAK RATE TEST (CLRT)
LEAK RATE COMPUTED USING TOTAL TIME METHOD AS RECOMMENDED BY APPENDIX J FOR 10 CFR 50 (REACTOR CONTAINMENT LEAKAGE TESTING FOR WATER COOLED POWER REACTORS)
TEST PERIOD STARTED AT 0915 HOURS ON DECEMBER 3, 1975 A LEAST SQUARES FIRST ORDER FIT OF LEAK RATE TO TIME SHOULD YIELD A SLOPE OF ZERO AND AN INTERCEPT EQUAL TO THE LEAK RATE AS COMPUTED AT THE INITIALSTART TIME THE EQUATION HAS THE FORM L=ST + R WHERE L CORRELATED LEAK RATE S SLOPE OF CORRELATION T TIME IN HOURS R INTERCEPT LEAK RATE LEAK RATE = 0.002 HOURS + 0.126 PER CENT MEAN = 0.131 PER CENT ERROR COEFFICIENT = 0.013 WHERE COEFFICIENT OF 1.0'MEANS A PERFECT FIT &
COEFFICIENT OF 0.0 MEANS NO CORRELATION.
INITIALCONTAINMENT AIR WEIGHT = 318709.3 LBS.
FINAL CONTAINMENT AIR WEIGHT 318624.2 LBS.
LEAK RATE FOR 4.50 HOUR PERIOD IS 0.027 PER CENT BY WEIGHT."
MAXIMUMNRC LEAK RATE OF 0.128 PER CENT PER DAY GIVEN FOR LOW PRESSURE TEST AT 41.868 PSIA MAXIMUMPROBABLE TEMPERATURE LOOP ERROR = 0.054 DEGREES F.
MAXIMUMPROBABLE PRESSURE LOOP ERROR = 0.002 PSIA.
MAXIMUMPROBABLE HUMIDITY LOOP ERROR = 0.296 PERCENT.
INSTRUMENT ERROR CONTRIBUTES 0.015 PERCENT PER DAY TO ESTABLISH 99.87 PERCENT CONFIDENCE BOUND CONTROLLED LEAK RATE TEST (CLRT)
SUPPLEMENTAL VERIFICATION FOR ILRT LEAKAGE OF 0.123 PERCENT AT 39.695 PSIA IS EQUIVALENT TO 3.372 SCFM.
SUPPLEMENTAL TEST (CLRT) DATA AND PREVIOUS ILRT RESULTS PLUS INJECTED LEAKAGE MUST BE WITHIN 25 PERCENT ( 0.843 SCFM) FOR VERIFICATION.
- " NOTE FOR GRAPHS ~**
BOTH SAMPLE NUMBERS AND TIME ARE SHOWN.
- '* NOTE FOR TABULAR DATA ***
TABLE VALUES OF ZERO SIGNIFY EITHER
- 1. DATA IS NOT APPLICABLE TO THE CALCULATION OR
- 2. SENSOR HAS BEEN DELETED FROM MONITORING
- ~* DESCRIPTION OF VARIABLES **~
AVG TEM VOLUMETRICALLYWEIGHTED TEMPERATURE AVG PRE AVERAGE PRESSURE VAP PRE VOLUMETRICALLYWEIGHTED VAPOR PRESSURE.
LEA COM FIRST ORDER COMPUTED LEAK RATE LEA TRA STATISTICAL TOTAL TIME LEAK RATE LEA SIM SIMPLE TOTAL TIME LEAK RATE ERROR STATISTICAL TOTAL TIME LEAK RATE ERROR
OBSERVATION NVNBER
'
2 3 . 4 . 6 7 8 9 10 11 12 . 13 14 15 16 17 18 19 4.650 COMPUTED LERN RRTES X X RELRTI YE STATISTICAL TOTAL TIME LEAK RATE TO LIMITS 2 393 MAXIMUM OESIGN LEAK RRTE NRC'TECHNICAL SPECIFICATION LIMIT INSTRUMENT ERROR LIMIT REDUCTION COMPUTED FIRST ORDER EQUATION -FIT 1.336 C3 le X . X
-0.321
-1 978 CL '3 ul -3.635 0
I
-S.292
-6.S4S
-8.606
-10.263
-11.920 0 30 60 90 120 150 180 210 240 270 TINE IN MINUTES
1
~
OBSE RTION NUMBER 0.64OO 1 2 3 4 5 6 7 8 9 10 li 12 13 14 15 16 17 18 lq CONPUTEO LERK RRTE F'IT RELRTIVE TO LIMITS HAXIMUH DESIGN LEAK RATE 0.5830 NRC >ECHRICAL SPECIF ICATION L IHI r INSTRUMENT ERROR LIMIT REDUCTION CONPUTEO FIRST ORDER EQUATION FIT
-
~~ -
0-5260 C3 uJ 0.469G 0 41:20 CC')
0.3550 l
G 2950 0.2410 0.1840 0.1270 a R s x x 0 0700 I
30 60 120 180 210 . 240 270 TINE Thl MINUTES
N 0 OBSER ATION NUMBER 1 2 3 4 5 6 7 8 9 =.
10 11 12 13 14 15 16 17 18 19 0.2200 CONPLITED FIT RELRTI VE TD CR IT I CRL LIMIT X X SIMPLE TOTAL TIME. LEAK RATE 0.2030 INSTRUMENT ERROR LIMIT REOUCTION COMPUTEO FIRST OROER EQUATION FIT
- 0. 1860. X 0.1690 ca
>- 0.1520 O
X X ul 0. 1350 X X g x X S l
0.1180 O.1Oia 0.0840 0 0670 0.0500 30 60 90 120 150 180 210 240. 270 TIME IN MINUTES
l DBSER RT IDN NUI1BER 1 2 3 4 5 6 7 8 ., 9 10 11 12 13 14'S '16 17 18 19 84.60 VQLUMETR I CRLLY NE I DHTED CONTAINMENT TEMPERATURE 84.58 84.56 84.54 84.52 84.50 r 'k 84.48 84.46 84 44 84-42 84.40 I 0 ~
60 90 120 150 180 210 240 270 TINE IN MINUTES
OBSERVATION NUMBER 2 3 -4 5 6 7 8 9 10 II 12 13 14 15 16 17 18 19 41.870 RVERRGE CDNTRINNENT PRESSURE 41.869 41.868 41.867 (0
Q z 41.866 hl lK 41.865 41.865 41.864 4,1 863 R r 41.862 41.861 0 120 150 180 210 240 270 T I ME IN MINUTES
I' OBSERVRT ION NUMBER 2 3 4 5 6 7 8 9 10 11 12 13 14 )5 16 17 18 19 0.4200 VDLUNETR I CRLL Y WEIGHTED VRPQR PRESSURE 0.4190 0.4180'Z Ol 0.4170 w 0.4160 0 '150 Q
0.4140 0.4130 0.4120 N h
0.4110 0.4100 30 60 90 120 150 180 210 240 270 TIME IN MINUTES
VARIABLE TABLE
SUMMARY
SAMPLE DELTA AVG. TEM AVG. PRE VAP. PRE LEAK COM LEAK TRA ERROR(T)
NUMBER MINS DEG. F PSIA PSIA PER CENT PER CENT PER CENT 1 0 84.481 41.869 0.412 0.126 0.000 0.000 2 15 84.484 41.868 0.412 0.127 0.185 0.000 3 30 84.472 41.867 0.411 0.127 -10.782 0.127 45 84.470 41.867 0.412 0.128 -3.951 0.061 5 60 41.866 0.412 0,128 -1.543 0.026 84.472'4.483 6 75 41.866 0.412 0.129 0.065 0.000 7 90 84.486 41.865 0.412 0.130 0.646 0.007 8 105 84.476 41.865 0.412 0.130 0.344 0.002 9 120 84.483 41.865 0.412 0.131 0.313 0.002 10 135 84.476 41.864 0.412 0.131 0.127 0.000 11 150 84.481 41.864 0.412 0.132 0.133 0.000 12 165 84.490 41.864 0.413 0.132 0.159 0.000 13 180 84.496 41.864 0.413 0.133 0.183 0.001 14 195 84 487 41.863 0.413 0.133 0.140 0.000 15 210 84.493 41.863 0.413 0.134 0.145 0.000 16 225 84.500 41.862 0.413 0.134 0.163 0.000 17 240 84.500 41.862 0.413 0.135 0.159 0.000 18 255 84.506 41.862 0.413 0.136 0.166 0.001 19 270 84.514 41.862 0.413 0.136 0.179 0.002 END OF TABLE
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 1 TEMP 2 TEMP 3 TEMP 4 TEMP 5 TEMP 6 NUMBER MINS DEG. F DEG. F DEG., F DEG. F DEG. F DEG. F 1 0 84.150 84.620 84.720 0.000 84.390 84.710 2 15 84.180 84.600 84.720 0.000 84.420 84.730 3 30 84.160 84.590
"
84.720 0.000 84.420 84.710 45 84.160 84.580 84.710 0.000 84.420 84.750 5 60 84.160 84.590 84.710 0.000 84.410 84.740 6 75 84.180 84.600 84.710 0.000 84.410 84.720 7 90 84.170 84.610 84.720 0.000 84.410 84.810 8 105 84.170 84.590 84.720 0.000 84.400 84.710 9 120 84.180 84.590 84.720 0.000 84.410 84.780 10 135 84.170 84.580 84.720 0.000 84.420 84.740 ll 150 84.170 84.590 84.720 84.720 0.000 0.000 84 420 84.430 84.750 84.790 12 165 84.170 84.610 13 180 84.180 84.620 84.710 0.000 84.430 84.790 14 195 84.170 84.600 84.720 0.000 84.440 84.760 15 210 84.180 84.610 84.720 0.000 84.420 84.700 16 225 84.200 84.600 84.730 0.000 84.430 84.800 17 240 84.180 84.620 84.720 0.000 84 450 84.740 18 255 84.210 84.610 84.740 0.000 84.440 84.770 f9 270 84.200 84.630 84.730 0.000 84.460 84.830 END OF TABLE
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 TEMP 12 NUMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 0 84.800 84.710 85.270 85.030 84.750 84.340 2 15 84,810 84.700 85.270 85.030 84.750 84.320 3 30 84.790 84'.710 85.260 85.020 84.760 84.300 4 45 84.790 84.720 85.250 85.020 84.770 84.320 5 60 84.820 84.710 85.260 85.020 84.750 84.320 6 75 84.790 84.690 85.280 85.010 84.760 84.330 7 90 84.800 84.690 85.260 85.010 84.780 84.340 8 105 84.800 84.700 85.280 85.030 84.770 84.340 9 120 84.820 84.700 85.280 85.020 84.770 84.340 10 135 84.780 84.690 85.280 85.030 84.780 84.340 11 150 84.800 84.710 85.260 85.040 84.780 84.350 12 165 84.800 84.690 85.260 85.060 84.770 84.360 13 180 84.800 84.720 85.270 85.050 84.760 84.340 14 195 84.800 84.710 85.290 85.040 84.780 84.330 15 210 84.820 84.720 85.250 85.040 84.780 84.330 16 225 84.810 84.710 85.290 85.050 84.780 84.360 17 240 84.830 84.720 85.290 85.050 84.790 84.360 18 255 84.800 84.720 85.270 85.060 84.800 =
84.350 19 270 84.810 84.720 85.290 85.050 84.790 84.360 END OF TABLE 7
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 13 TEMP 14 TEMP 15 TEMP 16 TEMP 17 TEMP 18 NUMBER MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 0 84.520 84.430 84.890 84.150 84.180 85.110 2 15 84.530 84.440 84.890 84.140 84.190 85.100 3 30 84.520 84.430 84.880 84.150 84.170 85.110 4 45 84.530 84.460 s4.eso 84.140 84.180 85.090 5 60 84.520 84.430 84.870 84.140 84.160 85.100 6 75 84.520 84 460 84.880 84.130 84.190 85.100 7 90 84.500 84.460 84.880 84.140 84.190 85.110 8 105 84.510 84.460 84.880 84.140 84.140 85.100 9 120 84.510 84 460 84.SSO 84.140 84.190 85.110 10 135 84.530 84.460 84.880 84.150 84.190 85.100 ll 150 84.540 84.480 84.890 84.150 84.190 85.110 12 165 84.530 84.470 84.880 84.150 84.210 85.110 13 180 84.520 84.47Q 84.880 84.150 84.210 85.100 14 195 84.550 84.480 84.890 84.160 84.210 85.110 15 210 84.550 84.490 84.890 84.160 84.200 85.120 16 225 84.540 84.500 84.890 84.170 84.220 85.130 17 240 84.540 84.500 84.890 84.170 84.210 85.130 18 255 84.570 84.490 84.890 84.160 84.220 85.110 19 270 84.570 84.510 84.900 84.190 84.230 85.130 END OF TABLE
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 19 TEMP 20 PRES 1 HUM 1 HUM 2 HUM 3 NUMBER MINS DEG. F DEG. F PSIA FRACTION FRACTION FRACTION 1 0 84.720 84.430 41.869 0.732 0.681 0.679 2 15 84.710 84.430 41.868 0.732 0.682 0.679 3 30 84.700 84.420 41.867 0.733 0.681 0.680 45 84.700 84.430 41.867 0.733 0.682 0.680 5 60 84.690 84.440 41.866 '0.733 0.682 0.680 6 75 84.700 84.470 41.866 0.733 0.682 0.680 7 90 84.720 84.460 41.865 0.733 0.682 0.680 8 105 84.680 84.440 41.865 0.733 0.681 0.680 9 120 84.700 84.490 41.865 0.733 0.683 0.680 10 135 84.730 84.490 41.864 0.733 0.682 0.681 11 150 84.700 84.480 41.864 0.734 0.683 0.681 12 165 84.710 84.520 41.864 0.734 0.683 0.681 13 180 84.710 84.510 41.864 0.734 0.683 0.681 14 195 84.720 84.530 41.863 0.734 0.683 0.681 15 210 84.700 84.570 41.863 0.734 0.684 0.681 16 225 84.730 84.530 41.862 0.734 0.683 0.681 17 240 84.740 84.540 41.862 0.734 0.683 0.681 18 255 84.720 84.560 41.862 0.734 0.683 0.681 19 270 84.730, 84.550 41.862 0.735 0.684 0.681 END OF TABLE
VARIABLE TABLE
SUMMARY
SAMPLE DELTA HUM 4 HUM 5 HUM 6 NUMBER MINS FRACTION FRACTION FRACTION 1 0 0.706 0.710 0.722 2 15 0.706 0.709 0.722 3 30 0.706 0.710 0.723 ~
45 0.706 0.710 0.722 5 60 0.706 0.710 0.723 6 75 0.706 0.710 0.723 7 90 0.706 0.710 0.723 8 105 0.707 0.710 0.723 9 120 0.706 0.711 0.723 10 135 0.707 0.710 0.723 11 150 0.707 0.711 0.723 12 165 0.707 0.711 0.723 13 180 0.707 0.711 0.723 14 195 0.707 0.711 0.723 15 210 0.707 0.711 0.723 16 225 0.707 0.711 0.724 17 240 0.707 0.711 0.723 18 255 0.707 0.711 0.724 19 270 0.707 0.712 0.724 END OF TABLE END OF COMPUTER REPORT ON CONTAINMENT LEAK RATE TEST TO NRC
APPENDlX 8 Operating Procedure No. 13100.1 1nte eted Lealc Rate Te"-t
1'LORIDA POWER 6 LIGHT COMPANY TURKEY POINT NUCLEAR POWER STATION UNIT NO. 3 OPERATING PROCEDURE NO. 13100.1 INTEGRATED LEAK RATE TEST Prepared for; FLORIDA POWER 6r LIGHT COMPANY Prepared by; William D, Roman EBASCO SERVICES INCORPORATED Plant Operations & Betterment Department November 1, 1975
PLOIIXDA POHEI< & LXGIIT COHPANX Tt)I<KEX POXNT UHXT HO. 3 OPEIIArXNG PROCEDURE 13100.1 NOVEHIA'El<~3. 1975 .
1.0 Title
~
XHTEGRATED LEAK RATE TEST 2.0 ~I~ royal and LisL of Effective Page:
2.1 ~drove 1 Revisited by p ".at Nuc dear SafeLy W~r,,,
Cosmittce/gidrz~'~r PlauL Supt.,+aam~~i-
)y 19,7~>
19z~~i
'Approved by Change DaLa1(
y
.,cvielled by PRSC 8:..~.
'9 App1ovcd by Plant Supt:., 19 2.2 List oi Effects~ye Pa es:
~Pa 'e Dat:e/Rev. ~Pa e Dat:e/Rev. Pape Date/Rev.
1 13./1/75 8 ll/3/75 App. C 11/3./75 2 11/3./75 9 ll/1/75 App. D lz/1/75 3 ll/1/75 10 ll/1/75 App. 1: 1'3 /75 Il 11/1/75 13./1/75 ll ll/3./75 App.
G 1'pp.
13 /3 /75 11/1/75 5
6 U./1/75 App. A ll/1/75 7 ll/1/75 App. P ll/1/I5 3.0 1't~>r.os<.;
Tne pul pose of his tes't 3s t 0 assu1 e t hest leal.clgc tl) . oul h t'e j)1'im "y L
xc lci:01 contaiD".icnt and sys t:clIls anc..ollll)vn 'll'Ls p net:). l 3.n'hc p):imax'y 9
containmcnt does not exceed the allo!rabl lea~age rate values at specified in. Technical Specification, section ~I.~.l and 3.001 R50, Appcndi)c J.
3.1 . I:.ethod and Dl...cussion of TesL Techniques
'he Xut:egratcd Lealc 1<ate Test "hall be performed by thc. Absolute method by lrhich tile actua). mass of conta3.ncd ai): is calculated As a funct:i.on nf t1me.
3.1.1 Cox').'obol.'a L'3.on ol. I'lcasu1 clllcnt Provisions shall bc made l:it:I!in this t:cst lych(d):(.by thc lealc rate mens(!):Cmcnts sha).l be validated indcpcndcntly by I:hc use of a Controlled Leal(agc Rate Tc" t: (CLRT).
This validation shal.l be pcrinrmcd foz a t'uffici.cnt duration to accu):ately..cst:ab) ish validat:inn fol.).cluing t:he mcasuremcnts at: PL. At t:hc cn(l of t: he ovcx '1). test, statistical 'alys. " of I:hc LOLil3. tillle lealc ):(lt'0 sha3.1
'ea pc1foai)ed.
11-1 "75 OPHRATXWG PROCEDURE 13100.1, PAGE 2 X1'TEG1NTED LEAl: RATE TEST 3.1.2 Test Com utations Thc equations used in tin s test procedure may be found in ORNL NSXC 28> "TesLing of. Containment Systems used wit:h Light-ifatex-Ccoled Power Re <ctors>> (i ratik C.
Zapp) as well as in the "Proposed St:andard for Leakage Rate Testing of Cont:ainment: Structures," ANS Standards Committee, October 1970. Basically the leak rate of a volume may be comput:ed by watching the .test prcssure decay, while at t: he same t:ime, compensating for any changes in temperature and humidity. Thus t: he leak-rat:e (L) becomes; L%=2(<
" ( 1>>
Qt fl ( 2 << ~ '7) ) (100, whore T2 (Pl - i<1)
Tl = Temperature (Rankinc-) at: Lp, weighted average, TQmpcl IL'Ure (R81Ik" ne) at t wQ) tdl ted average Pl = Pressure> psia> at 'Lp~
P2 Pl essule psia >
~ a L'l I
= l<atcr v"por partial pressure at t:0, psia H2
= Hater vapor part a'ressure aL t~, psi'nd C
(tl t p) hoU 8 0 J: tes t: duration L(%) = Percent mass leak rate comput:ed ovc L'he durat:ion of t: he L'esL' sample sheet: marked POR XVIORi'1ATXO>t Ohi'IY may be.
used for manual calculations a>>d i" attached to this l roceduI Q Refer t:o ht pen Iiz 1 DiscreLe t:emperaturc and humidit:y elements shall be placed t:hroughout t:hc containment:, each plac< d spa-tially wit!Iin a calculated fractional volume The ~
temper..t:urc, li, therefore, will bc the weit,lIted average:
A
~total Vi ~ Xncrcmental volume <<t T, an '1 495 800 0. 320 VT T>aaE,OGO T2 ~ 0.3620 wher.e, VT2 559 ~786 0.362 VT 1,550,000 V].'q T8 T3 t:hru T8 = 0.0200
'llere VT 187 4553 1,550,0CO 0,120 e n T9 thru 20 = 0.0165 where, VT9 90 3C6. BCil 0.198 VT 1,550,00C Vital 3.. OOOO
= 0.3200 ]rhero> v~1 -- 495800 = 0.3200 VX 1,550,0]00 VP2 =- O.r']820 wh<.re, ~1~2 747 339 = 0.4820 VT 1,550,000 3 Lh1u VP6- 0 00 5,r']ere V.rp~V)'c,. 30 (51 = 0. 1980 VT 3., 550, 00<]
3.1.3 Statistic..l l!andling of Test Dat a Tntal '.- 1.0000 Least squares .nalysis of thc leal< rate calculat:ion." ]ril3. p:ovide th<. best linear regression fit to the data for the duxat.icn of th t..st perio<1. The effect of inst'xunent: c"ror on tot;al-time leal< rat:e anti statistica3, leak rate shall be computed st]ch that t: he resultant: 3oa~ rate inclu<!ing 'i is possible error shall have a confi.dcn"e level of 95%.
4;0 Procautio]]s and 'J,i]nits:
4,1 The primary containmont ]adust be p).'ossurizcd wiLh a'r of ..uch qua3.ity (oil and l]u]nidity) that it can b done safely with thc 3oast negative influence on the progress of t;ho t:ost, Thc air. shool<i be Ui3.-free and should bo cooled with an 'afLcrcoolcr to approximat:cly 80P to 85P.
4.2 Thc air. in the contuinmcnt should be circulated sue!] t:hat t: he pres<<
ence of absolutely st:agnant: air can bo p):ctront ud. lkxe it is i]]portent t:hat: tho energy given to tho circ]]lating air is mi]]i]nal.
A f<'.tr ho).sepowcr ale all L'ht]L'r('] le<!Oiled ) 0 nn)1'c tile.l th].ec l]orsc-powcr shall suffice. Thc reason for thi... is to maintain a nearly adiabat:ic condi(:icn of th<: co>>tainmcnt: environment: once t'no t<]st is started. Thc less energy i>>t:rotluccd, t:hrxcforc, thc smallc1 tho u]]ccr taint.y in t ho 1 Qsul t:ing mens.]re]]]cut:s .
in tc]npo).attire (:uch as cot]3d bo produced by l.a): t',o fa]]:;) ]naslet] t: he leal<, rat:o ~ <<t1%, ~ ~ .'L L ~
11 1 75 OPHRATXNG PROCHD!JRH 13100.1, PAGE 4
~
.. XN3.'HGRATHD LEAK RATH TEST NOTE'ny ian placed in t: he contai!>ment must pump air of density up to approximately three Limes greatez Lhan standard condit:iona; modificat:ions, either i.n supply volt:age ox blade size/pitch nlay be r. quixed.
Once 25 psig (PL) is achi.eved, appx'cximatelyfour (4) hour" 'hould be allot:Led for. stabilization of t:cmperat:ure. Conditions l~ould normally be considered stable when the avera e 't:erlperature does not: vary by more than 1.0P pex hour foz the last two (2) ilo<<lrs.
Access azound t:hc periphery of t:he containmcrt sho:lid be limi.ted Lo approximntC:ly 100 iecL during perio of pzessur'ration.
These areas should be po ted during these pexioc'.s and limiLcd t:o authorized personnel only <<!s determined by t: he Lead Test L'ngincer.
Those areas <lo not: i.nclud thc Fuel llandling 33uil<ling, R'acLor Auxi.liary Building (except electrical and nlechanical pcneiraLion
).ooms), and any elevation above ground leve3..
<'1.5 Xf a containnlent entry is required prior Lo 14.3 psi,, cowpctcu!t medical personnel sha13. be avai.lablc. No per<<'o:lnel. shall bc allowed to enter the cor.tainslenL above 1~1.3 p"i<< ithout: conforming 1 t:o U,S, Navy Diving !lanual, NAVS!!XPS, 250-538, January 1<359, s 'L ipu 1 a t; ious ~
4.G All systems <<!sscciated <7ith the conLainmcnt nnlsL'e aligned as zeruirea by the Contairnnent Xsolati.on Signal (CXS). All boun<lazy valves shall ba closed. Any block v'1)e 1)hich could prevent: a conL'ainmerlt: isolation valve. from b.. n<<<<sub';cct:ed to containfncl)t.
aix pressure shall be left: open, Tnc. posiLion of thc .a1ves
.shall be per hpp ndix A ..Closure of containnl nt iso3.atinu valves shall be acccn>pi shed by normal operation an<'. ")ithout <<ny pxc-linlinary exercising or adjustme>1ts (e.g., no L'igllf:ening nf: va3vcs aitcr closure by valve mot:or).
~ 4.7 All prcsslllc-danragcable equipnlcnt should be rcmove:d from thc contain!ncnt or vent:ed. NOT included is an> inst)."~mentation associated viLh contaill>nillt iso1.<<.tien ol !lloniL'oring of acci<lcnt conditions. Rcnloved equipmei~t slrall oc properly stored. Xnciu<1cd Would be L'he folloÃing;
~Hui. nient Protect:ion Reactor VcnL0 Cont:<<1 nnlcnL Prcssurizcr Vent to Contain!nant Prcssurixcr Relief Tanlc VcnL'o Cent)<).nlllcn t Reactor Coolant: Drain Tanlc Vent Lo Contailznent Steilm Gener<<L'oz Snubl)cr VenL'o Co!1L"lin)ncnt 0$ .1 3!cscvoir (if required)
Polar Crane liydraulic Reservoir Vcllt: Lo Co!it:ainmc:lt and ('car Boxes (ii re<I'ui.re<i)
OPHRATXNG PROCEDURE 13100.1, PAG)'. 5 XHT)':GRATE)) LHAK RATE TEST 11-1-7
~H< ui >mani: Prot:ec Lion Hanipulator Crane Gear Vent t:o ConLainment Boxes (if required)
Nitrogen, Argon, Oxygen/ Remove from Cont:ainm nt:
Acetylene, (etc.)
BoLt:les Pire HxLinguishers Remove from Cont:ainmcnt Wooden Scaffolding Remove from Containment Refueling ))achinc
)?quip rent:
TV Honitor Remove fron Containment (if required)
Posit:ion Readout: Unit:s Remove from Contain!nent (if required)
Dillon Load Heters and Remove fro Cont:a i nmer n t:
Power. Supply (if required)
~!.7,1 All instrument:s locaL'ed inside the containn!cnt s)lould be chcclced a>>d properly vented, if recessary, inorder Lo prevent damage. Refer. to Appendix ).'.
l>.8 All .wood plat'forms and wood sraffo)ding should be rcravcd. Thc porous naLure of wood will coriplicate the I'est and !nay abort i.t.
Any water standing on floors, in low spots, in open piping and in tall)adage should be removed Qs re;)uir d and the <<rcas lef t <.ry.
The success of t: he test depends also on t>>e changes in humidiLy during the test:. These efforts will tend t:o stabili::e the relative h !>idity.
4,10 Open vents or drains as shown in Appendix )< L'o sinn! 0'to those conditions that would be expccLcd durirg a LOCA. A).l vented sysL'cns shall be drained of'ater to assure ex))o"urc of thc cnntainntent isolation valves t:o conLain:ncnt ai.r. prc..sure.
4.13. Cher)> prope" insLallation of pressuri-.ing system 'and blowdowa piping wi.thout opening inlet: v"lve at pe!teLration.
~ ~
11 1 75 OPHIQTXHG PROCEDORE 13100.1, I'AGE 6 XNTEGIIATED LEAI'ATE T]'.ST'.12 Checlc that: the oil and moist:ure cont:eat of the air do'mstream of the iilLers and t:emperature are saLisiactory. Air qualit:y may be checlccd by discharging a quantity~ of air on a piece of white cloth or paper at: a convenient: vent or drain connection.
4.13 GI)eclc Lhat insL'allat:ion and calibraLion oi inst:rumantation for t: he XLRT is complet:ed and properly documented.
4.14 Xnsp"ct:, close> and seal personnel and emergency air loclc inner anti out:er doors.
4.15 All electrical equipm"=nt shoulcl be de-energized within the cont:ainmant except for those services required and power requirement:s for circulat:ing fans. Rcf<< t>>ppe>>dix G
- 4. 16 A general inspection oi the accessible int:erior and ext:erior surface of tl.c containmenL structures and cobra)poncnts has been satisfacLorily.performed with no cvid'nce of strucL'ural dct;er-oration thaL may afiecL'ontainment struct<.lal. inLegrity or lealc- Ligh tncs.
- 4. 17 A dcslc calculaLor. or cquivalenL insLrtU<tant shal.l bc available in the unlilcely event: t:hat: t: he corn]);<ters; phone connections):. or terminals are inoperable. I<sc the d..t.a sheet: in hnr)cndix
'4.18 The Local Lealc Rat:e Tcs<'s should be coo)pleted.
5 0 Relaied S~~ste<)! S<tat:us:
5.1 The following instrumentaLion or equivalent are required for Lhe Xntegrated Le..lc Rate Test: nd are recently calibraL'cd and properly document:ed:
XTE':I NI]HB].'I< DH SCRX I'TItlN TX"1, 1 Temperature Honitori). 6 'ln]icaLii>-,'lys Lem-consi"Lin" of 0 (3 spa"e ) sc:nsor ,
selecL'or svitc]res, con La<)< curt<<nt supply and digitt!l inclicaL'or systrm accuracy of Oo 2 )' Leeds & Nortltrup ins I:runlcu tat).on utilizing 100 o!lm cop])c'). Lhc:mo]a<is >
Cat:alog 8197-10-S. ('atnlog No. 900-9999-9999-1"S numatron num<<ic display.
PX-lA 1 . Plots~ Nr.Lcr - Brooks lli-accur;!cy full vier'
).'otomr L'cr, Hodcl 1110 Range 0-10 scfm 25 ps'xl > 70 I' ~
OP!:ItATXNG PROCED'JRE 13100.1, PAGE 7 XNTEGIULTED LEAI ltATE TES T XTEN NtIHHER DESCRXPTXOIC Devpoint Temperature Xndicator - 6 (2 spares) de(rt)oint reading, Pan e -10oC Lo
+40oC, accuracy of + 1/ full scale, sensitivity of 0.1%. PanameLrics.Hodel 1101 Precision Prcssure Gaupe <<
(1) Rea<lout unit, c libraLion accuracy of 0,015% of reading, xesolution 0.001% full scale, reado t 100,000 counts=full scale.
(2) Absolute pressure capsule-a) Ruupe 0-49 psi b) R&n;ce 0-100 p 1 Texas Xnst:rumcnL liodel 145 PX" 2 2 Pressure C~.!u~e - R n"c 0-100 psi&,
graduation 0 1 psia accllracy 0. 1/ full scale, se:!si~ ivity 0.01/ full scale.
leal.lace 6 Ticrnan 'iodcl >:61A-1A-0100.
5.2 The daL'a for. t:his test: shall be manually acquired irom the X],RT cabinet containing the instrumentation liste<! above. Ti!ese dat:a shall be entered into the ILRT'comj)uter. prop.am uti;i;;i>>f, a Tc>;as Xnstrument: 700 terminal or. equivalent. The computer generate<1 report
'nd assiciat:ed data shall be apjcnclcd to and form a part of this proccclure.
5.3 'J."nrougho;!L thc t:est:, temperatures, prcssure au<1 vapor. pressuxe are monitored. Ti!ese d'-!La arc Use< t:0 comput:<'he le.k late from the perfect: gas law, PV=nRT, using eit.her the point-to->>oint method or, thc toLal.-t:im m t:hod. Leak rat:c prc:dict.iona an<1 estimates of error ax<'- j)rovidc:1 by first order. linear regression over the test: dux&Lion nominally of 2'. hours. Further, thc seu83.t3 vl.Ly t:0 sensol in<!ccu!.<lcy 1. comp!! t cd a !d Lhc final Ii~1(C report: should dcmonsLrat:c t:h&L the t:cst has mc:t t.'.!e minimum allowable NRC lcalca<,"c vat:cs vitltin statisL'ical error bo.!>><is.
5.4. Cont&i>>ment IIVAC syst: em shoul<l bc avail(!blc t:o maint:ain a temp rat>>re oi not higher than 90 P or. lover t:hau 80 E within Lhe containment. Thi t:cmperatuxc vaaj",c should bc maint:aine<I, if'possible, for. a matt;cx of clay before t:hc bc~inninc; of thc XLRT. A pux"e p viocl may b<!,p<;rfovmed 4>hereby Lhc i>>it:ial volume of "moi: t" containment air. is replace(1!rith "dri(!v." aix priox'Lo actual XLRT prcssur3.Nation ~
OPEINTXNG PROCEDURE 13100.3., PAGE 8 XNTEGRATED L:.A!i I(ATE TE.">T ShorLly before tl>e-XLRT, the Containment I!VAC systc~ is t:o be shutdown and isolat:ed from it:s electrical and cooling vater supply 5.6 The react:or shall be in a cold shut-dotjn condition.
5.7 The following pressuriration and support equipment or equivalenL are required for t: he Xntegrated Lealc Rat:e Test:
I:pointment Ottantitv C~oacil:> Mode". Iio.
Aftercooler 2 5000 SC!~)I/ea. GT A?00 (American St:d.)
'Ccn'rifugal Moisture 5000 SCBI/ea, GT Separator.
(Am rican S Ld. )
Mechanical S cpa r . tor.
.(Coale cent Oil Separat:or, 2 6503 SC;II/ea. S10 A30 for oil type compres ors only)
Air. Dri'cr - Chiller 1 3800 SGFH NC-3800 (Application Engr.) 1 ~>800 SCF!'I Air Coml> esscrs (Atlas-Copco) 7 900 SCrrI/ea. PT-900 1310!v'cr.s (Coppus) 6 1500 SC!3l/ca. IIXT"3050-18 5.8 Valve line-up, as delineated in Anpeni~ix A> shall be comolctcd.
6e0 References; Tnc principal guides foi. th preparaLion nf Lhi t:c: t: procec'<<!rc vrcrc t: he 10 Ci'R pa': 50 and tltc American National Standard documcnL out:-
lining the metl>ods for 1calc-rate t sting. 0th rs vere consulted, in addit:ion; 6.1 "Leal<age Ra,tc Testing oi. Containment Street<<tres for Nuclear.
!reactors" American Naticnal Standard ANSX N!'I5.~< - 1972.
' "Primary Reactor Cont'nment Leakage Test: << for Pater-Cooled 6
Po;ver RcacLors" Appendix J. Title 10Ii gPant 50.
6.3 "Tc, L'ing Containment Syst:cms used vitlt Liglit:-Natcr-Cooled Power React:or.." Prank Za!>p, ct al., 0I',NL - NSXC " 26 UC - 80 RcacL'or Tcclrnolcgy.
l 6.4 Turl'cy PoinL'lanL'nit No, 3 Tecltnical Sp cific!Lions.
OPHRATXNG PROCEDURE 13100.1, PAGE 9 XNTHGRhTHD LHM RhTH'TEST 6.5 llechtel Corporation preopcrational test procedure and final report for Xnit:ial XnLegraLed Leak RaL'c Test: of the Reactor, Containment Building.
7.0 Records Recptired:
7.1 Cttrrent X & C calibraLion sheets for all instrum ntation li"Led in secLion 5.1.
7.2 A dated log oi'vents and pert:inent observaLions shall be maintained during t: he Lest, 7.3 Complet:ed XLRT procedure> Lest log and daL'a shccLs constitut:c, quality assurance records and,. therefore, shall l>e routed t:o the Technical Supervisor for review> and routing to t:hc Quality Cont:rol Surveillance Technician in accordance with Admini. trative Procedure 0190.16, Sched.!ling and Surveillance of Periodic "'ests and Cnecks Required by Teel!nical Specifications, and shall l>e rct:aincd in accordance with AdminisLrative Pro"edurc 0190.1~)
Do"umenL Control and Q.!ality Assurance Records.
8.0 Xns tructi.cns:
8.1 PrecauLions and Li!)!its and Rcl".tcd Sy tc"! Status (sections l!.O and 5,0, rcsl>cctivcly) have b en satisfrctn):ily col!pleL'cd.
'vaxHied by gg~<$~t~~))g nato )f->G.')A 8 Start pressurization and continue to'pressurize unLil contain-ment. air pressu).c reaches 25.0 psig t. 3 psig, -0 psig. Honitor every half hour physical para'!"t:crs as outlined i!) "lLRT Data Shert". lla>tim!!m pressu",ization ra,L'c should bc t:o 6 ps'/hr.
-'<
D.ll ing pres Qul iza t i.oil:
8.2.1 Haint:ain moi.store and oil content as lov as possible.
8.2.2 Haintain containmcnt text>cratu):e above 60l'nd belotI 120P.
8.2.3 Cneck for leal;s.
Xl'! any case> the pl psig for. t:hc tluration
"'rc should not fall below of thi.. test.
25 ~ 0 Yerified byg~g ~i~)g Data 'l) Z9 >5
OPERATXNG PROCEDURE 13100.1, PAGE 10 XHTEGRATFD TiEAti RATE 'J.'EST 8.3 The folio:ring shall be monit:orcd during Lhc pressurizaL'ion phase of thc t:est.
8.3. 1 Containment inlet air tctmperat ure.
Verified by t. 0 te ll" ZW "75 8.lt !~hen desired pressure is achieveD, isolat:e contairnn~rt pressuriz-ing sysLem and leak check the pressurizing system valves.
Verified by < Date tl"Z.% 7S 8,5 Using ulirasonic leak detect:ors and/or soap solut:ion, checl Lhe condit:ion of each suspect lo"al 'exterior 7eak ar a.
leak test measurement for u pact leaks ii required and Perform'ocal records Verified by ~ )ate lI- 5P.7 8.6 Record daLa as out7.inc:d belo:;~ in Appendix D <<min>.. um of once every one (1) hour, lio rep lira arc a17.o:.e< once. t.tc XLI;T commence 4iLhout: returning t:0 this po" nL' 8.6.1 Sample number Q i4:
8,6.2 Date and tin>e 8.6.3 Dat:a 1.ogger s name G.6.'t Cont:ainment Lcmperat:urc. - 20 3..6.5 Cont:airnn'nL vapor pressure - 6
'.6.6 Containn:rnt pres urc. - 1 8.6.7 Outside atmospl>eric Lctnp'aturc: - 1 8.6.8 Outsi<le. atinospI>eric p> .ssure anu/rr relative htmudity- 1
~ I 8.7 J.'ro>> tlte data gaLhcrcd on an'hourly basi.s, dctrrminr that::
8.7.1 Titc cont:ainineut conditions are st:a~ilizcd and tron<'s are p).cdictablc ~
Verified b.' ~< Dat:c:
8.7.2 Eorccast:cd leal: rate i'ignificant:ly bet:tcr tl>an allowable limiL's. Pcrfornt local 1c;tlc survey. Stabiliza-t:inn should tal'c approximately foul. (~:) hours, Verified by D;:tc 0I9
OPERATXNG PROCEDURE 13100+1, PAGE 9 XNTEG}@TED LEAK Rh.'LT; TEST 6.5echtel Corporat:ion preoperational Lest: procedure and final report: for Xnit:ial Xntegrat:ed Leak RaLe Test of the React:oz Cont:ainment Puilding. 7.0 Records Required:
7.1 Current
X 6 C calibration sheet:s for all instrument:at:ion li.st:ed in sect:ion 5.1. 7.2 A clat:ed log of evenLs and perti.nent observat:ions 'shall be, mainLained during t: he test. 7.3 Complet:ed XLBT procedure, t:est log and data sheets constitute quality assurance recorcis and, therefore., shall be rout:ed to ': he Teclrnical Supe visor. for, review and routing to th Quality Cont:rol Surveillance Technician in accordance '4~iLh Aclmin:strative Procedure 0190.16, Scheduling and Surveil7.ance of Periodic Tests and Cnccks Required by Technical Specifications, and shall be reta .ned in accordance with Aciministlativc }'zoccdure 0193. 14, Document ConLzol and Quality Assurance Recorc's.
- 8. 0 Xns t:r:tc Lion.";
8.1 Precautions and Limits and Relarccl System Statu" {sc:ction 4.0 and 5,0, rc'.spectively) h ve been atisfacLorily complc-.Lc:cl. V>>'..>.j:iud l>y U p>>r> Par l>H'73 8.2 St:art: pressurizat:ion and continue to pressuri::e. un rl c ontai:.- mcnt air. pxessur reach " 25.0 psi; + 3 psig, -0 psig, Nonit:or every half ho ~r physical parameL'ers ts ouLlined 'n "ITRT Data Sheet:". Haximum pres urination rat: should bc -'t t:o 6 psi/hz. Derring pressuriza tion. 8.2.1 Haintain moist:urc anil oil content as low as possible. 8.2.2 1!aint:ain cont:ainmcnt: Lemperatuze above 601" ancl helot; 1201'. 8.2.3 Chccic for lcalcs. Xn any case, the pressure shoulc! no(: fall b low 25.0 psig for the ciurat:ion of this Lest. Verifiecl by
OPERATXNG PFOCEDVltH 13100 ~ 1 s PAGE 10 XNTEGRA'i'ED LEAK RATE TEST 8.3 The following shall be monitored during the pressurization phase of the testa 8.3.1 Cont:ainm nt inlet air.t:emperaturc. Verifi.cd by ate~ ~~) l'7$ When desired pre"sure is achieveD, i olate contairm t pressuriz-ing system and leak check the prcssuri."ing system valves. veri fied b.yoit, ~ 9< ...Junste Doe.ll')7s'
-t Using ultrasonic leek dal:ceno"s'and/or soap solution> ebeo1 Ibe con(lition of each suspect lo"al exterior. leak area. Perform lo al le'1(', test l!!Qasurcment fol suspect lcalcs. if required and record.
Verifi.ed by ~ ate ~.)> )~ I 8.6
".C ):ecor(l dat:a as outlined belo;l in Append>>:: D a mi.nimQn cf once every one (1) ho; z. 3>'o rcpai<rs are 'allo!led once thc ZLIIT commences !litho(1 t return3 ng to th3 s .po3!1 t:s 8~6~1 Sa'.llple number 8.6.2 Date and t:ime 8' ' Da1ta Logger s name 8.6.4 Cont:ainment: t:empcrat<<re - 20 8,6.5 Containm"n'apo" prc sure - 6 8.6.6 Containmcnt prcssure - 1 8 a6~7 Ou tsi(lc a tf<losphcr3.c t:c!1!pc a'ure 1 8.6.8 Outside atmospltcr3c p3.cssurc an(l/ol relative hum'dity- 1 8.7 I'zo31 t: he data gathered on a:1 hourly oasis, dctcr<mine that::
8.7al The contai!tment conditions arc stabilized and trends arc
~
pzedict:able.
'erifie by f %ieinuL<d( nate 13st I 8.7.2 leak rat:c i" signi.ficantly bcL(.(:r than
~d/s'.'orccast.cd all.oÃahlc 13!1!its. ).'crform loc:1). lc;!l. s(!rv(!y. Stabili.za-t:ion sho:tld tal(c approximately four. (d'() hour ..
,0
.OPJ'.RATXNG PROCHDJRH 13100.1, Pt GE 11
- XNTHGRATi.D L('AK RATE Ti ST Continue XLRT measurements unf:il intexpret:ed data indicates i:hat 3:he XLRT cziL'Qx'ion is met for a minimum period of tventy-Xpur (2ti) houxs in accordance Nith Appc>>dix C.
J Verified by DaL'c ~.9 ]Qg5 Once 1)zcdictable 'and alloNable t:rends have been e ablished, verify the tesL result:s by superimposing a leakage approximat:Q3.y ey>ivalent to Lt. Test: duxation shall be approximately four (t() 1>ours in le:!gth t:o verify the ability t:o m asure thc leak. Verified by ~g( Date 'i 1)~
.3 e
Xhe following sha3.1 be recorded during th ., phase . t: he t.est. 8 9.1 Cont.ainment air flo~('rotametez), 8,10 Compare the XLRT leal'aLe and vezificati.on leak raL'es, Xf '!.e comparison above indicaL'cd th;!t t.he XL]tT leak raLe is not sub-stanLiatcd by tl. verification tcsL (difference sryit>>ir( 0.25 L.) cont:inue t: he XLRT leak zat:e and rcchcclr, A'; t!>Q end of the extendedtcst: period, repeat t >c verific <Cion tc t:, if r('.q<!ized. Verified byQ~r ~d O.:ie dree,9 i!'7B
'mple conLainm- nL't Mosphere prior (.'o blow]o;"n. !>on permission f ro(11 Lead Tcs t L lgincez> opcl! bit)NdoN '! v lve and 1 clc isc air
~
izom cont:h.l.n Acnt u L iliEing a (!!axial!!:1'(( deprc sux .i'.a(:).0(. ra te of
~
'pproximat'.e'y 0 t:o 6 psiithz Yeririe" bygbrclb t b."rc Kle'-. 3 !'75 ~
~
Nhen aL(".Ospheric pressure is t(chicved, contai>>:!!Qut at:."(osp!tere shall
.be sa.((pled folloNed by containr:cnt e>>'ry and in"pection.
yare'fied byg+$ y carel)ee, g<lg"/Q Xnfozm Unclear P3ant: Supervisor tl!At: X] ttT is cc!lip.wt:Q .nd affccLQd syst:Qms and Qquipmcnt are turned-over t:o OpcraL'ions Dcpartmc>>L. verified by@(eep bd]~ly, ,'ere~ ei (R~w
- 8. 1t( The complct:cd copy ol t]tis;)roerdurc <blth Lhc da:hect(s) should ])('orvarde:1 t:o tltc Tcc]u>ical ]'epart:mcnL for review~ and handling. 1ol3.ONing review'y Lhc Technical Depart.mani:, t]>c data s]tccts shall bc scnL to tl>i: Quality Cont:rol DcpurtmenL.
Verified by .idge.itarc&C-.(.<i.(27
'7 V tk
'1 0
~ ~
IJ hPPEl<DXX A
- 11-1-75 OPLRATXNG PROCHDURH 13100.1 PAGE 1 XHTHCRATHD I,HA1( RATH THST hPPHl<DXX A DJKC'fXON VAI.VZ,"P POSXTXON RB 1 le(S v.,Rxr xHD av/DhrH To RllR ViOV"750 Open System in 110V-751 Open sezvice TC" 1 Closed duxing TC-100 Closed XI.RT
" HOV-7l;lqA Lem in 8 i( ~~-~r 1rom Rlil<
i- 0->> I'ys 1 lOV-7(JIB Open s cl'vie e 7611'pen 1'CV-605 llVC-758 Open CLGSGQ Open during 0e <~Me.g XLRT ia- L"I- 75 b +l-7 Closed C! Tw(; 6O CGC L'o RC'"s 737 NA Clleclc V've
.
i-O'- s 7l6H HOV 716A Open Closed n=iS'-
'1 lOV-7169 Closed <<3'Cp l,l-< I->4 716D Closed $ l-P.'1-a s 716C Open g( - i I -wl-'1 o CCll l'rom RCP's fOV-730 Clo cd , 7.Z-~S 1
Closed M+~x1- )S
)32'C-65 Open Pg~ -P'D7-7J 7301) Closed ~)
73GC Closed C) 730E Closed. Oper. lI"Q.l -" '! PRT L'o Gh CV-516 Clo cd 8 u-m~s 552 Closed ~ Ll->5 5171 Open fC O.- h l-7g TC-2 0-'6 - 75
'rC-80 Open Chcclc Valve !V/l!
N2 Lo PRr 518 NA I J'~ ~ '7 ~ TC" 3 Open
'rc-81 Open
ll"1"75 01'ERATXNG PjlOCEDURE 13100.1 PAGE 2 XNTEGRATED LEAK RATE TEST APPj VDXX A FONCTXOli VALVE 8 POSXTXON m jARKS VERXFXED a;."/DATE PM to Stand- CV-519A Closed 9e p3.pes CV-519B Clo ed CV-522A Closed CV-5229 Closed 5-U CV-522C Closed TC-4 Closed TC-82 Open px'~~ s S tm ~ CV-951 Closed 96 u-x~ San:pie cv-956A Closed 989A Closed C>>.i=a> 950 Open TC-5 Closed ir-g ( Tc-83 Pg~~ /l-e 7 Closed TC-85 Open -4~ -~~i-Px's o L1qU'3.d CV-953 Close J Sample CV-9568 Closed 9898 Closed 952 Open TC-6 Closed jc-86 Clo ed TC-84 Open RCDT & PRT CV-'<658A Closed VenL' N2 to CV-li658a Closed RCDT Tc-7 Closed Tc-8 pygmy Open 549- Open <j-S~q r-~a r+>>~>. 1<656 Closed <IX', q6<g TC-8/ 4!MA 54QQ<-Q ~a~ ~1 ~>n~ ~g.(
<4',pc>~~ y g.
=
<?W (D ALT. Lo!read HOV-872 Closed SXS Tc-6~i Closed TC-9 Oprwm <<~(:.g zan e;a~ Ogg. 94 ~i~a c7S< "$ 0 Ccho Excess 738 NA Clirclc Valve LTDN. !jan, 737A Closed Qy-"L t
/ Tc-10 Close<1 TC-66 Open '(
Tc-88 OjiQn 5 6-'LL
11>> 1-75 OPERATXNG PROCEDURE 13100.1 PAGE 3 XNTE'mern LrAK RATr. zrsT APPENDXX A 1~ UNCTXON VALVE If POSXTXON RLl IARICS VERxrxED BV/DATE CCI) from Excess cv-739 Closed LTDN. )DC. 737B Closed TC-11 Closed TC-09 Open ((-~1 7 e tdo(m to CV-200A Closed Repen IIX CV-200B Closed CV-200C Closed
'v-204 C'sed R4 <<-~l Tc-12 Open TC-67 Closed 87-TC-13 Closed v-).z TC-90 Open CVCS (:o RegCn, 312C NA Cl>ecic igloo/PP Valve
)K ~ ) ICV"121 Closed 4 JIM~ Closed 333 zc-u~ 4p~ CU- IOA )cgaopn 3 l2c. 'A 4A p'4 ((-J 202A Open I L LI i() TC-91 Open I4& t m iv.wvo- goal C.Cl P PACVS ) IV"3" 1 Closed 11V-3-2 Closed
)IV>>3-G Closed
~
HB + &ARM ~~'6 one
)IV-2 Open r'/'" + 7
)IV-7 Open IIV-9 Open SXS Tcs L'l.nc 895v Close(1 Tc-68 Open zc-16 Clo ed TC-92 Open SXS >IOV-866A Closed HOV-866B Closed CV-S69 Closed Tc-17 Closed . ('.p Tc-93 ten nr~t n <,OP S> S Q o~l~~]
g!SS
11-1-75 OPERATXllG PROCEINRE 13100+1 PAGE 4 XNTEGRATED LEK RATE TEST APPEI<DXX A PEN. fi 1lJNCTXON POSXTXON RHhAPZS VERXFXED BY/DATE Cont't. '890A NA ChecIc Valve Spray A HOV"800A Closed TC-18 Closed TC-94 896C 891A Closed 4pen Open
~A Cor.t t, 89QB NA Checlc Valve Spray B HOV"880B Cl.osed TC-19 Closed 896D Closed 891B .op TC-95 Open AGB Hot Leg CV-955A Closed i/- >7 Sample CV-955B Closed tl-2. 7
'CV-956C Cl.osed z/- Z-7 989C Closed i/- ~7 954A Open 954B Opc'n TC-? 0 Closed TC-96 TC-97 Closed Open ye'ir(W/ -87 CCil to HOV-1417 Closed 9~6(. i~
Coolers TC" 21 Closed %Co ~! -2.'l TC-98 Open 22 CCN frolll HOV-143.8 Cl.os ed 3@ '(k-]:] Coolers TC-99 Closed ~%~a i
. TC-101 Open 9< ~~~
23 Cont t. Sump CV-2821 ('V>>282? Closed Closed Yg].~('l.osed TC-22 TC-102 Open Valve H Open Open ].]='4 L
'PERATIIÃ: 1'ltOCEDURI'3100. 1 11-1-75 PAGE 5
~ INTEGRATED Y..EAK RATE TEST APPEIIDXX A PEN. 8 1'UNCTION VALVE fE POSXTXON RENA1'IiS VERX1'IED BY/DATE 24A Seal list'er 298A NA Checlc Valve C+-r/-Z
~
t:o RCP-A TC-23 Open Tc-103 Open 24B Seal I;at:er t:o RCP-B 298B Tc"24 Tc-104 HA Open Open Checl: Valve 94 h=L~ 24c Seal Hater 298C liA Chealth (~alve t:o RCP-C Tc-25 Open TC-105 Open RCP S.Ii, HOV-381 Closed Ret:urn Tc-26 Clos"..d Tc-106 Open 306C Open St:earn Gcncrat:or HOV"1410 Closed Blovdovn 127 C'sed W'alve A Gpe 1 HOV-1411 Closed ~-~ l 227 Closed Valve B Open 28C HOV-1412 Close.l 327 Closed Valve C Open V'.!=<'.z TC" 27 Open Tc-28 Open Tc-?9 Open 29 Xnst:. Air 336 HA Chcc<<Valve Suppl)" CV-2803 Closed Ti-58 Opcl TC-59 Closed +ZF1H " .~Z.~-< TC-107 Open /Ji .3'.Or ')~ 337A Closed 1',CDT to GA CV-4659A Closed i-L7 CV-4659B Closed 465-'< Open TC-60 Closed TC-108 Open
11 1 75 OPERA'I.'I)AC PROC)'.lXJRJ: 13100.1 PACJ" G XHTJ;CJV THD I.HAK RATH TEST
. AivrxDIx h PHJ. fP FUNCTION VAIVH 8 POSXTIOH RHNAIKS VHRXFIHD L'Y/DATE 32 Cont't. Air TC"30 Open
>>/'/-
Sample Return Chock Valve l3 lych CIleck val.v
>(- '- //- ~. V Valve J TC-31 SV" 2912 Open Closed Closed
-c .+/- u~
TC" 109 Open Cont't. Air Valve I( C //-2.7 33 Sample SV-2913 Open Closed W v-'L7 SV-2911 Closed TC"32 Close.cl 9(( TC-33 Close<i - I I-k<J
\ \ ~
gQ TC-110 Open Service Air 205 Closed 203 ETC-G9 Closed Closed jc.'- I
~
TC-3fI Closccl TC" 111 Opel I Cont'. Inlet Purge PV-2601 PV-2600 TC-35 Close<1 Closed Closed
. I;flf-) If- 1Q
-aS 9
I Cont'. PV-2603 Cl.cs ed 9iP= i( <((-
.Q 6 36 Purge Ou "let PV-260~ Cl.o se<l (( - z!(
H,-36 eloee(tl pili"q +g)uvc8, FOv'.'6<(3, 9.('(I .! (.~< 10'lI c<(c:Z <('A ki'((m< ~. 9PQ c'II+ 42 to Ac cum o llCV"936 Closed CV-853A Closed 4 ll.~~% ~ CV"U53)3 Clos <!d ll 'L1 CV-S53C Close.cl CV-S55 Close.d TC"38 C f.osed TC-50 Open )l~g7 9.g CCH irom RCP T)le1lll<ll Jlarr ie1 8 HOV"626 736 Clo: (,7
<!d o('ed J(" ggx~ il:C g')
TC-70 (:i.oo<<l LI= TC" 39 Closed ~ 1H - ~l-V/ TC-112 Op Cll << -A')
11-1-75 OPERATXl)0 Pl)00'I;03RR 7.3100.1 PAGE 7 XHTHGRATHD LEAL RATH 'I'fST APPE!IDXY A PEN. 8 rumcxzow VAT.VH 8 POSXTXON REMARKS VERXI XHD 8':/DATE 47 Primary Haec:r Valve L Closed t:o 4'ash 11eader Tc-40 Closed ChecIc Va've A NA Checlc Valve Tc-113 Open Prom RCDT Pumps CV-4668A Closed ~ e-
-
cv-4668@ . Closecl 4663A Open Open 4663'c-41 Closed I I-RK
-TC-114 Open PACVS 11V-3-3 Closed Rote: Lo 11V-3-4 Closed Pen. il 16 HV-3-5 Closed 54A Recirc.
SU)mp HOV-860A HOV-861A Closed Close
)i i7-T '-4, Closed 54m 110V" 860 Closed HOV"SG 3.17, Closed Tc-43 Close.d I I'L77 !I-ry TC" 115 ~n. 4cMR e. l I f 1<-'c r TC" 116 +pen ~~/ 4w~
0fsc "~go
~ g~-/)
Accnmula I:or 954C Open Sac>pie 954D Open 954H Open
,CV-955C Closed.
CV-955D Closed CV-955H Closed CV-956D ('1osP d TC-44 Closed 989H Open Tc"117 Open )
11-1-75 OPHRATXNG PI(OCHnVRH 13100.1 PAGE 8 XNTHGRATHD LHAK RATH THSf hPPHNMX A PUNCTXON VAI.VH 0 POSXTXON RHHAM:S VERXFXHD Bv/BATH Hi llead SXS 873A NA Check Valve
'rc-45 Open i - p-'Z7 Hi'ead SXS 8739 NA Checlc Valve TC-46 Open
~z/-Z 7 60 IIi Ilead SXS 873C ~ NA Cnecl; Valve Tc-47 Open 58/59/60 SXS IIOV-843A Closed Ilov-843m Closed rc-48 Closed t I -s'7
~
TC-49 Closed Tc"118 pp'A ) cc~>f tee-~c,
. Tc-119 Closed 9 "p i~-isc, '<60 Dead'"eigllL Valve, C Closed pc'- -il A 7 Tes L'el 'Vaive P Open lv"51 Closed T(:-120 Open I
64A SL'earn GenevaL'or 2O-307 Open SalB pl e C TC-52 Closed <<-v IIOV-1425 Closed l( 1'1 4~9~% W~ QP- ) t-2 I I 6~iB S L eilm Grnc1 a Box; 20-306 Open 'k.l.l Sample 8 Tc"53 Closed I IOV-9~26 Closed ~t'. ~i-~i Tc" 122 Open ('4C St.'enn CeneraLoz 20-305 Open
'6- L1 Sample A rc 54 (",losed A4 g 1 "l HOV"14? 7 Cio ed Tc-123
11-1-75 OPEiiATXNG PROCEl)JRE 13100.1 PAGE.9 XllTEGRATEO LEmC Rh.'>'E TEST APPHI)DXK A PEN, 8 PUHCTXOH VALVE N'OSXTX014 REHARKS VERXPXED aV/DATE Prom XLRT Valve H AS Re( U iled J-z;7 Compressor TC-55 Closed ~ p ) ll- p / ILRT Press. Open Xn service g~Q ll- g~ Sensor Line Valve 1 Open during, QqPQ TC"56 Clo cd XLRT 6 CLPT ~P ll' 65C CLRT Plow Line Op Qll Xn service TC-57 Clos eci during Valve G Open CLRT Xns L'rumen t CV-2819 Close:d Hc - I i -2. I A'r Bleed TC" 37 Clos eel e-CV"2S26 ClosccI ~p. c t ( ~) 7 P~rg-p/W/
hPPEHDXX 3 Valve Dra~si~r,ps
OPEI<ATIII<", PINCE>>ter<I;" 7.31.00.1 INTEGER TI O u.uuC IJiTI; TEST PAGE 1 APPENDIX )$ I ll-l-75 INSIDE CONTAIlBKNT OUTSIDE CONTAYHHENT t Vcm 74l D B~of L 4 7444 7d-I
I I ~ t I I J
~ ~
PhCl 3 Al?PIHDIX 8 3 l 1 75 XNS'JDE CONTATIIIKNT OUTS XDH CONTA'lNHEI!T PRT Gt78 Gfb Gf7A
~~F-I i L
OPEIUCJ.'IldU PROOEJJIJRJ J.S J.UU. J. XHTEOIViTI'.I) J,I'.hl( ll/iJ.'I;; TEST PhCE 4 APPEHJ)D( Jl 11-1-75 0 XNSXDE CONTh.XIIIJEllT OUTS XDE CONTAXJIIKNT 5!BQ ir 522.A 1
XHTJ GRA'l%:I) LJAK I&TH TJ ST PAGE 5 Al'Pl tll)1X D 11-1-75
~
t OUTS TDJ'. CONTAXNNENT DJSTDE CONTAINHKHT <~49
Om;IIATaIC; PI;OI:I'.DIII,I? 13100.1 PA(1I', 6 XxnXI:(IXI:.O >.I?AIC I<AI.I.'. XLrSr 3.1-3.-75 OU'I.'S XI)I," UOI'I'J.'A I:tNENT Al'1?I'.HDXX II n<S1DI.', CO~W.33ymT t4I7 855 D pQ,(d 855t" 788/'. 9584 7+3
'7t5 855 8 7578 rc ll 789 5 p4 rcqo tl QOI J -.'RI.-.(gent L ZOO 8
)(ZGS 8 E~'5 VV tg
OPJllATH'JO I'J(O(ll.'DJJI(J"; 13utU. L X'NTJ'CJ(hl'FD 1 1'/ I< J<ATL'.'J'ST PhGJ: 7 Al'J'J i<J)'IX JJ 11-1-75 OUTSTDE COt~TATPHFNT j ZJQP
APPf.i'IDXX 8'AGE OPl'.fATXHG PRO(::f)UfiH 1:3100. j IHTE(~ffhTED J,f'.Af; PATE Tf',ST 11-1-75 8 INSIDE CONTAXNMZNT OuTSXDE CON J.hINVEf"T 85oA, 8-5 f( lt 6~@/ 89'> P BMV 856 L 837 . 8956 869
~
$
L.Q,
OVER.TIN('ROCEDURt j.3l.uu. j D<TlXRA'i:iD 1.)!hl,'A'i'L 'i:I!'T PACE 9 APPHHDIX lh ll-l-75 INSIDE CONTAIN KNT OUTS IDH CONTAD!1%NT
- i 885 <(
0,1g 89nA, COs 5 PHhg 9 lO f+/x Cct~(At fk, LPt~ ~3<pQ A QgP 1q Q:1
~,Q
( a ~ GAZE(
~f I
pgJ t 'SHL l ., 8~i~ a t'O!.)-t'L..i ';.>" Sent 8 QQQG Sit
PhGJ', 3 0 11-3.-75 XHS7.DJ? CONTAT.HtKNT DUD>XDJ," COHTAXJB JJ.'? JT
'/xKPLp ptg I <~ AFB f saic.
H~) ~c.s [ta Lj ./gled f I f vc 'fQ
),AH XICTRCIC/iTl'.0 U'./iK RliTl:: '/:I'.l"I' Al'er;Hu>Y 31 3.1 l 75 wszor; cowvaxnmwT OurSXOr Cp.nhXW~Cn II II p) f RC DT
,
+i@ 7i 53UTAltJ , Qr~)-
L~,:~ SUE"gP 2Q Z7- ~Qz(
~c lC'-.K
/t I
~'
~l 25 r RPiB A, c'.~7 Joe) ) /'>
ti I")
~~gp-i vc z~ ~- to~i.
twCP ~ f.) l g"rsvp pe8t t
~,]
Z.C C> 0 Qz4.- PQ rP,
)05'Tc't-'a~": Pvr~,~
~Cq jar ZG GCb,t- iv';.'w", r='R
>u, Wr'=c7" 798X P~CP C I ~~r-
C ~ I
PAGE 7.3 11-1-75 BIS7;DE CONTA7;NHENT OUTSXDI'. CONTAIttt~B>>T 1
'Vl J ~ ills.lJ ~
XllTEClUa'J.'3'.D 3.3'Jaf~ 3JiTE Al'PEfll)IX IhCE 4l i. ~ 41/E>islJVaElr i a v~ Ti ST c le ll-l-/5 INSIDE Cpm'.XWE3<T OUTS IDE C013'fAItlHENT cl!.Vh'. P C'( Vc.v e f ~ tl/ C,oQT'Ai~> ~we <<>7
XHTESI'ATEI) 1IUUC III I'E TEST 1'hGH 3.5 Al'l'RHD]X )l
!
~ ~
XNSlDE CO'fTAIMHJ HT OUTS XDE COHTADB4i.'HY
~cd& P ~M pg p coo
'l)I, lal'VLI'JllJ A JlatVI> ~ / I S ~ I s as,vu o a
~ ~
31)T) G)(/x'J.')'.)) ).UA!'AT)'. 'J.') ST APJ'J H))XX )J XNSXDH CONTAXHi~j'.NT OUTS IDE CON'J'ATlfNENT )(CV +)~~ Q
'~i(~'~: t
.Jy~
i~a p $ ((t
PhGE l7 ll-l-75 XNSXDH CON%'<XNt<ENT OUTS XDL CONTAXtM.'HT vair I+lG i~"8 C <<)(0
., r1 GDSB l~~ p 7w~e ~
) (
7zQC
~ ~
.
APPLtl 0'l.lACl"'8 BlTH(DILATED I,l.'1 Y PATf'. TLST ll-l-75 OUTS3$ E COHTAXNPKtIT d.Q( g
+~6 ><gLQ4 wc~i E foui p~ J Pico ~
~ rlktg f~~,",fogy"
~ ~
w fq
Vl'l'ilaill lli<v l.'3'OUI i'rllUi'sL' DAVV~ J. 19 INTli(.'IJiTRr) 1.$ LI: I<A'r.'i~Tfi!S'r'PPJ'.HJ)HAGJ'. 77 7'5 OUTSXDE COVTADJHJ',HT 893 F aso P INSIDF. CON'I'AINJJJ HT t~4~ R R r Qc- Q(g 9415 Ef
XHTlCBAThl) LI'.Ali lCATI Tl ST PACE 20 AP1%;tll)7X )i 11-1-75 INSIDE COilTADllff;llT OUTS')H COllTAIHHENT GAL uonn 695 W 83i M P>4(l; 1 GsSC. 878 c LQoP B~iZ) b>> J.
%s ~
1 1 i
~
t
)lp> Xi~o p VAlv 'C 0 )
t.~...r. pg P( J'.~i'"
>
~ f Tc IZED~
~ ~
Vl J>IQYJ.'J I )kl J /(()( ) JJ1Jl Ja J 0 J QU a b
~ ~
78rl'.( f(ATI!I) l,l!Al: RATE 'iBT PAGE 23. APj'Jil<U1/ li ll 1 75 INSIDE CONTA33WHNT OUTSIDE CON'fLBl"JHHT 2,0>>fgG (
/Z( (
I )cp gQ
~B c~(> ') )
WRa ~ Sty( o C-20-Bc ..i y l fP CIAO
~
ph
~res
~ t <I VA() e F I
'Av:
\
I jc g.,-
)goal t:I I).,g~ ".g',l, 1~1Ug. I a<TEGBATED LEA> 'TE TEST APPENDIX 'B
'i'.NETRATXQiiS Iii r'IPE G.VALVE ROON OUTS "DE COt<TAi~~~ifEiXT VIEV
~ 59 g 453 45C 44B 23
,CC arced
- S to i ~
CC ". tu e Crom. E-...e per.v CC uc", v to Emer.enc. Cont.Su-..p .cPS ~ I Con". Cooler" >n el'oox~e~rs to h.-:T e gt~ 3 243 2ltC 7%A 25 58. 14 15 60 ACVS Cnc.,- R~'J 7 to RCP eal ( R ater Seal SIS to Le tdcvD har ging SIS to ceca a eturn Loop A 5 on Ref, o Regen. Loop C KC EK 645 18 19B 43 13 52
'.G. SIS ro Cont. Cont. Alt- Lo" Service Cr c CC free RCDT e ~ot S" "'sy i ead SIS Air RCP Ti.er ... :z. Le tdc>>-.. Pu-.p Spray Barrke s Disch.
. Legs HX 0
42 7 21 RCD "PRT Inst+ Air H to PRT C )o 5f C
~ 12 ~
.~l o to Vii N H to I
s SIS Line Test Bleed ~ PACVS h~Revaova iP'IStand -'-- F-t.'oier's -"-'IShor I o c'aMm~ l. Mes I ~ v4A ~~>,. 11 - 31 to. W4 Dx A.
" S.=.
~ ~
/ CC to CC fro-.. I 56 55 H2 alo RP.R out CCl? to R:.iR In Suop1y Excess Le- R& Oil 9 ar P336C to to I
cC RCP '.m H), 0016rs CC a- ~ es PRT
P<<g 1'lL'( 3
.'BTBhTiOYS LN PIPE 6 VA= ROO>!
~
. iHSID:" COY:AIiif&~.cT VIEN
<< ~ ~
<<a 23 i
- t. Su-.. )orQ 22
,CC 8",oa r") Fsz-Z> Cog+ CC iu 4 to RL"ie j ace 4iA CC R
.
tur fro 45C:
.. F~e zen 453 59 SIS to to s::).e~d" "' at. "o'ezs oat Cooiers Loop 3
'ooierry C
-60 15 58 25 24A 24C 243 53 fS
.ocp to C Ch" zgxag
";eg n.
to ED'4 yo Le tdoe-6
%~
Qo.- i',C,. rk SIS to Lc 0'p A RCP Vatez Re tu Sea1 Cha" ing o RCP Sea s PACVS H Reox 2 1 13 43 34 11 193 19A 18 643 i CC =zo=.'x CC fzo . SezvLCQ AIt. Low Coat, Cont. SIS to l'!35' g
<<p Le d o'pit.t RCP Therm Aiz Heal SIS Spzap Spzav 'AG3Ho 'Sa~p 3.e -
scn! 3azzic:-:~ Legs "1:. 16 53 17 42 9 10 64C f~ Inst. SIS 'es. to
~
i) jPD g PAGUS Ai",.~ H PRZ-Liod P.CDZ AM. "C" S,Q. Akc's I l t R7. ~
<<pc.s I St~ .8 H2 joe..ov g*eed ~o
- i. 'as Z) noz ~eg 7o VH
~to S a-pie Samp1 ); apples
.31 L 1
'
C.:" CC <<:zo. C >2t. CCh to RBR Out ttAlt g
- 56) RCP Q~l <<'-cess Le, S S-""~ Coo czs 'om HX Supp17 '"-".6C 3.Cps S"=p1e Sa:;~": s I
APPHHDXX C Definitions and Acceitnnce Criterin
PAC).' ll-l-/5 OPERA')'1)'G PJ)OCE))U)t).'3100. 1 XHT) (lRhT);)) L);hK )l'ITE .T)',ST APPENDIX C
~ ~
Dafiniciona and Ace~a>l:ance cxiccxxai Pa (50 psig) - The calculat:ed peale containment internal prcssure rcl.;ed t:o thc design basis accidcnL and specified in thc Techni.cal Specie i.ca t i.oui. Pt (> 25 psig) - The containm"nt vessel reduced test pressure selected t:o measure the integraLed leakage rat:e during periodic Type A t:ests. Lam/Ltz (%/24 hrs.)- Ti.e tot:al measured containment: lealcage rat:es by kleig)It at Pa and PL, respectively, obtained irom t:est:ing the cont ainm+I.L',11th components c,nc sys te..!s in L'hc 8 LQLQ 0 as practical t:o that: I"hich laould exist under design 'lose basis accide:lt conditions (e.g., vented, draiocd, flood<'.d or pressurized). L~ (0.25%/day)
- The maximuin a3.lovable leakage rate b> IIeight at 50 psig as'specified for preoperati.onal t:eats in the Tcchnica1 Specification and as nlccified ior p riodic t:esL's in tlic operat:j.n j li.cense.
.. (%/24 llrs.) - HaxiInum allowable leal'age rate by weight aL't derived from t: he prcoperation'll test daLa as folio.:.'s: Lt. = L. Ltm Lam where, La = 0.2500 atm=. 0.0667 Ln 0. 1020 therei'orc, L(. 0.2500 0.0667
- 0. U)20 I 0.2500 (0.6539g
-"
0 1135 For periodic '1'y!'.e A to ts at: P,. LL = 0. 75 (0. 1635) LL ~ 0.123 %/dIIY by 4'Cia;)It Q 25 pai
I I Ar rrw~mx n Dil 1:i~ h) 1 ('. ~ t'. 8
PAGJ," 1 11-1-75 opH!eATxna I I;OGJ;DURE 13100.1 XN'l%:Gleh'I'I'.D J.J h>i Rh'I'I', TEST APPHHDXZ D AHJJXEIJT TEHPEPi'~TURH JIOUR NO. JJAR0NHT!exc PREssURH DATE ROTA! JETHR FLO!I VHRXFXEJ) P>Y XLRT DATA Sl!HHT TX~I',/SAIJPLH VO. RTD fr' RTD ir' RTD >r' 3 RTD 8 RTD
'i,65
."I RTD RTD )i 7 RTD 8 8 RTD 0 9 RTD -',
10 Rio ~ 11 RTI) f~ 12 RTD -.'i 13 RTD I'. l4 RTD:. 15 RTD -'6 RTO =.".- 17 RTI) ".'8 P,TO ..'.- 19 RTD )'.- 20 RTD i 2l. RTD 8 22 RTD )'3 R!ID;- RIID:.'- 2 lellD ~r 3 I',IID 8 ls Ie!!D -. 5 Rill) 8 6 Rill) ia' Rill) i 8 Pres use "P 1 Pre. GEL)'.e ii 2 P RTD <<Res'stance Tempera!.i've De!:ector, Rill) Relet:ive Ilu>n'l.<1J.ty I)et.'ecl:or, Prc's sll). e
APPE!JDXX H Data S3ieet for 3lanual Calculat-.:.ores
PAGI'. 1 11 1 75 OPERATXI..", I?ROCEDUN: 13100.1 XHTECI'J) TED LEAK RATE TEST rOR XHI'O.aWTXOH OxrZ LEA!; RATE TEST DATA SIIEET 'HTEC,ATED Xo CALCVL~.TXOi~lS Pi Wi Vi 100 z 2I> Ti pr -"s: P2 " l>q) Tg % p r. day A. Qt = Du1atxon oi t:esL = hours C. '. i 7.' 459.69 = psia
~sia R
E. Tj: r+ 459.69 = R Xn t: he unlikely event that: tire co!iiputrr is losI:, a cle lc calculator or. similar'nit !r.ay be uti.li.;:ed and shall be avail.ab'!.e for. this pu):pose. XX. RESIILrS
= 2l.C0 per 7,
- ) ( 3 % clay (2'~) ( ) ( )
All par.anetezs Lo be zccorclccI fo1 all t:est: I>hasrs ccce>>t I)xcssuriiat x.on ancl dc.pzessu1i;:ation. All 1cadings Laicen at o::e (1) hour. intmvals, 1AQX'J.lllu!!t ~ Ver.iflccl by: Da I'e-
I APPL'NDXX F
'&C Inst:rur>ent List I
CONTA II'VEIIT EQU IPl4EH1 CHECI' I ST
- 1. Fischer Porter/ffaaan Transmi I-fers - On al I below listed transmitters, insure cover o-rings are Installed and in good repair. Tighten cover hand-tight.
Transmi'Itor P/ Function Performed By: Restored Q.C. P T-3-138 Excess Ltdn Line Press JFT-3-436 RC Flow Loop C I'-3-435 RC Flow Loop C WT-5-933 Safety lnj. Line Flow Loop B
'(T-3-4 34 RC Flow Loop C &T-3-424 RC Flow Loop R T-3-425 RC Flow Loop B 6-3-426 RC Flow Loop B fA-402 RCS 'Hide Range Press.
Pf-3-i0~ RCS N.R. Press. f&3-416 RC Flow Loop A F&3-415 RC Flow Loop A R-3-414 RC Flow Loop A P I 1004 RCS Drain lank Press. PP3-155 RCP >>B>> Seal AP PV-5-128 RCP >>B>> Thermal Barrier hP LY=3-484 Stm Gen >>B>> H.R. Level Ch. I LM~-485 Stm Gen >>B>> H.R. Level Ch. 2 LTW-486 Stm Gen >>B>> H.R, Level Ch. LT&487 Stm Gen >>8>> N.R. Level PN-455 Przr Press. Prot. Ch. I PT~a-'456 'Przr Press. Prot. Ch. II I PTW 457 Przr Press. Prot. Ch. III PTW-415 Przr Press. Control LT4 462 Przr Level Control PT-'>-444 Przr f'ress. Conlrol PT~~-4583 Przr Press. Cal. PTM923 Acc. Tank A Press. PT-~1 31 f<CP C Thermal Barrier PT-8-156 RCP A Seal hP
Restored Transmitter /I Function Performed By Q.C. T-3-0/4 Stm Gen A I'I.Ri Lvl Ch. 1 LT-3-476 Stm Gen A N.R. Lvl Ch. 6-3-C75 Stm Gen A N.R. Lvl Ch. 2 T-3-477 Stm Gen A ('I R. Lvl
~
I T-3-921 Acc A Pre s. t T-3-925 Acc 8 Press'cc Kr-3-927 8 Press. P1-3-929 Acc C Press. L f-3-494 Sim Gen C N.R. Lvl Ch. I Li-~-495 Stm Gen C N.R. Lv I Ch. I I LT-~-496 Stm Gen C N.R. Lvl g>> +Q L 3-497 Stm Gen C W,R. Lvl
~1-3 5 y gD P7-3-931. Acc C Press PT 3-154 RCP 3C Seal 1'later hP PT-3-125 RCP Loop C Shaft Seal ~P FT-d 494 Ssm Gen C S1'm Flow Ch. I FT-9-~r 95 Stm Gen C Stm Flow Ch. II FT-<~85 Stm Gen 8 St'm Flow Ch. II FT-f-48ci Slrn Gen 8 Stm Flow Ctr. I F T-F474 Stm Gen A Stm Flow Ch. I FT-3-475 Stm Gen A Stm Flow Ch. II
- 2. Barton Level lransmitter - On all below listed transmitter-s, insure cover o-rings are installeci'nd,in good repair. Tighten co'ers.
LT-3-459 Press. Lovel Prot. Ch. I LT-3-460 Press. Level Prot. Ch. II I i -~1-~5 LT-3-~i61 Press. Level Prot. Ch. j III 3. below listed eqrripment. Restored Instruinent Function Performed By Q.C.
~ P,m FIC-3-~92 RTD Bypass F low C FIC-3-491 RTD Bypass Flow 8 J/-3 ) -~~
'TD FIC-3-~i90 Bypass Flow A I" I'7)
- 4. 8; ooks Flow Indicator/Transmi1"lors - Loosen tho covors on all of tho below lislod equipmont.
Restored Inset rument Function Performed By Q.C. FT-'3-156A RCP A Seal Leak Off (Hi) FT-3-156B RCP A Seal Leak Of f (Lo) Ff-3-154A RCP C Seal Leak Off C Seal Leak Off (Lo) j FT-3-15~i 8 RCP
' Flow RCP C Seal i'Iator F I C-3-15~i FIC-3-635 Low RCP C Low Flow CCi'I p cM I
FIC-3-629 RCP A Low Flow CCi'I FIC-3-832 (Unknown) F I C- 4-155- Low Flow RCP B Seal I'later F I C-3-156 Low F lo:v RCP A Seal I'Iater
- 5. Pressur i zer I ns I.rumon I. Cabinet Hea.l ers De'nerg i zo hea I e. by per-f'orming the fnf lowing.
Roslorod lnsf'rumont Required Aciion Porformed By Q.C. TC-3-440A B/S switch lo test (Rack 2) TC-3-441A 8/S switch to test (Rack 12) I TC-3-~1 ~'i B/S switch to test (Rack 15) TC-3-~i43A Remove output fuse (Rack 7)
- 6. Rcmovo the following equipmcnt from the "ontainmen";.
Ros t'oi ed
'Equipment Performed By Q.C.
Flux mappe~ Gas Bottles Contaitnnent Sump Floats tu/k ARTOIS G.I I. Tube Di I lion Load meters (iiianipulator 4 polar crane)
'l
- 7. lns'I a I the fol lowing jumpers, wi' 'Temporary jumper tags, Restored Racl: Termi na I s Performed By Q.C.
3Q R 51 to 5 3Q R 51 to 3Q R 51 23 to 25 3Q R 50 3Q R 50 9 to 11 39 4o 41 p k'Q R 50 373 to 377
- 8. Conduct Inspeclion of all levels in Containment and ense re Restored Performed By Q.C.
All Local Gauges (Pressure and Temp) faces ai e Removed All Local flowrators'ave al least one 7 glass face Removed /g
I AXB OPERl'(TED CON TA t t ÃclT VALVE FAILURE MODE 1 Valve l.'lluxo H odo Blvo 1"aalu'.o Ho.-.'e
~
k
'CV-3-200 A closeQ CV-3-850 E closed CV-3-200 B closed CV-3-850 P closeQ CV-3-200 C. closed ~ CV-3-852 C closed CV-3-307 closed CV-3-853 C clo eQ CV-3-310 A open CV-3-851 C closed CV-3-310 B open CV-3-936 closeQ CV-3-311 closeQ CV-3-951 closed CV-3-387 closeQ CV-3-953 closeQ 4"'V-3-460 open CV-3-955 B closeQ CV-3-455 closed CV-3-955 C closeQ CV-3-456 closeQ CU-3-955 D closed CV-3-456 A closeQ CV-3-955 E closed CV-3-455 A cl'oseQ LCV-3-1003 A closed CV-3-455 C closed LCV-3-1003 B closeQ CV-3 455 closed C V-3 519 closed
=-"'.;= CU-3-522 closed CV-3-5l9 closed CV-3-522 A closed CV-3-522 B closeQ CV"3-522 C closeQ CV-3-523 closed CV-3-549 closed CV-3-544 open CV-3-389 divert CV-3-853 CloseQ CV-3-851 closed CV-3-852 closeQ CV-3-850 A closeQ CV-3-850 B clo'sed CV-3>>853 B closed 38rl closed CV-3-85? closGQ CV-3-850 closed CV-3-850 D closed
APPHHDXX G Breaker 1.is(:
11-1-75 ELECTRICAL EgUIPHlHT INSIDl'NIT !J3 CONTAINHENT Canister No. T3C21 Containment: Cooling 1'an A 38051 S l<OV-3-865A Accumulator A Discharge to a Cold Lcg 380532 RCP 83A Oil Lift Pump 38055~! Containment Sump Pump 3A 380667 Cani.ster. No. 3C22 Cont:ainment: Cooling Pan 8 3806~i 2 Control Rod Drive Hechanisms Cooler 3A 380629 HOV-3-750 Loop C Not Leg to RHR 380615 HOV-3-7~!48 RllF. Ret:urn to Cold l.egs 380613 1 HOV-3-S668 Delayed Hll SI to Loop 8 llot l,eg 380671
~
'OV-3-8658 Accumulator 8 Discharge to 8 Cold Leg 380631.
HOV-3-535 Pressurizer Po!"er Relief isolation 380606 Reactor. Coolant Pun!p 38 Oil Lift Pu'mp 380679 React:cr Coolant Drai>> Tanlc Pump 3h Tl!ermal Cut-Out 380662 Canister No. T3C13 Contai>>ment Cooling Fan 3D 80829 I Canister No. T3023 0 Contai>>r!ent Cooling Fan 3C 3807~! 2 Control Rod Drive Hechanism Coole~ Fan f/38 380727
\
Reactor Coolant 1'>>mp 3C Oil Lift Pump 38076? HOV-3-865C Accumulator 3C Di. charge to l,oop C Cold Lcg 380733 HOV-3-536 Pres. urizer Power Relief Valve Jsolatio>> 380713 HOV-3-751 Loop C llot Lcg t:o )NlR Pun!p S>>etio>> 380731
PAC1', 2 1 l-l-/5
. Canister No. T3C23 (Continued)
HOV-3-744h R11R Return to Cold Legs 380722 1<OV-3-866A Delayed High Head SX to Loop h 11ot Leg 380732 Reactor Coolant Drain Tank Pump 38 Thermal Cut-Out T 380787 Canister No. T3Pll Emergency Containment Filter Fan 3A 380611 Normal Containment Cooler Fan 38 380642 Control Rod Drive 11echanisms Cooling Fan 3A 380629 'Lighting Transform r 36 380658 Containment Elevator //3 380619 Canister No, T3P21 Reactor Crane 3 3803 04 Normal Co>>tainmcnt Cooler Fan 3A 380518 Li.ghting Panel D.C. Feed 3Y0605 Canister No. T3P32 480 Volt Receptacle 817 and'"17A 3806'3 Reactor Coolant Drain Tank Pump 3A 380662 Canister No. T31'33 480 Volt Hisc Containment Distribution Panel (3Pll) 380673 Canister No. T3P12 Emergency.Containmcnt Filter Fan 3C 380719 Normal Containment Cooler Fan 3C 380742 380727 Lighting Transformer (f37 3X07 Contafnm"nt Entrance 380/68 L
PACI.' 11-1-75
. Canister. No. T3P22 I:,mergency Containment )'ilter Pan 38 B0806 Normal Containment Cooler Pan 3D 80829 Canister No. T3P35 /~80 Volt Misc Containment Distribution Panel 81 (3P10) 380771 Rea c tor Coolan t Drain Tanlc P ump 38 380787 Canister No. T3P41 Pressurizer Ileater. 2, 23 and 50 381101 Pressurizer ))eaters 26, 53, and 54 381103 Pressurizer Heaters 7, 29 and 57 381105 ~
Pressurizer lleaters 10, 32 and GO 381107 Pressurizer lleaters 12, 35, and'/~ 381102 Pressurizer !Ieaters 38, 67, and 68- 38110'~ Pressurizer Ileatcrs 17, /il and 71 38110G l'ressurizer !1eaters 19, /i4 and /5: 381108 Emergency Containment Cooler Fan 3A 380G50 Canister. N o. T3P 51 Misc AC Instruments 3P0610 Space lleaters 3YO-'i 39 Space ))eaters 3Y0521 HOV-3"S658 Accuuulator 8 Discharge to 8 Cold Leg 380G31 Reactor. Coolant Pum!> 38 Oil Lift Pump 3806/9 HOV-3-8668 Delayed )Ill SX to Loop 8 )lot Lc), 380621 HOV-3-535 Pressurizer Pnvcr Re1icl 7solation 380606 Containment Sump Pump 3A 380667 HOV-3-7/i48 IJIR Return to Co1d Lcg. 380613 ..HOV-3-750 Loop C )lot Lcg to )UIR (1HII) 3)30615
Canister Ho. T3P42 Pressurizer Heaters 21, 4i7 and 4i8 381201'81203 Pressurizer Heaters 3, 24 and 51 Pressurizer Heaters 5, 27 and 55 381205 Pressurizer Heaters 8, 30 and 58 381207 Pressurizer Heaters 33, 61 and 62 381209 Pressurizer Heaters 13, 36 and 65 381202 Pressurizer Heaters 15, 39 and 69 381204 Pressurizer Heaters 18, 42 and 72 381206 Pressur'er Heaters 20, 45 and 76 381208 Emergency Containmcnt Cooler Pan 38 80820 Canister Ho. T3P53 Space Heaters 3Y04G7 Space Heaters 3Y0501 Space Heaters 3Y 0502 Space Heaters 3Y 0504 .Space Heaters 3Y 0503 Space Heaters 3Y 0505 Space Heaters 3Y 0506 Space Heaters 3Y0507 Space Heaters 3Y 0508 I'lisc AC Instrument. 3P 0814 HOV-3-8G5C Accumulator 3C Discharge to I.oop C Coli) Le); 3I30733 Reactor Coolant Pump 3C Oil Lift Pump 380762 HOV-3-866A ))claycd High Head Sl to Loop h Hot Lcg 3)30732 HOV-3-536 Pressurizer Power Relief Valve Xsolal ion ')80713
)IOV-3-744A R!IR )ieturlL to Cold Le8s 380722
PAGE 5 11-1-75 Canister tip. 73P53 (Continued) V@V-3-751 Loop C llot Lcg to PJIR Pump Suction 380731 Containmcnt Sump Pump f/38 380778 Fuel Tilting >linch Panel 38 (IC) ~80763 Canist:cr No. j.3P43 Pressurizer lleaters 1, 22 and 49 381301 Pressurizer lleaters 4, 25 and 52 381303 Pressuri.zer Ileat:ers 6, 28 and 56 381305 Pressurizer 1'.eaters 9, 3'nd 59 381307 Pressurizer lleaters ll, 34 and 63 3D1309 Pres urizer lleaters 14, 37 and 66 381302 Pressurizer. 11eaters 16, 40 and 70 381304
- Pz'essurizer lleaters 43, 73 and 74 381306
.Pressurizer lleaters 46, 77 and 78 381308 Emergency Containment Cooler Pan 3C 380729 Canister Ko. T3P5? Hisc AC Instruments 3P0917 S pa ce llea ters 3Y04 39 Space Heat:crs 3Y0521 Hisc A.C. InstrumenLs 3P 0714 HOV-3-865A Accumulal'or. A Disci!arge Lo a Cold Leg 380532
'
RCP //3A Oil Lift Pump 380554 Space llca ters 3Y0403 Space llcatcrs 3Y 0404 Space llcaters 3Y 0410
PACr. 6 11-1-75 Cani.. ter l<o. 5>'.V 'A'CP Reactor Coolant Pump A 152-3AA01 Canister 1<o. 51iV 'O'CP Reactor Coolant Pump B 152-3AB01 Canister No. 5KV 'C'CP Reactor Coolant Pump C '152-3AB06 RCP 3A Heater Breaker 3AA01 RCP 3B Heater Breaker 3AB01 RCP 3C Heater Breaker 3AB06
PAGE 7 11-1-75 Canister No. T3C32 Fuel Tilting Hench 3FTS/3C08-T3C12/1
&el Tilting Hench 3FTS/3C08-T3C12/2 l
Code Call & Fire Alarm H6 Canister Hire rcf. 26 spare Canister Hire ref. 6&8 Canister No. T3C31 spare Canister Hire ref. 7&12 Public Address Communication System Canister Hire ref. 11 PAX Telephone H3 Canister Hire ref. 9 Canister No. T3C41 spare Canister. Hire ref. 12 Telephone Circuit for. Haintenance H7 Canister Uirc ref. 11 Public Address Communication System Cani. ter H-re rcf. 7 Canister No. T3Cll spare Canister Hire ref. 5,6,8, 18 & 22 Remo te Con tro1 LP 37 Canister Hire ref. 2 Canister No. T3P31 spal e Canister. Hire rcf. 25&26 Canister No. T3P3<~ spare Canister Hire rc .. 7.5&26 Canis tel. No ~ T3P36 SPQle Canis tcr Hire ref . 25&26 Canis tcr No. T3P61 spal'Q C ~ni~'tcr Uir< rcj 1,/<&23
ADHINISTRATIVE PROCI'.DURE 0109.3, PAGE 6 1$ /16/75 ON TIIE SPOT C}lANGl S TO PROCEDURES OTSC N
',
1.D Receuest: The following change to Procedure Ho. 8'F5!o~ / Dated /i g 7 is requested: PROCEDURE T ITLE: r Z~ 4 PAGE, PARAGRAPH 6 LINES TO BE CHANGED: CHANGE REQUESTED:
EA W ))
OH FOR CHAHGE: )I REQUESTED BY: . g QQ DATE: 2; 0 ~Areve1: Change Recommended By: Date li Z Date~ Change Reviewed by PHSC 19>$ Change Approved by Plant Supt. 19 3.0 Hinimum Distribution: (Change Distributed to:) OTSC) Log (In tluciear Plant Supervisor's Office)by Date bl @ ~5
- 2. Quality Control Supervisor by Dete~JI z'r )S
- 3. On the job procedure(s) af'Fected I i st: For retueiing: Control Roon:,
Containment and SFP refueling manuals)
~IL e)e) . )ee)here by by T ce Date Il Date 2.
by Date
ADMINISTRATIVE 'OCEDURE 0109. 3 ON THE SPOT CHANvr.'S TO PROCEDURES Penetration Original New Number S stem Valve Number Position Position Reason PCV-605 Open Open/Closed This system is in service during the ILRT. The valve position is changed as needed. 10 RCDT and PRT Change CV-549 Open Open Upon loss of instrument Vent; N2 to to 4653 air, CV-549 fails closed. RCDT The desired results may be obtained by opening 4653 and leaving CV-549 closed. RCDT and PRT TC-87 Open Closed If this valve is opened, Vent; N2 to the vent header will vent RCDT and depressurize into the Auxiliary Building. Alt lo head TC-9 Open Closed Valve 887 (upstream of SIS TC-9) leaks through the seat. If TC-9 were left open, the RUST would empty into the pipe and valve room. CVCS TC-14 Open Closed Since CV-310A fails open upon loss of instrument, TC-14 does not need to be open for 312C to be press-urized. This arrangement also allows a boron path to~ the core. PACVS HV-1 Open Delete This valve is only on Unit f/4. 18 SIS TC-93 Open Closed In order for this valve to be open, the SIS pumps must be racked-out. This is not possible considering the long duration of the test.
P ration Original Ne. Number S stem Valve Number Position Position 36 Purge Outlet TC-36 Closed Open Since POV-2063 was a known leaker, TC-36 was opened and the boundary was extended to POV-2602. 54A/3 Recirc Sump TC-115 Open Closed Since the RHR pumps are in service during the ILRT, TC-116 Open Closed these valves should be closed in order to prevent the loss of RHR fluid. 58/59/60 SIS Open Closed In order to prevent a spill this valve must be closed when the BIT is periodicall recirculated.
l. Raw Data
ye l
OPERATING PIlOCIDURE 13100.1 XNTEGRATED LHAV. RATE TEST APPENDIX D t AMBIENT TEIPERATURE EIOUR NO. ( BAROMETRIC PRESSURE .. '. DATEJ3~~~/ ROT&ETER TLOR VERIFIED BY 4' i XLRT DATA SHEET Tr,Z/SKI~LE I O. N~<<C
/ /6,4s I75~ Y8.
RTD ff' C'g g ~QG2. S'9 gg.s ( RTD 8 2 RTD i= 3 "S, TP F.0Q < RTD ~~i 4.OM . 7. 7 RTD !P 5 RTD >fx 6. ! 7 oGY
.RTDfP RTD .P 8 RTD 0 9 RTD 8 10 7
/O
~ 7. S4 f(,.g
.EL 2
7 C'Q'~~I 3 P7. F71 o7 l'. <y 0 . gp@ RID RTD '2
<r RTD 2," 13 11 g(g.g5
~O.o 1 4. og r
~
Tg 23 F~, S'/
. RTD ff 14 F>> 79 l
RTD 8 15 RTD '6 g4 ~ G.o
&f.
g h.~5 E j.Z~ RTD,'-'7 h.F) g~ <s. Vc) RTD Ll 18 ~C-Mo P,TD i'i 19 P~.S3 RTD ',< 20 .5 o'> RTD 21 I'2
~F RTD RTD 'l 23
.C RIID REID P; T.E 1 2
~e> zr'-
7
/A R1ID 8 3 R11D
"
RIED -'o 5 a~so' RIU) !'P 6 C.7 6< 'res RIID /P 7 RIID g 8 ure ~t 1 Pr.essur.e ~< 2 RTD <<Resistance Temperature Detector, RIID>> 'Relative Ilumidity D" tectox, Pressure Terminal Operator. 4'(4
.~/'Paa~
JJ'4'tMt CSICC O'A'~L4u~~+ Q
3,1-1-75 OPERATDl" PI'OCEDURE 13100.1 INTEGRATED I.EAR RAT['i TEST APPENDIX D ANBIENT TEHPERATURE PD. (3 HOUR NO. BAROMETRIC PRESSURE ~, 0 .. ~ DATE 4~ ROTAIKTER FLOll VERTFZED BY . Q,),M~5 J ILRT DATA SIIEKT TTLK/BA))PLE NO. /7++ gazoo Y 18> 5 lp RTD 8 1 RTD ir'TD 1j 3
~7. 85'- 0 RTD P, .S 'K7. 9 l RTD i 5 5. 7 RTD fr' .7 rc s RTD fi 7 RTD 1'." 8 (. za RTD 1' Fg. rye wC-8 X RTD " 1O P .3o. K.2 o 8')~O RgD TS C o RTD '.~ 12 'ZZ~>' p's. 5/.
RTD i 13 I 7(k 7
~ RTD f> lt" FC.Q < ~75, ~c/
RTD 1'5 gS. 7g / RTD )'k 16 5 ~+ ~
~S.aG RTO -:r 17 gS 2.5' RTD "- 1S Tb.oC
'7
. OC V/
P,TD '..'9 5. ~a'5 8 RTD 8 20 RTD v 21 f g g ~ r 'F~ 32 5 2. RTD .'r 22 RTD Tl! 23 RIID /E 1 QZ'5 RHD f' k&.o @ r RHD 1'F' Q Q RIID > ~7 S/ ~MR~ R)!D - 5
'
R)D) 6 6 g 7 C g.~S RIID t,' RllD 8 8 Pres"ure 0 1 Pressure f 2 RTD << Res-stance Temperature Detector, RIID - Relative llurnidit>'etector, Pressure Terminal Operato
' 11-1-75
~ ~ ~ ~ OPERATXNC PROCEDURE 13100.1 XNTEGRATED LEAv. RAT); TEST APPENDXX D AMETEET TEEPEPJ TUEE HOUR NO.
BAROMETRXC PRESSURE Q 0: / g .. ~ DATE%) ~c ROTAIETER FLO)l VERXFXED BY XLRT DATA SlfEET
..IE . 'o. lE 3J j'~<6 AO i EOO/ IRIS l(2 RTD fr 1 RTD Vr'
~0. 70 RTD )'r' RTD Tj ~~&. cZ RTD 8 5 F .35 RTD ",
RTD v 7 6 ~0. vZ RTD i.< 8 g0,@o
'g5,'5 RTD pc 9 RTD T'.) 10 Ri0~11
/COD ~5't S, S. RTD!r 12 RTD TPT 13
- 6. Cfb . S'Hc
~PS. 6
.RTD 8 14 >. (pO E'S gR RTD Tc 15
" ~S 65 85. c~
RTD RTO RTD i" l.'l 16 17
.18 f>. Z-Z
, Cjg ki<
V> 84 S.:7~1 RTf) ii 19 7<34 QS 92. ~5.5. gg RTD 0 20 8'S. j F7 5'. I b F5 (+ 2 RTD ~i 21 RTD ~'2 RTD E) 23 RllD Pi 1 RIID RIID )i'3 T'c RIID T'.r 2 Cc 4~@ ~b. ~-J ~pc,gq M< ~ ~X RIID -".r 5 c7 '7/ 3 R)ID ji) 6 C . Iufn t 7 RlfD <i 8 Pres ure '< /Shan 0 Pressure g RTD << Resistance Temperature Dote"tor, RIID - Relative Ihnridity D" Lector, Pressers,
I l l&r& ll-l-75 OPERATXNQ PROC?'DURE 13100 ~ 1 INTEGRATED I.?'.AK R'ATE TEST APPENDIX D AMBIENT TEHPERATURE 78 tHOUR NO. s BAROMETRIC PRESSURE 9 0' e~ I I
/I s. I ROTArlETCR PLOT1 VERIFIED BY ~
QA~~i~'r XLRT DATA SHEET D:IS<>err RO. I 7 BO+ I 3 I 9 "t5 ~4- oooo P)g- zolS IIC RTD ir RTD fi
-Pr 1 2
3 Zb.:sl b,o. 51'C ~ 3 r>>. i' RTD ~P >>~7 Ccr3 ~ & e'TD RTDI 5 S~ G& C RTD II 6 RTD 8- 7 4,3o
.RTD Tr 8
',~
I /tg RTD PI 9 6 /3~
'c V~6, o RTD Ti 10 F'5 V5 RiOii 11 +5. '7 ~
>>
Q5 6 ~ kTD rr 12 5.<4 FS.
~5'W
~
RTD r'3 ~ 5 58 g'5
, RTD ft 14 5,
~ss'7K5~ kS. 9Z
~3 RTD 7'i 15 F5 5 g6 >C RTD 8 16 .2~XL ..
RTD i'-'7 5 0 8'5', 0 l ~5.u J RTD 7". 18 ~ ~ I 7 RTD ft 19 5 s. 2k gq' 5>>o 25g RTD Pr 20 g>> g7 RTD 7'r i21 RTD ~'2 RTD i'.t 23 RIID ir' I 75 C g C,g/ RHD ii 2 "RIID N'
'
ra I'7 101D RHO R1>>7D
-'r' Trit 6 ~
0 /
&5.
~'o7 4 ~
~77 vo. / t'.
'TM
~g~O 7 tp a RIID $ '
RII0 rr 8 Pressure,", P's s'4'5 Pressure g RTD - Ras'steeca Temperature Dateeter, R11D - Rema tive ltumid i ty D tee tor, Pressure >> Terminal Operator
OPERATEll" PIlO I DURE 13100.1 XHTEGRATED LEAV KATE TEST 4 AMBTERT TEttPERRTURE~S APPENDlX D HOUR NO. I BAROHETRXC PRESSURE BO'l ~ DATE~ er ROT&IETER PLOll VERTPTED BY~t' / Vr TGtE/EAIPtLE NO. 3030/ / 7 / i 9'/oo/ XLRT DATA S?IEET
>>95 Jq RTD 8 1 RTD ir' RTD I'I 3 ~Q. I 8 a,o~
RTD )'i RTD -'.f 5 RTD PR 6 X. 0 gS'. '>3
~
~5~2
- 5. v5 RTD t 7 " o+ C" r RTD F. 8 5.
RTD .P 9 00 o'abac.
. S.
V+~. RTD .." 12 RTD i 13 5 RTD iit 14 S~ A$
~s,ei
~
5'3'5 RTD T/i'5 WP RTD " 16 1$ RTD i."- 17 RTD R" 18 P.TD -.i'19 M~C ~L gr g RTD 8 20 ,C@ RTD g 21 '5 RTD !i 22 RTD,!-'3 RIID i/ 1 e. ~/ /5' c., + RIID $ 2 R)ID '.i 3 RIID '-'IIO
!I' oI .OC RHD Ip 6 o. x4 O. 3 ~ &
R)ID iF 7 RllD 4i 8 Pressure Prcssiirc g ltt 1 2
~~>
RTD - Res'stance Temperature Datectar, RllD -. Rc 1 a tive Ibm id ity D" tcc toe, PrcssUrcp Tcrmlnol Operator
FAGS l 11-1-75 OPERATII')G PROCl'DURE 13100 ~ 1 INTEGRATED LEAK RATE TEST APPENDXX D AHBXEHT THIPERATURE HOUR NO. BAROMETRIC PRESSURE Q~ l l ...DATE~r~ /ri ROTA)'ETER FLOs'1 VERIFIED BY PC2.<8 ~ ( XLRT DATA SIIEET TDK/SA)lPLE NO. Zlzz lzI zgoo P<s . 7 RTD .-8 1 .FS, -0 RTD 8 2 RTD Tr 3 RTD 1 RTD /: 4
'5
~S
.'.
4 o 5
~k~X +AD RTD sr 6 5 b.
RTD fF S.' I ( RTD '~ 8 K$ R, l ~ RTn iI 9 i5'. Cj I 5' ~ p'g, g RTD i 10 g5.' s,-S R7. D~T 11 ~5." 3 RTD i
~12 RTD;r'3 P'Ss C)
S'5 3i
.RTD RTD i'514 8
a~.< b g~aO ~SaP ~5
~ I3 RTD J 16 RTD R'-'7 g ~ '72 '7D g~C
~ h'6 RTD,".18 R ~5R &A l>r" g 5, gc' i
~
PTD 19 PE~S ~5, /B RTD i'E sr'1 20 r c'Q g,C RTD RTD ~'2 RTD i'3 R)ID /I 1 '70 0 po. / I 70.3& RHD ~~/ 2 s.3g cs so RHD 2 3 RIIn '. hZ 9& Ks'mi' RI!0
'
Q.>o RIII) FFL W7 0( ~ Rlln 2'. 7 RIIO <j 8 Pressure 8 Prcssure ~ RTD - Resistance Temperature Detector., RIID - Relative IIumidity D"tectnr, Prcssure Terminal Operator
11-1-75 OPERATIN PI!OCEDURE 13100.1 INTEGRATED LEAK R'ATE TEST APPENDIX D AtBIENT TltfPERATURE HOUR NO. I aARomTRIC PRESSURE 3D /3 DATE~7e~ce ~l~8< ROTAI ETER FLOT/1 VERTFTED BY~(. e/PEP E~ ILRT DATA SIIEET 2295 F2@
/0 ~ /
g 300 II TTEE/RAt~LE RO. RTD .jr 1 .34 ~PcG~/ RTD Yi RTD;P
'3 RTD ir' 4
's'.
5
~g
~
'
K5 <M 8~+.;9 RTD:/ 5 5.; 6 5.aB $ s RTD fi 6 5 ~ & PRTD 8 7 5. @6 g ~ (o~ RTD Y." 8 ~SF 6 ~5' +~( RTD Pr 9 RTD Y't 10 Ri~ Y'l RRD Jt 12
~* M5', '7
/sZ>
5,>5 C-RTD -.'I'- 13 r' 5;AO R'5,/.
. RTD P '14 ~g. OO RTD /'5 gG. 33 RVD:.." 16 8'as -~ 7'4 RTD >.-'7 RTD,'8 5 5. S,SO S.O P.TD ji 19 RTD Pr 20 RTD 1'I'1 M!D~
RTD / 22 RTD )~ 23 RI 7geZ$ 70's RIID p." 2 &S~h 7 RHD Y'i Y 3 +~5 55 5't C 5.Qg d 6', '7
~~'
RIID RBO 'i 4 5
~OQ 5'M%&
G+t RIID 8 6 RIID f,' RIIO fi 8 Pres ure,", ~<>Uk Pressure g C4 RTD - Res-'stsnce Tempetetute Detector, RIID - Relative IIumidity D tector, Pressure Terminal Operator
11-1-75 OPEIIATXll~ PIIOCIEDURE 13100.1 TBTECRATED LEAK RAT.: TEST
'APPENDXX D AFmXEET meERATDRE 75 HOUR NO 3AROHETRXC PRESSURE 9+> /D .DA,TE Dc:~Art I-2 7~
ROTA1IETER FLOT1 VERTFTED BY Z R+ XLRT DATA S)IEET jg/? TDS/SAI I P LE NO. ~aar~<1- OOOO< I5 .: rDo /5 +/ / RTD /E RTD ir RTD irL RTD )r 1 2 3 zr~ T
~ D S.g S. 6-s 5, OQ 5'GS.
RW
' P-f.'1 t-f 85 'I")
RTD .' <~a. iZ RTD >rT 6 ill9 8 5. ZC RTD 8 7 + ~& RTD 8 8 5.'~ ~5: vz RTD RTD 1r~ L'0 9 Ss;Ã C BS; -Is R~trr i 11 S <M2 gy+. 07 RTig 8 12 P( i7c 8'4, 78 RTD 13 S<
~ RTD ii 14
/G'S
' S~'/ 5 ..~<3
'7'5.
RTD -" 15 .3 Erg 7 cd s's ~Q~ . +'I RTD 0 17 RTD,',-'8 rwwv 2.~~& SS RTD ii 19 8+AP RTD TN 20 89. 7'7 RTD ')i '21 RTD t'r 22 RTD 't 23 VD,5 9 RIID P)ID R)ID
$r' y,
)r'
.r't
~ 5P
~5.
- o. gg ~
4S. r'~ Cs: q R)ID Cc I- 2.o RI!0 -..r 5 Q~g, c r 6~i. o ~ R)FJ) fs 6 za.@ 70-6 r R)ID /P 7
~
R)ID ~i 8 Pres "urA 0 Pre~sure '> 1 2
~g Ssz, ~8'5) 0 BS"3 6 l C RTD - Resist:aucc Temperat.urc Detector, RIID " Relative I!umid i ty D tcc t:or, Pressure, Terminal Operator
11-1-75 OPERATING PliOCJ DURE 13100.1 INTEGRATED LI;AK KATE TEST APPENDXX D AMBXEHT TPrIPERATDRE~O / HOUR NO. / BAROnKTRXC PRESSURE 90 12- .DA,TE /2 - 2. /PS ROTAIKTER FLOIJ VERXPIED BY 5: R + ILRT DATA S!IEET Oa<5/ Ie C5l &n / (~y c>i f 8' z.c . RTD fE RTD RTD Y'E prE 2 3 e>S. I s. Il 8s'. 'B 7
&S'D RTD fi 8S.>V S;'7D RTD 8 5 8 S-<7 CO+ g < >~. 09 Cl c~
RTD " 6 ~W 2.t* 8~~ /9 RTD d 7 QS.Z Gs: 3> RTD F 8 GS.S I 5', &8 65. Wl RTD fr'
~8.~. 5~
RTD gr'0 5;"I I gs; ~I PTD T 11 a s.c@ ~s. o+
-RTD Zr'2 6'l.>V -
9~i Q ~n RTD i 13 i n/ ~B. 'p n/
- 89. R7 gs 8$
~ RTD fr 14 SH.
RTD ir 15 Gs,'z I /9 RTD RTD i~r n.-'7 16 GW. S l ~r. G-9
.gn~i 65 ~:4 7 RTD 18
~S. 'I oT RTD -.'9 GS. rH RTD Pr 20 Bg.a 6 88. rz 21
'TD
)'i RTD Pi 22 RTD 23
'C i'.> RHD fr RIID T".2 1 7 /..0 G. og Z. ~/. // 7l, l8 4d. 2 Tf. Z. RIID i" RIID v
,3 Co
<5.8+ @S. rg @6. Oa Rll0 ~c Cg. // @ i- Z.~
RI>>> e 7'a. 7r T< '7~ 7'. 7 7 RIID f' RIIO g 8 Pressure 'P 8s3S BS'3'/0 J Pressure g RTD - Resistance Temperature D" tector, Detector,'IID>> Relative Ilumi.dity Pressure 7 Tnrndnnl Dpnrnror+ 8 R~
4 11-1-75 OPEICATlll" PIlOCI DURE 13100.1 XNTEGRATED LI'.AÃi KATE TEST APPENDIX D CI AHBXENT TEHPERATlJRE 70 HOUR NO.
~
/C)
~
EAROHETRXC PRESSUICE Q 0,' /z- - z >~ ROTAIZTER PLOU VERXFXBD BX~ d XDyla!~iB VO. Ol3O 1
/ 2oolm'3 q, 7M RTD Pr RTD gP 2 .GS RTD ii 3 5 Z.S RTO j 4 8.
RTD " 6 ~./C C3 5' 39 w tZ'S'. RTD ~i 7 < 5. RTD s gs.,a9 RTD t" 9 g~, & ~~. s9 ~5 ~h RTO r'r'0 es.. aw 85.& { 8 5~5 8~i < i-9'9' Q. PTD RTD 8 12
.r'3 H. C-;c~
. RTD 8 14 g c], Q'p S,S RTD il 15 h~fB 5,/7 SS I& 65( /S' RTD )j 16 leg RTO i.'-'7 RTO '! 18 35, 3-'I GS; 5>
P;TD i 19 RTD 8 20 a f..7( G~I.? Q~c. g 1 RTD i'i 21 RTD ~'2 RTD j 23 RIIO 8 1 7'/ ~7 7/.92 7/ R!IO ii 2 6. 27 Kc). B / RIID /j 3 C 6 A "7 c<. s& cc./w c /-a
~
RllD c/ >9
-"
h'IIO 5 COhi. ? 8 6R. EG Co, v RI!D !'r'- 6 '7h-h 17 7/( OI ~/,0 RIID i,~ 7 Rllo /' Pres"ure 'j 6'5D /3 Pressure;;. h RTD - Res-stance Temperature Detector, RIID - Relative Ilumidity D" tecto Prcssure h'erminal Operator
11-1-75 OPERATING PilOCI,"DURE 13100.1 XNTECRATED LEAK RM'I TEST APPENDIX D C) AIBXENT TBIPEBATURE 1!OUR NO. /i BARONETRXC PRESSURE MO, t & - DATE I + A />+ ROTA! ETER FLOTl VERIFIED BX~~ ILRT DATA Sl!EHT TIIK/SAIPLE NO. oT.'/5P 2.C a~o YZ 7 O3I > +~8 RTD Pr 1 RTD E' Qe. o~ ~S'. a i RTD Ti 3 RTD T'i Bs, &8 Et5, +Z RTD P 5 G'+ l f &y. HB RTD i" 6 5. 07 85. o7 RTD fk 7 g 5. 2."7 5, 27 "5; mV. B~r Z7 RTD >> 8 6'G, 2-/ 85, Lf BS', IS RTD f,'.9 5;W7 65,>> RTD )';-'0 P.T RTD i)~f11 RTD f'12
.RTD 8 T'i 13 lk B5, '52
&ni,GS 8 l7 5'1 ~ ~
8& ~~8
&S,Z
,,&
89( 7Z 9'9'.V~
~n.
fn RTD 15 65, OV RTD l.'6 5 89 57 81 37 +~'+4 <~ RTO T'.-'7 Q f,5o Bf "IQ RHa~~ RTD T" 18 O' . 'E I Og)g <5 Z6 B~&6rrZ~) RTD T'r6 19 6'q,Q7 RTD d 20 H8. G6 BA, G6 RTD )i 21 RTD fi'2 RTD;i 23 'C R11D P R11D Ti 1 2 "71, 6> 5 I ~ Wl C6. S-/ RllD l'r'
%66 ZM gc~. z.e RIID fi ~ 6 se. vo l"'. pz &~r. M:b RIID 6lr. VC C V.M6 65 /r &l,M/
w/, //
~ ~ .
R11D >'3'
> C>~ 7/, /5 RIID P 7 P.llD fi 8 Pres ure "f Pressure g 1
2 859 c.s- 85 2 F &~ 85'2 // RTD << Resistance Temperature Detector, R!ID - Relative Ilutnidity D" tector, I'rc ssure 6 Tnra>innl ODnrnnnr~g &~MA
I 11-1-75 OPERATIHQ P)lOCI DURE 13100.1 INTEGRATED LEAK KATE TEST APPED)IX D 4y NKIENT TEMPERATURE HOUR no. /< BAROMETRIC PRESSURE I BR.YZ < ~/R ROTAHETER PLOU VRRXFXBD BY ILRT DATA SHEET YDB./Bnnviz xo. 03 no +<'l O3n/5r Ze On/era Pp /, O+/5 lZ ~ RTD Pr 1 Q~( (2 2 -R7 &w. e RTD 8 RTD Y'.r' BS,< S. r/ RTD HG;m fr'TD
/' s ~7
~ 8 6 GS.C a 5',OW c> P P.TD RTD
',i fi' BS', '2 9 85 I ns; 'I BG/
l5
~
R'I'D v' ~5, RTD ir' &S, )7 5, as., vc RTD >-'0 'Z a 85, w'7 85, Riff1)12 zG'~r,
~
",;TP P G {.C RTD vi 13 M. R I RTD 8 lk ~S-, Ca9 RTD ir 15 GS, I Qs; op RTD 16 ay, gg PTO f.'7 B n'+~
RTD Y'..'S QS; ZS PTD rr 19 Qc.), Q Sg. 8/ RTD 8'0 RTD irl 21 RTD 8 22 RTD R)lD /i R)ID g" RHD
'-'3
,2
).r' 1 m'{ O'S NG. Ca~
6N, 9>
~f cc,C NG. AS 5M i~c Ei 6. 66 G6. >8 7/,6~.
4'&. VM RHD -'-' CV ce. em 6~. R){D -'.) 5 &~i. O'5 6>. eG 6Z V6'r. R)l)) ~'f 6 "7/. I 7 7I, /Q 7/, 2.> '7/. R)ID '-' RH)) 8 8 Pressure nr Pressure g 85~<) e5xei j ~SZ~C RTD - Res-'stance Temperature Detector,-
~ R)ID>> Relative I)umidity ))"t:ect.or, Pressure Tnrn>lnnl Opcrnnnr~ +~/
11-1-75 OPEIQTIHQ PllOCEDURE 13100.1 XNTEGRATED LEA>'AT!', TEST APPENDIX D J AMBIENT TEI IPERATURE
~
HOUR NO. r I BAROIAETRIC PRESSURE ~ + "d 3' . DATE ROTAIKTER FLOP VERIFIED BY~- XLRT DATA SIIEET ( YAK/SA)lPLE NO. Or/PSY W)/- OSOO PM H G'5/S'~&rr RTD I' , a~Z RTD G .R~- pq Qe i'TD li 3 H, I l 9 O'.Ci 7 es.96
..
QS; & (DC~ RTD )i RTD )rl ' BS.'7 2. ~BC a
&") I'9' RTD RTD RTD lr'
(/ 8 7 8
~~S. I & 'B <
mS -09')
~ 6 8S;i9 S~r'ig 0 8 ~ ~AJ Bs.
~
RTD RTD PRD i'
)r i
10 1"
~.5 eyC~ j~
2.)/
~) g)
~8. 8 8S. lV gq B RTD RTD Zr i 13 12 ~8 5 ~ 7 8+.75 1>>w
~O', 4"/
RTD f'4 89,6/ RTD;r 15 ss',o SS,o&
~
RTD ).'r'6 ~~(.2 9
".17 8~) 3
~l.
RTO ~ RTD )" 18 )>>5; PS ,'2 + RTD .'i 19 ~/ Q~(. 8& eu. 7V RTD )I 20 RTD fi 21 CI9'.5 9 ~) ~ S)E l GH 59 5' RTD fr'2 RTD D/> 23 RIID (r' 7/,7 7t. 7) /. 78 R!ID )i RHD )I lr 2 3 4
~6, V5 Cc'9, 5 C G.+C 4C,Si
~6.s6'8 ~6 .
SG,~~a'))D 5"~>> 6~5'9'. av. '2- ca '7 Q P. '7Z
'Co RI!0 r 5 .
RI!D -'.j 6 /F'l, Zz.Z & Z. 7i.' / RIID 8 7 RIID !'. 8 Prcssure 'h 1 Prcssure )i 2 RTD - Resistance Temperature Detector., RIID <<Relative Ilumidity Detector, Prcssure 1 Ynrninnl Opnrrror&l
11-1-75 OPERA'IIN". Pi:OCEDURE 13100.1 INTEGRATED LI'.hK R'AT! TEST APPENDIX D AMBIENT TQIPERATUPE IIOUR NO.
n BARONETRXC PRESSURE ~ O'X $ ...BRm~Z< Aa ROTAltKTER FLOll VERXPXED BX~n.
TDq./SPI. LE NO gag 0 XLRT DATA SllEET oSv 11
$
ypM+
tmt 1 4' RTD 8 12 RTD -.'r 13
.RTD f.'4 Pr 9 72-
~
8'f, too oq, ~g
~8' vz.
BS.S Q '4. C9'S'.o RTD T'r'5 8 .Qw s,ew 85, C)l RTD RTO,'.-' r'6 8vg 233 Bs. 3v B9(7
~9 37 7 B<,PC e.l. a~
RTD Trx 18 RTD ." 19 RTD T',< 20
~n'9 5, 6'L ~&,2 6 f,7$
I SH, 7> 85 H ~i 76
~
Z.i RTD l'rl 2 1 RTD ." 22 RTD )r'3 RIID Pr 1 7/, 78
&6.85
~i, d'z m/.
6&, 6'& 82 7!,
~6. 7&
Cr'G. RIID B" 2 RllD r' 46,5j r'6.6r RIID &~i, agn 6. no 5" d~
-'.; 7~r.
T9
/5'z RI!0 - 5 n . Ci V- 79 I'!ID 8 6 7/n 3D Ml, &8 Vi.
RllD f> 7 P.llD ~> 8 Pressure 'f 1 S~ 5g Pressure ~ 2 RTD - Resnsteuce Teir.paratura Date" tor, RIID>> Relative Ilumidity D" tectox, Pressure, Tnrndnnl opnrnnov n A Eccrrcc'
11<<1-75 OPERATING PltOCI DURE 13100.1 INTEGRATED Ll;AV. R'ATI'. TEST APPENDIX D AHBIENT TEMPERATURE
~
HOUR NO. I EA.RO'AETRIC PRESSURE . DATE~/+ Z. ROTAIIETER FLOT1 pJ /A- BY~K.. /C 'ERXPXED ILRT DATA SHEET TDK/SAMPLE NO.
)
CD~ OO /g"P RTD 1 ~&9, c Qq'} Q a~i!
-Pr RTD )p 2 7 "7 RTD )'TX 3
8 5. 'Qe ak, 65. c)4 RTD,'r'TD 8' C.2- .Ci RTD '.i
)t 5 6 9~9 6&
- 95. c-5 PTD fi 7 RTD )t 8 RTD P 9 QS,~ es. s C'<~
7 BS'4o RTD )'x 10 85, 7 8 S./6 Cd, IQ
'-t R'iD )~all 8~83 ~4
~ I8 Qa<m RyD t L2 RTD i 13 Q~, Qn
~B.Gtl
. RTD /f Lc'; Qg. DS RTD =- 15 e Q. g7 RTD ).- 16 RTD -" 17 SH. v& 6 'rB3 QC~Q /
RTD )'8 BS, /8 Bs',t7 PTD )x 19 Bu. 77 RTD fr'0 Q RTD )i '21 RTD ~r'2 g,5'/. RTD ',-'3 C RIID RHD Pi
~i 1
?
g Cc C ~ z6
/
RIID 5 3 C~ci&. RHD &9. '7 Z- C~i. 7Z
-'='l!0
-.s 5 sg. 88 ~co QY Rl'sD J 6 "7/. 9 7/ B 7
~
R!!9 9 7 P.HD J 8 Pres"urc Prcssure
'px 0
852 es ~~ t RTD - Resistance Tctcpetatutn Data" tet, RIID - Rclat:ivc Itu:nMity Dct:cct;or, PzcsGUrc Terminal Opcrnt:or
A ~ 11-1-75 OPEMTXI)G PllOCEDURE 13100.1 XHTEGRATED LEAK Kerr'. TEST APPENDXX D AHBXE)iiT TEHPERATURE HOUR NO 1)AROHETRXC PRESSURE QO, N I . DRTE~I2. Z. 7+ ROTA) KTCR FLOll 'ERY FYED BY~4~
~l TV!I',IrSA)PLE HO. c>g~S/g ae RTD .Pr 1 Qg. DQ
~ q.at RTD jr'
'3 RTD ii RTD iE RTD d 5 2~i' ~
c) R 9'7 ~<I. ) "/
-' Q'7 PTo RTo t RTD 'E 8 RTO f,'
7
~~P @5; DG '65 3T
>-co
~I.
3) RTO <> lS P,To .'. 19 gag( 7~ Qq.z3 6 "I-7Z G'I . RQ RTD N 20 R'rD;,'- 21 RTD ~r'2 FTD )'E 23 R)ID Pr 1 77.o9 "7 Z.c O3
)V R)ID ii 2 RRD 'I 3 ac 8 68-7' R))D " 4 C~7~
6 rCVB N9. 79'~PW F'f RIID 'E R)ID iE R)ID i' 6 "7'4 7/'~ 7 I ~ 5 7 5 Rllo ~j 8 Pres ure 'E SS2 i> ~>> 7<8 Pressure iE ' RTD Rl)D
- Res-'s tance Temperature Dctc" tor,
" Relative llumidity D" tcctor, Prcssure Terminal Operator ~' ~~
kVlbb A 11-1-75
~ ~ ~ OPERATIHQ PllOCI.'DURE 13100.1 INTECRATED LI.'At'ATE TEST APPENDIX D AMBIENT TDIPERATUPiE HOUR NO. /7 I
BAROMETRIC PRESSURE SCAN'/ .~~/< z/~~ BY~~ Q ROTi&ETER FLO',1 oooo>> ILRT DATA Sl!EET g.. VERXPXED
>(P
/7 TIIK/SAIlPLH NO. Oooo FgV Oe~S.ISJ c yon PW/. o v~s.l~z RTD.8 1 BLi, >3 8H.B~ ~
8V. SC ~ Qq. eR. 7< -7Po
~~g
%S'TD jr' 89.7!C s RTD i'i 3 +~1. 9"7 RTD 1'f 4 C) ~ C~c~C '<>. Ga
- SY
. RTD if'-
RTD:;-'
>x-I ~ 8I 7
B~.BV C.f Cj
'5 C! g C)g C/5. o 8 H.
RTD /i 7 ~ 69 8B
~iS'9 RTD i'! 8 ~
R'1'D f P $ 5 3-~ ~ 85. >~ 5. 'B~~ RTD P 10 8;O3 5s.aC . gq o>r Q5. Q3 PwJLD ik 11 ~~r L- 8Q-'7
'4 t j$ 4 RTI) =,." 12 >u. 36 I ~
j'9.9 QV
- RTD -
13 q.G j ~9 Bx S l l-5o. 5 I-
~
8 .5o So. 9
'w. . RTD g" .1l; KZ'u.
RTD i/ 15 el II SR i/~ 8 f(R~ RTD 8 16 6 .I 8~. '7 eo',/+ p RTD i'.1 17 '6 l.'ZD gH. L9 dg 'sp I
~ f2 35; // 85. It
'Gc RTD 1 1S O'S. I
<<TD RTD "
19 20 es-7~ ew. PQ QQ, 8 t-6I 6 H.R7 RTD vl 21 RTD g 22 RTD 1! 23 RIID Ir' . VZ. /6 C~.zs
'72 /f w< /6 6 7. 2-z-67,2
~6. 83/
RIID if 2 RIID 'f 3 c..C. 85 s ~.sg ~ 6S. CV RIID 4 g~es gg Gg G~r. 8$ TGo 2 70 S'M RIIO - 5 D/02
'T/ Wf
~
~/.
~
Rlln .'P 6 . 7r.S RIID P 7 R110 </. 8 Pressure lP 95> 09 SSZa~ c!5 E.O/ 85 Z. C)a Pressure fj RTD - Res'stance Teisparature Detector, RIID>> Relative Iiumidity Detect.or, Prcssure l i~47 Toradnal Operator
I R RnVRn I ll-l-75 OPEIIATXH PROCEDURE 13100.1 XHTEGIIATED LEAV RATI'. TEST APPEHDXX D 4 rCc ~ AMBXEHT TEI IPEPJ<TURE HOUR HO. BAROHETRXC PRESSURE :DATE ~2 Z 7W ROTAiETER FLOll VERXFXED BY 5rg ~~ . XLRT DATA S)IEIP TXHH/SA)lPLE NO & 120 1&9 IOoo /Ww /lOiM P~g RTD fE 8 2 f. 'T~~ 6 M.7 RTD ii 3 P .87 G nl. 9"1 RTD fr' ~f'S RTD 8 5 RTD !r'- 6 t S 9-53 8 ~t- " S w. B R-~i2-a~
~
RTD 7 RTD a> 8 c.) ~ c'. Qq Ci,2P V>~~'TD RTD (' Pw a5. h2- O'- H~ Gs. aS BG- R~ RTD 2," 10 Ks'. on QS,C>> 5 5.o~ P> 5.Ow R'lp l 11 C>q Qn j ~~(. 6V Q~J. 1' RTD ',.r 12 CnN. '3'I ~ eR ~ ~~ RTD ~'i 13 Bg. &C~ e<s8 /'u.sS
. RTD fP 1/;
ir'5 BR 9-/ ~ 8 "f- 8 f 0 "f. 8 Gw.~ 8~18 RTD 8 9 Gz~". RVD )'6 89 <4 Bq. <s Pi 9- I V RTO 2'.-'7 8~Z.(D 9'+. I 'I RTD 2.'8 Q&- /2 C) ~W y(' mrna PTD ri 19 BH-?( RTD 2f 20 c./ c'/ ~ RTD <<1 2'l RTD ~-'2 R'ZD '.> 23 RIID fi 1 '7Z. /) ~Z., /G" R)ID ii' t- 'v- > v- &>-2 5 Q7- Z RHD i'f 3 &C,gr 56. ~z 2- 6c w~ ~ HG. ~z5 RIID &O'. W Z g C~Cj cc&. 9w
')1P Wn,aa gg,oy FQ. a~
Rllll P 6 7/ G/ V(i 56 DS R)ID ',I 7 R)10 innl Opnrnror~g
11-1-75 OPERATINQ P)lOCEDURE 13100.1 XNTECRATED L);AY R'ATE TEST APPENDIX D AHBXENT TD)PEP'.TlKK HOUR )O, MRO;mTRXC PRESSURE DATE j~lZ I+~
~
~
ROTAHETER FLOll VERXFXED PiY XLRT DATA SHEET rvztsue'rz vo. lo3o Z~> //oo 7~q /i/5 /go RTD 8 1 'P+,29 89'-2 j RTD jr' 8 .70 ~tC.'I. PV, C / RTD ir" 3 SY-BC P'/. / PTD 8 4 C~P Q~ RTD 8 5 ~B ~ SI n Q( S~ -r8 BW. 8 P.TD fi PTD J 6 7 'g.~i
'<.. 78 I c/. ~p j &"f 6'9.8 7 RTD i> 8 r 18 RTD G's'. '3m SS. ~l ~5, '2
'-'O
],I,D BS. Oa 89'-0 j p5.01 O'LO k'l 6 '/- rG RTD i< 12
'13
&~/.~/ R ~) - "5 I pv s-r
~ zz RTD -.i BV-- 5p ,~ V.
~ RTD 8 14 as- /8 em. s9 RTD g 15 Q cp, Q'~j RTD )'.-'6 H" ./ 8+ /V-RTO;.. 17 RTD " 18 5'V z I O'S'- / /
6'/~
~~S /' 8 5'.J P,TD .'9 B ~4.66 <y ggc RTD 8 20 S's'r- V7 8 V.+W RTD fF 21 RTD I'2 RTD g 23 I' v2. Zs wZ- 2-7 7Z Z7 FB.
R)1D RllD $ 2 d7- ~+ 6 7~'> V R))D )i 3 HN- V7 G'. ~re g( Cp Cg ( p.O'l RllD ir 6 ~r. F~ R)10 WD, ro op 'o-R)l)) 17 6 mA 5 T Vtr >7 R)1D t/ 7
'R)10 ~F 8 Pressure Pressure
'P 95te> l5/ 9o pP C4 RTD Resistance TQlnpera'turQ DQtQQtor)
R))D " Relative 1)urnidity D"tector, I'XC S sue e Terminal Operato
a ~ a 11-1-75 OPERATII10 Pl(OC) DURE 13100.1 INTEGRATED LI'.AIAT.:. TEST
'7~ PNS APPENDIX D AMBIENT TEI IPEPATURE 110UR NO.
BAROLLETRIC PRESSUhE g O. I/ . DATE 1< Z ROTkiIETEPL FLOU P VRRIFIRD BX . LS~ ILRT DATA SHEET TBK/SA)IPLE NO. //3o /4/ z/os. g~'z / Zc3ca/!c; 3 lz/MIC+ gv'w RTD RTD RTD fr ii fr2 1 2 3 ~Y. r3
~t~p RTD // lV./3 Pv.7/
RTD g 5 V '/ RTD i C n RTD $ i 7 Pv r/ RTD <<~ 8 ~V. 7C RTD /r' ZS'/ g5 Q RTD J 10 wS'l Ci' R'iDiD 11 P"/ 67 V. G/ h I.'f. 'L /
~
ilTi) 8 12 JP a/ 7< ~ 2. RTD rr 13 RTD >.'4 0 +~M. i7
~
ia RTD Ir'5 PV.P7 8 "/. RTD i'/ lta / "l ~ I "/ RTD <<-'7
".18 RTD PTD Tr 19 RTD Tr'0 i/s vs6/ Pv.
P~vv c/ RTD 3i 21 RTD !-'2 RTD 3 23 C; RIID fi 1 72'y 2R -"M7z sz. R)ID =f 2 C7 3S 47 YZ, RIID 'P 3 OB 47. oS IIHD -' 7o o< ~ O6 + g(f Rl!0 - 5 Tt3 ~! R)$ 'r 6 2/ .~Z <~ j'p'O M7 ~ R)ID f~ 7 RIID ~j 8 Pres .Ure r 1 px i RTD - Ras'aLaacc Taapatatu".o DatacLot, RIID>> Relative IIemidity Detector, Pressure Terminnl Oper+.o
OPERATIH PROCEDURE 13100.1 INTEGRATED 1 EAV R'ATE TEST APPENDIX D AIUIXEPZ EIDIPEPATURE FI-) 1!OUR VO. C77 / El!ROHEPRIC PRESSURE 't3C3 ~
! 0 . DAPE~
FLOEl 'OTAIIETER ttERXFIED BY XLRT DATA S!!EBX TB.K/SAf,ALE HO (z4~ z~j, L[38@ Y~ gai~ Pgg RTD fr' S4, a~ pW, RT0 9r 2 8 3 RTD 8 iV,) ( RTD P 5 RTD;r' FV 7 C <<'Z( RTD ill 7 g %r'TD RTD RTD
).'
1' E+ g4.9 RTD Ri~02 11 RTD 8 12 10
~LI
~V." 4 g
I EV( C RTD ~'r'3 'P ~+~cd f.a 3 E~S(
~ RTD RTD i'l'TD v'r'.5
-"..'7 RTD P 18 ZV,/
gQ,EC
~VP~
3 ~t.(, gV, M.
~S
$ S 9
E( I'. og Q RTD .'9 Y v;&7 RTD f-" 20 WN3 gQaf Z, RTD i 21 RTD IE 22 RTD I.> 23 IUID lIID D 2 +7r 0> R1ID iP 3 Q 7.d Q7~/ R!!D 16. 2'." RI ID:.' &.Z ( 7G, Co RIUI ~ '7(i~V R!ID iE 7 R110 '.I' Pres"ure 0 1 ES /8o Pressure 4 2 RTD "" Resistance Temperature Detector, RliD - Relative I!umid ity D t:ec tor, Pressure c. Terminal Oper.i:ox
OPERATXII~ PllOCi DURE 13100 ~ I INTEGRATED LI',AV~ R'ATI'. Tl'.ST Q~Y APPED)IX D I APSXENT TEHPERATURE~+ ~ HOUR NO. EARomTRTc PREssc RE~CO. Q . DaTZXG~ c ROTA) KTER FLOIl 'ERXFlED BY XLRT DATA SIIEET TLRK/SAIPLE NO. ]Ho< /g F/A /p ~ RTD .fP 1 RTD ir 2 RTD ir' 7c RTD i 'PQ~ '7 RTD 8 5 RTD: 6 I:V, gQ RTD i7 7 Fv; F,7 ZV '<l RTD,' g<7 RTD f- 9 RTD i." 10 RTD -',.r 12 PV.E/ g Z i'r'3 RTD
.RTD RTD
.',
ir'5 KV,gC RTD i.'6 RTD i.'- 17 ~V< / RTD i.i 18 85. o RTD rs 19
" ~VP~Q M4'?J .
RTD 20 f4,Wi gQ~ RTD !i 21 PTD ~ 22 RTD i~ 23 RIID /r' P.)ID 8 R)ID i 3 7'. 0>
-T RIID RI!0 .'
4 pC>, 2 i7 F2 7 ~~ RIID './ 6 R)ID N 7 7 Pi)ID fi 8 Pres ure 8 1 Pressure 5 2 RTD " Res is teucc TcmDcr L tu re Det:cc t OL p R)ID <<Rely tive llomidit:y D" t:ec I:or, Prcssure Terminal Operant:or
~
I a aVEr 11-1-75 OPERATXNC PI;OCI D'JRE 13100.1 IHTECRATED LI !V KATfl TEST APPENDIX D AMBIENT TE IPERATURE 11OUR NO. t ERROHETRTC PRESSURE BQ 0 6 :,... UATP~ ~ X
/
1 ROTA':ETER FLO(l VERIFIED BY XLRT DATA SHI'.ET TEE/SA)i~LE NO. RTD Pi 1 RTD r'P 2 ,<p' n RTD li 3 RTD 8 4 .I l-RTD 8 RTD;,' RTD RTD" fP 5 7 8
~<, S'/ r .7p 7
~l"
))K 7F
.7 RTD /,' E 3~
RTD 8 10 p+ 4) F'f.9tr" PTD DFll RTI> PE 1 c (fry .Cv Q
~gl Pg RTD T'1 13 6~@. S FF~H-.
~ RTD f 84'c SV i 15 14'TD FV's i',
ZK 8'7 e<FC RTD 8 16 z RTD -l 17 ~~- y cL FA. Z, RTD 1". 18 RTD 1'i 19 Pa Tu FV' RTD 't 20 8'<, v RTD '21 f'2 1i RTD RTD )l 23 C: RIID b'IID T'; 2 7 oP RIID r$ R)ID 8 RI!0 =" 3 5
'),//
& Z7 7e Rl)D 8 6 7~r', D RIID /s 7 RIID '.i 8 Pressure 'h Pressure ~r RTD - Resistance Terrrperature Detectcr, R))D <<Relative llrrrrridity D" tecto Pressure Terminal Opexal
11-1-75 OPERATIl10 PL'OCINDiJRE 13100. 1 INTEGRATED I.EAl: R'ATI'. TEST APPENDXX D AMBIENT TEIIPERATUP.E g( 1!OUR NO. BAROclETRXC PRESSURE BQ. Q 4 . D!IT~ ROTAIIETER FLOH VEP.XFlED BY XLRT DATA SHEET IIIV/SA,PI.E NO. +~0 /5~~ ~+7I ~/ / -QC1 +7 // /~ +Z~au RTD fr 1 RTD ir'
,7 i.
RTD 1F 3 RTD 7 u'c g(- RTD 8 5 v. v7 RTD li 6 c 7 RTD t 7 pv:Z V 7s RTD P. 8 PV. 7y RTD fP 9 RTD iF 10 p~l.'~/ r P.S.D RTD iF xl ll 12 V P6 fi$ ~7 P~c3 ( I RTD -.'r'3 I'r'4 ~~~cC
~ RTD RTD ir'5
'6 ~</ '7 ~<,F7
~V;l 3 .r>~(
RTD a <~l RTO i.-'7 r4 /I's-o iv(7 RTD,'! 18 RTD I9 F'F. 7/j RTD g 20 RTD ii 21 I RTD ~r'2 RTD i'5 23 C; RIID fr' 72.5 $ PHD 8 2 PHD g 3
~c3, /C.)
RIID fi RI!D -.' RHD i> 6
~>- >2 RIID f," 7 RIID ',F' Pressure 'k Pressure g
.ZxdZZ U
( RTD <<Res-'s tance Te.npera tu re De te" ter, RIID - Relative Ilumidity D" tector, Pressure, TermI.nal Op ntn
I r rwul 11-1-75 OPE!MTXIJG PllOCEDURE 13100. 1 XnTECRATED E.EAV. Kh.TE TEST APPEN)IX D JrMBXEITT TEI EPERATURE HOUR NO. Z4 RAROHETRTC PRESSURE D. 0 3 ~
.. DATE~~~ R I
/
ROTAI ETER FLOTJ VERIFIED BY I ILRT DATA SHEET TDJE/SAI JPLE NO. Q~ Yrlg~lbV~ +fz. jq,- l 10'/ting /7f> <~~F4 RTD 7r 1 RTD ir ~V~C- x . RTD irc 3 RTD ii ~A, $ Q RTD "r', RTD ..'P 5
&D'>~B RTD d 7 RTD P. '8
~+K( Mr 7>
RTD fr' '4, Z/ RTD T'," 10 RTD ii 1>> i~~ C~2 F<. C~C R'l'D ?! 12 ~kr3( P c r~. z c RTD r'3 S ( RTD fl r.'~, W/ 15 li'rD,",
~K>'Z. Eg $ 7 RTD 8 16 P~M .F.
RTO -:.'-'7 Z. p c~/./ sr,/
~
RTD P... XS g+,Q P.TD ~'i 19 7 RTO,'! 20 gear VC RTD rr 21 RTD rrE 22 RTD P. 23 C RlfD RHD,r ir' 2 Rl!D T'f'
- 7. 2~0 'Inial 3 7~4 u~
.
Pi!D 8 cg~ 7 CA
}0!0 -"
RJ~J) Trf 5 6 7CJ. M > &. Mc" Ri!D fi' RllD <i 8 Plcssule !' Pl'cssu1.Q g 2 RTD <<Res-stance Temperature Detector, RilD - Re 1a tive Ilumidity D" tee tor, Prcssure (w Terms 0 cr, t
OPERATXHG PIlOC)rDJRE 13100. 1 INTEGRATED LI'.h>'ATI'. TEST APPENDIX D N SIEHT TENPEBATvrc IIOUR I'O. I sAaomTRxc razvsvr'E~C'.~ . DATE ROT&IETER FLOlt VERIFIED BY XLRT DATA SHEET TXIK/SAIlPLE NO. RTD RTD RTD RTD RTD RTD RTD RTD
.Pr 8
fi 8 8 fi w P,'8 1 2 3 5 6 7
~QB~+7'//
~Mr y// ~. 7 u',
k'; (g 7&
/7.'/
EP
/1< /4 Qr g Y
f M. Zwf M cpf CV; r'Z RTD f,' gr . rs. 3z. RTD ) 10 E. 9' F<. i7 r4,c~ 7 -~a R'JD RTD RTD
~i 11 8 12 i 13
- 4. Cp 7
~r. c.a
.RTD 8 V, RTD ir~ 15 RTD )i 16 ZM~/
RTD ) 17 RTD;.-'8 lr /f 85:o9 PTD i'i 19 < 8<7 LTD ir" 20 RTD fi 21 7/'r P.TD i~'2 RTD ',l 23 C RIID fr RIID 8 1 2 RIID 5 RIID 3 ~3 >. < Z~ fr'I!0
-'.r 5 Rlln f7 6 RIID g 7 P.IID fi 8 Pres ure 'f 1 .Ig yP Pressure j' RTD - Res'stance Temperature Detector, R)lD <<Relative IIumidity D" teetor, P'ressuxe, Terminal Opernt x
OPERATXIIG PI'OCEDURE 13100.1 XNTEGRATED LEAIATI', TEST APPED)XX D AMBXEET TBfPER(TDRE 7F HOUR NO. BAROHETRXC PRESSURE ...DATE~ FC)r'OT&DIETER FLOY(l VERXEXED BY XLRT DATA S!IEET TDIE/SAIPLE NO. pgn PFp~~ IF~~IF'~ ~s HOG r( o/a-.( RTD fr' I~V z~> RTD li RTD fi RTD )'i 2 3 Ir+z~ RTD 8- 5 RTD T 6 9:7~ M7 RTD $i 7 + V'(ED RTD 8 8 RTD Pr 9 RTD 8 10 C'4,~i 7 PI. A~ox 13 RTD fi 12 RTD i 13 RTD 8 N gpg ) F~ 8'g RTD Fr 15 RTD i'i 16 q'4; /4 i.'7 RTD RTn;;: 18 RTD .'- 19 FS <( ~r. ~I RTD x'r'0 RTD /rt 21 RTD lr'2 RTD )',< 23 RHD fi' RIID xrt RIID fr RIID 8 2 3
~ 4~2 Y.~cC Ri!0 O 4 RlxJ) ii' RIID P. 7
~ RIIO -'.
8 Pres"ure 'f 1 ~+~ 7 Tressure Pj 2 Qi4 RTD R88 tttl'ICC TC!IIPQI'CIIICC DCtCCCCtt RIID>> Relative Ilumidity D teeter, Pressure Tern>I.nel Op(;r" .o&
Sa% JJ I 11-1-75 OPERATB10 PIIOCEDURE 13100. 1 INTEGRATED LEAV R'ATI:. TEST APPENDXX D AMBIENT TEMPERATURE~f HOUR NO. I BARO'METPIO PRESSURE~~6 OATr: D ROTQKTER PLO!1 VERXPIED BY XLRT DATA S!IEET TI)K/SAl~fE NO. ~~I+d +it/> /@+~ ++ +g RTD -Pr 1 RTD IE 2 RTD )Ui 3 P'Q c. RTD 'E RTD E 5 6 'P4'( - 7 RTD )PR 6 RTD 8 7 M.'P C RTD 'E 8 Z'W. V RTD )'! 9 FS. gu' RTD )E 10 'ooC R"AD rf 11 4' RTD Jl 12
~OS
~P ~ RTD i 13
.RTD ll 16; j
RTD )'/'5 RTD )P 16 P~. /a .g.~4'/ RTD 'l 17 g~ 2.3 +Y.Z S B.V RTD P 18 P) Z RTn .'. 19 7i A%7% ~V'c 7 ~ RTD SE 20 c4 V7 ~Me 4/C P~ V7 RTD )i 21 RTD PP 22 RTD ) 23 RIID (i 1 P. RIID J 2 75'C'C RIID )f 3 lOin 8 Z3 RllO RIID ~i '6 5 RIID fE 7 RIID g 8 Prcssure lf Pressure fj 1 2
~)2L /7 4 RTD - Resistance Temperature Detector.,
RIID>> Relative 1[umiclity D" tector, Prcssure Terminal Opc.ator
i 1 iLV<'m L 11-1-75 OPERATXl'IG PI',0".EDURE 13100. 1 XHTEGRATED LEAI: KATE TEST m APPENDXX D AHBXEV.T TEHPERATUP,E 1!OOR NO. 2~9 MRO KTRXC PRESSURE gW r//Q D/!TZ ) L /'Zi ROTAHETER FLOll VERXFXED BY XLRT DATA SHEET TDK/BA1PLR NO. ~l~s/+~ ~t) RTDP, 1 RTD Tr< 2 E9 RTD i'/ 3
.
bW'TD
)i 4 e t
RTD -'.i 5 %<V RTD rr' ~Su RTD $E Mi tZ ~)C RTD 'l 8
~5~75
'5 RTD i" 9 RTD fi 10 <5;oM t))'
P.7~J) RT!) !'i '<2 i 11
~e/ '(D 7
~8"Py, vb . s~rc-RTD i 13
~ RT d 14 >~i.S 4 15 f 5( p t., Cjf ~
RTD V// JJ
/
RTD )'P 16 RTD RTD '. 18
'7 K~. /(=
roc rv ~ e R >, //' f g)g 5
$'5 /&
C RTD '19
..i ~V(7 f
<T/ P' e
RTD )'r< 20 RTD g 21 RTD i,'2 RTD )~ 23 72 3'3
/'. 7g,g~r .
RIID 8 1 ~
- 7 F3 M7.
R!ID ),t RHD)i IIHD ),"- 2 3 "
~
~m 7
WC ( (-7 5j ze MZ RIID ."..' Ie5C ~c Rill) P 6 RIID </~ 7 F.IID g 8 Pres"use i Pressure !/'. { RTD - Re" stance Tampa"stere Dete"ter, Rill) - Relative 1!umidity Detects Pres"ure
~ ss R Terminal OperaLor
PAGE X r ll-l-75 OPERATXHQ, Pl!OC! DURE 13100. 1 XNTECIMTL'D I.EAR R'ATI', TEST
~
APPENDXX D AllDTEllT TEtlPERATURE 7 ~ 'IOUR NO. EAROIKTRXC PRESSURE 9 0'0 ...DATE E eW /P ROTAI ETER FLOIl VERXFXED BY XLRT DATA S!IEET TPiII'./SAIPLE NO. a l s ol'~A~l g >DO Y~g RTD 7f 1 ~HAS FV~4 a RTD fr 2 c7 RTD ii 3 i7 cI
... RTD !'i ~C.L Wl:-Q D~+~> I:- '+mJ,L. EJ2 RTD N 5 pV PTD / 6 8D RAD ~d 7 I 0.< /
FTD RTD
".8 fri 9 85 BS RTD fi 10 5rOg Mr 3 /
V'~ .7 5, <,'+, wq. tf fl RTD!r 12 r< y RTD 2'ri 13 ~ 6G ~
. RTD 8 14 RTD Tr'5 RTD ~v'6 RTD )" .17 '55'/'AS RTD -.',.'8 F,TD .'9 c/
RTD I'l 20 g RTD li 21 l. FATD /r'2 RTD !! 23 C RIID RIID Ir'
~j 2
~~Vga RHD RIID 8
!i 3 4
S2'M RI'0 7p, ~ Ca,a c RIB) ~j
"
6 D~YC RIID 7 RIIO ~j 8 Pres"ure 'r Pressure g
~ZI y RTD - Ra 'ataace Tipanatrar aDeatectar, RIID " Rectal:ive llurnidi.l:y D" I:eetnr, Pressure I
Terminal 0>>ernPAr
J AVE 11-1-75 OPERATXNQ PROCEDURE 13100.1 XNTECRATED LI'.At.'ATI TEST APPENDXX D O AMBIENT TE!fPEBATIKH~/ HOUR NO. BAROHETRXC PRESSURE ~ DATE~rp c ROTA1ETER FLOU VERXFXED BY XLRT DATA SHEET r/aS TQK/SAI.lPLE NO. 2 XZO~Q/yQ gF +~~5 + RTD .Pr 1 ZVDi RTD 8 2 RTD ~i 3 RTD I= L- TB'9
'TD fr' c~~<)
RTD li 6 RTDt 7 RTD '~ 8 RTD 8 9 5~3; Z<~< 8'~~A RTD f:- 10 7's.c) 7 ~o8 R"xD vi
>',-'2 ll 7 RTD 4 /~6~
RTD vi 13
.RTD )7 14 RTD R"'D " 16 FH J~
RTD P 17 RTD '8 PTD ii 19 RTD ii 20 RTD ~i 21 FTD i,'2 RTD )P 23 C RIID 8 RIID i r2 1 RIID >'r'- 3 RIID 4 C>.~W RII0 -'i 5 RIID 8 6 RllD fi' P,IID ~' Prcssure 'f Pressur.c .~< S'n
'TD - Res-'stance Temperature Dctc" ter, RIID - Relative Ilumidi.ty Detector, Prcssure
I PARI' 11-1-75
~ ~
OPEIVTXHG PllOCI DURE 13100. 1 XHTEGRATED LILAIAT!', TEST APPEHDIX D AIRIEHT TEt!PERATVPE IIOUR NO. BAROIIETRXC PRESSURE ~ DATE /Z 2 3 ROTALETER FLOU VERXFXED BY Q XLRT DATA SIIEET TINE/SAIPLE NO. Z. ZBe>/iGQ~ &RICO Gs. 2.7 RTD f' RTD 3r 2 8'-~ Q1. 8'+ 7 rr RTD li 3 RTD,'h 4 I'X RTD d 5
~E.I=7~t='&1" RTD ix 6 RTD 8 7 RTD Y.l 8 8~
89 77 8 f.'1l CI. Y ci RTD P 9 8~- 26 RTD I 10 85; 9 '7 W P'i. i fs 1 1 gt-('. 7~ 89. g~D'2 6'~. 9<i RTD i'i'3 <e. PV 8~/ ~~8 5' S'; sj D]'X Gg. Q'7
. RTD P. 14 RTD i'i 15 RTD i'i'6 rM. '7 ~ gy 9'z IFti
&~i~ i RTD;.'-'7 .4 2. &~ Z5 RTD ': 18 I'lG ~A ~ 8~,ii~
RTD 2'it 19 ~&~, 7S RTD ~'i'0 f&
~
RTD i'i 21 RTD i 22 RTD L% 23 RRD ii X 72,9g R!ID l'l 2 Ca. r4 RHD
'RIID IF' ii
~ ~. ~aC) C7t &
RII0 RID)
.5
-."
ii 6
~d ZZ. a/
6 RIID I 7 RIID ~' Pressure 4 1 g5> 7( Pressure g 2 RXD RQQ 8tCl'lCQ XCCIPCCQtctC DQI:0 "Gty RIID - 1(elative I!umidity D" tector, Prcssure Terminal Operator.
R tnVle 11-1-75
~ ~ ~
OPERATENG PllOCI,"DURE 13100. 1 INTEGRATED LEAtATI', TEST APPENDIX D P 0 AISXEHT TBiPEPd<TUPiE IIOUR NO. t DRYE~r> BAROHETRXC PRESSURE ROTJQIETER FLOll VERXFYED BY~+ XLRT DATA SlIEHT TLZ/SAI~I.E NO. Od3O r'76
~ II Z~
0098 / ~~V Q/OO ~ ~78
~
+ l/9~
RTD Pr 1 RTD 8 2 8-I. &C RTD lr' eR >8 ~ 8 '"I ~ 79 RTD,"i RTD t 5
~iLBil+ ~~Li 6 .S i=Md ~~/ ~~I v(w8 C'I CICI RTD 1i 6 e,>8 Cr O I.o
{ D RTD >i 7 RTD t' B9 77 7 8+1W / 3< 8~. 95
'i'.
RTD 1i 9 nk BS. Bq'- RTD '. 10 8< </ 8S; 0- 9z~. i Ri~ V 11 8+. &8 7~ &~~/ a~. 76, cj, p7 6+. m~ RYD '.! 12
-." 13 + un CCO e/u8 8~/-~'/-
. RYD F lo e I. S.z. 8~/. SB RTD 0 15 8.v 7<
RTD ir'6 3< /
$ G~./ / 8"j. i /"
RTD !'.-'7 SV. ~~ RTD ).'8 9~, /'/ S. iW 8>~ /g es, /v P.TD 1'i 19 e~. ww gg. /z R~/. 7 'F B+.'~ 2 RTD 1'.t 20 8~.5 e ~ +) 8</ '/'6 RTD i~i 21 RTD RllD .'1 ls "7N ~~., a9 Q DG NS'o. 7r RIID !." 5 /C 7/ 7Q. T/ RIFD 8 6 ~.Z.oa "7Z, QS wz, oe RIID fP 7 RIID '.i 8 Pressure 'j 1 GSl 7 ~ g5/ 1 l 8~1 Il J g~] 7o Prcssure f< 2 RTD - Re -stance Temperature Det:ector, RIID - I'elative Ilumidity D" t:ector, 1'ron"ere Yern>lnnl Dpernror C'P /miioif
11-1-75 l ?'PERATINQ PltOCEDURE 13100.1 XNTECRATED I.EAR R'ATl:. TEST , APPENDIX D AMBIENT TBIPEPJt TURE IIOUR NO. BAROM:TRXC PRESSURE ROT&ETCR PLOT 1 D< R// VRRTFTRD BY~8 ~~
;... DRTR~<~- ~>'7S XLRT DATA SHEET TDV/SAieLE Vo. ofa F rjo ~)vs',
/iS
~@gy RTD R 1 6 l,~5 gj; 8Q Cu7 z.s g q',~5'TD i 2 Q~C ~r Q. "78 8%- 7'8 6<s. ~7 RTD2 RTD RTD 8 v'
3 5 B~l'I
~F~r~
BM. W9 I r=. ~f:-'wi= GR. ~7 TEfh ~4.C fEIQ P~S' P.TD i 6. 9 6
~
6'3'+. v.G~ ey.e, RTD f 7 G9 f9~ iD RTD RTD i 8 B R.'>7 8 grig
~iBaG,'7W g3 Sv 76 ~
c/ (r-' RTD ~-'0 65. os BS.C+ g~p. C>8 Ss.
&9."77 G .l 78 ~
I,~'1) zt '32 RTD T1 13 8'1 52-g /~ Q,i,, SR ~8~. GYM~ 5 RH.5 j 87'~,C (
+ .
GV- i G'+. VM RTD g 16 c H.17 8~ ~ / RTO i.-'7 9. 2->~ BRe <3 RTD,'..'8 GD, lE' CJ g /Q 85, l<< VZD,'; 19 Qg. 7& Q'g. 7D RTD it 20 g+ Qa ec/ l7 RTD J 21 RTl) fT'2 RTD >: 23 RllD Pr 1 7Z. PS vZ 8~~rC RHD if 2 Ci /~9+ g C~ 4 7-RlfD 1'f'3 Qw, 6< Cv, Ga K~. <'T ~ V- C~+ 101D " '7<3. >~ B7 TOi 9 Rll0 -..T 5 WO, N woOr vo.c r RIU) i7 6 78 0@~ 7ZrO> 72-. 0( Rllo 8 7 PJl0 '.f 8 Pros uro f 1 QSt 70 Bgl 7O Qs /6' J 6'5'igg PFessure 9 2 RTD - Res-'stance Tomprraturc Detector, RllD - Relative lhunidity Detector, Pressure Terminal Oporat:or
ll-l-75 OPERATII10 PllOCI DURE 13100. 1 XHTLEGRATED LI AK KATE TEST APPHNDXX D O AMBIEHT TBIPERATURE (o8 $ 10UR NO, I BARO IETRXC PRESSUI'E H. // ...DATE~/+ 3 75 ETL'R PLOll 4'OTAI VERXFXED BY jC4 XLRT DATA S?IEET TDZ/SAI{PLE I O. RTD Ir' I'TD RTD !i '3 {i 2 D~t'~cc.0 8 <l. IP 7-6 RTD )' Pc= CG RTD P 5 RTD !r 6 8"f '79
~
RTD fi' 89, SS RTD 8 8 GH.
~~'~
B VS'5. RTD" 9 I R'lD '-'0 +5, t p,5.09 85 G6 RED !i 11 hv. ve 6 <. "77 Q'~. z t RTD .! 12 Q ~. Gw. ' r'3 +~i., +
~B'
~l.
~E5 RTD .4G RTD 8 14 V'~/
RTD !'r'15 6 VG RTD " 16 Qc/ / 69', ! ~i 8" le 6~( {8 RTO !.-'7 RTD,",. 1S RTD .'- 19 ec/. Z.~ B~l, 7& G'/. z
&5, /
8'/. '7~
~s, Qg.7 ts 2.>>
RTD 'r 20 89. RTI) !i 21 RTD i" 22 9'p,g 'C RTD !9 23 RllD 8 R!{D,j 1 2 7z ~r3 6T
/3
<u- co 7. 98 c/
RIID & 3 87, 6) QCy C 7. '7/ I{?ID -',: 4 T ot '5Q ~ra'z.. 7o. B9 7C)r &8 5 wa.6> 7D. T 0 7m
~
R? i{{) '..r RI!II) j 6 m<- /8 ol 72 ~O RI{D fk 7 RIID /i 8 Pres"ure 8 1 astra Mi 68 Pressure g 2 C4 RTD Rcs stcllcc Tctllpcrctclc Dctc LGr t RIID - Rcla{:ivc 1{umidi{:y D" L'ecL'or, Prcssure
PAGE 1 11-1-75 OPERATING PI'OCEDiJRE 13100.1 INTEGRATED LEAK KCTI'EST C APPENDIX D AME7EET TEMPERATURE CoCa ~
' HOUR NO.
BARO IETRIC PRESSURE QO,/0 '... RATE />/ a />~ ROTAxIETER FLOr/1 VERIFIED BY TDZ/SAIIPLE NO. RTD fE 1 03&a I ~S ILRT DATA SIIEET ODt/SI ~ay @qadi 1 Q 8//Q RTD j/' 8 ',Q7 i-I, Co 7 RTD 1/ 3 e~. 7C 6 s-g-7 g//9 RTD RTD PTD 5 8 ii 5 6 8 9.VC oLI a EC.c:
$i R.~7 ~+.9~K /
%6 RTD 8 7 6 +.81 ap RTD '-'
9 E77 cD ~.'I~ RTD /rt 9 R/A. &5:30 GS,A ~~5, H 9,0$
~
RTD 0 10 5 o'7 85.0 J RTD lF 11 8 ~ 8 8+i //> 8+ 7~o RTD 8 12 / RTD /: 13 R ~ 5I 6 ~5~ Gg C
.RTD 1.'4 g9.e x Qcj. g RTD TE/ 15 . C=f 3 RTD 8'6 8 f. IG 6~/>
RTO ip 17 Sq. z.z ~~c.Z y RTD ".18 85. IQ es,rV B&.iY RTD ii 19 .v3 ~Y.VT- BY. 73 RTD i0 20 8+,vT RTD i'i 21 RTD t/'2 RTD '-'3 RIID ir 1 /2. g'6 B.. o/ 7Z 9 "7 w B.a/ RflD fi 2 67. 78 C'V. ee RflD 4 3 g Vr /PZ- Co 7,'7& ii 4 7G/ 70. 9Q 7CDr ~~+ RIID Rf!0 RflD
.5
-"
8 6 2 0
>9'6m
'70r '7Z po.
72., 0 vj TCD 7~/
~
7?~/ RIID $il 7 RIIO fi 8 Pres ure /f Pressure f< RTD << Res'stance Teiapereture Detector, RIID " Relative liumidity D tector, Pressure, Tarn>inal Operator
rc~ur
- 11-1-75 OPERATIC PflOCEDURE 13100.1 INTEGRATED LEAK R'ATf', TEST APPENDIX D AMBXENT TIPfPERATURE 6Z e ~
HOUR NO. BAROMETRIC PRESSURE &)-)' 0 ...DATE ~2- 3 ROTAllETER FLOP VERXFXED BY~~ TDX/SAifPiE RTD 8' NO. GV3O /w/Z'7 XLRT DATA SHEET gZ. <39'+~X RTD.j-' 8 9..cs .CB RTD ir 3 8%. vc L. 7 RTO N FLF) mMZ c. RTD E 5 P.TD fi 6 &Q. 7M Qg.'7? RTD 8 7 G 'Y. 87 RTO:=' 6 .a> RTD fr 9 BS. D 3s'w.cw 5'9 S RTO ~i'0 SS. a7 R~000 11 5'~1 > RTO 8 12 RTD 0 13 6 5v~ RTD lr 14
)'-'5 Gq.s RTD 6 "I I2-RVD )! 16 RTO u'7 8 .f8 e .z~
..st'~
~R ~
l 2 RTO;.-'S Bs,iv 8S, eg RTD .'i 19 Qgs7& V. '7+ RTD Pr 20 H~/. M 6 X7 8~g RTD ii 21 I'- RTo 22 RTD P)23 G'V. RlfO 0 ~3.
~
M~.V8
~7.7pi lg f.'HD OV'H.C
~F 2 RHn .! co>. ~S. Gv- Ts RllD 8 4 70V ~&. +Z RO Rl!0 9 5 T+ 75~ 70 1:
~ 7 O."1 R16) N 6 WZ ~ G 7K. a"7 7 RllO i'P 7 PHD !E 8 Pres
'V ure 'k BsiC + gSt ~q ~5 tg Ll Pressure f!
RTD - Resistance Temperature Detector, RHD - Relative lfumidity Detector, Prc ssure
-
Terminal Operator / C~
PAGE 1 ll-1-75 OPEIKTIllG PROCEDURE 13100. 1 INTEGRATED LFA),. RATI TEST APPENDIX D AMBIENT TE'IPERATURE Cn 2 1- HOUR NO. BAROMETRIC PRESSURE QD. (6 ...DATE~/2-I ROT&KTER FLOIl VERIFIED BY +' ~( ILRT DATA SHEET TIHF/SAlPLE EO 6)+Z> '+ /BV +~+ +~~+
/B~ +~~
+7 + ~/8 ~/~ + W9 Pi 1 St-2 I RTD ir es 4 RTD )i 3 RTD ii 4 RTD fk 5 Q'TD "i RTD RTD i~6 Sg. 8 RTD RTD t,'
.8 7
~ ~l ~<+ (
)r'0 b.P 7 eb 0 es.o(
RTD g~i~
~
R i~0). 11 PTD 8 12
~B RTD:" 13
~ RTD fr'4 RTD )r 15 RTD fk 16 gi <l- Q 1
~84 8< v.3 2
Gs. wg
~e8~92 RTO )r 17 v. ~i 8> I'3 RTD ii 19 RTD 8 20 18 )
8 Li. i I ~R. 7i RTD fi 21 RTD &'2 RTD "23 C: RIID P. 1 75 OL 73 07 5.0 RHD )i 2 oo pa Rs t'o g.o 3 RIID ) RIID 8 3 4
~7 ge.N~
~ 7Q g+I RIIO -' oM l> 82.
RVJi ii' 7 72MB. l2- I RHD /r' RllD ti 8 Pres"ure 0 Pressure 0 RTD - Resistance Temperature Detector, RIID - Relative Ilumidity D te tor,
, Pressure
I PAGE 1
.11-1<<75 OPERATING PllOCI DURE 13100.1 INTEGRATED LEAi~ RATI TEST APPENDIX D AMBIENT TEaIPERATURE FLOtl'g BAROMETRIC PRESSURE so.
j['OUR op
,... DRTE~/Z BY O NO.
W
/7'ERIFIED ROTAlETER ILRT DATA SHEET TBK/SA'.PLE NO. CM S> P'gyro 0695/ ger O><rD 7 HoZ RTD Tr 1 o Bq,zz RTD fr 2 ;6% Ac 5 " RTD I'I 3 (. 7 RTD RTD RTD fi li P 5 6
Qct y { lg 7'P n~t OCLE(e RTD 8 7 RTD 8 8 RTD /,' PS. 3 I RTD -'-'0 f', O5 Bs. 06 '
,
Rid<11 nS'c~Z
+ S f ~ 7 RTD 8 12" .3Z RTD 13 ~ $$
~ RTD i-'4 /7 'V.
RTD Tr 15 Pf, g 6/ w-RTD 0 16 RTD '..-'7 RTD,'.I 1S
~ I '7 65;/2
~I.
~
I. IC,
- 2. e~zr~~
&5;
~Z RTD .'i 19 -13 <'n 7/
c- a/ c~g RTD j< 20 RTD li 21 RTD I'2 RTD 8 23 RIID 6'HD
>$
8 2 3 0 3.{o g Ol ~e.c
.8S Y ~r" O7. ~B.
- 73. I z-
+8, Cg T. ~~
/Z-RHD 70.'I'L rc- vs RHD RHO 8
9 5 QO, Q~ O,Z3 re. WZ / r" s3 RHD ~i 6 RHD N 7 RHD 0 8 Pres ure 9 4ressure
~S IbZ BiOI~ 85)< l P RTD - Res"'stance Tenperaturo Dote tor, RIID>> Relative Ilu.nidity D" tector, Pressure Tarnlnnl OFcrnror ~ E g~~~
I PAGE 1 ll-1-75
~ ~
OPERATING PROCEDURE 13100.1 INTEGRATED LEAK RATE TEST APPENDIX D
~ AHBIENT TPfPERATURE 6O HOUR No.
BARO!KTRIC PRESSURE ~OF /I ,..:~~ /z/>/7~ ROTA'TER FLOl1 VERXFXED BY C g ILRT DATA SHEET TER/SAtPLE NO. over/'P,'< o <<7'%< ogre 8"P.'H. RTD Pr 1 gkzo O'K zo gg Zo /8 RTD pi' RTD x'x 3 BV 7W 8 7'W Re. zc
~lur
~
RTD Pi 4 ~WC c-~~@ Dc=(.&7&D 8~ <K7 &D C= I C. E> RTD 8 5 ev. 0 $ 4/ 6F&;~y RTD
'-'
c, P 8~/. v~ SG" RTD f' C< . Ge.~ z / RTD 8 85'/
~~
RTD'P 9 +5;Bo C5', D/
,r~
,RTD ~ 10 85.ot BS.~S GS.O U 9 "77 Q.
P.i~OX RTD RTD 8 12 i 13 8 .S
~B "S ~
~ ~ DZ, ~P + ~
SV. 5&
'~ r.
~ RTD i-'4 8 6'~/ V6 8~/. P7 RTD 15 6'/ 8+-8/ %<no RTD RTO
>P fP x.-'7 16 Zdf .2 f BW, /W Q'+, RO 8//~
~Ge', c RTD P.. 18 5; IN HW, G+'. To r~ 85 /f 7~
PTD ii 19 8 ~r.v RTD 8 20 gc/ RTD RABID fi 21 RTD ~~ 22 RTD d 23 8 ~3, I 5" v3, /8 z3, /'6 R11D Rl!D i Rl!D 4' 1 2 8, //
&'7. S> (7 ocj C W.
c>
~r r
RklD P Rl!0 Rln)
-'..'
7P 4 6 7P. ro,8 4
~B6 O.
~Z~ZD Wl Vo. So zo.
FP . /'~~ iP 7 Rl!0 'i 8 Pressure g B5lC O g5'/ @o Pressure g RTD <<Resis tance Temperature Dete" tor, RllD " Relative llumidity D tector, Pressure, Ynrnfnnl Opnrntor C.
l PAGE 1 11-1-75 OPERATING PllOGEDURE 13100.1 INTEGRATED I.EAR EAT.': TEST APPENDIX D AMBIENT THIPERATURE HOUR NO. BAROK'.TRIG PRESSURE 0/ j~/~/vs ROT&ETER FLO>J VERIFIED BY-ILRT DATA SHEET TZV/SAMPLE NO. carol'- 08<~ ~ice'gao <,vo
~
r'l~~ RTD 1 89, lP 6</ ]9 Pr e'6 ~ 8e- 6/ B f,C/
.RTD RTD RTD f-ir i',"
2 3 ~8- wD C'e-E C. Ceo
~V'9 Vc. ~wc IO B~s. >z.
QM~~ CJO a 8 42 i'6 RTD v~ 5 gi RTD . T8 8 9- 7S' RTD 7 o~g . 8'2 R~D RTD
<
ir'- 8 9
&W / .
Qs; z4'
'7/
5; '2.7 RTD l'0 S~O 8& DH Bg. ~g RID '~f 11 ew 6 g'c/. + / RTD -" 12
~~. S'I ~
RTD RTD RTD RTD
-< 16 13 15 j'+/7 Q~/. +c O'V-G~'-
Qc MS 89 jg 8< SV-RTD g 17 p .z/ ~B. /'0 / // RTD ~'. 18 8g, GW, RTD ii 19 /0 RTD Pr 20 RTD 21 RTD !'2 7i RTD 8 23 RIID 8 1 D.'/ w3, /8 Q. Z/ RtID ii 2 g6'. r6 C8./ C7.+~ RHD 8 3 RllD 8 4 ~o. WM po, 54 RHO -< 5 70. 70 ~0 i gQ VO. 5'3 RIS ii 6 MZ. zP 72, Z/ RIID f~ 7 RHD /A 8 Pres"ure 'E 85~% 8 Pressure RTD - Res- stance Temperature Detector, RiiD>> Relative Ilumidity D" tcctor, Pressure Tcrmina1 Op'er'tor
PAGE 1 11-1-75 OPERATING PROCIRDURE 13100.1 INTEGRATED LEAi RATfi TEST APPENDIX D I w<pf i AHBIEN EI IPERATURE HOUR NO (
/In BARO IETREC PRESSURE ROTA'.ETER FLO!I 3) 9 'S.~ R. f BY~8 IT-/~ITS'ERTRZED
'PI)-R, IA.~
oct /5 C I ~l I RT DATA SII;ET TTLK/SAIC'LE RO. C 9 Z tn ( Z O T q~( 89 I'7 BH. IS 8w. (8 ', /6 RTD fr' 6 RTD i" 2 BV 6I~ e<,c z. 8 f,Co RTD fr' Bw, ~x eon 72 ega 1 Z- 9'( 7 2-RTD 1'T 4 Ot=iPtC WF LC 1~ 5E.LC n- n
'W2-RTD " 5 gg, g~ W.3r 88, fz- 8 RTD ii 6 Oq 7~ 7 I oS.VW Sy. T/
RTD f' .8V, BI Q,g 9s 8f ee, ww RTD TT 8 8 < o ~~a., 7 I eg, 8s. RTD ir 9 85. 2v ~~s Z.7 c~ RTD 4-'0 03 gS', C3 > Q5, 03 Gs, R i~Bi 11 /B '8 fn 7S 8i. w6
~
RTD 8 12 RTD 1I'3 RTD i" .14 P-Ir &I 8g.~w
~g, 8v, 5S Q </,Bo GV, SR-8 I'-I- "l 3 RTD Tr 15 ev. es 84. GB RTD iT 16 iS 8'g.
RTD T'l '17 8 I~ ~<. /'p IS'c~ RTD i" 18 85 II 85, io ( RTD T'ri 19 ~9 "7 I~ GV >Z. Ge. vl 9g. yo RTD 8 20 , 9'3 8~.~~ RTD ~i 21
, RTD ~r 22 RTD IIi 23 RHD 7X2I 73, '2.W 79. 23 ir' 8'IID GQ, io 68. /6 @9,/'o RHD 3 ~"7 ~~ V
~cn 1'! ~Co RIID i'r' Wa ~o, sg 7o, S 70( S9
'RI!0:! 5 7D< 7o, P6 '7o, 9'5 7O( r)C RRD P 6 12, 2.(
RIID //' RIID i48 Pres ure 'k 1 equi mM p 5'az Pressure >ri 2 ( Rl'D - Resistance Temperature Detente.",
- Relative ihanidity D" tcctor, RiiD Pressure Tnrniinal Operncor 't
PAGE 1 11-1-75 OPERATIHQ PROCEDURE 13100n1 INTEGRATED LEAK R'ATE TEST APPENDIX D AMBIENT TEMPERATURE
't /5 /2
~ HOUR h'0.
~ /~5 BAROMETRIC PRESSURE ROTNKTER FLOll Hr S,c, F.M. VERXFXED RT
.DATE~/2
- a. E /(~
XLRT DATA SHEET TVK/SAMPLE NO. /'Dao IM /a/W Z+ df. RTD RTD RTD ir' ii 8 1 3 Bq. u/ JC
'f. 7/ ~
/'. 7wG/
Pg RTD iF ~~L.U "pC D~MC=ia,g C Lcvc 0 PG L.B. L9 6 J'. Ql RTD 2/ 5 B~, um ~F RTD tj' 6 8 .-vS ."/. 7w J'/ RTD QLf,MP RTD 8 8 8 7/ RTD RTD P d'0 9 65. 26 Qg, o~
~
H, 'Z.t" ~5. Pg. p/ 2F
. G Pr.z c, gr. o/
R1 0~1'Tfl 8 ?7~ "/ ~ 7C
~! 12 RTD 2'I'3 pe.s <
.RTD 8 1/; PV. VC RTD 2," 15 C
Bf. 87 Zv. RTD 8 16 / P'/. /3 RTD ~J-'7 'Bl/8 4J N'S. RTD P; 18 85,oa 5,/ gs'. / /r PTD x/ 19 89. o se,6$ "/ 7 gy.7C RTD kt 20 89 "l3 BV. VV J'~. gc RTD 21 RTD ~-'2 RTD i! 23 C MID f.-'HD TF' gO r P)'Z i 7B, 32
/g 73.L l RHD f 3 &'7. ~7 ca,o/
vo,55 a1. 9Q
.RHD C 4 Ol lOV '? p. Qg ? o.(V RHD -"'
70 c] 7$ .0/ 7/ I
~
RIII) I1 6 Q Z. 2.z. ~ '7z ~ z 7 Z ~ Z RHD /F: 7 RH0 F' Pres uze 'j 1 BSi s/ Pressure j2 RTD << Res-stance Temperature Detcctcr, RHD - Relative Humidity D"tector, Pressure Tnrndnnl Opnrnnnr ~ P~
I PAGE 1 11-1-75 OPERATXI'JG PItOCJDURE 13100. 1 INTEGRATED LEAF~ R'ATI TEST 4 APPENDIX D 0 AMBIENT TBIPERATURE HOUR NO. BAROaKTRIC PRESSURE .DATE. >~- '3 -7 s
+~ ~
ROTAIIETER PLOIJ 3,'I/ s c FN VERXFXED BY~8~ TDIE/I SAMPLE NO RTD Pr 1 II oo / 'r / XLRT DATA SHEET Ill~ /g I/3o / II IIV5 RTD i' RTD 7P 3 RTD 733 4 9 ~~ r=7t'b eL ETC' rXG LO 0 & ~TCO RTD 8 5 f. r// RTD iw 6 Iv. >/ $ 1. 7~ P-~ 7s RTD f/r 7 RTD Y.r 8 j'9 7 RTD f,' '~5. z. zC pg o> gs, o'/ X/'S. RTD 7'," 10 o3 RTD Yi 11 IH. 77 P 'f- 77 l'y. VP
- RTD /-'2 RTD;i 13 P/.3 P1. s'/
Cv, as-PV.S 'f
. RTD f/ 14 PV. V< Pg. //C lv'. vP RTD 3/'5 gv. P/' fY'P RTD Pr 16 /. / "f ~
py. /s / "/ /J RTD P.- 17 Pl. /7 RTD ", 18 RTD )'i 19 P/,C 'f 7 RTD ji 20 I'. vv Pv 0 RTD ii 21 RTD i'2 RTD ) 23 RIID I/' '77 23'../f
- 73. 3V' 73 ~ 3f RHD 4' P. 2r' .P c7 RHD fF 3 C P,OQ i.oz ~P. oX RHD RHO RHD f
-"
ii 4 5 6 Pr'J~ ~ 6) 0/ 7o 7Z..3 I I. o ~ (S'>, ZI 7o, c,P 7/. o~ 7 Z. 2 7/ LE
~ OS 3/
RHD foal 7 RHD 4j 8 Pres
'V Pressur.e ure 7P $ $/ v7 /3/'fb J PS/ Y~
f/D 2 RTD - Resistance Temperature Date tor, RHD - Relative Humidity D" tect:or, Pressure j Terrrlnal Opcrat:or
f PAGE 1 11-1-75 OPEIUlTXNG Pl;OCEDURE 13100.1 ItlTECRATED LEAK RATE TEST C APPENDIX D AMBIENT TEMPERATURE HOUR HO. s MROHETRXC PRESSURE O t> /s ~
.DATE c.
ROTAIETER FLOP VERXFIED BY XLRT DATA SHEET HD .f~(-I +(Q IR(>~+I ( +BC> X I g O'ZIIR/3/IlPLR ( &LI5'(( RTD $r 1 RTD 8 2 RTD 'r' Y;7 > RTD $E RTD 8 5 RTD ~'
, 7 PTD )/ 7 RTD 2." 8 9'.7W RTD fi' s.AC RTD f> 10 r~ oC
'KV; 7C RID 11 RTn 8 12 RTD -.'i 13 '~/< .W
. RTD 8 14'TD r
R3.D 0) 16 RTD 2'- 17 RTD " 18 RTD >r- 19 r f~c RTD 0 20 f4.s i
~ RTD ~'i 21 RTD ~~'2 RTD P 23 Rlrp P.
Qu/ R11D RHD RIID vF (~3
"
2 og. j'0 RHP C. OI ? RID) RllD iP t,' 6 m -3 Rllp w' fj 8 Pres-"ure /( 1 Fb /4W SiQ sP&c 4 S s fs~cl RTD - Resistance Temperature Detector, R11D - Relative Ilumidity D" tector, Pressure
.Terminal Ope.s..
PAUL ll-1-75 i OPERATXNQ PI'OCEDURE 13100.1 INTEGRATED LEAP, RATE TEST, APPENDlX D AHBIENT HOUR IIO. TEIPERATDRE~G'IAROmTRT.C PRESSURE ',* 5 ~ DATE e. w VERIFIED BY
~
ROTDETER PLOT 1 7 L 'gQ t S 4 5S!JEF ILRT DATA
) 3qLP RTD Pi 1 RTD jI 2 %.4 W RTD 7'I 3 RTD 7~F 4 RTO 8 5 PiTD g 6 RTD 8' RTD 'l 8 RTD 8 i-'0 9 5.>
RTD ~5. c>S Q. P.TD 7F RTO 8 12 RTD,'3 11
'.3&
.RTD 8 14 bO RTD 7; 15 ~% Xl RTD RTO 7<
L-'7 16 ~+. t4 RTD " 18 PiTD I~i 19 'E +7 RTD " 20
~
RTD 7'fI 21 RTD g 22 RTD I~1 23 RIID /P 1 3 RIID RIID 7'f 7 2 3 4 X~~. RHD
.5 7'FL Rl!0 -"
RIII) P J 'M 2J r RIIO /' RIID f 8 Pressure RTD RIID
'k 1
;r-
<<Res-stance Temperature Date" tor,
" Relative llumidity Detector, 3~mW ~ .SCC-nr si4
- 2. >C.~ 3'.
J C&P7 Pressure r
'Termt,nnl Operator
, ~ 2. Test Log
~
C CV
/ 4 J'J ZC~
cMcz c~ mc~ o ~ ~ widow Cr
/EWE r c'Cave< cg io ~ c ~ c ~ o~
P~O o cLc Q pg ~V cp lip 6
~
).30 fl 45 J.gg Q 'P~Zp ~(L4RT) 8~ Q (Ass LCD Q '
~m~A~
l5 &9 . LLRT
~
- 78. $
cclz7 g5o
//go P I8 J5: QOQTplQIVlE,Q ~
1 f45 PEQ i lOQ ABOQT7 ~ 8+6hhlERS IJOT yaw <4 vcae.a, <Hwi e.e. m.rap,) W 4a
~
ow r-u o~ C a.csv. ~ 14. Q>u. IUD'pEa.r od
> ePTE.R. 1VE~ U o vEO PATE.
~ j a.caaQc.o hP. I~
gC tr ~ 5
'I I I .f;1 '-0;~ 1 t
rr "1 I'I 'f, I; ~4 I' I It
- t li Je ~
> tp nt t,
~ I IV
'C
'.4 1 tt "I
~ \ , ~ ~ +
t '"
/g ~
I t 1 1 Q IT t 1171
~ l S Y
cV 0:
/05'0 sc F~
~ ~
j 3"
~ en~~
'f l5
~
Ig I
~ ~ jd ~
Cf~ t r P I 'DD
'V
."'J~
Je '4g
, ",r P8 lola'-
/gjo MP I 815
~ \ ~ tago 9~( (ex& 4~
/cg/$ o Xo Jc~-
g ops'oggy CAZa-oc@( ~vip /M~~~~ . lcm~~ gl Vl 5'0
~ .C g I it+
)
gl 4( u fg
~ '8 u'P I 3. I
, PPP.D 0
$.$ 58 l8 P~I A j
@goo
~
Cbn
'r
~
(C
~w p 'n~
~" Ccev/.
. ~CP - 0-EP
~a 0
lr J r S
~ ~ a k t ~ I A ~
r 1 B' 1
'
4
'l 1
- , I ) 7.a <..
I L
~ I 1
I V l
- g~ '
l
~
~ 1 I
I c
~ P t
J C'
~
/
I J i I
/
\
l f.'p~Ct
Cow 7 i~u< D CoM TW/iv&DMF g)gals U/c /45) ccrc (on) usaf 4 s'&i~ ro YA ~ v< f P) c'rnrd Zoo 8 AW. BLDG. ]o CHMK I=QC d <8 <S'nJ SYS'<~W.. PR c.Se.~ ~Rc=S SV fZc= paewrssi8c.< g4 v-C
~ ~ ~ ~ ~
SAT: 'nroV Zp 5~A'pa~ REr9D/ives 7AK&U 7- 8'. /A/Pdr r7aa Dwc g
~o Cong/~<.
4'~scour '/ccbaez'8 78, p P. 8, (A,. p+~ssc/4< rp~D/wQ QC), Z P S. /.Q. C ~f8 ) /C i i / 7 2 5Z p 12/~ g C-f ~Wc ~48~~ M~~ ~ca&7 i MoM
/A/ZS~<i i'O& ~r-AW i'~ Yi9<yC= + i /&~G Em4 PR<SSdde /e.HD/~6 g2, iD P.S, l. A.
L Aw='~~~~ Mw~i~a Z4 z Aa~<
~wc r/>HswraN wcA4
.'eed
~
Dd . M~ wHPA'
~
I p~&
.I j ~:
P78N, rS>. V<cuw +~< ~&4'Wr~c Cc WA H~m&c~ ~~& i~a pe~r 2 A. ~ zn/5/ c'c ZiAJ f'O'QCC. /8 J 7 C- /~ 7 c.-6'9 Z pe~~.dg~ gA'~p,~p ~e) $~~~ v~/~e zan
/HA 4 Wp.
J CcPM MC' I I
+~~~~i~~e~ 7 pic~~rC r S +~ + 7 para. ';
pf+p p// cp/g cowprds'58M wecvrWh gc
'KzDGM /W+clzdw PRE'CA<f I'8 JCYAJC 4g7~At.
2r po 5$
~CA) )ea As, ~/<a P4 C
J~l~lcd j'r~~ z ~ <~ l fd PeW
, I
I
~M&Sro&+ S
~~7 ~r~
~wc ~72M was~ 4 PwPu+>8 iPM@ZWP /TS C.+57 Clio/o WM~&rMcp
~r~
nm oD Mcr~Ma .. ~~mrs im=c r I I 1 I t WA~ rr
&A>cF.
~~ Am ~m rW27
~uM~Mmw~ ~r~c e I
I f f
~ 1 I ~ 'gss g l~yp do or@;~~/ ~ ~p/~ gg
~ '//p I f
//WG ~ZlM4WW R~~~Pne7ces ZdmwDe ~m u~A Wor7~i~
~Kp'A< JJJ~
~ ~~~y. ~~MS~~ ~mp~sraM s~riMauzxy', Purgri~m Z>ra~<> ~~~as'ram~
~w Pm ~o Fm ~~a.
a,~~ Ax.~-Q~~ ~~= ~ ~y~~ dzw m~ guvw woFTwco 4f gzw PRES~~~+ &
~86<swy. Q~~. zw~a z~ 4~~~ WH~~w
~<y~~~ ao
-uD ~~m ~g~ico~
~ Qa Psov&ra W~Wi~c=
pgcmi cSi/6'~ CiC ~C r@g /W CC~ASiW &< Wp'~ RlhR iA j@de
~ 'R8Rp'~
aa cvrQ S g( a~< M
,** ) ~
~
I
'
g I~ N
'
~ ' >
~ 4~
4 i ~ 'l,k ~
'\
~ ~ ~ i
~ I
"
~
q % I~ ~
'I
~
ll ld I 5 Zaj5S S/g 't3R d
/ gg5 T.~Q. t
\
/Pcs Zdis 5gg~s /~~s ~ +ca'v-4~~.
if') Dg~~z
/4l 5 cAICC5;H Do ~. M~
+~CEJA~ ~C/6 8). g9 PSA'y
& ..
4 P/ /5 ~ g gp+ ~<tt+gg~ 8&NC+A~ P
~c ~~ N~w snWca~~ a~ZuZ-Qg~MMMd~A,
~
MW-u-~ ~ ~& u PATE, 0 P c
0
.gd." go~ .(+mr'."
u~,X~e co-g~.~
~ A&7 pyC55A'r'jg ea g z 8 / 5>~~.q .
44 A%5 AW~ cZ, 4p A 2 ~~++~z/
@~ JCP~AP ~~ jA. n/ ~ 7
'.
I
~~fHQ54 l/ ~ >M Q~i~/&PW~7 gmurr'y'~~~ ~
~WAS@/~~
S ( io r<~P/om
- 38. 8~W(A. ~~~ S CO~a
/3 c.a~ Da ~u + 4~~w/~~
4 13
. 5'(r]vaq y'y A'o v Ag. TL- /sr@
/O'S'~br~,
sMW~ M~~i ~.~ ~St+ $/8j( g/(7~c3~ ~Mk4(~ ~ pj's, C . S J PS'~< rewed P~J': Z+. 7S ~Zh
~
p~ 'I
~a.z/
l
~@0 ~ ~/. ~5 C
.p(g~P AA~S J pl 7gg ~~ S ~~&iMC C
~
-. /7,go pPrs- ~%/~2 ver) &WE& ce~~zM&m~ 4l~
P~ EO@
/
er>rEd. II 6834 PA'ass. gewawrG l6. ~W Zg"R g IAJ~p~C r rOnJ i &g+ ~PNw r/L/70 C04l 4IIQM C.AJ p.
3.4 MUQQ9 30 klov 7D PRE.SS. PC@,~i~C (5, /S'.S.].R. CorvTAC r 60 /PL Wl'Cn g ZuMM /P~Re 5'c4 rdrivK3 AmD r zrz yes~ Pica~.s, A'ewoi~G l~ Wa PA'e,SS. E<RD(~G' /G. P. D. /R., P+Es S. R<ADiWG rg. 8. P<as s. ReweiNG x+8 P, S.r.R. 8z.o~ Dom~ V8wg~ ~HU7 Zy'. )b9< ~ . ~t l5 /GAEL'VR 5 D15 CRCPQ ACY PiEPd R~ FRO~ CQg TA.l h3 AC Jh) SMC.~I c M ~a.e ~ Q>'RRt4.
'O<&c.Rapist-lc.S >
pg~gzg.A ttCH l 4 Yc. - <'L 5buv, SHoo<9 Qe. NP~nD t QVT' S F U~ ~ oF <A TKR-. pe.&E.WR.KTi o H-QQO f ~QOQL.D 5G O'P6W~ 8Q'T 15 F'Ul
>C-'A-1<<
PE~ vrz~~iam- 8 (~(~ 4 pCLh~ ~+ k Qi~C (0 4)j cv-~si (4~~ Po~>a~y
~
mW
-
Mom t=u~~V
. sip)
~ ~~
Ccosab. p
15 s
~U ph gQW) Zo Aov pcnJe.TyZ.P T I OnJ l
+c 7pgs Hp <6 i<C o4 5T~& C E.a ~r p Ywvs.
WHIST.lk MCQw SA<T HLJQG 5 c -t oo ~ AG o4 CoRRcc 7 VL~.
~P~~D, .~T~M . LEaKcF'F VwVS, QPy F~unJD kJQ Fnu&Q ~c -CG 4 We
< C. I 1-AG-. (TC l dvu8s~z
-t' l eAKiMC gag pa.~Z~~T ie hJ 25'3~ ~~~ g (~ Q H c H ~~<.~O QLV. <<Q& -VP.
1 I pic.s s. R~~oruc Iw.'75'. s. l. A. f84'oO Pr~~. p-ea8q I n ]4. g Ps./.A . Me M~~l~mmN ~ 6a4. sn f~y IZ. ~/a nile & /2 ~o o~ 5'h imp PY I CR L /Vg S'. SC gn 9'f/ Q t) W7 P~~~ 4~ ging //.8Z P~ig
~ ~
igloo
/>0
- /MCG Mc~o W7 - Wr4- Gv M c~ N~v D~ ~~ V<&~s ~mr~ ~~r (~~ r~, Ecer~r~
A~u ~ ~7'/L4s 0 ~; lcd'~ (g+~ Awe ~rr7Y '~ Mw~g jPid~rx'rg
~c~~ W&~ ~~~~,
'"Q,
.~ ~~'
YN4w ~am 4e M~ "C." os,
~ p ~
l ~
~ '
t
%i JIM ~ ~ ~ l
~ ~
~ ~
~~y. Cmo (~n vC
/1 re IL Q > C.N I @AC. D3L</ cdGI&
24SCIRt4> +jgD +OKSpa 78 Q ~
~
AISDM
~c A~ys.
'~i'~85~ /&~
ppp&&S z4$ ?ZY5 Sy~~ ~u ~z jjVps gear a"Mp s
~Ma~
~ r /P, C
'pP
+<<< k~~?- V~rr Hive H>>es same
~W/WS 4CJ~ IR~~~ WWC?V QA/u&.' rc c. CDBct Pc ACE ~A'A'V lM~ v~ dug~ ~8~ z~C rO~D (S'~H 7@0gs 4W C~za C 8 OO 4rcm~
/M QOuaurvt~?CC4, ~-. CCCZrC?C
~ceo.
~N . rasrxcCiaC>. ZrV-8 ~~ n..
9, ?- ~V~'4 PO PSC~ 8 &+44~~ ~/B&~ ~&C. ~BwMa70 As'~p~~~
~qA.
&A/7A'/rl/<~/V7 P). emu~ w .
~4 )~P&l~ ~utvi~~enr Qg&ssu~
/@5'CL~~ S A~j~ ~ W~f/26~mmw
~ ~
18 I l I ~ h r I 0 l
'
J
\ '
r E h ! I l I I l
gg/5 By C'W JY~~~.~f ~
+ Mi. g<~
,4e~Z~7 J+Rp+i lM
. ~~
QQ(A& N .'C/Sgg ghlZO 457iA(dl- oe /l1/7~V /Q ~~rC ~ /4'Cc un~~ pJ/~ s JU s ~~~f0, gQ ~u~~ie~ ~Q 5 Z Pot- O~ ~rua~w~ > C~~c~, Ck s ZL~cvzs'~zw:
-
Aka A"k8D PWd~ A'h'A'&~~u-
~
1 aPW~ p~k+ gP ~ w8 wk a Q M Mp a.<g
~XcLg ~4&,CA~Af/,
Z~ ~5
/
C8+l87CS> i'uspi~wtio<
~T&zW~~~ AJ/R ~t/~V A~a goe~a
~V+'C gave~ /Dc-Aec
\
g g~>U& pCtOr~u@ gs Ep /aM~ (p~p e Sdur
I ~ 20
~ 'I r
I* ~ 'E '\
'
qo pp
'
- r I I
I f
~
p
'I 7.
21 Z/Z~ ~~c"r~V l& Ij47 l721aZ))By'Ao~ Qp~ ~ - r~:
~@Cubi~ ~la%& y S~s~ ~~ ~+w- lMo t
~ ~-/l~
f
~ 8e, /Nj
~p A~7 N+u cawxwcr~o ~u cc~p-.
F+ ~CC ~~AC/ CilPCCI=W .Srg1ir:W
~,( J gL Ii /~ gus ~~om J
~uC. M~gcP~ ~ C4E~
'
~y g~ ~Dirrn~ ~n +~ ~~~. ~~ny'
.~z"-...~ g 4s.=
,0 k
'T tl
22 0: e I V 0 I
'L i ~ ~
'I 4 A
l I I 0 I P ~ g
I ~ i lC.~~ ~~~5~ WCC ~gWzM~wKl~
~~WDom& < w~W~ u~. ~~C- Mome M~~rN~zrm~
+7&/~~~c. &&~ST/A~~. P+.'W/&if/AJ Hik~c/CC'CECA
, K~~+ B. W~z~> r GM~l~ g Cau~M +lWAJ
.gal rC red 8p -X p -~EZJE714 r+4v-r pQ ~~~m~ nu Mw ~w '
~or ~wren l 'l m+a~o WAa~ m d ~w~+w~ /A.Z7=.:.:
/tSWZ C4CL BZ eP'S~~y yoD -p;~am~@
O~ . CEIL/ M (+~g E2M) N~ '~aim~ l
/W~~~~on JCDHA(Wj&g
&WJl>%Ac. ro wy'WCA
&67~ M ~z7a Ac c. ~red ~~~~mc~
AP8KPK& d'Wl 4>~~ EQ, Q.Q~d V A44E'oS LTlo QS a.T"RZ:PBQ C. Ae c.h4 0 l ~R3 ~QLMW1&M A ~MA. ~ C ~
J
~ +l y L 0
e k L a~ ll k I I l I I I I
,, ~ ~ e
~1
C~ I, I'f15 Wr~~MC S1'gLTCy CJlec,klhlp Atk. pelt.l7$ (CVCL/ hour qme~vacs)
//VZ-rgb rrgp'PA' r
~~rN ~g. 7p d Akl'~
// KF
~
J
~?), z~ ~cia ~>~
4r A4~ Q4'. p4rdo~f mid- ~~. g-H
.c. el~
g ~m~ ~ II Z?K ~ rm g'.@. AbI,k -ig.~.
~Oz~Cqg W~~ Z~ pN ~R A'Z3o
~pv~~O< ~~&id&
8 vl Srure<.j7& ~mr //~ ~~g
~ .
4 z M~C Q~ JFi - QX><EE'~ Qjscg i rUQg4r c/f' I r c4
'
r ~
$ 4
)'I II
~ ~
C" ~
\
<<
$ ~
~$ $ < $ i $
l.
$
~>> vA I
~ ~
~ ~
<< ~ ) \ C ~
'
'$, )
~ ~
<<r <<w
~ ~ $
l3oc id' pig. STIIL )LCP. g C.lceRS n<g fnwmua, . ~ac.k,~ 4>ua.1p 4y T;o . /5oo P~~~. 5/..4o ..
~~ c)~ /5$ Q fdQo ~e~zp~rrurigaa c ~ p~ Pc> ~ gem>
ron Ac~r 8=@ <~d SA. w~- za.zzr~, W~ cd~ V+Lu8 Q p
~~ez~c.D w~~zo
~~eGD Pg ~~~H
~ ~M~z~
S. )ho
~ADA .~~
V ~ A4> Jw ~ve~~
- S'r~ O~~~ ~mt>g
~
P~izl Q~+~~l'S~ WQ7vWi~. i6e Q}AAF/lWcP /~ra/Quz g~wz(
) ~> llnaw'ak Wu~ E< ~AP-<A
<
gg C d<u'~tp~
J ~ ~ p J ~ r~ 'k r ~
~ 'W r ~
t r ~ ~ 1 ~ P
~M ~~~ ~ ~
~ ~~~
~~77au~ CCp-i9 @CPA'~ S~
.e.
Cocyzsov
~M. ~W~c~
~ . W ~~&re c 1
/915
,~~6 rN u'MJQ a~i~ f DW~& <6tp
+yj~j ~8W ES gM /AJC S /O g L E + j'tied/
jhow Cal/8 pe.~eve.d s~ J.
/~n 4 .
r'Od&', 7 g'y C/062 7 g+>g5 OC Pg C~A+S 7-c9 l C r I~ S~g/g/VC
+A~Ms Cp VE t
~ ~
'
1 II I r V \
'h 1
~ r Bl
~i t
I 925 0 'r S+ Ps rp5 Ku&7g 4" COC~ qg I W em@ wpuylert g J,A-c
~ ~-. ~
rri rr 4 au ~.g,
~rr f2 I
~,~. p j'r a/
I
'50> ~ ~~
~ aiumv il 1
,I C4r /ter/enjoy'I
~uar7 A ms
.z. Z. On ~
<<A.<9~~4'ac
~ +~s QpCa MpS ~wM r~ ger ~My>'.
I
!~So
+~ -~ ~7 ~-p, H.
~
I I
- 8 Pcs(g, +
~
(y g~ P~Hipse ~c9 g->> a~~~Fgf W-
~<UN@Vr'g~&dMMQ, 8 CgQX~~
rr e r 7wbc~~&M~ Zt rr ~p id'r sr~~ P ~, ~
4 h
~ h h
h
I
~~ 4 l
~~M~ 1 M
+'~ ~GMH
~~~tc 2 p 4~~+
( I+4~~u~W ~u~. Mls p~ + +~ /) Qg~ Q~ l&x ~
~v kwsvew.
'W H~c M~c ~>
~~
- r. s~~r~<
/~/
@> 1 P7~ Cd)v'v zwuco Pc.W~
1 i CC~~~z&~ C L~' cK & ~~~
'zlzz WRe~~aZ
~Qg l~All=~ZwCr~vw~ iB
/ZM -
~~ A
~4r~-.
z= /vaZl-
- QA'/nWn~
B.l, - g?p7 V/. A. ~BByrr P
*i (jg.Q, ~. d gQGe8
~ SiCr P
I
~ I
~
I', t 'I I
~
'
I a r ~ ~ 7
~ p l 1
1 1
~ ~ (
r
~ r
~ t l~
'l
4g/2~ Q~ 7vauz~ QS &WAS CZ+I ZOO
~ g ~
8ym~sr~ ~ '7/og S8o A/. 86/ Mm ~ (g~/. ~> acta) v r~ O4(ping
~~ ~prCP ( +OX/'~
~O 4& ~~.~ /ru. ~.
/jg ~~~
.'ip~
>~~~~ (
~~~ AD B~C'am eC N~Zo Tr~WW W~ Fc~~g M6e- r Wm~ ~
CLCT q ~ c w+ )55'z. 76=f 4 ~ Icons~~,
~4 ~
4c~~~~ Y4 h~ ~w awrhp ~~~
'
> 4~
++~
n bM
~
*
~~~+ N6u~ ~n OW /can&'
Vpcpg9 HKK tEAQ id' l g vS l A e ~ h~ (gT'oTBl o plass uk< p2&idc 3 9;8 PS IR
~~ i
E Qc)u 6 cP ~5vA inc g~M Cps L~ Vec.. 0 4 (OO (ga so Sm lP 6c 5'o f0'ao 3o bo CO 5o (00 QO 5& 5'Q Q 60 (go O Q iS F00 QO 0 ~D
- c. f QQ bo '30 O'Q bled too bo ZD :Sa taboo ~ iOO &o
)~<S l~ 5o 20 ) l ia ge 20 4e -SO l'745 loO &o RQ ge -Zv ]QOD (OQ ke 4o O'O
( )00 &o gQ lS 3o ~ )OD 6o 50 SO t& <5, ~ t0o ko 2a So C. (OQ 6o 3o-SO 11>> Cga .,2' ~-3O logo ~ )OO lg d.z w gb ZQ p Q~~ gO cG ZD Zc
~(5 ZAP 809'i3 /00 Z0 wood A /R CG
- Sligo
'~ ]60 Cpa ~O fO- ZrO
< GO QG 3'0 /g- b0 u/9o (yO ZO go -ZG 2(y+ &0 z.e l~ -~
r !
+ping~ C)A ~~~ + LP ~
J ~
~eat~cgg~ &cia> ~B WAR3 Qpw pa~ t V~
OO ~ ~oo Coo l&-~
~(OO &o Lo -~ fo -~
(QD 8n (o -~o IO -~. 45 ~'oe) r . 'oo 46 ( lh 55 ps'<A)
~
oO < ee &.o ro-~ gS' (o0 Qe to -~ (o 2AD Sn (b-~ (g ~~Q 30 (i5 45'ys i a) 4S ~ too Go fp-2 C lo -i5'Q
@o ~(oB lo .~N lS Oc> ( i'5 . 9 a ~< n) t.'5 ~ I Oa ko Lo -w /0-<~
3e ~ t.~ go (~- cQ G f5, w <0Q 6o a0 -~ ~o -i5 lo0, ~ tGO -u3 0-tS i i5'0O Cou
~g go-~
)
tp <<~ WM~Do~> ken isa
~kt4LQa
~iH 89
)
P'6'e~&uR'E kw Cec ~ez+e'D 87,8'~(8,
- -BW~i&,
- +9 ~v,eb A, g.Q,gk à dhM~- I .
F <BP~m~
. /ad 9 ease v Ce C>~~>>C o~ a 24.Q PMQ C>% ~~eh 6;i~4o.~ 1/<(V~ cled.Q l, /il. O,d)'~'+v'+ 'l u~v <.
p4 ~u ro4 ()
'(?EQ rSRcl ~~ Q 'ZC p>>lo dam $ 4 lfoo PwesSu.v>>. CP g>C oo.M ~g 7 )Ac g>>$ L< o ~
g~~~go6.~4. 7 7,a P~sSu v>> Q C~~pw C'arr l 4S' I ga
~A ZSy (w fa r Z <..~~
. Zc33d gl ~ E c<
I 4
,, MBC3
\
..( lf,7 4 IK
.
'iv 2-18< 4 g lz yg*
~i
I ~ ~ 40 P g I p I r
~ l'b L.
41 I C 22 L'5 l"l ~ ~ ~(A Bceuf
'Zgg Va 9e ~sin 2 ~45 I g.~ ASIA gg.~y.'m~. -A~~
~xi r
~w
~
~ ~(
'7't- ~z -'R~
.', 85OO >0 p~l A
+'7 9 "tf~g.guuc- Etta+ I Q~. <z. r- %no t I t z~ (.~ JQ. lQ pan m ~-
4& . sQt c- ).~ v 8> "" ~ fS, 7S paid ~~ g4> ~/
~s'un.
RYD (8 L P I
I I I
,42 I
~ I A t J C I I r 4 t I
~ ~
1 I
r
'
~ ~
F
r C$ u l
/WM> pmi4 po Pea- Pu~- ~p ~Zo pg, V~"M ~f Q~.
Q ~ QO p56g ~ < p~~ QM. Z-~ /a g~. ~um ~ f~&
'Fg . o z. C-
?- 4-- l~ ~~~~~~M ~i~
i'5. ~o 44.. 8'v % ~.~~ @
~
P-6-D
+i WiD
., CoaW <$ . QD +<*
+~. ~ ~/~ ~-M~. + < ~A~
aq.+a-r-. " i ~~ [4 ~ 8> ~id,
+g. 0 4-~/o ~-+luw- ~(
7Q. 7 p, r= ~ i ~~t too i 4. 6e ~~g 43 54. ~pa ~'the + l ~D So. o& t= ~( Rrc 1 at(S (4 go)p-g, c ~~~~ 5g % BeC-'44m +~
~D
~
)
l 8Q A t*
~ I c
S 4
.1 g ~ lL 1t
'
~
I I
~ 4 ,I
~ ~
4~~z ~.(upas ~~ ~ ~- >~Mw
~coy ~~. g(-T m ~
ChetxcT
~mu'R ~Cp. ~ Kutl4( ~LP~p&-"t-
~ '.
~~bP (gad g
~ V Ill. H. ~D 4c~.
CSOW 3 S ~ t0
~(LEE)
~ p.~pc
~
c
.egg~<~~ lO~~ CLPE~r4:. ~&jgi3+
~ 'ppiu~. 'Ups &A.w~R~a m0~
I
~ -%AM l
I
~p~~ Cbi~ M Q~?
tb ~
.'.(~~~~~~M~~(
J CBH %~TER- ( ': amer ~Sp. ~L~ Qg~ <<Q~ a+ g T lM~. %~pm C)( t~ wl ~pM ~~'RC~ qadi~ ~~~
)
Q" I P v~~ Wt=.hlR iver p Amp>
~ca ~
3
\
YPL
-
~
'lhasa
)
&'lu~ V ~~ ~~~ p PcrC4<- - ( ~.N)
-MA- ~l
+au I" l'L P7P 9< P I
- 4 46 I
I I ll
'I
)HpP
'I
,h t
'
'I
-I I
t I
~ I I
r l I I I ~
e i~cmimN~ib A~ C3n~pce~
~g'rc-~~pc ~h + ~ ~~p g'4 mr= ~~~ ~ ~
pp.ac.. L'3 <6> ~ f ge ~i0i r~
~~ p ~,
V~tc g ~ gg s~~~ ~ ~rN peed
~~cf ~CXOC4l4Ci ~~~ ~Q ~ ~IDIOM g lu p ';~QL- ~~~ VCC)M Z y A~V ~CD@. LW C
t I
'I I I
APPENDIX C Periodic Type B And Type C Test Reports
CONTAINMENT LEAK RATE TESTS (TYPE B AND C TESTS) The following routine local leak rate tests were performed during the reporting period on Unit 3; i.e., since the Unit 3 pre-operational ILRT (Type A test). I. Penetration Tested
- 1. Personnel Air Lock (entire air lock test) tsAS LEFTY s Test Date Leak Rate (cc/m) 3/9/73 0.0 7/9/73 0.0 10/30/73 0.0 4/1/74 0.0 8/8/74 0.0 12/3/74 8.16 3/20/75 0.0 7/9/75 0.0
- 2. Emergency Air Lock (entire air lock test) 3/8/73 0.0 7/10/73 0.0 10/31/73 0.0 4/1/74 0.0 8/7/74 61.2 8/12/74 12.24 12/2/74 20.4 3/19/75 10;2 7/10/75 0.0
- 3. Fuel Transfer Flange 10/27/73 76.77 12/19/73 0.0 3/23/74 0.0 11/26/74 0.0 ll/27/75 78.9
- 4. Equipment Hatch 8/6/73 0.0 10/27/73 0.0 12/18/73 0.0 10/15/74 0.0 11/8/74 0.0 11/27/74 0.0 12/2/74 0.0 4/10/75
(0
- 5. Isolation Valves (after repair)
"AS LEFT" Test Date Leak Rate (cc/m) 3-873A 8/3/73 21.0 3-873B 8/3/73 0.0 3-873C 8/3/73 28.0 MOV-86DA, 862A 3/25/74 0.0 MOV-880A, 883M 3/25/74 0.0 MOV-880B 6/11/74 0.0 The above tests were performed in accordance with Technical Specification 4.4.2 (Local Penetrations).
II. The local leak rate tests on all boundary valves and penetrations were conducted during the Unit 3 refueling shutdown from October 7, 1974, to December 4, 1974, to meet the refueling surveillance requirements. The following procedures were used: Operating Procedure 13514.1 Personnel/Emergency Air Locks Operating Procedure 13531.1,. Equipment Access Hatches Operating Procedure 13104.1 Containment Purge Valves Operating Procedure 13404.2 Electrical Penetration Canisters Operating Procedure 13404.1 Containment Isolation Valves Operating Procedure 16004.1 Fuel Transfer Tube Flange The total "as-found" leak rate was 125.67% of themaximum allowed in Section 4.4.2 of the Technical Specifications. Repairs and retests were made and the total leak rate at the time of heat up above 200 F was 21.21% of the maximum allowed in Section 4.4.2. As part of the local leak rate tests, the following valves were repaired to reduce their respective leak rates: Leak Rate Leak Rate Valve Penetration cc/min. cc/min.
~Re aized Number As-Found As-Left Remarks 989A 8 203 0 Disassembled and cleaned MOV-869 18 216 6.42 Tightened packing 298A 24A 4,826 540 Installed and lapped new plug 298B 24B 3,217 0 Installed and lapped new plug 298C 24C 7,239 0 Installed and lapped new plug MOV-1410 28A 630 0 Cleaned and lapped disc Isolation 28B 450 0 Cleaned and lapped plug Valve B POV-2603 36 21, 240 1704 . Gasket leak on body, reduced by caulking The following table lists the valves and penetrations tested, with the "as-found" and "as-left" leak rates.
2
LOCAL LEAK RATE TESTS FOR REFUELING SHUTDOWN IN FALL OF 1974 AS-FOUND AS-LEFT Lowest Leak Lowest Leak Penetration Pressure Rate Pressure Rate Number Valves Tested ( sia) cc/min. sia) cc/min. 1... MOV-750: MOV-751 65.55 540 65.55 540 2 MOV-744A: MOV-744B: MOV-734 70.50 0, 70.50 0 3 MAV-716A :, 71.00 0 71.00 0 3 MOV-716B: 717 77.40 0 77.40 0 3 717 72.10 0 72.10 0 4 MOV-730: 732 70.50 0 70.50 0 5 Valve-A: 517: 549 68.95 0 68.95 0 5 CV-516: 552 70.40 ~ 0 70.40 0
'6 Check Valve 518 70.60 47.08 70.60 47.08 6 550 69.10 0 69.10 0 7 CV-519 A & B: CV-522A, B, C. 67;77 0 67.77 0 8 CV-951: CV-956A 69.85 486 69.85 486 8 989A 66.00 203 67.10 0 9 CV-953: 956B 69.70 0 69.70 0 989B 67.80 0 67.80 0, 10 4658 A & B 70.20 0 70.20 0 10 Check Valve 4657 71.50 32. 1 71.50 32.1 ll 12 MOV-863 A & B: MOV-872: 887
'37A 71.45 69.30 10.7 '
71.45 69.30 10.7 0 12 738 68.60 0 68.60 0 13 CV-739'37B 68.80 0 68.80 0 14 CV-200A, B, C: CV 204 68.20 0 68.20 0
,15 Check Valve-312C: CV-310 A & .B: CV-311 69.75 21.4 69.75 21.4 15 HCV-121: 333 68.85 25.68 68.85 25.68 16 Valve A & B 68.30 0 68.30'9.20 0
17 895 V 69.20 0 0
'18 MOV-866 A &': MOV-869 68.50 216 68.10 6.42 19A MOV-880A: 883M 68.50 0 68.50 0 19A Check Valve-890A 66.90 12.85 66.90 12.85 19B MOV-880B: '883N 68.60 0 68.60 0 19B Check Valve-890B 66.00 38.5 66.00 38.5 20 989C: 957A 69.70 27.82 69.70 27.82 20 CV-955 A & B: CV-956C 66.10 53.5 66.10 53.5 21 MOV-1417: MOV-1418) 68.55 12.84 68.55 ,12.84 22 MOV-1417: MOV-1418~Tested ToSether,- 68.55 . 12.84 68.55 12.84 23 CV-2821: CV-2822 68.50 0 68.50 0 24A 298A 68. 00 4826 65.40 540 24B 298B '68. 00 3217 73.80 0 24C 298C 1 68.00 7239 76.00 0 24A,B,C ?97A, B, C 69.50 0 69.50 0 25 MOV-381 '69.70 0 69.70 0 28A MOV-1410 64.70 '30 70.20 0 28B MOV-1411 65.50 450 70.00 0 28C MOV-1412 68.40 0 68.40 0 29 Check Valve-C 70.50 21.4 70.50 21.4 29 CV-2803 a 71.30 0 71.30'8.60 0
31 CV-4659 A & B 68.60 0 0 32 Check Valve-B ~ 71.55 21.4 71.55 21.4 32 " SV-2912 67.00 450 67.00 450
~ y (
g ~ ~ V yJ Al
AS-POUND AS-LEFT Lowest Leak Lowest Leak Penetxation Pressure Rate Pressure Rate Number Valves Tested sia cc/min. sia cc/min. 33 SV-2911. 67.00 486 67.00 486 33 SV-2913 67.00 450 67.00 450 34 Valves A & B 72.40 0 72.40 0 35 POV-2600: POV-2601 65.00 0 65.00 0 36 POV-2602: POV-2603 65.00 21240 67.30 1704 42 CV-855: CV-853A, B$ C: HCV-936 74.00 0 74.00 0 43 MOV-626: 736 '8.40 0 68.40 0 47 Valves A & B 67.00 2170 67.00 2170 52 CV-4668 A & B 68.20 0 68.20 0 53 'alves C & D 69.80 0 69.80 0 MOV-860A: MOV-862A 69.20 0 69.20 0
'4A 54B MOV-860B: MOV-862B 71.00 0 71.00 0 55 CV-955C, D, E: CV-956D 68.50 0 68.50 0 58 Check Valve-873A 68.40 0 68.40 0 59 Check Valve-873B 68.40 0, 68.40 0 60 Check Valve-873C 69.10 0 69.10 0 58,59,60 MOV-843 A & B: 837 67.30 0 67.30 0 61B First Valve Outside Containment 71.70 0 71.70 0 63 CV-2819: CV-2826 67.60 27.82 67.60 27.82 64A MOV-1427 66.70 0 66.70 0 64B MOV-1426 69.70 0 69.70 0 64C MOV-1425 69.40 0 69.40 0 65A From ILRT Air Compressor 69.80 0 69.80 0 65B Pressure Sensing and Flow ILRT 70.60 0 70.60 0 65C ILRT Leakage Flow 69.10 0 '9.10 0
39 Transfer Tube Flange 66.0 25. 7 40 Equipment Hatch 68.7 0 41 Personnel Air Lock, Inner Door 66.7 0 41 Personnel Air Lock, Outer Door 66.7 8.16 49 Emergency Aix'ock, Inner Door 67.0 0 49 Emergency Air Lock, Outer Door 65.8 20.4 r The total leak rate from the electrical canisters equaled zero. Total As-Found Leak Rate '= 43,023.10 cc/min. Total As-Left Leak Rate = 7,252.61 cc/min.
The local leak rate tests on all boundary valves and penetrations were conducted during the unit 83 refueling shutdown from October 25, 1975, through Dec'ember ll, 1975. The following procedures were used; Operating Procedure 13,514.1, Personnel/Emergency Air Locks Operating Procedure 13,531.1, Equipment Access Hatch Operating Procedure 13,104.1, Containment Purge Valves Operating Procedure 13,404.2, Electrical Penetration Canisters Operating Procedure 13,404.1, Containment Isolation Valves Operating Procedure 16,004.1, Fuel Transfer Tube Flange The total "as found" leak rate was 546% of the maximum allowed in Section 4.4.2 of the Technical Specifications. Repairs and retests were made and the total leak rate at the time of heat-up above 200oF was 27% of the maximum allowed in Section 4.4.2. A new maximum allowable leak rate was established using La, of .25% per day as per Appendix J of 10 CFR 50.
-5>>
VALVE REPAIR LIST A Leak Rate cc/m Penetration Valve PHO AS AS Number Number Number FOUND LEFT Remarks 6 518 5872 15,000 195.6 check valve; disassembled and cleaned 956A 5873 44,000 21.5 lapped and cleaned 951 F 10 4657 5871 2,200 38.7 check valve; disassembled and cleaned
'19A 890A 34,506 37,000 4,000 check valve; disassembled and cleaned 20 CV-955A 34,508 44,000+ 0 lapped and cleaned CV-955B CV-956C 28A MOV-1410 34,509 4,000 279.3 lapped and cleaned 32 VLV-B 26,789 2,400 6.86 check valve; disassembled and cleaned SV-2912 2,600 301.8 33 SV-2911 8,792 6,900 130.3 replaced valve diaphrams SV-2912 1,080 178.4 36 POV-2603 .5, 897 70,000* replaced shaft seals, bearing and seats 64A MOV-1425 5,870 5,900 0 lapped discs 4
5KVA South 3,600 0 lower left hand insulator was cracked Canister at the base. The entire insulator was-replaced.
- Calculated from pressure drop test.
4
LOCAL LEAK RATE TESTS FOR REFUELING SHUTDOWN IN FALL OF 1975 AS-FOUND AS-LEFT Lowest Leak Lowest Leak Penetration Pressure Rate Pressure Rate Number E ui ment Tested sia cc/min. sia cc/min. 1 MOV-750: MOV-751 66.0 2500 66.0 2500 2 MOV-744A, B: FCV-605: HCV-75B 65.27 34.4 65.27 34.4 3 MOV-716A 69.43 29.0 69.43 29.0 3 MOV-716B 67.52 37.0 67.52 32.0 3 KC.VLV-717 67.5 15.0 67.5 15.0 4 MOV-730: 732 67.6 30.0 67.6 30.0 70.3 0.0 70.3
'.0 5 ~ 552:CV-516 6 CK VLV-518 66.0 15,000 66.0 195.6 7 CV-519A,B: CV-522ABC 68.3 0.0 68.3 0.0 CV-951:CV956A 66.0 44,000 66.1 21.5
'88 68.5 0.0 68.5 0.0 9 989A'V-953:CV-956B 70.07 0.0 70.07 0.0 9 989B 69. 32. 0.0 69.32 0.0 10 4658 A,B 70.0 0.0 70.0 0.0 10 CK VLV-4657 66.0 2200 67.72 38.7 ll
.12/13 MOV-872 737A:739 66.89 70.0 0.0 0.0 69.89 70.0 0.0 0.0 12/13 CK.VLV-738:737B 71.15 0.0 71.15 0.0 14 CV-200A,B,C 66.0 3500 66.0 3500 14 CV-204 67.78 0.0 67.78 0.0 15 CK VLV 312C 67.53 10.75 67.53 10.75
- 15. HCV-121:333 70.32 0.0 70.32 0.0 16 , HV-3-1:HV-3-2 69.6 0.0 69.6 0.0 17 895V 72.11 0.0 72.11 0.0 18 MOV-866A,B:CV-869 69.56 0.0 69.56 0.0 19A MOV-880A 70.1 0.0 70.1 0.0 19A CK.VLV-890A 66.0 37,000 66.0 4,000 19B MOV-880B 68.60 0.0 68.6 0.0 19B CK.VLV-890B 73.55 0.0 73.55 0.0 20 989C 69.43 0.0 69.43 0.0 20 CV-955A,B:CV-956C 66.0 44,000 68.45 0.0 21/22 MOV-1417:MOV-1418 68.0 0.0 68.0 0.0 23 CV-2821:CV-2822 67.5 0.0 67.5 0.0 24A CK VLV-298A 67.'60 10.0 67.6 10.0 24B CK VLV-298B 70.0 5.0 70.0 5.0 24C CK.VLV-298C 68.91 10.0 68.91 10.0 25 MOV-381 69.6 0.0 69.6 0.0 28A "
MOV-1410:127 66.0 4,000 66.0 279.3 28B MOV-1411:227 67.2 0.0 67.2 0.0 28C MOV-1418:327 66.2 0.0 66.2 0.0
,
29 CK VLV-336 65.8 0.0 65.8 0.0 29 CV-2803 68.13 0.0 68.13 0.0
'31 CV-4659A>B 68.2 15.0 68.2 ~ 15.0 32 CK 66.0 2400 69.83 6.86 32 VLV-'B'V-2912
- 66.0 2600 66.0 301.8 33 SV-2911 66.0 6900 66.0 130.3 33 SV-2913 '6.0 1080 66.0 178.4 34 203:205 67.95 0.0 67.95 0.0 0
AS-FOUND AS-LEFT Lowest Leak Lowest. Leak Pressure Rate Pressure Rate
'enetration Number E ui ment Tested sia cc/min. sia cc/min.
35 POV-2600:POV-2601 10.0 67.5 10.0 36 POV-2602:POV-2603 66.0 70,000 70.2 0.0 42 CV-855 68.3 0.0 68.3 0.0 43 MOV-626 69.0 15.0. 69.0 15.0 43 736 64.8 60.0 64.8 . 60.0 . 47 CK VLV-'AI 66.0 279.3 66.0 279.3
'G'7.5 52 CV-4668A,B 70.2 0.0 70.2 0.0 53 HV-3-3:HV-3-4 68.5 10.75 68.5 10.75 54A MOV-860A:MOV-861A 68.0 0.0 68.0 0.0 54B MOV-860B:MOV-861B 68.6 0.0 68.6 0.0 55 CV-955C,D,E:CV-956D 69.5 0.0 69.5 0.0 58 CK VLV-873A 69.95 0.0 69.95 0.0 59 CK VLV-873B 68.6 0.0 68.6 0.0 60 CK VLV-873C 68.1 30.0 68.1 30.0 58-'9-60 MOV-843A,B 67.35 0.0 67.35 0.0 61B Valve 68.6 0.0 68.6 0.0
'63 'C'V-2819:CV-2826 66.0 300.0 66.0 300.0 64A. MOV-1425 66.0 5,900 68.0 0.0 64B MOV-1426 69.05 0. 69.05 0.0 64C MOV-1427 69.22 0'.0 69.22 0.0
'65A ILRT 74.1 0.0 74.1 0.0 65B 'F'
'E'LRT 68.0 0.0 68.0 0.0
. 65C ILRT 68.4 0.0 68.4 0.0 39 Transfer Tube Flange 66.0 78.9 40 Equipment Hatch 70.1 0..0 41 'ersonnel Air Lock (Inner Door) 70.2 0.0 41 , Personnel.Air Lock (Outer Door) 66.1 0.0 49 Emergency Air Lock (Inner Door) 68.1. 0.0 49 Emergency Air Lock (Outer Do'or) 67.0 0.0 The total "AS-FOUND", leak rate for the electrical canisters= 3600 cc/m:
(the only canister that leaked was 5KV-A2. The leak was due to a broken insulator which was replaced before heat up) P The total "AS-LEFT" leak rate for the e1ectrical canisters = 0.0 cc/m Total "AS-FOUND" leak rate = 245,576.20 cc/m 'herefore, Total "AS-LEFT" leak rate l
= 12,127.56 cc/m
~ p J . ~
F
~
+
}}