ML20081C001
| ML20081C001 | |
| Person / Time | |
|---|---|
| Site: | Turkey Point, 05000000 |
| Issue date: | 02/14/1976 |
| From: | Roman W EBASCO SERVICES, INC. |
| To: | |
| Shared Package | |
| ML20081B916 | List: |
| References | |
| FOIA-83-296 NUDOCS 8310310067 | |
| Download: ML20081C001 (56) | |
Text
{{#Wiki_filter:- .- m .J I FLORIDA POWER & LIGHT COMPANY TURKEY POINT NUCLEAR POWER PLANT UNIT NO. 3 REACTOR CONTAINMENT BUILDING INTEGRATED LEAK RATE TEST
SUMMARY
TECHNICAL REPORT I Prepared for: FLORIDA POWER & LIGHT COMPANY
. Prepared by:
William D. Roman EBASCO SERVICES INCORPORATED Plant Operations & Betterment Department February 14, 1976 1 0 e f \ 8310310067 830706 . PDR FOIA l CONNOR 83-296 PDR . .
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TABLE OF CO" TENTS I. INTRODUCTION.......................................... 1 II. S UMMA RY . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 2 III. TEST DISCUSSION A. De s c rip tion o f Con tainmen t . . . . . . . . . . . . . . . . . . . . . . . . 3 B. Description of Ins trumen tation. . . . . . . . . . . . . . . . . . . . 5
- 1. Te=perature Instrumentation................... 6
- 2. Humidity Instrumentation...................... 6
- 3. Pressure Instrumentation..................'.... 6
- 4. Nu=a tron (Digital Vol tme ter) . . . . . . . . . . . . . . . . . . 6 C. Description of Computer Program................... 7 D. Error Analysis.................................... 8 E. De s crip tion of Te s ts . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 8 IV. RES ULTS AND VERITICATICN . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 11 V. CONCLUSIONS...........................................
12 VI. F IG URE S . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14 VII. APPENDICES A. Computer - Generated Report
- 1. Integrated Leak Rate Test (ILRT)
- 2. Controlled Leak Rate Test (CLRT)
B. Operating Procedure No. 13100.1 Integrated Leak Rate Test
- 1. Raw Data
- 2. Test Log C. Periodic Type B and Type C Test Reports l
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1 1 ,.- I. INTRODUCTION A periodic Type A integrated leakage rate test was performed on the containment structure of the Florida Power & Light Company, Turkey 4 Point Nuclear Power Plant - Unit No. 3 pressurized water reactor in November and December of 1975 utilizing the " Absolute Method" of testing. i I
;. Tinis test was performed at the reduced pressure test (Pt ) which is defined as not less than 507. 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 utilized for I . verification. J 1 l li s 4 i
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y /' II. SlDMARY 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 E. The measured total-time simple leakage rate was 0.0407./ day 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. (\. 4 l
7 III. TEST DTSCUSSION A. Description of Containment The containment s,tructure co=pletely 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 h" thick welded steel plate to insure a high degree of leak tightness. Principal dtmensions of the containment structure are.as follows: Inside diameter......................... 116 feet In c id e h e i gh t. . . . . . . . . . . . . . . . . . . . . . . . . . . 16 9 f e e t (including dome but excluding reactor cavity) Inside depth of reactor cavity.......... 29 feet 8 inches Vertical wall thickness................. 3 feet 9 inches Dome thicknes s . . . . . . . . . . . . . . . . . . . . . . . . . . 3 fee t 3 inches Foundation slab thicknes s. . . . . . . . . . . . . . . 10 fee t 6 inches In te rnal f re e 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 l emergency escape lock is located on the east side at elevation 52'-9". l i A 14'-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'-6", 25,'.10", 58'-10" and 73'-8".
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! 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 stairway is provided from the personnel access platform to the base floor and from the emergency escape lock to the operating floor. A ladd'er access is also available from the base floor to the emergency 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 generators and the pe=ps are located in separate compartments around the reactor vessel. The prtnary shield wall (7'-0" thick and c'ircular in shape) and the secondary shield walla (2'-6" thich) fona boundaries of the com-partments 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 periphery of the operating floor there is a galvanized steel grating plat-
! form which supports the containment normal and emergency coolers and filters and permits air circulation and flow path for water from the containment sprays.
4 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 transfer tube and mechanism. During refueling, the canaljis filled with borated water which provides shielding and cooling for the spent fuel elements. The reactor refueling crane (manipulator crane) spans across (s the canal and travels longitudinally over rail tracks.
(' The reactor vessel is supported on its six no=zels, each of which sits on three structural steel beams cantilevering from the primary shield wall into the reactor cavity. The steam generators and pumps are supported on 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 were designed to support the deme liner during construction. These trusses were then lowered and tied to the supporting brackets. They carry the hangers for the containn.cnt spray piping. . B. Description 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 ligures 1 and 2. /
( l. Temperature Instrumentation i The containment was equipped with 20 precision RTD's plus 2 sparcs. i The accuracy of these detectors is within 1 0.2F. The maximum probable 'I l I temperature error is equivalent to i 0.054F. 1
- 2. Humidity Instrumentation The containment was equipped with 5 RED's plus 2 spares. The accuracy of these detectors is i 2.57. relative humidity for a 0-1007. relative humidity excursion. The maximum probable humidity error is equivalent to i 0.296%.
i l 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 secle and readout of 100,000 counts = full scale. The absolute pressura capsule had a range of 0-49 psi. The maximum probable pressure loop error is equivalent to i 0.001 psia.
- 4. Numatron (Digital Voltmeter) i A I.&N digital voltmeter (Numatron) was utilized to obtain direct readout humidity data. This instrument has an accuracy of i 0.01 millivolt which is insignificant.
Consequently, the maximum probable total instrument loop error is equi . valent to i 0.015% per day at a confidence icvel of 99.87%. Additional information concerning all the above instrumentation may be found in section 5.1 of Appendix B. J 4 1 m
- d C. Descrintion of Computer Program Thrcughout the test, temperatures, humidities and pressure were monitored. These data were used to co=pute the leak rate from the perfect gas lau using either the point-to-point or total-time method. Leak rate predictions and estimates of error vere 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 yeighted average temperature was computed according to the fraction of the total free containment volume each ETD sensed. A veighted average partial pressure was also computed according to the fraction of the total free containment volume each RHD sensed by e
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utilizing " built-in" cenputer saturation tables. Data were verified by requesting a tabular listing with actual sensor values and other computed values listed in tables or plotted as requested. At 2030 12-2-75, RTD #4 was deleted as a result of this sensor malfunctioning. When this sensor was deleted, the volumetric fraction vao 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, poin t- to-poin t, and total-time statistical leak rates were evaluated in these forms. Appendix A contains graphs of major variables, statistical I and sbnple leak rate results, instrument error analysis, tabular listings ! I
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1 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 Analvsis - 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 refl,ect actual test conditians. Total instrument error reported is established by the likelihood J 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 fi,rst set of dcta 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 duratior.; in particular, this provides regression errors which diminish significantly as the amount of collected data increases. .
E. Description of Tests Interpretation and final analysis of test data show results well within the specified Itmits 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 ~l
- " correction" of relative humidity detector (RHD) problems encountered.
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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 approxinately 41.47 psia pressurization was secured with data acquisition comnencing at 0515. However, due to malfunctioning PdlD's,and excessive leakage, the II.RT was aborted at 1845. During the test period, four (4) RHDs had to be deleted with numerous leaks detected and repcired. At 0028 11-30-75, containment blowdown to atmosphere commenced following contain-ment air sampling. This sampling (utilising a Tracerlab Model MD-12C beta-ga=aa 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 ILRT. These sensors were then installed in the same (.
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location as the previously discussed instruments and the system was function-ally tested. Upon achicving satisfactory results, pressurization again co==ct:ced 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 are 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 hour stabilization pericd. The ILRT was successfully completed at 0900 12-3-75 followed by a 4.5 hour CLRT at an average flow rate of 3.4 scfm. This discharge was also monitored with no detectable gaseous or particul. ate activity observed. At 1330 the CLRT was satisfactorily completed with blowdown cc=mencing at 1449. Continuous monitoring during blowdown again revealed no detectable gaseous or particulate activities (see Appendix B - Test Log) with ctmcapheric pressure echieved at 0116 12-4-75. Following satisfactory containment air sampling, an internal inspection was performed , from 0149 to 022S 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 607. of the maximum allowable leakage (La ) at test conditions. The total leakage from these Type B and C tests was within these Ibnits and is presented in Appendix C. 1 ( l 1 I
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- IV. RESULTS AND VERIFICATION i
The reduced pressure test (Pt ) was conducted for a period of 24 hours i 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 hours. The re-f sults of a computed total-time 1 cast squares statistical fit of all data revealed a leakage rate of 0.05S7./ day by weight or a total-time sLmple l leakage rate of 0.0407./ day by weight. For the purposes of this test, the f total-time simple Icakage rate shall be utilized due to comparison to the l CLRT data which are of nuch shorter duraticn. Since the least squares i . j statist 4. cal fit of the first order regression is a function of tect dura-t 1 tion, the regression errors during the CLRT are high. Consequently, for j comparison during the verification phase, the total-time simple lenhage I i , rate shall be utilited. This Icahnge rate corrcapands to an initial' con- , tainment air weight of 318,634.2 pounds and a final containment air weight 1 of 318,704.3 pounds or a loss of 129.9 pounds. Maximum probable instrument 1 error for this test contributes 1 0.015%/ day. f Following satisfactory completion of the ILRT at Pt, a 4.5 hour veri-fication test or CLRT was performed. This test was conducted by super-
- imposing a known leak of 3.37 sefm at 39.696 psia which corresponds to a i
leakage rate of 0.1237./ day by weight. Consequently, Lt m Pl us the super-imposed leak equal 0.163%/ day by weight. The measured total-time simple 1eak was 0.144%/ day by weight (0.027 x 24 hrs. = 0.144, reference Appendix 4.50 hrs i 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 1 0.015%/ day.
( V. CONCLUSIONS The 25.0 psig integrated Icakage rate test provided acceptabic resulte as evidenced by the computer printout and graphs in Appendix A of this report. These Icakage rates are well withir. the specified limits. These Ibait's are as follows:
- 1. The maximum design Icakage rate (La ) shall not exceed 0.25%/ day.
- 2. The maximum allowabic reducsd pressure Icakage rate (Lt ) shall be the lesser of:
- 1. Lt = La Lem or L t"La[P__t 1/2 k""). (
where, Le = measured leakage rate Pt = retest pressure, 25.0 poig Pa = peck accident pressure, 50.0 psig
. 3. The naximum allowable operational leak rate (Lto) shall not exceed 0.75 L t. ,
Preoperational test have provided the following results:
- 1. L e3= 0.0667
- 2. L,3= 0.1020 As a result, Le shall be equal to the lesser of:
- 1. Lt
- La Lem = 0.25 0.0667 = 0.1635 0.1020j
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- 2. L t*La[Pki/2=0.25[25.0 t 1/2-= 0.1768 p
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As a result, for future periodic testing at the reduced test pressure: Lem $_ 0.75 Lt = 0.75 (0.1635) = 0.1237./ 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 betvcen the ILRT and supplemental test provides suf ficier. : data to validate the ILRT results. The r.iinor differences between these tests and the ILRT hesulte are attributed to rotameter accuracy tiich is i 1.0% of full scale or less than the accuracy of the ILRT measurement system. r
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VII. APPENDII I C-30 Test Procedure 9 e 9 1
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. PREOPEILGIP::A!. TEST C-30 ,
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E# PR12:ARY CO."TAlt:ib'T LEA! RATE TEST PhEP.i!M'D ny .R.E. Sojka/li.H. Fitzroy/D.W. Tdwerds _ Vermont Y ankee , TWIG 10:: I;'i . _ _ 5 ._ gw m;rg 9/15/71 - s l'rior te finc.'i tzation, thic procedure has .bcen revicued by those reprewn-t., l . a. c f Eb a s e. . G.",, nr.d Vermont Ysakte.uno na ec cenpencibility in deoJ gn, Inst.$1--
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TEST Pi:GCEDURE RELEMED YOR EXtCUTION 3CO ( cr A -' *t S0 0 .t. ...C Ent,incer, Ebance
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i Q .N, . ~ "'6[ 7/ Pldnt supchu'tunder b)}] it V'u;PC JTC [ica.bcr '[l_ _7_' _ .- vy:wC TE_S..T.. COMPLETED Sycte:. satisfocterily operable with reasonabic c>.pcetation oO continacd satie:fectory operation , subject to cenplctf on y.u of .qxception u a.,,, e- */ e ,a alig.t itens.],y . , , , s . . . . . , . . . > I. .
. j((__ __ . [7, S Operations !!anager, G.E.
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Page 1 of _ ,_, e DC:: # jk). * ], _ DOCU1:i'.::T CllA::CE : 0TICE . Docur.:ent/Tes t I;o. C-30 1;c v . 5 Ch:mge : o. 1 l - Title Primary Containme:tt I.eck Rate Test Date _1)_L1J/71 Change Initiated by D. W. Edwards l Document Change Authori::cd: k y, & s-x-W
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. Change: '.,
6.3.6 Remove the recuire..mnt to vent the personnel lock durin?, the
. remainder of the test. A 6.3.8 - 6.4.1 Reversa the order of the 24 psig test and the 44 psis: _
test so that the 44 psig test is conducted fi.St. Notes, cautions, precourization and de-pressurization rates are to remain as specified in the procedure. [' G l
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t l i DCN # //3- l DOCUMENT CllASGE !;0TICE ,, , 4
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-' C-30 Rev. Change No. 2 Document / Test No. 5 , ,.
I Title Primary Containment Leak Rate Test Date 11/16/71 , . l.'+ ,
' Change Initiated by _ D. W. Edwards Document Change Authorized: 7
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JTG Member , [ l l l i I ) Change: , Attach Addendum #1 and perform testinn specified thereon. j Reason: Correct defficiencies encountered durinn the conduct
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,,,., , Page 1 TEST PROCEDURE SU'0fARY EXCEPTION LIST
Title:
Primary Containment Leak Rate Test __ Test No. C-30 R-5 Date: 11/16/71 Corrected Exception Disposition by/Date Penetration No. Line Verified by Date 3.3.1 Verify zero leakage from inner X-11 IIPCI Steam bellows of type 1 penetrations X-12 Rl!R Supply ' . , , . 2 /,,e.,,,d_ (' X-13A RHR Return i f-X-13B RHR Return N '"" X-16A Core Spray W<' i'D* '"T *# X-16B Core Spray ~ /'m5e " / " * ""/
,,, Jir' < WJM 3.3.2 Perform 24 hr. drop test on Penetration OCSheetitt. ached)Verifigd,.bv Datg the spare electrical penetra-tion & attach QC forms.' '
X-101B X-106 .Mi
# ..k ) i ': p V -
('.. .I6 .4 3j_ X-107 /]F' p/ l , y ,, ,J.N p7 & -.
* ,U . 6
.c c p 3.5.8 Calibrat& the following Instrument Actual Set Point, Verific(by Date instruments and check set POS-16-19-31A ) ; ;._, m.S ,,y .(_fo Pt?. # 7f. .y. 7 .
points. POS-16-19-31B ,J , <.~n.P',4 fa,{g .hjf , FT-1-156-1 ;i..(' r ,0 - u , > ..,.' '.
- y & Q A l', V y.&% + TI-1-15 6 ,W >> h n ~ '.'.' s t - th l < ', /, r !
LSH-16-19-26 r 4 " (. ? i e . ~' .., . T 2 < m/, / > r O! s T1-1-156-f9 f:.r *
- e. < r ' / . ,,' . %f H./: m)
Indicating; Section 6.1 Cycle the valves listed Valve No. Lights Closing Time Verified by Date using any convenient remote actuator. SB-16-19-6B '.,. X - . Verify proper operation, proper indi- SB-16-19-9 :./t X ') ' cation, and/or closing time. A0-20-82 X s. m. .. c F- f:'c.% A0-20-83 X s i,, ..,r .. SB-16-19-11A 46(' ~ /. Ge. , i-!'/.4 5,Um.G is'ln/9 i [bhr SB-16-19-118 6K ~ t. L.$s, A0-16-19-23 h I,y,/ +e M P # y. ,y.
~ ~
& ;1 _.G N'__,43 MS-86A m ./. i; % d, y.
Leakage Rate 4 n'% ' Section 6.2 11easure isolation valve Valve No. SCFH Lbm/hr Verifivd by_ Date seat Ieakage in accordance uith,ste s MS-86A 9, , .J,,Q nu j,j a h siA.A, 6.2.1 Jo 6,2.6 of C-30. p , . ;'S 51S-80B g .- S .; (jg,.rfacy _ _ _ . , _ , , syrpsi e 5" ~'tS-868 gigh 3,s Abt.') 9%* 4 tw,*sp n/;yjp,i___, U VIS-80C llS-86D
~
y e').4,"taf 'h e rs1cj '
>& h L &( .;t.*s _.p,/i d j Personnel Lock G ,g h a / J / g # w ,bj',j'_f M ' ,,.i , 4/n RCIC 15 /. .;' / A.n s W,X/,M/4 ., ',; /.f
- kPPROVAL All outstanding exceptions have been satisf actorily resolved and the test is c. lored complete in its entirety.
b arm.h,b' Y 7 '/2 VYNPC JTG !!cmber dg; / / / 1 CF. JIG Member VY 'iTIF 010.01
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- Page 2 i
<- TEST PROCEDURF SIFMARY EXCEPTION LIST l . ,
Title:
Primary Containment Leak Rate Test - l Test No. C-30 R-5 Date: 11/16/71 ~ g Corrected Exception Disposition by/Date Valve No. SCFH Lbm/hr Verified by Date Section 6.2 (Continued) &MZ"JI,v.d1 .Me/n/ RCIC 5 ~ /,5 Ae4 < SB 16-19-12A s i * ., ,1,J b , ".//.' /, _ SB 16-19-12B /" #;*" ^~
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General. Complete Change-2 Change #2 Completed dO/,Ik,rila_ /.tN>/7/ Addendum #1 to C-30. Verifle'd by ' Date Leakage , , General. Measure leakage for each Valve No. SCFH Lbm/hr_ Verified by Data main steam isolation valve-@ 24 psig MS-80A LT n , c? ,,ip M.M g/yf MS-86A Jgzj_ .L l ', ljQ,f. ;t .) _.th ibt
. NOTE: This will provide base line
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M - 6B
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_g,
# ## N b '
eM . A n!Er.u w _sy g//
"b k '/ ! - data for future measurecents M -80C 3o A d g a p,_ q . gif of MSIV leakage.
,; MS-86C 3 2 6,71 r.ji6p i aft.!);
- MS-80D 4. ef n_ cic .i W e,6, d 1.ggj)/
MS-86D .qo s . -m MGd gfit AS - so A . 1 O
- 4 I- U W'0 ?'O 2. Y (fou .
,, a n uwn .- w?no 1
- . .:. y. )W,y,j,,
~ , .$ a g- ,, .,.c . :ao .y p. usa t/de .' 8.//p 3 j'(/C /S /O GLE d $b't . ',l'b 2Cjc ,(, .}.:.Q. p.19 fh ff nath !!/$,b>
- APPROVAL All outstanding exceptions have been satisf actorily reco1ved and the test is considered complete in.its,e.ntie)ty. o' Yf W.. % 4.dwre , ' './ f g#1,)/ // VYNPC JTG Me.-.ber
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- T.xceittoa Exceptlea' Corrected
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a & (7. ,6 64 dd'!A p,ci y
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e4
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.. jz,: . A o /21 0 0 6 0 ,'lf 4' ave- 12/r/7, 40 40 ggf ,, ,
O' O ' RCIC Ex- RCIC 50 RCIC-SSC None G55 '
/ //
9 & 50 tff,,?/7,t , .. . (, c;; g : . '- ' ' t.c 2: . .. ~,. y . haust ,, ,0,. . RCIC 38 RCIC-SSC g' '14l < 0' /t 0 03 6.09 0 02 ek'Eflte),'JV!c/$i RCIC Va-- None 7 -C cuum Dis- 10 & 38 j <.w&w( -- charge IN" HPCI Ex- HPCI 65 HPCI-65 None ,/. W .J . k5/ d d /< /'M /
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'"?/Y/rr haust & SSC-12 .
HPCI-SSC None hg N O. 05 0 K' O. O 3 Otl[A:eeb /2AW'?! , gC,1 E IfPCI56 ,,.. 13 & 56 n/ac/ri f#' W-A W-28A W 28A & None') M 29A ( *Cf OO # #' ' iW A W-96A W 29 & Nonc - . 933 4hw u g" eedl, f c
.u, ,.g? i l Total Leakage: l2.6'T /* /0
. I l
' ':.D[r C-30/1 PRIMARY COSTAISMCt;T LEAK TEST -
~
C-30 ,*r. l
~
1.0 Purpose - The purpose of this test is tuo fold: 1) To verify that the 'r degree of leak-tight integrity of the primary containment in its final
. state prior to reactor operation conforms to plant Technical specification requirenents, and 2) Establish leakage standard for future tests. .
2.0 Retcrences . 2.1 Purchase orders 2.1.1 NY-706102 Nuclear steam supply system 2.1.2 NY-706162 Concrete and Steel Shielding Door . 2.1.3 NY-706177 Electrical Penetrations i I
. 2.1.4 NY-706216 Reactor Seal Well Bellows ,
i 2.1.5 NY-7d6221 Primary Containment Penetrations . 2.1.6 NY-706252. Primary Containment Atmosphere Compressor i . 2.1.7 NY-706271 Primary Containment Leak Monitoring System'
,2.1.8 NY-706272 Mercury Manometer
[, . 2.1.9 NY-706274 Access Door Locks 2.2 Specifications , 2.2.1 VYNP-VI-P-1 Containment El'cetrical Penetrations ,; . 2.2.2 5920-S12 Reactor Seal Bellows , 2.2.3 VYNP-III-P-12 Containment Penetration Assembly , 2.2.4 VYNP VI-III-C-I-A Containment Atmosphere Compressor 2.2.5 22All67 Penee. atieno - Primary Containment l 2.2.6 22A1104 I.rywell Atmosphere Cooling System 2.2.7 ~22Al204 t.cnouphere Control - Primary Containment 2.2.8 22Al23.1 f1 pics Insulation - Primary Containment
. 2.2.9 22A120.7 P n ..: n r.ontainment 2.2.10 22Al;"G *
..A Lo'i alnment Penetrations 2.2.11 21/..' :'.1/ 6 . Lopp tcasien Cham 1,ict Co:itainment Vessels.
2.2.12 NID '.C 'n -
.:rt.' 2nnce Calculationo .
2.2.13 2?A!4**fl .
;7rs 8.
'~~ C-30/2 2.3 Diar,ranc nnd Dravings ~ ',
'_r.*
.a . j ,
. 2.3.1 Flou and Piplup, Dravingu '> / (.;
~ , *p 2.3.1.1 G-191L79, Rev. 2 Nozzic Clonure Assenblics
~
. 2.3.1.2 '5920-41, -45, Rev. 7 Containnent Penetrations & Vessels (GE)
. 2.3.1.3 5920-227, Rev. 4 Drywell Stretchout (C8 4 I) 2.3 1.4 5920-432, Rev. 4 General Plan (CB 61) .
I 2.3.1.5 5920-419, Rev. O Prinary Containment Data Sheet (CE) 1 2.3.1.6 5920-569-71, Rev. 5 Nuc1 car Boiler Steaa Piping (GE)
^3.. 1 .
2.3.1.7 G-191205, Rev. 1 Composite - Primary Containment 2.3.1.8 G-191180-82, Rev. 5 Main Steam & Fced Piping 2.3.1.9 5920-298, Rev. 3 Equipment Door
- 2. 3.' 1'.10 5920-221, Rev. 1 Personnel Lock
~
2.3.1.11. 5920-214, Rev. 2 24" Manhole s l 2.3.1.12 5920-250, Rev. 4 Suppression Chamber Accc'ss llatch. go... g,,, . , . 3, , . ,,,
'( /. 4 n n i ui i v g i. 717._. 3;--.__ c _ , ,., ; ,
2.3.2 Electrical and Control Wiring Diagrams . . 2.3.2.1 B-191301, Sh 1229, Rev. O Atm Cont Systcu . I 2.3.2.2 B-191301, Sh 1236, Rev. 2 Cont. Leak Det6ctors , 2.3.2.3 B-191301, Sh 52, 62, 64, 65, 69, Rev. O Control Room .
- Panel Annunciators ,.
2.3.2.4 .B-1913nl, Sh 1226, Rev. O Atm. Cont. System ( 2.3.2.5 B-191301, Sh 600, Rev. O Dryucil Atm. Oxy Analy 2.3.2.6 B-191301, Sh 834, Rev. O Reactor Protection System 2.3.2.7 B-191301, Sh 1023, Rev. 1 Raduaste Instr.,- Dryuell Drain 2~. 3. 2. 8 B-191.301, Sh 1000-3, Rev. 2 Dryuell Drain Sunps 2.4 Manufacturers' Technical Manuals 2.4.1 GEK-27753 E1cetrical Penetration Seals . 2.4.2 Atwoort 6 :'orrill Instruction Manual - Vacuum Bres.'a:rs 2.4.3 Rochuell Instruct. ion Manual - Steam Isol. Valves 2.4.4 C . !) . 1 I Occratiny, mrl Malet . Insti. - Drya ll
C--30/ 3
.. IIrGT.
2.4.5 C.n. I. t Air I.ocks I. Clusure - 2.4.6 ?tercury itanon:cter Instruct ion 1: umal - (.'!a r lan Ins t .) . .
- t.
- r Operating Instructions 500 Serica Servaanoncters *.
2.4.7 , , 2.5 Other 2.5.1 O M L-NCIS-26 Testing of Containment Systems used with Light-L'ater-Cooled Power Reactors 2.5.2 VY'FSAR, Vol. I-V Tech. Spec. 4.7 2.5.3 G.E.' Itark II TSS Users Guide, Number E07232B 3.0 Prerequisites 3.1 All equipment and piping have been properly installed and the Ebasco
- installation check list signed off. ,
Date j,,/w /jL Verified by /) /[, o ( M Vermont Yank'ce visual inspection that the Drywell, suppression chamber, and all associated piping and equipnent have been properly installed as required for*the inplenentation of this test, t Verified by - M Date //[')/)/ 3.3 7tereuuistce instine comniara
- 3.3.1 Class B t'ests cemplete in accordance with the attached Quality
- Co=pliance Reports for the class B tests and leakage summarlzed on Table III. ; -
4 2 9 l,d2 f M f f VcrifLedby,A)&J0,.sn{,1_Datc y/g// - 3.3.2 Construction' leak rate tests for all containment clectrical penetrations have been cuccessfully completed in.accordance with references 2.1.1 and 2.4.1 and the Quality Compliance Reports for the F.lectrical Penetrations are attached.(m f,#[
., y-icy 4,f p
Verified by /_ M, g e Date fj/ > M ' age, g
, , Ayhip 3.3.3 Primary contair.nent Itcating & Ventilating fans available and operable. .
Verified by frifLf,u$ Date ; ,z_
. 3.4 Deficiencies corrected that ffect the inplementation of this test.
Vcrifled by f', Dato /////// 8 . e - v - - -
-e , , -, , - -. .- ~- e, - - -
C-30/4
* :rr:i c '
3.5 Readincon Verif icat ion 3.S.1 Syni.m n p:, itir.,:J. (All n,rt inns locate.' :ith t:, t he prinaiy to aad .acludim. the first leah te:. u'la t ion containee . vatve cutai,ie the pritar, <;ontaint;ent c:: cept w: .-
. t'
'i.).
Conon ie nt r./ S v_ i ten Verified by, Da t e,. ,
/
Personnel Access I.ock .fr . _
- f/rd '
9/y/yn Equipncut Acce:u llatch llachiare j d/h
- Dryvell llead linnditnt; Gear _g.p. _
,1.fr/21 Main Stcan Systen 4 f.t',-/ _ , gg/ /_
Feed' eater Systeu 4.-44 " W p fg)4 , g _ ,f(r JL
, g//
RCTC Syaten _r #.se;/7 llPCI Systen [fr)J }/st' /
~Rl1R Syctcn Aus i'.uu g'kO w y _ J d J} je;/ /sk/>f
>'///
s-Reactor Cleanup System _Jr7/1 - __ /e if,(tA) /,/Af7f Core Spray Systea ou e,hi&h"
, /;e/7/
Reactor I! cad Spray in.r/ _9p.'/7/ Dryucll Floor Drain sump jw d _ _
//A /p/
- Dryucil Equip Drain Sump /e_ r.J
_p# , j.///// Service Air Systen Inttrument Air System _jf..t/ pf. . dff, RBCCU System /'r ._ 3 sj, , ,f:4,/#
;x//Mf ,(M, ' d'd, Containr.
C.R.D. Sys. ant(coctplete, Atc. Control filled,Sys Yg _,6fL - ( nornal lincup) 4.(a ff _ ' , mAi ./y-Reactor Vcasel Instrunentation __.d'P */ - p/u/f/ /ef
- W actor Rr.r ric. Y n c r rom <m e - r i an 2gL _,, ,
S:an2b / !.i:in' .! c.'.. c.* 0, ;. /f A Condensate & Denin Water Sys. _d7A ,jegg/.W d6 Ncutron Monitoring . - /p >J ,,:/>; /7/_ Travelling In-Core Probe Sys. f,. 77 s. 74 /pf , All Containment Penetrationn _ ,gE' r., v/ gag se # All Containnent Vacuum Ercakers 42 gf ._ 3.5.2_ All drains, sumps and tanks which are to roccive or discharge fluids are ready for operation. All drains and sunps mopped
- '~
z,7 dryandallleakofjsshut.gjd % 4'u k ff /j' <n' ja'<'j-Verified by __ M / A Ct/ Date [f .
#- 3.5.3 Electrical Services Operational 3.5.3.1 4160 V Swar #3 or I/4 for Service Water Puep
- 3. 5'. 3. 2 480 Y ;'cCSD for Trr.velling sc'reens . .
3.5.3.3 480 V Sugr (!8 or J9 for R!:cCt.' Puups ; y$-6+ s' lm j 3.5.3.4 480 'I 'jCc 8B or 93 for 1 RU-l or: 3 y,yi,.v,,3 gg// . '
/ !
3.5.3.5 480 V ECC 89 for Rnt'-2 an.1 PRt'-4 aanwad'{}dNis
.h y . (?h j. ..) LU.5 {
u b .,s , ,
~' $.n.LI Tenporary Puuc r Supply f or Faan of parar.t api'. 3';6.5 5,4d/' ' ,
3.5.3.6
- Ur,$ica:lN>.:-b'N J)ef - ~
Irl)/ -),
' ~
I Cont.rol circulta checked v.:J avail lo!e f or nervice 3.5.4 f
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,, j g Ver a !** 7[ , p. -
/ -{ ,,4,* Na(U * / "[ ! ~,#[ _
\.m . v ._ . . -
IfrST c-auf o
~
3g0 Ample fita <::tinguichers available at containment entrances.
. Verified by , - A _
Date / / b b.e i i 3M :'o gas bottl.:n or CO2 extin;;ui:,hers in the containment. during test. '
.Veriffed by __g y, ' [./ ..bDate ,<- */
9 s - 3.6 Equipment Check 3.6.1 A coriplete survey shh11 be made to locate and remove any instrumen- , tation, which could be damaged by external pressure for the conduct ! of the Class A test:
}
Item Verified by Date, (1) Containment narrou range pressure instrumentation e isolated and vented I -'& 3 ilW ///f!1/
,(a) All 1cvel switches on Recire FDI M3) M jj M Pumps (3/ pump) removed (unless M 1 m FDI 133 is complete) M,/' /g w///7/ .
i l l (b) ' Equipment & Floor Drain pM pgh g, 1 Sump Floats removed g / ,
~
(2)
~
Recric. pump seal instrumen-( ' taciou Asuia ud ,@ f ~ c'r'r' 4c,0 cV /,w I,,w ma ' ( (3) Drywell pressure suitches ato-seg , '
' g isolated 4 rf % /t[9f21 n o 3.6.2
~ Primary Containment Integrity <stablished in accordance with l the attached valve lincup sheet. .Q1 1:CCS Systems in the normal valve lincup cond on. g d ,,dM ,"'
Verificd by .p! Date Ild/7f 3.6.3 The reactor vcsnel head off or the vessel vented to the drywell kfj!' and Main Steam lines drainedf Drywell inspected for cleanliness c pf cr.d all missile hazards remo cd (e.g. , light 13ulbs). Verified by [r b #'Date /
- 3. 6. 4_ Install neti nheaves on tuo of the bicurers in the containment ventilation nystem. They should be sized for about 1/3 of design speed. The other bloicrs will be turned off and tagged out. 't'his will allcw sonc forced circulation in the containment without overloading the motors. Make provision for nr.peranc
, n.onitoring of the blowers uti.lized.
p .../ ; i i {,Date s ' ' N /
~
Vcrified by ,,_e' g. e ar - _ U
-- -. . . _. =
I
- U T . . C 'l,0/7 3.6.5 I.M L.t l l LW m dlo ire indus t r i.t l cuan ci rculat ion iam; in the toru[
t o. bin t i . L p.e imu be r i t' .+i . ' - po ra r i l y . rhene faiu should be of i the 1 to 1 l'/ ;' IH' t.ype, uit.h t, .arar h i. li n;; ina u'l lod 8. hat i . noma l ly coujd be lor a J/4 t.o I /? lil' l' a n , f o r the .;.m. .. on ny '* ( ~i explalid:d in 3.6.4 / y/.76% d u_, NOTE: If tek;.orary blades are not available, a resintanen ^. Each valve listed in Table 1 is cycled by renote actuation to demonstrate proper closure of norna11y open valves (or opening and closing of nornally closed valves) Pectinent data such as stroking time, indicating lights, and motor current is recorded for future reference. Where possibic, data is transferred from other preoperational test procedurcs. Isolation valve seat leakage measurements are performed by local pressurization between isolation valves at the peak accident pressure on lines uhich penetrate ~ the prirtary and perf orm a containaent function.. Temperature and pressure are recorded and a leakage rate normalized to standard pressure and temperat:ure frem the pressure decay data. All field velds betueen the icolatien valves under test are soap tested and the results recorded. . 1 Two containnent leakage rate tests (Class A) are perfor'ned, one at a retest pressure of 24 psig and the peak accident pressure of 44 psig 'to obtain neasured leak rates. All systems uhich, under post accident conditions, become an e:: tension of the containnent boundary are vented to the containuent- atr oophnre prior to the conduct of each Class A test. Closure of the containment isolation valves is accomplished by the normal mode of actuation and witho'ut any prolini-
. nary exercising.
The absolute method of Icakano rate testing !s enployed for each of thenc , . Class A tests. This nethad calculates the actual mass of air, in ponuds, that is uithin the contafnncnt. Values of this mass of aic arc deter:1ined for each hour the test is in progre..1 and a regression enalysis (Icout square fit) of the data is used to nennure the actual leait rate as n l'uact.;on of time. l L
Th. . t .a t i on i. c . im ruter in int ..:.Ad t e be u;ed for al1 date. Ic.:ing and ca l cu l a t i . .a s . c.e >;:. are wanned a- 00 .;e- d intervata .:ad t he - c; of air . calcul:.t ed at b "rl. inter"als. 'the cM eul.ted "alu.:, are stored J arly arc rag . are o c ta:e;i . .u t . Det ai ls of this r.:lculation are pri"ent4 'i. Atpendin l A an. r W e ri a c - ;'. . ' [ 2 . '
, Each leak rate test ulll be verified b: u,'tering back into the contalnnent a quantity of air approxb..ately equal to that prrviousl: deternined to have leaked and calculat tnq the new n.u.s of air within the containnent. The test is verified when the difference in the nans of air af ter the char;;c and bef. ore the charge is equal to the uetered char;;e value. With the computer functioning, t! tis ~ verification can be cor.pleted in less than one hour.
6.1 . Cycle cach valve listed in Table 1 through one complete opening and closing stroke using any convenient renote actuator. Verify proper operation on Table I. The acquence of operability tests for the valves listed in Tabic I is not significant; however, the valve seat leakage measurements of Section 6'.2 cannot be perforned until section 6.1 has been conplated for the valves in question. Note - Uhcre possibic transfer data from other preoperational test procedures. p g Veriiicd by WJfhA)' Datc n/e j 6.2 Isolation Valve Sca: Leakage Measurencnts s 6.2.1 Stroke close cach pair of isolation valves listed in Tal'le II using any convenient rcnote actuator. Tas, dcenergize, or
. , othe rui n t~ e'nretivate unive o ~er:~rern en prev:~-e <~.a.*-~~~
( vee m ivu. 6.2.2 Drain the volume betucen the isolation valves, depressurize the volunes outside the valves to be tested, and attach a . regulated nitrogen or instrunent air supply with pressure gage, flow r.:cter, and suitable relief valve to the test tap provided. 6.2.3 Pressurize the volume between the valves to 44,psig and soap test all field ucids cnd rechanical joints. 6.2.4 Maintain the regulated pressure source on the volume betwen the isolation valves for suf ficient tire to deternine the st.wdy state leakage rate by measuring the makeup flo" -raquired to maintain 44 psig. , , 6.2.5 Using Tabic II, record the valve seat Icakage rat e in SCMI from the flou uctor. Convert this valve to Lil /ifr usia; the follouing expression: O ,,
). .M 5' % h'
% lL C' . '. ? . 3 V aus ., ?k , ,} j./'1 j)Jf 6.2.6 Depressurize the volu". hetueen tho isolatlea Tcvelv[n, h 'R re.iove all test gear, securc G.e test connection, and return val es to pretect conditions. j . E JM i~ Verified by ,, M I g ,._,Date _ d n
+-
I
- teS C . C-30/]O f
6.3 Con t e. i nnen t Le sk nato l'eanurcaent (24 psig) 6.3.1 D. tam inh prinary cm.t ainecat integri ty in accordance with L fi.2.
, Af t er cunductinn a final inspection of the interior of the
. coatainuca: :rca to innure all pretee:uinites and precautions of th!s procedure have been observed. All isolation valves are to be operated by the nornal moans provided.
!!OTI:: Leave open one large connection to prevent t'he formation of a vacuum in the vessels.
1
'ictified by
&))h yat e' ! /
1 - 6.3.2 Record the following water contents:
- Reactor Vessc1 Level Af8 _ in.
Suppression Chamber Level I _ __ ft 6.3.3 Secure the remaining connection to the containnent and immediately ! conraence pumpin3 air into the vessels. Pressurize:the containment vessels to 5 psig. Verified ba/ Date //// /' i . s NOTE: If any leakage is noted the first check should be nade by applying a soap film to all double gaskated manholcs
- [, .n d a c e . . . *. w m i.m u. u .u a ., inu un '.un inue t and outer doors and associated penetrations of the personnel access hatch, and instrumentation provided for this test.
NOTE: Enter the personnel access hatch in accordance with reference 2.4.4 after inspection of outer door and penetrations is complete. . 6.3.4 Apply a soap film to all field welds listed in the attached Quality Conpliance Report forns for the Class A test. These velds have been completed since the conutructica leak test was conducted, ui/14/7/ Verified by [ [ _ - Date // /0 2/ ~ 6.3.5 Should a leak be noted during the soap test at 5 pain or at any time f before the finni. pressure of 24 psig . . reached the following procedure shall be observed: . (1) Complete the soap test of all double gasketed seals at the existing co:itaini.. cut pressure. i
- (2) Vent the contalonent vessel pressure to ataosphere.
1 NOTE: Tenediately after pressure han been relcated, open a l .- large enour,h connection to prevent the fornation of a vacuun in the vennejs. l~~ (3) Ik fore perforoina any sorP that. nbbt cause P "Pe rk <n ad.ittu.:. re c:.ec.nel 1:.t ., i hn coa t , : ..: mt v.:ss e l s V.c i 17 f.hO C'!!! :8Ilh'd '? : ' 'T ht? ! U 1o I' [re' hI 1 (5X i t' .!n'l
.i
* :;I '* *
.'t n ,n *r 1
- . ' d '. -
IftqT . - C 30/11 (4) nepaic .o.d inupect the defect in accordance with pproved
- precedv o .. - ,.
($) Continue the leahap,e tent, begin.iing ui th pa ragrahh' 6.3. l ., 6.3.6 Inaure that the personnel arcesa leek renains vented to the outside
. atmosphere for LN reiuinder of these tests. The Icakage test of thia lock han bt en previously perform d in paragraph 3.3.1 W a* b on*
- Of .
- Vetificd by __ _/ e i Da -
6.3.7 Start cach of the four fans provided in paragraph 3.6.4 and 3.6.5, , if not aircady in service.
,, Verified by 1 I_ _ .
Date
,it , f_
6.3.8 Increase the containnent vessel pressure in 10 psi increnents until D .sifL the final test pressure of 24 psig is reached. At cach increment j perforn a. rapid visual inspection for leaks. These inspections should
. M be' coordinated with the rate of pressure rise such that the air pf-"/pha cenpressors may run continuously until the final test pressure if .
J reached.or a Ic s no g -
.p $
' [6hwt.
_ Uarning - Before pressurizing t c containment vessels ab c 22 psig, the vessel tenperature must be 30*F or greater. Verified by t/k m _ Date MMk
-- T g ; *0. 3. -) Ui mo m.i.ie v i ny. hu L es i. pressute vi 24ft'+0.3. us uuru. ornn a .
final soap test of all ficif velds. Alo[e. rd w:td. >uMCd
# e
~
k,4 t 4M h 8t(/,t244M VerifiedbyS3 Date _ll /p 2/ / M gg.Jggd r{ 6.3.10 Isolate and depres .urize the air supply 11ne to(1'd . the&'dntarnment c/ >-slts <tx/.6
% gf art 4 vessels then the test supervisor,is satisfied that internal ,4 % g tenperatures have stabilized. Begin recording pressure, tengerature, at and humidity data on an 1ourly basis. rAL.CE,C g Verified by th.& cjf!dCD.UY 0 h f b, .g, g .
gr$t]d Date ffA MA 6.3.11 Maintain a continuous hourly plot of the follosiina dcta until - at least 24 consecutive hourly values are obtained:
#_ (1)~ Reactor building tenperature *F.
f (2) Atcospheric pressure -- inches of mercury, absolute (3)r"Containuent abnointe pressure - inches of cercury absolute
.(4)p/Cen t.a ina .:n t avera;;e internal air tcaperature *F.-
-(5)/Dryve1L 6 Tornu air partial pressure - inches of t:crcuty absolute (6V Mass of the contained tir
- f.
b fdYs ' i
'jfg,W
, Verified by __ -
Dft e
. 6.3.12 A miniaun of 24 consecutive hourly va. lues will bc Jeast stinarc fitted n deterai.no the containment Irahnac rate. . 1 A
/ } - I M ",,:. d Date J/,.lm,'
-: Verified by - /'/
- r
msT - C-30/12 6.3.13 1:stabl f :h the validity of the leahane measurements at the end of the test period by introducing a r:etered quantity of makeup air to the contalnuent. , rij .?s .
^r
{' Verified by //. / ka- Date
/
6.4 Containment' Leak Rate Measurcccat (44 psig) , 7 A 6.4.1 Increase the pressure in the containnent vessels to 44 psig in the r.anner specified in step 6.3.8. Repeat 3a'rdgrap
.3,Y e
, J lj 6.3.9 through 6.3.13 at the 44 psig pressure. i Verified by h ) C ] v g Date a i f f 6, 3 il *% . p n/ti h t_
6.4.2 Vent tha containment and reduce pressure to atmospheric at a rate not to excced 4 to 6 lbs/hr. Innediately after pressure has(.4/.i b m been released, open a large enough connection to prevent the formation of a vacuum within the vessels. Sampic the containment M air prior to personnel entry. Verified by g6 % Date a- /p-# 7.0 Acceptance Criterin. , 1
- 7.1 Class A Tests ,
s 7.1.1 The measured leakage rate at the peak accident pressufe of 44 psig and ambient temperature (L ) shall not exceed 0.80 weight
, nercent of the enntained air ner 2Phnnrm. o pf,yd/
( 7.1.2 The ueasured Icakage rate at s50 percent of the peak accident pressure (24 psig) and ambient temperature (Ltn) s all deccMnd. The leakage characteristics yielded by measurements L and L shall establish the maximum allowable test leakage ra Lt for periodic tests as the lesser of L (L ,:a) # La (Et)l a .-t "0'09 (bpm) 7.2 Class B and C Tests . g p 7.2.1 The sum of the leakage from all penetrations (type B & C) shall not exceed L p. . , 8.0 Return to Normal - .
/ tic 4 hleceS<Ary ,
'g.gq.ah bg%ly 8.1 Replace Recire Pump oil level switch instrume 1on, ump seal instruraentation, i
t c,.,;, c / sump instrueentatign,
.s. u.<.... !- A> and de-isolate drywell instrumentatica.
Verified by ' , , d.'. L' ,,Date / "!7f
. .'/ 9 l 8.2 Positionvalv%slistedinAppendixAasrequiredbyoperatiopCneeds.
Unblock all Drywell/ Torus Vacuum Reliefs. g,,[ //////// Verified by Ib h te /7 /// ')[
- 8.3 Dryucil RRU blowers restored to nor ktemporar-'fana, remov ,
- Verified by .6/ / g[/d,,ml1 Date 4/6/7/
{ . (
n :, t t ,, , L-Jules APPE." DIX X ,,
- i. Autetutic data acquisit'ir'n and rtduct f un is perrm od by the p1s ' :.: miter. .
f-The conputer progra- is based i.pon the ab.:olu:e :..ethod la t.hich the ::.. u:s! v s., ] of air in the containment is calculated by applying the perfect gas laws to. ',.. 1- tenperature and prescure measurements. - 4.r , , y I The computer reads 19 containnent temperatures and calculaten a volume #
- weighted average air temperature. From the Exactel servenanometer,'it reads j
the containment absolute pressure and corrects this to partial presnure" of dry air by subtracting the partial pressure due to water vapor as determlncd from 4 dew point temperaturc' readings. From this data, a constant value for con-tainment free volume, and the universal gas constant it calculates the mass of
? dry air in the containment.
4
- A printer provides an average of input data at 10 minute intervals.
i This output represents an average of all one minute values in,that interval. Calculations arc. made hourly of the contained mass of air and these results
*are provided on an hourly basis. The computer calculation is summarized below.
Refer to Appendix A, Figures I and II for sanple point locations. J Calculation Units Description , Weight of MLBS CA = DA + TA Contained DA = Ucight of Dryucll Atmosphere [MLES] { , ... . '...::: i i TA 'M.ch t . f '"^-"- a r".^q '"'~ '." "" ? , Height of MLBS Drywell DA = K en (0.l91 x_ HAl:006 - DNPSI)
- DUAT + 459.6* *
- Atmosphere 5
K51 = (1.34 x 10 )[ft 3](1,44 x 10 )[in /ft ],= !362 2 2 3 (5.334 x 10 )(F,t lbs ](10') l Lbm *R ' ]
- [MLDS/ PSIA /*R]
1 * )' IIAM006 = Hourly average drywell absolute pressure [In Hg] 4 DWAT = Ilourly averan,e drywell temperature [*F) DEWPSI = Vapor pressure of drywell atmosphers (PSIA] -
, 0.491 converts In !!g to lbs.
- 459.6* converts *F to *R
,1 4 Drywell In Hg 11AM006 Prescura detector is acanned each 15 seconds 4 Absolute and a 10.uinute average of thcan 15 sec. l
-Pressure scana'in calculated. t he <;ix 10 .dunte arceap.cn are aver:.y..d cach hour.
. - - - . . . _ . - . . - - - - ., , , . - , , , , .~ , - - , - . , . ~ . - ~ . , ,
l
, Mi'ST .
C-30/14
. _ _ =_ -. -
Calculation Units Description '
. . . . . . -.. - L -. .... ' .
Vnpor Proscuro PSIA
' DEUPSI is calculated as a function of dryvell dgu ,
of Drywell Atmosphere potnt tenperature in a nubroutine called '., .
~ VPDEU, which i:, a conversion of water vapor -
dew point (DDPT) to equivalent vapor, pressure. DDPT = (M031)(K.t>6) + (M032)(K' )' (See Figure I) te ? M031 = Dryucil deu point #1 [*F) M032 = Drywell dew point #2 (*F] K = Dew point weighting factor (0.5) K6= 8s7 Dew point ucighting factor (0.5) Average *F Drywell DWAT = A(K g ) + B(K,>) +C(Kc) + D(K D ) + F(K p,),, 2.0 5.0 Atmospheric . Temperature KA = .2784 Weighting factors to acight
.KB = .1467 temperature readings from the KC = .1467 elcments by the voluna of air.
Kp = .2433 at the clevation of the detector. _ KF = .1849 \ A = M01'2 + M013 Dryuell temperature sensors (Soc Figures I & II) B = M014 + M015 ( e i a: = unen.a. un17 8 D = 1:018 + M019 F = M020 + M021 + 1;022 + M023 + M024 Weight'of MLBS ,TA = K '(0.491 x 11ATAP - DEUPSI) Vol Torus Atmos- 52 ATAT + 459.6* ' phere K = (L75x105 )[pe3 }-1.44x102 )[gn2 fge3 ] = .473 52 5.335 x 10'[_ft 1bs](10b) ~ Ibm *R . {}iLBS/ PSIA /*R] .
!!ATAP = Ilourly average Torus absolute pressure (In lig ATAT = Ifourly averaDe '1;orus Temperature (*F] ,
DEWPSI = Vapor pressure of torus atmosphers (PSIn] 0.491 converts In Ilg to lbs - 459.6 converts 'F to *R
' Turus Absolute In 113 !!ATAP = I:006 + M007 '
Precourc MC')6 - Drywell Absolute prl'ssure (In 11p,] M007 - Drywel1/ Torus Differential Pre 1sure [In 1!ql l
/.'.' * ? *e O'si.'!!sd Id
. ,i
. ' 'P ;'. ri y ;g : M *
- JfV, ,
1
C-30/t'a Calculation l'ni t s . Dc;cription
. _ ~.. ..- .. . \
Average Torus *F ATAT = (M02 SI M026+M02 W ;-:02G+M02?if030) * *
. Atmospheric '
6 . 0' ~
~ < .-
Temperature ';, . $ M025 N.
}t026 ,
M027 Turus Temperature monitors - M028 M029 M030 - 1 Vapor Pressure PSIA DEllPSI is similar to DEilPSI for the drywell Of Torus (See pg.15) except that torus dco point Atmosphere TDPT is used. TDPT = (M033)(K48) + (M034)(K49) , M033 - Torus dew point"#1,' 'F M034 - Torus dew point #2, *F K 48
= dcupoint vol. weighting factors (0.5)
*- ' K .9 = dewpoint vol. ucighting factor (0.5) 8 i --
Torus Volume Ft 3 ol = (K60 - TIN)/K i
, { 60 28 -
K g = Total Torus Volume (174) K 28
"" E ** "" (*
TLV = Torus Liquid Volume (KGAL)-
. Torus Liquid GAL TLV =
- Volume
- 1) LiquidLevelbelowcenterlineoktorus=
RAD)(180-2 SIN I L ) - SI,N(180 - 2 SIN I,I r. R , it K xK 60 28 *
. 2) Liquid Icvel'above centerline of torus =
(1-RADQ60--? sin "I4 ./R)-SIN (180-2 sin ~IL/P.) x
. 21
' K xK .
60 20 .
- 3) Liquid icvel equals concerlice TLVal/2K xK Le d i: :;mc.e from 1Iqu!d icv.i! to torn l- (FL j
, R r.renlim; of ino.. [Ft] '-
s- , e
. ., - _ . , . 7,0 .. :, . . . . . , .
- rst . - l c-Ju/ Ati 1
At the coapletion of the dryucli Icak rate test at c 1 I I w ti) -
- 1 ct i 1 age a c ti c., -
o 1 cast-squares linear fit. 8+ 5
~'e , .
y (. '
, *f.
/,:
s s*
- e .
b o e 5 5 e S e O m O e e m.i 8 0 a h* e
- e
- e 4
I e 0 e 9 e e 0 0 0 6 9 9 9 l t l l l
- e
<- A III OlX n . .~.
s s .; G..: , . s' ,
- 1 .
q,,i e. . 9,,
!, ,/,
,i
/* ,. (, - .'
~ a s'-
.{.. p o,"r.- '
\ -
S E H S O R P D ir.rT S
.- , . . . h , MO26 x.
4 N m..o
, ~ . . '., NO33 .
- I .
NO34 I.x 1
)
ws /
+ '
. \. MO.27 i .
MQ29 N['%
,/
'%. .s' MO2,8 I ,
. -. , J.tct3
/.1081
- s SUPPRESS'.ON '
CHAid.6ER q
'(- ' . I I t i .
J 1 i 1%IC 1 .
- e facty '
1 E y,
\ >
/\Ol6 J j.;c 20
,i f. FC2l .Ti -
M0 ?'t e *
* . rlc22
--'2/.:0.' :a. --- --
' ,1 013 e .
r '
. , ~K iln's / N. .
,/- \
.: ~ ., / ,
.( , -(/ \, \, l N ,
\
\. '
. I
, > C. u . ,. . . . ,
. ........ ...8
- ~ .
~ SE ilS .;R P';!i!'l S F Z ~-- - - ~-- , f _
s I - N..... . . . - - . . .
-{ ,- -
, , . is
,- cc .
5, i o .. . ' /* t~ ~ ; ' -.' 19y UO.1.s U). o .'9 . ' r0
?
i
- - G. . , oi -
U --:;::.O...V.d. gg (V fM 3 g s x
. v: .
LtJ 3 L_ .<
-Qs. .. ~
/
.F.
7 [ N
/
,. . .. s _ -
f $12. s
.t .
s g s
~
- / ,....., N -
[ /N .- Ng\ e
- '. M..\ i T' c.,
. O.
m i i c,f- , . . , i 5 \ \. \ Y* ., /Kl /
\
s :. g - / ./
/
_1 __
- o. - /
Li_1 N ,_ ,g,/- f \ Z~ .
\
N s
~.-
[. _. _... y
/ '~ '
[ N
.. . c. .
(!> s \
,/
?
/,s h. .
'/ \
s %ca / N f. D' ,
.r \.--
g : oig. . .._=.,i . ; ; ..g_...- . n m ..;z ....
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g'
, x
k rS'f - C-30/19 4.- TABLE *I j? - -
' ISOLATION VALVE' OPE! ABILITY TESTS -
\, '
- Valve No. IndIcat I.ng Cle:61.h Valve Description _ Verified by Date Lichts Tine SB-16-19-7A Drywell Purge & Vent ,,.b i /- qy;. t '
. //7- o- -
Exhaust (18") r :.3. . .: t SB-16-19-6A Dryucll Purge & Vent Exhaust Bypass (3") f'A?"- - __': > 'iT- 3'- '" -
?:yx > r.si SB-16-19-7B Suppression Chamber Purge f > ' ' e ' d .*/'% l7- '
& Vent Exhaust (18")
pa,vs'C 2+ SB-16-19-6B Suppression Chanber Purge ] a A. 's*/ < - */ / - / e . e 4/C
& Vent Exhaust Bypass (3") / - '
pxw C 34 SB-16-19-6 Drywell Air' Purge Inlet 9 /". /' M ee-s / <r/.*fh'. SAT . 0 :. (18") ' Pi:w Cd4 SB-16-19-9 Dryvel). iir Purge Inlet p E .- u c.u c h/. ;/t- /' (18") Ne:y - y
. SB-16-19-10 Suppression Cha:aber Purge ///.v /J cc .s ."/:'de M7 - -
1-Supply (18")
. . ' .-qu neun e. .avvy m.
ums 14
<J* .J .fi'C .
71
. (Outboard) (h")yu. gggp g f.c/lmp g , // / ' / 7 / /, P SE-2-39 'Recire. Loo 2 Sample Lin fa- #
. . . M. . h '; P ...'..-- tdY -
(Inbear1) (f4") #d A0-20-82 Dryvell Floor Drain
~
EAI' ~ //[f[7/ 47 [ (Inboard) (3")
~
A0-20-83 Drywell Floor Drain ct.l, ///87/ /1-7 ! (Outboard) (3") A0-20-94 Drywell Equipment Drain [3 4 // '7/ () /[, /M C.,. (Inboard) (3") ~( -
~' ' ~
A0-20-95 Drywell Equipment Drain pl _ff if'J / (Outboard) (3") ph., U' ', 7 SB-16-19-11A Vacuun Relief fron Sec. ((//dtb _// ( / OU. + /d,.u< Containment (18") . (/ SB-16-19-11B Vacuum Relief fron Sec. M Containment (18 ) . ___ M____ //!) 4 7f Of "/.ht - . , ' ' ' -6 Exhaust to Standby Cas . . - N-Treatment Systen (LO")
~
SB -7 Dryuell & Supprc.sn ton , Chanim e M. sin 6.h-ust (16")
;Sg , . ,
C-Sq/20 - Indicat'ing ClE it'a-lp1ve No. Valve Description Verific_d by Date I. i *,h b; YJ . e_,, - 4- -2; A .
;-AO 16-yf-;d ':ake-up ::itrop,en 'to
. . :- *' . " . /
_. O..- '
] Supprensjon Chanb.r (l") '
TO' -s! 6 .- ') .
~:;d-AO-16-),9'-74 Make-up Nitrogen to Drr.icli -2
( - * ' (l") .
^
J.c b> c - a b < r.u- . , ,
.c B- AO 19-22 Ma'/.e-up Nitrogen Supply (l") s'
-j 0 2- ' -
53-AO-16-19-23 Purge Nitro uuni ( "I ski -
.ke n E- -
A0-2-80A Steca Line A Inbo so . _ffl?!. g' f d.
/,. As.M
,_ ,/ e/- 1/ c// // /. u, (18")
A0-2-80B Steam Line B' Inboard Isol. ~ ~~
. .I Atcl// '/ -7/
/,. b O /c' __, # ~2 .1c c ..
(18")
,W4 /
/,0-2-80C Steam Line C Inboard Isol. ~,,h ! d. _ // </ - 7/ C// _ _ gd
. (18") -
ny Ad - A0-2-80D Steam Line D Inboard Isol. /fm f_ .3 d // </ - 7/ O // //,(- , (18") A.g o, Ad 2-86A Stcan Line A Outboard Isol. , e ,) / . . ( c ff t/-7/ e./c 2/. (- ', (18") ,
!.0-2-86B Steam Line B outboard Isol. M: 7/_Adjy e/-1/ ev //.'T
{- t_ I w s ra A0-2-86C Steam Line C Outboard Isol. /h, - (( f f / <;/ - 7 / r. , ___ //, 7 (18") -
/> . kx '
A0-2-86D Steam Line D Outboard Isol. frf /. ,,. / / </ 7/ t>// '/. . ~ (18") te.0-2-7 4 Steam Drain Inbcard Isol. td n!7 f o f' / 6. J 74'C .
~
(3") [/ T' , MO-2-77 Steam Drain Outboard Isol. )[fm ~
/I 'i l D.[(. ,,/_o.016C (3") f l/
MO-23-15 11PCI Stm Inboard Isol. (20") y.,n n t.hI ___hK l].f. bkc. g ' MC-2f-16 !!PCI Stm Outboard Isol. (20") ' :a
') 'c l'+' / . . ,,
M0-13-15 RCIC Stu Inboard Isol. (3") / . , 1[7j/g/ f-y d _ / / ()3 g MO-13-16 .RCIC St.m Cutboard Isol. (3") ' fe- - e' '
/ hj_-
. MO-12.15 RWCU Inboard Isol (supply) I. / ' f. ' '
' s'T -
l' / 7 's. "
~
(4") -
.. . r- .-
. ' ! ;. -18 RUCU Outboard Inol. (supply) ,,_ _
-(!- / *
(4") l - g
- . 68 R'.'CU Outb ia ed I'."t" rn ino (4"); . . . a .l,, , ., _ ..___,.,___,_,,1,._.,_,.,/'. .
l
. . T AP, L,':: II '
l ISOLATION Vid.VE S E '.T LEAKAGE TEST ~ Line Valve Tested Boundary Valves [ir ] [Ft ] Leak-Rate Leak-Rnte Dian er Volune S CF//.c. [LTJi/I'R] Verified by Date' SB-6A & 7A ! I ' ' ' tcinnent Purge SB-6 6 SB-7 SB-6B & 7B 11 309.71 l\
'ji'h/ ,y
/tk+o ,A S1L-F. L 1 -
_.. w ) V-16-12A
.ua Relief SB-12A SB-11A 2( 11.25 ,
(') l', _ w eoE b'YU r (' tum ?.elief SB-123 V-16-12B l 2C 11.25 SB-11B ),,,, ( f ,", y ' ,p/
/
SB-9, SB-10 SB-8,9,10 , 0-
.:.'.in ent Purge S3-1-156-23 m gmaag SB 6-23 lE eu o sp, a . p5.7 /
p , ,,,,g( o 0 gg jj/g/W
, MS-77 s:ca: Drain ::S-77 M.., 2 .61 l a- 74 C '.-
ir. Steam A :-!S-86A -80A lE 38.14 / s MS-86A i-y l Sten: 3 :'S-363 !S-803 '
;h /,-
16 37.2 #A ' ' XS-863
, , I / , ,
A& l / .: S eam C :'S-86C XS-80[" ,, 18 37.2 . '
.s . ,,.a- c 6. ,, ,-
., /. .
o,
. \
~
- S t e .;_ . D l::S-S6D c.S-86D
. 18 '38.14 '.[
f
~
I. i -
/ '
. . -'i s\ C- \/ '
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'9 tp. Drain Dischargy ED-95 . .
-95 3 . 147 o o M ///pg r i
-rOrr.inbisch'a'rgE
[ J' - p.Of ' FD-83 82 .
- e, ., r, 1
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TABLE III ,
- s. .
No::..ru.cTatcAt TesTAntn ci.::ET1'.iTIO!;S A.' D SEALS ,I ' . ,_. , c'.
\. -
l's ~
.' l.eak b, ,', ja P ei. ation No. Descrintion Rate Verified by Date _ -
vet "tM
%-7A Main. Steam Line "A" t '.
X-7B Main Steam Li.tc "B" X-7C Main Stcan Line "C" __ X-7D Main Steam'Line "D" d X-9A Feedwater Line "A" W3/ X-9B Feedwater Linc "B" Y X-ll HPCI Steam Linc X-12 Supply to RilR Pumps X-13A RI.lR Return ,to Rx X-13B RHR Return to Rx' __ X-14 Supply to Rx Water Cleanup i x
- nre snray rn wr ,
X-163 Core Spray to Rx y T DOUBLE CASKETED SEALS Leak - Rate Penetration No. Description LB/11R Verified by Date d X-1 Equipment Access Hatch
--_o_ MM
__ /[/
,v,/7/ . g, . --- Drywell Flange () MB /u MW l/6/7/ <# 43 X-4 Drywell Head Access- O [_ //I/rf/ 4 y.
X-6 I Removal !!atch J_ J _ l/ //. X-200A & B Torus Access 11atchs(2). J_ g _ #/7/7/ j Shear Lug Access (8) _ k h , [h . ![!7!7[ t [dE, oca.m/
--- Vacuum Relief Access rg/ /od=3e. o f//a/7/
. Hatches { 80) ( 0 '^' * ) .
4chst.'
,6? A -
X' 2
- Air Lock (Sce page 27)
&_ .4 Q W
,vg Turi.L !.c/, v:r. RATE ,Q_, _ _ _ __ _ _ _
'i',ESO.N;!!?L 1:ATCl! LEAK TEST , f NOTE: Test of the Pernennel Air Lock shall be co:alucted as a ,
separate test after the inner door has been secured with ,
*, strongbachs and the cuter door L.u; been cloned.
\ *
.(
- 1. Pressurize the' air lock to 10 psig
- 2. Observe and record the pressure at the end of 1 hour Time Start Pressure -
Time Finish Pressurc .
. Pressure Loss Leak Rate Verified by _
Date e
- er I *P .
l
. / 89a p!;g. % /co+ a c&d d fdeugc f A "&
~ '
w+ ms leakp. i- g)c .>d // i 7/ ' ,
. t.
e e , O e O $ e t
- 4 g a 4 G
i . . e 9
, . p g
\
e
,,. i
- e
. . l
o.
' ,8,h, ' .
,~
VAlNE LINi:UP Sily.ET , ) ,,3
,, )
e '.c ,j , c> . 4 DATli il <f/7 / '~',.') , ' o e
- -- - ~
,. Cont.rol 'i
.' ' ' n'
,, y Der 2rintion T.oca t i on Por.! t 12:r_Init:a)'
40-2-SOA Main Stcan Line A Isol (Inboard) CRP 9-3 [ M3-FOA
- l. -
, Sl!UT g
g3 003 A0-2-503' Main Stcan Line B Icol (Inboard) CRP 9-3 SilUr
!:-00C A0-2-800 Mdin Stcon Line C Isol (Inboard) CRP 9-3 SIIUT ,
Wh_. v I
- 5-80D A0-2-80D Main Stcan Line D Isol (Inboard)
CRP 9-3 SHUT N.jg , ~ . . j v
- !s-86A , A0-2-86A Main Stcan Line A Isol (Outboard)
CRP 9-3 gg g
- 5-86B- A0-2-86B Main Stean. Line B Isol (Outhoard) CRP 9-3 I
. .. : .S11UT
_ '_ gnQ
.$-E6C A0-2-86C Main Stean Line C Isol (Outboard) CRP 9-3 __ (-
SHUR .
, N tL_-
M5-86D A0-2-86D Main Stcan Line D Isol -(Outboard) CRP 9-3 gj;gre gg
.. . e .g..
. ::S-74 M0-2 ,74 Main Steam 1.ine Drain (Inboard) CRP 913 SI'UT
]t,g6
. MS-77 ' , MO-7-7.7 v' Main Stean Line Drain (Outboard) CRP 9-3 ' SHUR II -
.( : i.n s .e c m r. n ev gr c._q z7 s$2 (n.. .;y . ..
8 s cry n . . c , , , ,-e g s_~.7 .
? . ._ _ t .. s. D1 SS-39 SE-2-39 Recire Loop Sanple Line (In' board) CRP 9-4 SHUT
_g ' IUIR-57 M0-10-57 RHR Discharge.to Raduaste
. CRP 9-3 OPr:: .N , .h.
. . , _ _ e-p.,
RHR-66 MO-10-66 [_ RHR Discharge to Raduaste 'CRP 9-3 SilUT v A kl!R-39A- ,RIlR Return to. Suppression I'ool M0-10-39A f CRP 9-3 SUUT " g RliR-393 M0 39B RilR' Return to Suppression Pool CIUS 9-3 SHOT %
~
GV8L...- 191R-34A MD-10-3'45 t/ SilR Return to Suppression Pool CRP 9-3 SHUT - R!R-34B MD-10-34B RHR Return to Suppression Pool CP.P 9-3 SillTr
- gub_.
h!!R-26'; !:0-10-263 i RUR DryveJ1 Spray CRP 9 3 Shirr __ . - . - (3 10in-3] L* M34d-37.f.h f h:m.Dryve11 Spray CIU' 9 -3 SIIUr - dR-26/c M0~-]O-3i'.t.-l4.',;' .
- m. . . k' Dryuell Spray CRP 9-3 SHUT y
. =
PlR-314,. MO-10-)fA*.d. iGiRGrywell Sprey CRP 9-3 '
~....,.
SltUT
]
. . .... mgm .
'k 38A M3-30 30A -
l
'ye. Ril.P. .< ...r Surpresr.!pa
. ~ .:; * ,Chanber Spray CRP 9-3 SlHIT gMg. . . .
_. ._ 1 J;h-3C:s M0-30-3CD d Rl!R Suppression Chenber Spray CKP 9-3 SHliT ^ '
- 3. _ ......-.. . .-h.
..... Par,c 1 of 4 .
1 l
l f' * . ' I * ..
/
,. DATM l'/'?[7/ _ ." .
T51ve Control ' ' ' " nu.ber Dencription 1.ocation Penition Ifal IA-96A V-72-96A Containment Air Compressor Suction U~s i
= T.ocal SHUT .
-i IA-96B V-72-96B Containment Air Compressor Suction 1.ocal SilUT ', ,
j Double Sets Drywell Air Sanpli.ng System SilUT v/ ' FD-82 A0-20-82 Drywell Ploor Drain (Inboard) CRP 9-4 Sil0T FD-83 A0-20-83 .Drywell Floor Drain (Outboard) CRP 9-4 guy 7 ED-94 A0-20-94 Drywell Equipment Drain (Inboard) CRP 9-4 SilUT ED-95 A0-20-95 Drywell Equipment Drain (Outboard) CRP 9-4' SiluT AC-8 SB-16-19-8 Drywell Air Purge Inlet CRP 9-3 SbUT AC-9 SB-16-19-9 Dryuell Air Purge Inlet CRP 9 '-3 SnUT AC-7A SB-16-19-7A Drywell Purge & Vent Outlet CRP 9-3 SHUT h
! nu-i-. .SL-16-19-6A wivwell futxe & Veu6 Oucleo L wo-: '
RT 3 ~; s ~dTv7 J ' !
*1 1 IAC-7 yg . g,4 IDrywell & Suppression Chamb'er liain Exh.
, CRP 9-26 SHUR g li)D s.
AC-10 SB-16-19-10 Suppression Chamber Purge Supply CRP 9-3 SHUT M AC-7B SB-16-19-7B Suppression Chamber Purge & Vent Outlet 'RP C 9-3 SHUT
)QM AC-6B SB-16-19-6B Suppression Chamber Purge & Vent Outlet Mvpp_s s CRP 9-3 SHUT Lt>D AC-6 SB-6 -
Exhaust to Standby Gas Treatment System CRP 9-26 SHUT RHR -17 MD-10-17 PJiR Shutdown Cooling Supply (Outboard) CRP 9-3~ SHUT WD RHR MO-10-18 RHR Shutdown Cooling Supply (Inboard) CRP 9-3 RilR-33 MO-10-33 SHUT
]sh RllR Reactor Head Cooling CRP 9-4 SilUT ph R!lR-32 MO-10-32 RHR Reactor Head Cooling CRP 9-4 SHUT -
g CUW-15 MO-12-15 Reactor Cleanup System (Inboard) CRP 9-4 SilUT y CUU-18 MD-12-18 Reactor Cleanup System (Outboard) CRP 9-4 g
.CUW-68 MO-12-68 Reactor Cleanup System CRP 9-4 SilUT s N
\)
llPCI-J5 MO-23-15 !!PCI (Inboard) CRP 9-3 SHl!T r ] s. Page 2 of 4 . e
=
j . , .. e.
.. *\.
$* Y/.1.YC 1.!::. i'? !;il;;i'.T , ,.- D/J1'. ,__Ma[7 8 .__
,. cen.a.ej
~
~-"'"----
1.oc.it i on
, }:
___.u..d., cr Des c r i p t i co.-=- Ponition ? . 4 ; i t.1. l, IIPCI-16 1:0-23-16 (, !!PCI (Outboard) CRP 9-3 3 iil'.f..---_ . . .' .,.i p'. 1
.i . -
-RCIC-15 MO-13-15 -'
RCIC (Inboard) \ 4 (<.. gg,0 . CIU' 9-4 SillTf
.- 'yJL.A._ ,x
..g KCIC-16 !!3-13-16 RCIC (Outboard) CRP 9-4 gggg. .g AC-11A SS-16-19-11A Vacuun Relief from Sec. Cont. CRP 9-3 SillTr :
1
.. \k~ A .
- n. ,
AC-11B SB-16-19-131) Vacuum Relief from Sec. Cont.' CRP 9-3 . Si!UT
~'
'hlAb .
AC-20 SB-1-156-20 IIU Nitregen to Torus CRP 9-3 SliUT i pl-) _I e
; AC-21 SB-1-156-21 NU Nitrogen to Torus CRP 9-3 SilUT
+
3) i AC -22 SB-1-156-22 YU -Ritrogen Supply CRP 9-3 511172 pp{, i SB-1-156-23 AC-23 Purge ':?itroacn Supply CRP 9-3 S!IIT - t.i. ; V-158-50 Drycell Pressure Sensing l M/177fi j .9'i.f . l Local DPr.:: t
,'t Y O.20 T,, . . ., !' i ..c.c. .. .
e.5:' '
f, ___ C . . .,1. 3, L . : .1 , Cr'::: -* V-158-40 Dryuc11/ Torus P Inst.
' ~
Local CPT:; fdwo-fpg - V-158-41 n Dryvell/ Torus P Inst. Local 'cf ' OPI::: ,
+ 1~)w ,
c%> s .~ .m.-/, S .fr.- e n-s - {-- 'iQir Mi V-153-49 Drywell Pressure Inst. g g g g,. g 'c'? Local .OPr,l' g, , 10 Valve s Drywell Torus, Vacuum Breake'r's l i.ocal ~ OPC:-nl.0C . ijy(y'g. X-2 Inner Door . Air Lock Door '~'
, Local' S!!UT \
E.. l$ .. Air Lock Door k-
.X-2 Outel Door Local SillTr N ,14.
, , ,, , .r3 2 Flange s Torus Manways Local SliUT {..
! X-6 --- CRD Renoval llatch - Local S11UT T i -- _ ._ Iv -..-- ~
~
8 Covers Access to Shear Luns " Local S111!T f'zT .,C -:..
~
X-1 --- 1? quip .cnt Accesa llatch Local S11UT [\C
.. . - . .:-r- '
CST-Il I _1 Service Connect' ion Local SliUT
'[i$] 4...
.72-90D 1A-90D Dryucll !!eadet 1 solation Valve Local Silt 7 , c'\
SA-33
. ~--- j'y('
lV-77-33 licader Irolation Valve Local Sill:? '. w-~~~--- . . . ... . _
- . . . . ~ . . . .
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e pd%
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APPENDIX A Computer-Generated Repcrt e 9 x 0
1 i ( 4 i i I 1. INTEGRATED LEAK RATE TCST (ILRT) e J B i
** " -+ ~ ~ ~ - -
~ ~ ' ' ' "- - ~ r,- --- . ,e- -, - ,., ___. , _ , _ _ ,_O, _ _ , _ _ _ ,
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 INITIAL START 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 CEhT ERROR COEFFICIENT = 0.226 WhERE COEFFICIENT OF 1.0 MEANS A PERFECT FIT & COEFFICIENT OF 0.0 MEANS NO CORRELATION. INITIAL COSTAINMENT 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 WElGHT. MAXIMUM NRC LEAK RATE OF 0.128 PER CENT PER DAY GIVEN FOR LOW PRESSURE TEST AT 41.890 PSIA MAXIMUM PROBABLE TEMPERATURE LOOP ERROR = 0.054 DEGREES F. MAXIMUM PROBABLE PRESSURE LOOP ERROR = 0.001 PSIA. - MAXIMUM PROBABLE HUMIDITY LOOP ERROR = 0.296 PERCENT. INSTRUMENT ERROR CONTRIBUTES 0.015 PERCEhT PER DAY ,
- 11) ESTABLISH 99.87 PERCENT CONFIDENCE BOUND '
. L
.f~
"- 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
*" DESCRII' TION OF VARIABLES "*
AVG TEM VOLUMETRICALLY WEIGHTED TEMPERATURE AVG PRE AVERAGE PRESSURE VAP PRE VOLUMETRICALLY WEIGHTED 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 4 a
- r . 4, OBSERVATION NUMBER 1 10 19 28 37 46 55 64 73 82 9'1 5.430 ''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''
l COMPUTED LERK RATES RELATIVE TO LIMITS XX STATISTICAL TOTAL TIME LEAK RATE . 3 783- --- MAXIMUM DESIGN LEAK RATE NRC TECHNICAL SPECIFICATION LIMIT m-= INSTRUMENT ERROR LIMIT RE00CT10N
*
- TMF'.lTEP F 1RST Phr;_R ECt!4Til%' FIT O
2 136-X M XX XXXx id 2 0'489 x***"" x p i xit,,is . F ,,,eit ["F-- ^ rNNNN H I I M U 33 H U O # # #iHHHliHHHt# tHe*t #1NHHr#1r#1rirvirits wrirst i w w w e . . . w i i m X
>- -1 158-T O
M tu -2 005-
' X H :
h o
-4 452-x
[ -6.099-
-7.746 -
-S.393-X l
-11.040- , , , , , , , , , , ,
0 120 240 360 480 600 720 840 960 1080 1200 1320 1440 TIME IN MINUTES -
r g /
; OBSERVATION NUMBER 1 10 19 28 37 46 55 64 73 82 91 0.6800 '
COMPUTED LEAK RATE FIT. RELATIVE TO LIMITS NRXINUM DESIGN LEAK RATE 0.6120- -- NRC TECHNICAL SPECIFICATION LIMIT w-m INSTRUNENT ERROR L'.MIT REDUCTION
* = COMPLITED FIRCT PRL'EF, ECLfRTIDN f ! T O
0 5440-W 2 0.4760-cn
>- 0.4080-T C
M w 0.3400-n. I- [ O 0.2720-M [ 0 2040-0.1360- ___________________________________________._________________
.=========;==============.====================;=.=====================;======.=;===:
0.0680-O.0000 1 ' 120 20 360 4$0 6b0 720 840 9d0 1080 1200 1320 1440 TIME IN MINUTES
ym. OBSERVATION NUMBER I 10 19 28 37 46 55 64 73 82 91
; 0 1800 ''''''''''''''''''''''''''''''''''''''''''''''82'''''''''''''''''''''''''''''''''''''
COMPUTED FIT RELATIVE TO CRITICAL LIMIT XX SIMPLE TOTAL TIME LEAK RATE 0 1480- 5-= INSTRUMENT ERROR LIMIT REDUCTION
= = C0.".F'J tic F T RS T ORf'ER EQUg ricil FI T 0.1160 - ;___;_ __;;_;_;;;__
tti 2 0.0840-oo y 0 0520- X x N g xx
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- x x xxX x x,xx,N,%. x **
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*
- X g x d -0 0120- x u '
et: [ -0.0440-x
-0.0760-x
-0 1080-x
-0.1400 , , , , , , , , , , ,
l 0 120 240 360 480 600 720 840 960 1080 1200 1320 1440 TIME IN MINUTES
(' , OBSERVATION NUMBER 1 10 19 28 37 46 55 64 73 82 91 84 70 '''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''' VOLUMETRICALLY WEIGHTED CONTAINMENT TEMPERATURE 84 67-H e-. W I 84 64-z W e I C 84 61- =
. Lt.
tn W
- W 84.58-
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@ 84 49- =
O. I W i H 84 46-1 i 84 43-84 40 i i i i i , i i i i i 0 120 240 360 480 600 720 840 960 1080 1200 1320 1440 ilj TIME IN MINUTES
- t
(- , OBSERVATION NUMBER 1 10 19 28 37 46 55 64 73 82 91 41.894 '''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''' AVERAGE CONTAINMENT PRESSURE 41.891-41 888 - *
= .
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o 41 877- ' " . ....
- 41.874-
- 41 872- *"... ....
41.869 -
- 41.866 i i i i i i i ., i 0 120 240 360 480 600 720 840 960 1080 1200 1320 1440 TIME IN MINUTES
*R, OBSERVATION NUMBER 1 10 19 28 37 46 55 64 73 82 , 91 0.4200 VOLUMETRICALLY WEIGHTED VAPOR PRESSURE 0.4180-0 4160-E m
m n- 0.4140-z W 0.4120-oc ==*=.....' a
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E n_ ,,,=..=.. . g 0.4080-C 0.4060-1 0.,4040-0 4020-0.4000 i i i , , i i i , 1 0 120 240 360 480 600 720 840 960 1080 1200 1320 1440 j 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 54.615 41.891 0.40s 0.014 0.000 0.000 2 15 d4.606 41.890 0.408 0.014 -0.020 0.000 3 .30 o4.588 41.890 0.408 0.015 -9.914 -0.072 4 45 84.582 41.859 0.407 0.015 -3.449 -0.036 5 60 84.573 41.889 0.407 0.016 0.773 -0.003 6 75 S4.577 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 9 120 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 13 150 84.525 41.854 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 41.862 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 24 345 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.%0 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 t 31 450 84.529 41.680 0.409 0.028 0.302 0.009 1 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 I 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
VARIABLE TABLE SUh!h!ARY (CONTINUED) SAh!PLE DELTA AVG. TEh! AVG. PRE VAP. PRE LEAK COh! LEAK TRA ERROR (T) NUNIBER N!!NS 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 Too 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 M.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 d4.554 41.876 0.411 0.042 0.108 0.013 63 930 M.546 41.876 0.411 0.042 0.105 0.013 64 945 54.552 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 o4.545 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 M.549 41.875 0.411 0.045 0.093 0.012 70 1035 s4.539 41.875 0.411 0.046 0.091 0.012* 71 1050 64.540 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 0.060 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 0.411 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 1 _ ._ j
VARIABLE TABLE SU3th!ARY SAhtPLE DELTA TEht P 1 TEh!P 2 TEhtP 3 TEN!P 4 TEN!P 5 TEA 1P 6 F DEG. F DEG. F DEG. F DEG. F NUhtBER h!!NS DEG. F DEG. 84.360 o4.740 84.o40 84.850 84.540 64.840 1 0 o4.350 64.730 o4.870 o4.830 eL540 M.o60 2 15 84.300 84.730 84.870 N.850 84.520 o4.840 3 .30 o4.730 x4.870 84 FM 84 530 84.850 4 45 o4 230 84.700 o4.o70 64.o40 o4'.530 o4.o40 5 60 M.290 75 M.300 64.710 M.870 84.820 84.520 M.810 6 o4.290 84.690 84.o60 d4.M 0 o4.510 84.810 7 90 64.290 84.700 84.o60 64.820 84.490 84.7o0 o 105 84.260 M.690 84.850 54.620 84.500 84.800 9 120 84.250 M.690 84.840 84.810 M.500 84.860 10 135 84.290 84.680 84.830 84.830 84.490 64.780 11 150 84.240 84.690 84.830 84.790 84.480 84.800 12 165 84.200 84.670 84.820 84.820 84.490 84.810 13 180 o4.220 84.6e0 84.820 84.810 84.490 84.800 14 195 210 84.240 84.660 84.820 84.800 84.480 84.740 15 225 84.250 M.650 84.810 84.810 84.460 84.780 16 N.720 17 240 N.270 84.630 84.800 84.790 84.450 18 255 84.210 d4.650 84.800 64.810 M.460 e4.610 270 84.220 o4.670 84.810 84.790 84.470 84.790 19 20 285 84.230 84.650 84.800 84.790 84.470 84.7o0 21 300 84.250 84.660 84.800 84.780 84.460 84.780 22 315 N.230 A4.660 o4.790 84.810 84.470 84.800 23 330 o4.230 N.670 M.790 M.610 e4.480 N.olo 24 345 84.240 84.650 84.800 84.820 84.470 64.780 25 360 84.220 84.660 84.800 84.810 64.470 d4.770 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 k 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 M.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 84.64 0 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 M.870 84.470 84.790 36 525 84.230 84.650 84.780 84.810 84.470 84.o40 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 M.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 l l l l l 1 I I l l i
+ ,- ,-, e
VARIABLE TABLE SUhth!ARY (CONTINUED SAh!PLE DELTA TEh1P 1 TEh!P 2 TEh!P 3 TEh1P 4 TEh!P 5 TEh!P 6 NUh1BER 511NS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 51 750 N 250 M.670 N.790 0.000 84.490 84.o00 52 765 84.250 M.670 84.780 0.000 64.490 84.760 53 780 84.250 64.650 84.790 0.000 64.490 84.810 64 795 84.240 84.670 84.780 0.000 84.490 84.820 55 810 84.250 84.670 84.770 0.000 84.490 84.800 56 825 84.250 84.670 84.780 0.000 84.490 64.820 57 840 84.260 64.680 84.780 0.000 84.470 84.850 58 855 84.240 84.650 84.790 0.000 84.470 64.810 59 870 84.250 84.630 64.780 0.000 84.480 S4.790 60 885 84.270 84.650 84.780 0.000 64.500 84.810 61 900 64.270 84.650 64.790 0.000 64.480 M.800 62 915 84.270 M.660 84.790 0.000 84.470 64.810 63 930 84.250 64.660 84.780 0.000 84.490 64.780 64 945 84.260 84.670 84.770 0.000 64.500 64.610 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 64.260 M.660 84.780 0.000 64.490 84.o00 69 1020 84.250 84.670 64.780 0.000 84.470 84.830 70 1035 64.250 84.640 84.770 0.000 84.500 84.810 71 1050 84.220 84.670 84.790 0.000 84.490 64.810 72 1065 84.270 64.670 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 64.660 84.780 0.000 64.490 84.800 75 1110 84.250 84.670 84.780 0.000 84.460 84.800 76 1125 84.230 64.670 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 64.760 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 64.220 84.640 84.760 0.000 84.460 84.770 84 1245 84.214 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 84.64 0 84.760 0.000 84.450 84.750 87 1290 84.200 84.650 84.760 0.000 84.460 84.760 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 64.780 90 1335 84.220 64.650 ' 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 l END OF TABLE l I
C
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1 i VARIABLE TABLE SUh!NIARY SA51PLE DELTA TEh!P 7 TEh!P o TEh!P 9 TEh!P 10 TEh!P 11 TEh!P 12 , DEG. F DEG. F DEG F DEG. F DEG. F DEG. F l NUN!BER 511NS 0 85 010 84.840 85.330 85.050 M.710 84.330 1 15 M 950 84.830 85.330 85.030 84.690 84.330 2 3 30 84.950 84.800 85.320 85.020 84.710 84.330 4 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 64.320 6 75 o4.930 M.800 85.330 85.030 84.690 84.310 7 90 84.910 64.780 85.320 85.030 84.690 84.310 8 105 84.910 84.790 85.310 85.010 84.700 84.320 9 120 84.870 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 5E310 85.010 84.670 84.300 12 165 84.900 84.760 85.300 85.000 84.690 84.290 13 ISO 84.890 84.760 85.300 84.990 84.670 84.280 14 195 M.890 84.750 85.310 M.990 84.690 84.290 15 210 o4 910 84.760 - 85.300 84.990 64.670 84.300 16 225 o4.880 84.740 85.300 85.010 84.660 84.250 17 240 64.880 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 M.910 84.740 85.320 84.960 84.660 84.290 21 300 o4.90 M.740 e5.320 64.970 64.660 o4.300 22 315 84.910 84.740 85.300 84.570 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 o4.730 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 84.880 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 64.890 o4.750 65.320 84.970 64.670 84.300 33 480 M.880 M.740 o5.310 84.950 84.660 84.290 34 495 84.870 84.750 85.320 84.970 84.660 84.2 M) 35 510 84.870 84.740 85.310 84.980 84.670 84.300 36 525 84.860 o4.740 85.300 84.970 84.660 84.290 37 540 84.890 84.750 85.320 84.970 84.670 84.280 3e 555 64.890 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 85.340 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 [ l . i
i
, VARI ABLE TABLE SUh!NIARY (CONTINUED)
SANIPLE DELTA TEh!P 7 TEh!P 8 TEh!P 9 TEh1P 10 TEh1P 11 TEh1P 12 N1'N1BER 511NS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 5: ,50 84 903 84.760 85.350 85 080 84.750 84.380 5* 65 84.920 M.770 85.340 65.090 84.770 e4.390 53 780 84.910 84.770 85.330 85.080 M.750 84.380 54 795 N.940 84.770 85.340 85.060 84.770 84.400 55 810 84.690 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 El 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 84.770 85.340 85.100 84.760 84.400 66 975 84.900 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 M.950 84.760 85.340 85.090 84.780 N. 370 71 1050 84.860 84.770 85.340 85.080 84.780 84.390 72 1065 64.880 84.750 85.340 85.100 84.770 64.310 73 1080 84.910 84.760 85.350 85.090 M.770 84 410 74 1095 M.890 84.750 85.350 85.080 84.770 84.380 75 1110 64.890 84.760 85.340 85.070 84.770 84.390
, 76 1125 84.930 84.770 85.320 85.090 84.780 M.400 77 1140 84.890 84.750 85.320 85.100 84.770 d4.380 78 1155 84.890 84.750 85.340 85.090 84.780 M.410 79 1170 84.870 84.770 85.310 85.070 84.770 84.400 80 1185 84.860 M.750 85.330 85.070 84.760 84.390 el 1200 e4.910 84.750 85.330 85.080 84.750 84.390 82 1215 M.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 N 1245 84.900 M.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 88 1305 84.870 84.720 85.320 85.050 84.760 84.370 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 84.350 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 l
l
5 VARIABLE TABLE
SUMMARY
TEMP 13 TEMP 14 TEMP 15 TEMP 16 TEMP 17 TEMP 18 SAMPLE DELTA F DEG. F DEG. F DEG. F DEG. F DEG. NUMBER MI.NS DEG. F
- N.500 84.910 84.160 84.190 85.110 I 0 o4.590 M.500 84.900 M.170 M.210 65.110 2 15 o4.590 84.490 M.890 84.160 84.220 85.120 3 30 M.550 84.500 84.890 84.150 84.220 85.120 l 4 45 84.560 84.500 84.890 M.150 84.200 85.110 5 60 84.580 1
84.480 84.800 84.140 84.190 85.110 1 6 75 84.580 84.480 84.890 84.140 84.210 85.110 7 90 84.580 84.490 84.880 84.140 84.190 85.100 8 105 M.570 84.490 84.880 84.140 84.180 85.100 9 120 84.570 84.480 84.880 84.140 84.180 85.100 10 135 84.550 84.550 84.480 84.870 84.140 84.200 85.100 11 150 84.480 84.870 84.140 84.170 85.090 12 165 84.540 84.470 84.870 84.150 84.180 85.090 13 180 84.560 e4.550 84.460 84.870 84.140 84.200 85.090 14 195 84.540 84.480 84.860 84.140 84.170 85.080 15 210 84.530 84.460 84,870 84.130 84.180 85.070 16 225 84.510 84.430 84.860 84.100 84.160 85.080 t 17 240 84.540 84.470 84.860 84.130 84.170 85.0a0 { 18 255 270 84.550 84.480 84.860 84.120 84.170 85.080 19 285 84.540 84.480 84.870 84.120 84.200 85.080 20 300 M.540 M.480 84.870 84.120 84.180 85.090 21 315 84.550 84.480 84.870 84.120 84.160 85.090 22 23 330 S4.540 84.490 84.870 84.120 84.180 85.090 24 345 84.550 84.490 84.870 84.140 84.170 85.090 25 360 84.550 84.493 M.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 84.180 85.090 28 405 84.550 84.490 84.870 84.130 84.180 85.090 29 420 M.540 84.490 84.870 M.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 M.550 84.480 84.870 84.130 84.180 85.100 33 480 84.560 84.510 84.870 84.140 M.180 85.090 34 495 M.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 84.580 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 M.890 84.140 84.220 85.120 43 630 84.590 84.520 84.880 84.150 84.230 85.120 t 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 84.580 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 l l i
/
l' VARIABLE TABLE
SUMMARY
(CONTINUED) SAMPLE DELTA TEMP 13 TEA!P 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 N.520 84.920 N.190 84.250 85.140 52 765 84.590 84.540 84.910 84.180 84.250 85.140 53 780 A4.580 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 57 840 84.580 84.530 84.920 84.180 84.260 85.150 58 855 84.580 84.530 84.920 84.180 84.250 85.140 59 870 84.570 84.310 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 84.580 84.510 84.930 84.170 84.220 85.140 69 1020 84.570 84.520 84.930 84.190 84.230 85.150 TO 1035 84.610 84.510 84.920 84.180 84.230 85.140 71 1050 84.610 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 84.500 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
~i 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 85.170 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 SUhth!ARY r SAh1PLE DELTA TEh!P 19 TEh1P 20 PRES 1 huh! 1 huh 1 2 huh 1 3 NUh1BER 511NS DEG. F DEG. P PSIA FRACTION FRACTION FRACTION 1 0 n4.700 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 M.710 84.440 41.890 0.722 0.672 0.669 4 45 M.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 M.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 f 0.671 15 210 M.6a0 84.430 41.884 0.724 0.674 0.671 16 225 M.670 M.430 41.883 0.724 0.674 0.671 17 240 M.670 M.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 M4.690 84.430 41.882 0.725 0.674 0.671 20 285 N.690 84.450 41.862 0.724 0.675 0.671 21 300 M.700 M.450 41.882 0.725 0.675 J 0.671 22 315 M.710 84.440 41.881 0.725 0.675 0.672 23 330 M.700 84.460 41.881 0.725 0.675 0.672 24 345 M.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 M.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 C.726 0.677 0.674 39 570 84.710 84.450 41.878 0.727 0.677 / 0.674 40 585 M.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 0.67; [ 0.674 43 630 84.700 84.470 41.879 0.728 0.676 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 j
46 675 84.720 84.470 41.879 0.728 0.676 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 0 778 Cf78 ,0.675 50 735 84.730 84.470 41.879 0.729 , 0.679 , 0.675 l
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4 VARIABLE TABLE
SUMMARY
(CONTINUED) r SAMPLE DELTA TEMP 19 TEMP 20 PRESt H'U M 1 HUM 2 HUM 3 NUMBER MINS DEG. F DEG. F PSIA FRACTION FRACTION FRACTION 51 750 M.740 64.490 .41.o79 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 M.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 'O.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 M.490 41.876 0.730 0.679 0.677 66 975 N.720 ~ 84.460 41.876 0.730 0.679 0.677 67 990 M.740 84.460 41.876 0.729 0.679 0.677 6x 1005 M.730 64.4e0 41.876 0.729 0.679 0.677 69 1020 34.730 o4.470 41.875 0.730 0.679 0.677 70 1035 84.730 84.470 41.875 0.730 0.679 0.677 71 1050 M.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 M.510 41.875 0.730 0.679 0.677 74 1095 84.720 84.500 41.875 0.729 0.6o0 0.677 75 1110 84.730 84.470 41.874 0.730 0.679 0.677 i , 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 M.730 M.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 M 1245 84.730 84.440 41.872 0.731 0.679 0.678 85 1260 M.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 0.379 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 f l I l A
VARIABLE TABLE
SUMMARY
SAMPLE 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 4 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 11 150 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 19 270 0.701 0.702 0.716 20 285 0.701 0.700 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 f 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 C.704 0.717 31 450 0.701 0.704 0.717 32 465 0.702 0.704 0.717 33 4t40 0.702 0.704 0.717 34 495 0.702 0.704 0.718 35 510 0.703 0.704 0.718 36 525 0.703 0.704 0.718 37 540 P.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 45 615 0.702 0.705 0.719 43 630 0.703 0.705 0.719 44 645 0.703 0.705 0.719 45 60 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 l
VARIABLE TABLE
SUMMARY
(CONTINUED) SAMPLE DELTA HUM 4 HUM $ HUM 6 NUMBEH MISS FRACTION FRACTION FRACTION 51 750 0.702' O.705 0.719 52 765 0.703 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 60 885 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 66 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 g
,4 1095 0.704 0.707 0.720 75 1110 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 S2 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 l 37 1290 0.705 0.709 0.721 88 1205 0.705 0.709 0.721 l 89 1320 0.705 0.708 0.721 l 90 1335 0.705 0.708 0.722 91 1350 0.705 0.709 0.721 92 1365 0.705 0.709 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 01 COMPUTER REPORT ON CONTAINMENT LEAK RATE TEST TO NRC
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2. CONTROLLED LEA 1: RATE TEST (CLRT) e k e 4
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LEAK RATE COMPUTED USING TOTAL TIME METHOD AS RECOMMENDED BY APPENDIX J FOR 10 CFR 50 tREACTOR 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 HATE AS COMPUTED AT THE INITIAL START 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 CEST MEAN = 0.131 PER CENT ERROR COEFFICIEhT = 0.013 WHERE COEFFICIENT OF 1.0 MEANS A PERFECT FIT & ( COEFFICIENT OF 0.0 MEANS NO CORRELATION. INITIAL CONTAINMENT AIR WEIGHT = 318709.3 LBS. FINAL CONTAINMEhT AIR WEIGHT = 318624.2 LBS. LEAK RATE FOR 4.50 HOUR PERIOD is o.027 PER CENT BY WEIGHT. MAXIMUM NRC LEAK RATE OF 0.128 PER CENT PER DAY GIVEN FOR LOW PRESSURE TEST AT 41.868 PSIA MAXIMUM PROBABLE TEMPERATURE LOOP ERROR = 0.054 DEGREES F. MAXIMUM PROBABLE PRESSURE LOOP ERROR = 0.002 PSIA. MAXIMUM PROBABLE HUMIDITY LOOP ERROR = 0.296 PERCEST. INSTRUMEST ERROR CONTRIBUTES 0.015 PERCENT PER DAY TO ESTABLISH 99.87 PERCEhT CONFIDENCE BOUND 1 CONTROLLED LEAK RATE TEST (CLRT) l SUPPLEMENTAL VERIFICATION FOR ILRT l LEAKAGE OF 0.123 PERCEhT 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 PERCEhT ( 0.843 SCFM) FOR VERIFICATION. l
. - . . _. .. _ _. - . _ .= - - ._ . .-
i
, f NOTE FOR GRAPHS *"
l 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
"* DESCRIITION OF VARIABLES ""
AVG TEM VOLUMETRICALLY WEIGHTED TEMPERATURE . AVG PRE AVERAGE PRESSURE VAP PRE VOLUMETRICALLY WEIGHTED VAPOR PRESSUNE. f 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 ,
- i d
f t t f a , , . ~ , , ,, ,. - - e ,. 1 +l.,' ? ,'i ' ; ',* * :' ? " ,
i OBSERVATION NUMBER i;
, 1. 2 3 4 5 - 6 7 8 9 10 11 12 13 14 15 16 17 18 19 4 650-COMPUTED LEAK RATES RELATIVE TO LIMITS XX STATISTICAL TOTAL TIME LERK RRTE 2.993 - ---
NRXINUM DESION LERK RATE NRC TECHNICAL SPECIFICRTION LIMIT m-w INSTRUNENT ERROR LIMIT REDUCTION w w ed.!*'U rtiG F I 4 ' T Oh'.d . t EQU<iT :1'i F i r U 1 336-u
' '- 5 : : : ;; - _ 5- -- E e 5 5 - e- e d 5 $
Z -0.321 - a3 x
>- -1 978-E C
w
- u. -3.635-
- o x W
f 6 u
-5 292-E W -6 949-g .
-8 606-
-10 263-x
-11 920 i : i 0 30 60 90 120 150 180 210 240 270 i TIME IN MINUTES
-_ _-_ _ _____ . _ _ _ _ __________o
OBSERvRTION NUMBER , 1 2 3 4 5 6 7 8 9 10 11 12 13 15 16 17
' ' ' la 18 19 0.6400 ' ' ' ' ' ' ' ' ' ' ' ' ' ' '
COMPUTED LERK RATE FIT RELATIVE TO LIMITS MAXINUM DES' ION LERK. RATE 0 5830- - - NRC TECHNICAL SPECIFICRTION L IMIT m-m - INSTRUMENT p r.; : . ERROR
' T ~ ' LIMIT
. A L'TREDUCTION
't ~ ' t '
i
~
a 0 5260-m u.s
'I 0 4690-en >- 0.4120-T Q
w u.s 0.3550-
- n. ,
F-6 u 0 29ts0-E 0 2410-0 1840-0 1270- ---------------------^--^-"--'--'-l--'--'--*--*----
- : : : : : : : : : : : ; ; = =
0 0700 , , , , , , , , 0 30 60 90 120 150 180 210 240 270 TIME IN MINUTES
OBSERVATION NUMBER 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 0.2200- -
' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' 'e COMPUTED FIT RELATIVE TO CRITICAL LIMIT' XX SIMPLE TOTAL TIME LERK RATE 0.2030- m-m INSJRUMENTERF30RLINI REDUCTION _
O 0.1860 - x 2 0 1690- , co x l >- 0.1520-l T l O l x x x x y u.s 0.1350- . x , . . (L *
- X
, , , , . . x l--
u 0.1180-x g : : ; ; : ; e [ 0 1010- , 0.0840-0.0670-0.0500 i , , , , , , , 0 30 60 90 120 150 180 210 240 270 TIME IN MINUTES
o OBSERVATION NUMBER 3 4 5 0 7 8 9 10 11 12 13 14 15 16 17 18 19 1 2 l I I I I I I I I I I I I I I I 1 VOLUMETRICALLY WEIGHTED CONTAINMENT TEMPERATURE 84.58-
. I-e-o w i j 84 56-W x
I E 84.54-b 84.52 - E w - 84 50- ' 2 , U 84.48" , , _ E - G
@ 84 46-n_
r w i F 84 44-84.42-84 40 i i i i e : 0 30 60 90 120 150 180 210 240 270 TIME IN MINUTES 1
OBSERVRTION NUMBER 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 41 870- ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' ' RVERAGE CONTAINMENT PRESSURE 41.869-41.868- , E 41 867-n. Z 41.866-W m 41 865-V3 ' w , I [ ' 41 865- " ' l 41 864- - - = __ 41 863 - , 41 862-41.861 , , , i i , , 0 30 60 90 120 150 180 210 240 270 TIME IN MINUTES
OBSERVATION NUMBER 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17- 18 19 0.4200 ' ' ' ' ' '
- VOLUMETRICALLY WEIGHTED VAPOR PRESSURE 0.4190-0.4180 -
G e-< U3 Q- 0.4170-Z - w g 0 4160-a to 0 4150-E , 0-i n.' 0.4140-G 0.4130- , l 0 4120- = O.4110 - O.4100 , , , i i i i 0 30 60 90 120 150 180 210 240 270
. TIME IN MINUTES
t . VARIABLE TABLE
SUMMARY
SAMPLE DELTA AVG. TEM AVG. PRE VAP. PRE LEAK COM LEAK TRA ERROR (T) NUMBER MINS DEG. F PSIA PSIA PER CEhT PER CENT PER CEhT 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 4 45 84.470 41.867 0.412 0.128 -3.951 ,0.061 5 60 84.472 41.866 0.412 0.128 -1.543 0.026 6 75 84.483 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 41.564 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 C.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 t' l i
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 4 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' O.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 e4.180 M.590 84.720 0.000 84.410 84.780 10 135 84.170 84.580 84.720 0.000 84.420 84.740 11 150 84.170 84.590 84.720 0.000 84.420 84.750 ( 12 165 84.170 84.610 84.720 0.000 84.430 84.790 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 lb 255 84.210 84.610 84.740 0.000 84.440 84.770 19 270 84.200 84.630 84.730 0.000 84.460 84.830 END OF TABLE (. 4 e
. . --. ,,.e .,,.g._+- '-
.- - . . - - - . . . m-w,. -
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 7 TEMP 8 TEMP 9 TEMP 10 TEMP 11 TEMP 12 NUDER 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 n4 720 85.250 85.020 84.770 84.320 5 60 54.820 84.710 85.260 85.020 84.750 84.320 6 75 64.790 84.690 65.280 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 64.340 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 M4.330 15 210 o4.800 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 i 'm 4 e_-
VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 13 TEMP 14 TEMP 15 NL'MBER TEMP 16 TEMP 17 TEMP 18 MINS DEG. F DEG. F DEG. F DEG. F DEG. F DEG. F 1 0 84.520 84.430 84.690 84.150 84.180 85.110 2 15 84.530 84.440 84.890 84.140 84.190 3 30 95.100 84.520 84.430 84.880 84.150 84.170 85.110 4 45 84.530 84.460 84.880 84.140 84.180 85.090 5 60 84.520 d4.430 84.870 84.140 84.160 6 75 85.100 84.520 84.460 84.880 84.130 7 90 84.190 85.100 84.500 84.460 84.880 8 84.140 84.190 - 85.110 i; , 105 84.510 84.460 84.880 9 84.140 84.140 85.100 120 84.510 84.460 84.880 84.140 84.190 85.110 10 135 84.530 84.460 84.880 84.150 84.190 85.100 11 150 84.540 84.480 84.890
/ 12 84.150 84.190 85.110 165 84.530 84.470 84.880 84.150 84.210 85,110 13 180 84.520 84.4"O 84.880 84.150 14 195 84.210 85.100 84.550 84.480 84.890 15 84.160 84.210 85.110 210 84.550 84.490 84.890 84.160 84.200 16 225 84.540 85.120 84.500 84.890 84.170 I~ 240 84.220 85.130 84.540 84.500 84.890 16 84.170 84.210 85.130 255 84.570 84.490 84.890 84.160 84.220 19 270 84.570 85.110 84.510 84.900 84.190 84.230 85.130 END OF TABLE 1
i t
~ - ~ -. . _ , , _ _ _ _ W 4 e ,
( VARIABLE TABLE
SUMMARY
SAMPLE DELTA TEMP 19 TEMP 20 PRES 1 HUM 1 HUM 2 HUM 3 I 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
- 4 45 84.700 84 430 41.867 0.733 0.682 0.680 5 60 e4.690 64.440 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 t 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 0.6oo 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 0.6Al 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 l l ( 1 l
/
- - - . _ " .'p=m --e -ew. , ,,
m ,
i i 1 i i e i i l l VARIABLE TABLE
SUMMARY
SAMPLE DELTA HUM 4 HUM 5 HUM 6 , NUMBER MINS' FRACTION FRACTION FRACTION I 1 0 0.706 0.710 0.722 2 15 0.706 0.709 0.722 3 30 0.706 0.710 0.723 4 45 0.706 0.710 0.722 5 60 0.706 0.710 0.723 ! 6 75 0.706 0.710 0.723 l 7 90 0.70ti 0.710 0.723 j 8 105 0.707 0.710 0.723 j 9 120 0.706 0.711 0.723 .j 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 , l 18 255 0.707 0.711 0.724 19 270 0.707 0.712 0.724 END OF TABLE i END OF COMPUTER REPORT ON CONTAINMENT LEAK RATE TEST TO NRC i 4 I i J ( l l l i .
~ - - - - , . . . .
t . ~ . . _ _ . . _ , . . . , . .
i t 4 f i t i APPENDIX B e, - Operating Procedure No. 13100.1 Integrated Len1: Rate Tect O 4
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