ML19224C003
| ML19224C003 | |
| Person / Time | |
|---|---|
| Site: | Crane |
| Issue date: | 05/23/1979 |
| From: | Boucher P GENERAL PUBLIC UTILITIES CORP. |
| To: | Maingi S, Vollmer R BABCOCK & WILCOX CO., Office of Nuclear Reactor Regulation |
| References | |
| TSG-189, NUDOCS 7906280155 | |
| Download: ML19224C003 (14) | |
Text
{{#Wiki_filter:Inter-Office Memorandum
====== mum==s r Cate' hay 23, 1979 TSG--189 j'~ f ) f M i - w b,uo.ec: Pro ced ure Z-63, Rev. 2 " Solid Plant Operations" 0 Unit 2 Control Room Shift Supervisor Location Three Mile Island ~ GFUSC Control h om Representative B&b' Service (Stad Maingi) MGU@@ PORC (Park Bezilla) The included Procedure 2-63, " Solid Plant Operations", has been revised (Rev. 2) to refltet current plant operation. ad Paul Loucher GPUSC Procedures Trailer 106 PB/a1 ATT cc: File m M 257 344- .- ~ 7 9 0 6 28 0 /5f '[ GPU Serv ~ e Corporation c a sutr4 ary of General PutAc Utihtees Corporation 'L c
54 u SIDE 1 -) AP 1001 Three Mle idand Nudear Statio E -6 3 6d p go, Figure 100* - 8 Special Operating Procedure (From 50P LaJ ino.a) NOTE: In.rv wct 6ons.no pu e so..n Ar 1001 Unit N o. mv., b. f oho .o we a co mo*.t tas Dau l-H ' 71 in e,m ' ~~ ~ I /2 L Title s 6 f 2. Purpose ti ci o. ou, . oe sori f 7 NL~ /% $]' /2C.] /-L Ll>. G~Dn &m :L./4X Q& mjg u-JtD b -, A.~T 2fnT nd 2ee o e ki> > So a sii 1 / / 3. Attaen procedure to this f orm writtm according to the following format. A. Limitations and Precatrtions 1. N uclear Safsty / [j' % 2. Environmental Safety a / 3. Personnel Safety 3 4. Equipment Protection. B. Prerequisites C. Procedure 4 Generated by (([ b Date [- 2 2 D 5. D ura tio n of S D P . n.n o. no ion.., in.n so a..,,om in..n.c,.- o... o, en.. op o, c.> o, tas u w - w, ace , ooew. t>=. (a) SDP will be c.ancelled by incorporation hto existino or new permanent procedure submitted by Ib) SD P is not valid af ter O ~ (fill in c6rcum.t.nc ,nica win urt in SO P b.arg e.ac.4.d) 6. (a) is the procedure Nuclear Safety Related? .............. Y es O NoO If "yes", complete Nuclear Saf ety Evaluation.
- i. r, m (b) Does the procedure af f ect Environmental P
.e-io ? ~/ .. '.............. Yes O NoO If "y-s", complete Environmental Evaluat r o. 2 (c) Does the procedure affect radiation expo re t p6:. el?... YesO No O. .n. ' e.., o
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..o av in. una suo.rini.no.nt. 7. Rewew and Aporoval A / g pproved - Shift Supervisor ~ R iewed List members of RC contacted Md ' @g. - / 7J h ~ $f5$,? &k Y c7.uAy" l f~. r.7f si A' C. ~ ~2r w K.h ntw gd gqL.f',, ,,$ u.2 Uait Suhir$tandent A r '> A 7h d * "# t i
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li w E. SOP is Cancelled Sha tt Sup.c.t.o,/3nt et F oe.m.n g,,,, 2S/ 345 1-...,,,
5/22/79 SOLID PIANT OPERATIONS ~1. 0 PURPOSE 1.1 To provide a eethod for taking the RCS pressurizer solid 1.2 To provide a method for drawing a bubble 1.3 To provide a method for solid pressurizer operation
2.0 REFERENCES
2.1 EP-5 loss of la tdown 2.2 EP-21 Total Loss of Pressurizer Level 7.dication 2.3 EP-34 Loss of Natural Circulation 2.4 B&W Transmittal fW248 of 4/13/79 2.5 EP-9 Loss of Makeup 2.6 Z-39 Natural ' Circulation Operatien 2.7 EP-12 Loss. of Instrumentation for RCS Pressure 3.0 PRECAUTIONS AND LIMITS 3.1 This proced:re temporarily p recludes perf or=ance of EP-21. 3.2 Caref ully m nitor pressurizer pressure while raising level. While a ge may be exuerienced due to bubble compression (especially at pressure su: excessive f: 11 rates), a sharp rise in pressure above saturation pressure ef about 10: to 200 psi will be an indication of being colid. When solid, pressurizer pressure will change by approximately 13 psi for every 10 gallens added to the RCS. 3.3 Monitor temperature indication downstream of primary pressure relief,.alves prior to raising level and following solid condition to determine if any significant change in leakage has b2en made as a result of going solid. 3.4 Cic3ely monitor the natural circulation data collected for RCS parameters to ensure criteria established for satisf actory natural circulation continues to be met. '(Re fer to Reference 2.6.) 3.5 Carefully mcnitor pressure while heaters are energized when solid. (Refer to Re f e rence 2., upon the loss of pressure indicator.) 3.6 Closely moni toc Makeup Tank pressure and Auxiliary Building ventilation radiatior monitors. Reduce letdown flow if Makeup Tank pressure exceeds 2 psig or a noticeable rise in activiry levels is detercined on the radiation monitor. Comply with the Makeup Tank addition rates established by J. G. Herbein. NOTE: The response of the radiation monitor to an increase in Makeup Tank Room activity will be delayed. 3.7 Observe the NDTT liuits'of Figure 2. ~ 257 346 ~
5/22/79 Page Yao 3.8 lf RCS pressure rises above the Safety Features Actuation Sys tem re set point, a limite d Sa f e ty Injection Actuation could be initiated wheu pressure is again reduced. 3.9 Utilize the pressure indication on the pen recorder as the prime control?ing pressure indication to establish the control banc. 4.0 PREREQUISITES 4.1 Initial Conditions 4.1.1 RCS pre';sure control in manual with pressurizer heaters cperating. 4.1.2 Natural airculation on OTSG "A" or "B" or both. 4.1.3 Best es timated pressurizer level )l00. 4.1.4 High Fressure Safety Injection System components shall be de f eated.such that automatic or manual initiation is not possible (with exception of running makeup pump). Initiation may violate NDTT lisdts or cause other RCS pressure boundary f ailures. 4.1.5 Low Pressure Saf ety Injection System shall be available for automatic or manual actuation to prevent total depressurization acaldents. 4.1.6 MU-V8 aligned to MU Tank. 5.0 SPECIAL EQUIPMENT 5.1 None 6.0 METHOD 6.1 Taking Pressurizer Solid NOTE: The pressurizer fill rate of about cne inch of MU Tank level every three minutes is selected to utilize approximately 500 KW of pressurizer heaters for the 10 gpm if cdded to the o ressurizer. Fill rates should not exceed about 15 gpm to prescive an adequate heater reserve to control pressurizer temperature. (This is for information only and not to be used as a limit.). NOTE: If an overpressure condition is experienced, a t t e =p t to lower pressure by: 1. C10 sing MU-V-17 and MU-V-18 to is>iate normal makeup, and if necessary; 2. Opening MU-V-5 to increase letdown, end if necessary; 257 347 O
Z-b3, nev. 4 5/22/79 Page Three 3. Closing MU-V-32 and MU-V-378 to isolate RCP seal injection, and if necessary; 4. If pressure rises to within 500 psig of the maximun ' lowed pressure per NDIT curve (Figure 2), consider eration of RC-V-137'at the ' direction of the shif t s up e rvis o r. = ,y - :_ -......_n --.~-. 6.1.1 Establish makeup tank trace at'50 -tES inches by adj usting letdown flow as necessary. to achieve a constant level. 6.1.2 Complete Table A on attached data sheet 1. 6.1.3 Utilizing the combination of MU-V-17 and V-18 and/or MU-V3, slowly raise pressurizer level while reducing Makeup tank level at the - rate of about one inch every three minutes. Operate. pressurizer heaters as follows: A. Initially leave control group as is at beginning of test. (Expect initial presr.are rise approximately 13 psi /,hr.) = B. When pressurizer pressure begins to decrcase (drops 5 psi' below highest previous pressure)', energize backup h.-ater bank'. C. Use the pressurizer' heaters to maintain pressure within 25 psi of the saturation p ressure corresponding to the initial pressurizer temperature. D. Monitor and control the tecperature o' the pressurizer within a control band between the initial pressurizer tecperature at which it was.at prior to filling and 10* below that tempera-ture (i.e., T initial +0 )'. -10*F NOTE: If it is icpossible 'to maintain this tecperature with all heaters energized, reduce the rate at which the pressurizer is being filled until this criteria can bt met. lf not possible to maintain tecperature within .10*F of its initial temperature, raise pressuri2er level in a series of small, step changes allowing pressurizer tecperature to return to within 20*F. Figure 1 is a typical acceptable operating range. 6.1.4 When MU tank level reaches approximat '" 30", secure raising pressurizer level. a 6.1.5 Refill the MU tank from the degassed source with appropriate boron addition to 50" {in the :MU" tank. 6.1.6 Monitor pressurizer temperature. Fnsure St _is within 10*F of the - initial te=perature. Complete Table B on data ' sheet 1. - . ~.. . ~, ~257 34f; ~ ~ a
2-63, Kev. 2 5/22/79 Page Four j 6.1.7 Repeat steps 6.1.3 - 6.1.4 until plant is solid. Indication of solid plant is when pre ~-e increases rapidly approximately 100 to 200 psi above the satucamion pressure corresponding to the initial pressuris.er temperature. Compare with pressures recorded in Table A on data sheet.1. See Precaution 3.9.. . ~--.=-~ - -~. . - ~, 6.~1.7.1' Maintain pressure between '100.and 200 psi above the e -- r saturatio pressure corresponding tW tWinitial* ' 'n ~ pressurizer temperature recorded Ja Table Why adjusting makeup and letdown for a minimum of two hours af ter reaching a solid condition. NOTE: Vnen first taken solid (i.e., pressure r narply increases approximately 100 to 200 psi.bove initial pressure), the Pressurizer may cantain a superheated, highly co= pressed steam bubble. This bubble will act as an ideal gas while superheated and will slowly (possibly over several hours) collapse due ' to-cooling through ru_ -, ambient. losses.and leakage. This sh'rinkage vill. _, .v. . _be seen as an abnormally.large amount of nakeup, . required.to maintain. pressure... NOTE: har every'i0 gallons added to the RCS, pressure ~ should increase by 33 psig. 6.1.7.2 ' Maintain pressurizer tempers.ture 'in a band of plus 0* to minus 10' of the initial pressuri?er temperature _ recorded in Table A. 6.1.7.3 If_ makeup. tank level exceeds.50., divert to letdown the flow.to.the 1.C. 11eed. Tank.~at the di'rection of the_shif supervisor.. lower makeup rank.to.below 50" and realign .MU-VS :to the makeup -tank.'i -- 4 6.1.7.4 Tollowing the hold period specified in 6.1.'7.'1, slowly _^ _ .Teduce pressure to'100 (f 25) psi above the.saturatira,,, pressure corresponding to _the _icitial pressurizer ter.:p-erature.ty carefully increasing letdown flow. 6.1.8 If it is"' desired to draw a' bubble, go to step 6.2. If it is desired. to r m in solid,' go:to step 6.3. 6.2 Drawing a Bubble in the Pressurizer
- 6.2.1 Operate pressurizer beaters as, necessary co establish th'e bulk fluid temperature.. Si the '.pressuriier'ut the saturation temperature for' the ordered pressure when the b'ubble is drawn.
Maintain this temperature, '+ 5 *F for-at least four ~ hours prior 'to draning bubble. .m
- The ordered pressure vill be 'sp' c.ified by.R. C. Arnold er J. G.11erbein c
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z.- o.3, nev. s. 5/22/79 Page Five { 6.2.2 While establishing pressurizer temperature, maintain pressure constant at 100 (+ 25) psi above the desired pressure when the b' is drawn by varying letdown flow to the M/U Tank. .During this pe. riod, makeup f rom the makeup tank may be., <M.t - - NOTE: m req uire d t o comp ensa t e f o_r.'le. ka r_e..._ If, p o.ssible,"MU n... a l. tank'. level. sh.ould be maintaine'd.in.the'. i
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...- lo. v. cad of ts,.Q y _c M. t.m ~. n. c - - to p sufficient- . i... receive. he flow.from therovid.e. t .capac ty -tu the bubble -is. drawn.. If level is greater than.50" in the Makeupia$k af ter the 6.2.3 stabilization period (Step 6.2.1 is complete,' divert letdown at the di rection of the -shif t supervisor to the R.C. Eleed Tank and makeup f rom..the Makeup Tank to'the Pressurizer as necessary .to maintain pressure (compensating for Icakage) until makeup tank' level:is less1than 50" -- .p.
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~ 6.2.4 : Place 'both Waste Cas Compressors in manual.r.un' immediately prior '.. - k - A. = (This _. -ens ures maximum venting (-...._-* to commencing ' drawing'- the bubble.'. -- capacity to.Malie~ up~.'TAnR :t'd preclude sp~urioEs relen'se'during 2,.- J'.:..-Q+. s. - .- w. _s - n,.....~..-...s.. r; _ maximum' letdown flow... condition ), (5;;;,'" W.R...,.r,',.l.N,:,-?..;i 7 D' % ' y'.U'? ' -
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.x-- 6.2.5 Verify Makeup ' Ttnk 'leve1~1s less than.50".and" stabilized at a constant level. Complete Table C on data sheet.1. ~ 6.2.6 Check.MU-V-8 aligned'.to.the M/U. Tan!. and'not -to.the Bleed Tank. _,. .~ -. 6.2.7 Energize. pressurizer lienters 'to maintain p ressurizer te=perature,' l',,' ,+ 3 *F a t the saturat' ion lerperature corresponding to the ordered.. .. p res s ure.,.n._ _; ;,.y a. g.,,,.. ~
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,.: ~. 6.2.8 ' Increase. letdown to nreduce _RCS pressure ?to ;the :seturation pressure... - f o r the tempe riture cs tablishe:d.._in.the. pres s u_r_ize r.". -. Limit ; the...' :-%... ~, ~
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.-~-e... pressure Beercase' to <5 ps1/ min. - -.- a.~. C.- .v o ; . "-~ ;..~'y _. 5-c.._ - 7_.,,, ; m x .,r NOTE: As pressure decreases, K'-V5 must be opened further. to.,_ _ f.';_ _... ~ maintain the rateT of. pressure decrease.' ,. -u.. =... .; -, _~. r _ -. - 6.2.9 Indication.thatja bubble has"been,_ formed will-include.a stabiliza ~ '_,,, _ tion.of.the. pressure 'while continhing to letdown to the makeup rank;. Mark the makeuo'-tank ' level -trace at -the point where pressure has been stabilized. Complete Table D. Return to normal pressure con-trol using pressurizer heaters to v.aintain a band '.as specified by ~ . the.shif t supervisorJf.- e -r. r M. J '." - 4 c-
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6.2.10 Closely monicar Ma'keup_ Tank pressure and Auxiliary Building'Ve ila _,,;;,,.. nt tion ron radiation monitors. "" Reduce letdown if tank p ressure3'.!.".G.. _.. ~ exceeds 2. psig or a noticeable -iise in ; activity leve1_is_.determin_ed_,. ~ ~.' on the. radiation r.onitors. If ' letdown -flow.must be - reduced; adjust;- ~ ;- : pressurizer heater input.to maintain' pressurizer. RID.at the- 'e s i re df.,u.'. temperature +.5.F. r. - =.c. "s _,... ,,,,.- : :.. ; w.- .c. - -' - Y],.;.m :.9*.
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5/22/79 Page Six T. 6.2.11 It is intended to draw a total of approximately 20 inches of Makeup Tank level from the pressuri.:er. When 20 inches of Makeup Tank level increase have been observed, adjust makeup and le tdown to stabilize makeup tank level at a constant value. Also, stop ,~.. i ~ drawing the bubble..sf eithe,.r: +. : =. w., %. ~ c. ~...e .... -... t..; m,...- ....<'.,p,.,%.1....,.m ~, .. v. ;,e.. -.:.- /. ~- .y..,-,. y d ',M; r.;o;r;%n. ~ cM b aoticeable incre i se in. makeup tauk. level.-. within '10 ininutes.,f increasing le taown Slo.is. m.ot o servew p er s tep 6. 217 .A. m ^ This is an indication of an improper valve: lineup, instrumen ~ #:' - tation~ failure or loss of letdown. Go to.EP-3 to restore letdown flow or:. .. -..._. c.. .:.~ B. Pressurizer pressure.is reduced to '50 psi. below the ordered p re s sure. Wb:.u.presst.re control has been re-established to within 50 psf.. of ordered p ressure, complete the drawing of the bubblo as'noted ibove. <.q~ g;.. - 6.2.12 Stabilize Makeup Tank '. level. Operate pressurizer heaters as ' nicessary to maintain. ordered'.j)ressure + 25 psi. Comple te Table E..._,. ~ <, ~.. -...:..... -.. ~ --.,.-., ,s .. +,... - ...w e-- -;,..-.....n.- m - .... n, n.: s 6.2.13 ~De termine. estimated. pressurizer,. level. a s - f ollows.: %. -. ,. -.w ;;.. ;., _. "---.g: :., _... u.m. w. _.. a.,. :. .m .-..-.,..4 .,. -....n: ... ~.. .u ar x.., ,:, p: r.., :,,,-.. Compa re.. Table s C,....
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..".1,,m_.-.-..-. . w.% .D and I.-us'- .a..,=. From the Makeup Tank. trace determine.the number of inches added to the makeup ~ tank before the ' bubble was formed. - (Use mark made ,C.s,',- '~. in step 6.2.9 above to determine when bubbic was formed.). ..:.e,- ~ ..: r h,
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1Pzr ". 42b.; J.227 y.W'MUT 7.. - ^ I- ?..~_... -.. leak' ATime (min.7 y- ~) + (.042)-(Rate X Since ' Bubble) . is w ' - w. ' MUT -g.. (gpm')' Torma tion' was - Q..cM.. e %. dY54.'~'.k.1-.. _ Total '... - Be t ore.l M~. h.:p i .s N .;- y. . Started %.;. _. ~. -..<.; y.. p _n..~,
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w.. ..a.,... f,A _..,, o... 6.2.14 Return.to EP-21, substic'uting the level cal'culated above.for._ "" -- - - - _ - L Re-establish new'TOF~ values in:EP-21 for TPzrcT .E U aves PzrTOF*. "':: i. :.,,. =.. L-.;;~.4 ~,. . M.; - a ~ ~~ 'MUT,nd.A.f rom._. Table EJ;d' r.- '. r- ~~..
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6.2.15 Plot! pressurizer " level and recommence EP-21. tracking metnod. ' '. '._-~ l.J ' The _ final ~1cvb in' thclpressurizer b-[be.Above %and of 'EP '21.. At' the direction of _the shif t~ control'i'~~ the
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., reduce -the level' of",.the' pressurizer to.vithin _the -control -Y.
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'......' w.. - - bandlby eithe~r' Alloking system leakage"-tio gradually bring.;Id 7; 6., "Icvel down or'.if' sufficient volume remains, addition' letdown ~~ h. - T .... er, -- - - -to the make up tank..,.. .o-. ._,,..,_i'.,*. ~ ps C)3 ... 1.-
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2-63, Rev.'2 5/22/79 Page Seven i. 6.3 Solid Pressurizer Operation During solid pressurizer w. ration, the pressurizer pressure shall be maintained at least.100 -(+ ;25) psi ebove the lowest approved pressure. ...T-' foroperationwithasteambubble.kU',-/-.J[.$ M.*~1 M?Y.[ M yj.-r??.-h,N-%U O "--* y' i 1-$. 3 -3 E d :F: ,Q w d ';;G ~ in i ' flow. pres. i.r's by..la]a.ncing"wlit'dodii -f. low' with s.e.aF:u j ect on = Maint. aid 6.3.1 s . :<*m' . n. trol;.p re.s su.re at.100.. (,+_25 ) -. np si:abov.-.c., -u e :the s (~~:. M --a.-..=---.a t u ra tionC- ..,.e Co . Use pressure corresponding to initia'l pressurizer temperature. MU-V-5 to. control.le tdown -flow.M. r.. u. - ;.. s em..:.,.
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s ,~ -ac . --, $g,.... NOTE: 'This procedure will ~ reduce letdown ~ flow to ca minimum. -- -c. Ensure -intermediate - cooling is secured to 'le. down coolers.,,- _._,, ' t n __ prior' to reducing flow to prevent precipitation. Do not . g,..{ exceed 150*7 in the ' Makeup Tank. "..If letdowi-is~ lo'st,. go - - 3... $ . to EP;5, -.Los s.of le td own.r +.w -.m. -. : w-. _. .,./. .,,c ..;. g.., e._ . 5 :'
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- :*.: -. X- ' " i 4.= ~NN L ' -'* 1..:.. r-4 (All three must be. met) ^-i. .r.. 6.3.2 Maintain pressurizer te=perat ': . ;; : -.: y g. :.:=t...> ..-.e.
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- t 7 east 100__ psi, tion.tempe.r.,ature. corresponding to.a pr.. essure at;
.At. the sa. tura. '1. saturation pressure -for t,h.. hird h...o ttes t - e-:-2 s,~--~ above .-v_ -. _.. .. et ~.. ...._r_. :>..,'.- _ %- , 8 4,. ~.** : .in-Core.the... --rmoCoUple_.".5:** '*" . ;r- ' ~ : ' h -mQ'$'5W:d %?.E.'.* Y. $ '-.,,.fs [$~. *.* . ?..,... t.&,.%'.~,.'k. f.< ?.,,,'. a% W A.-d s..'A: " T*= . ~ n c r .f.f.- - -**e - m,..;u.q w".~" r 7 g H
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At least.50*7. greater than -the highes*'.T..MTo _ insure _,-~ ' pressurizer remains the hottest place ia the ~RCS.').1..*, ' i ~ C. 'e *~;-j. t.a s.w. e--m. ' :'., v.
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3. At l_eas t.70 *_F 'be' ow..the,satura ticn recperature correspon to the pr 1surtzer pressure. (to prevent.inad.v rtent reforming.9.-.Q . r c. s..1,.,, ...--....--.x..4.~.. - n...:., o'.. n. a)..a m : - of.the. b. v. ~. - g e. . -i.; n.: - C " w, u.t-* '...:. ( *% 2'.. . t ;.'. -...4 T-a :: * .,,,g RCS,p ress u.re wil17.g- ;. c.. .e. . y. w...m.- a.c _.w . - n. e. u,... v- ...%.: J;..E~9--- . NOTES: 1.~~:;,To,r..r eryJ1*_F change.inl'T ave,.. r ' * ' ' Od*W"'%.wfS..jpfw :M..-M., _.T,-~My 110_y sia...m-2.t-W@ -e. C D. J.n Z'._c;j'."I 'I 2 - .-in c re a s e~by_._ -.:. approximate'l - ---.r>. ...m. C.. . ~. ... @ =.,.,,:;.;j} W. }6 h! l ' or everf'10 gallons. add,e'd_-to; the' RC._Sh.gw._CMmg .....g'.~ c - 1; - .'r--, ed.w T.,'h.. s pressure r - i .p ,,y.+.. ge by. ->.-apprordma.ely 33.psw. w;5. q - ....s otil. han. 3,4,,. . "-ca
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. i .' U.: Natural.Circu'lation..gosto_IP-34 loss of. Natural.2 - . -.= m a: c JZ;' -- * -. :- 3 m-g.,,L,4;,.. w e. m,....::tz-n. m%.y-w;.
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..t . Circu'lation. .r ~r,. c y: ., :.%q. ~ 4,c,:. r . - ~- :,--~..,: w -.-c.c g.2: n. r n.:.1 ..p= y,- -,.n...cg: ;a-t - e.. a 2,..c.- 3p. 4 .. - c.--
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A:=;. ~ y =_.12 % . r. 1:.r.M:: Hourly..cnni.d;he. RI.D..',s ~ on, the. outlet.of -the'ZPressurizer relief rT,.M.,. '- 6.3.3 tor.,t__ valves.scocputer points -402,;403 :and 404). .A~10. degree' - rease' ';_.; ;.. ~ in any one of.hthese tecp'eratures'is indicaffori of a ch'a.%a in' ~ ~" ~&.^ - ~ Chakage rate through.there valves..New leakage calculations,will:.. n - - ~.
- be. needed rto; determine :the new 3 eak. rate. Ref er - Lo 2P;21 loss of ~' :-
".,.l"t .;,..w:=. - * - - Pre s s urize r.'l.evel.~1ndica' tion. 4.
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~ - ' -. 6;; 3. 4 Every '1/..l'hFur,- recorr' the 'da ta ~ 11s t'ed in~ Tab'le F on da ta shee t ~2..*..*C' ",,, -4 ,..*- + y.m e>.,pu.,%.r.m-o?> .,.a a.:-,.' m.W. -. m ..::a._- e... .o c e. o,...A.. w.. - - - -. _ -:.g.m....at .c. .r .r-6. 3.3 Every 4 Jhours,.p erf oun a u. as s bal.ance - on -th,e sys..te.m.t.o.;...de.ter.:.11.e.'.-if.T. ".r t. e- ~ cany. change.0in lea.ka'ge rrate can' be tietected._,.. Utilize equation 1..,.on t.t;;v,J..h..
- c c.y e.';r K.T.:.; c r.~.:, f, + _'.,.;d C L.r s $ g*.= Q Q P.
3ata sheett2:f* ~;i.=:V& [ j T gmm nr . : -u.. ;$. ~~-- -;;,We-g<.g:m-/;.6.q,,,,rm.wa.g ,.a gg.cg,:n.g 6.'3.6,W7f makeup pu=ps ;are lost:or seal inj ection is secured, go -to ~EP-9.gA.-- t , g. o r U I 7. 7.i.. I 3 3.j k, % f-M $ D N M M E. d T M y g h k M M M $ k.; - :.:. m r C : =. % y % &. a %. v g. p y W M M.e p y w p %s = n q %,2 @ n M.wny ""-- -~ ~.,Y:.Q-w._y"%~&i:t3:*.zr*:c.; m~:.u-=;7.,a.p,.-. A;g;4pr.p. :: ~. A MEct'R u." d vr-m _e c;.T sM.- W:.;,m 4 ~m7
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unun anec< 1 t-us si : s a s TABLE A TABLE D TAR'r r Time 1 Time ri-n Tc loon A Tc Tc Th innn A Th Th ..n..- -3M p p femp II C h? p'" Pzr 'Tsmp _ --_
- - ~'
Pzr.Temo =- MUT level MUT level ,MUT level i RCS oress 400 RCS press 400 RCS press 400 RCS oress':: RCS press RCS oress 398 (Pen) RCS press (Pen) RCS press RCS press (Pen') i MUT oress _MUT oress } MUT press TABLE B TABLE C i i Time 'AUT Level MUT Level Pzr RCS Time Before After Temp. Press Fill Fill Tc i Th Pzr temp i MUT level RCS press 400 RCS press 38 RCS press I MUT oress Bank 1 On Off Bank 2 On Off Bank 3 l 0n Off 1, Bank 4
- On Off Rank 5 On Off 257 3 13
~~ ~~ srr.T rnnt. I t 3V5 Settipoi t
Z-63 5/7/79 Rev. 1 DATA SHEET 2 l TABLE F Gallons ._ _. _, 2 Added by ~ ,.. : -; g _- _~- ~ Totalizer ;- S =.q_- - ~- Tave -=-- aca MUT During A Tc Th (Tc + Th) Temp. A 3 Time Level Period 2 Pzr. O MUT Inches AT0F = Gallons AT pzr oF ATave " of At = Min. Pzr. K 200 .850 300 ' 875 400 .897 500 .916 600 .935 700 .951 800 .970 900 .986 _ 1000 l1 1
- q. 1:
Leak Rate = 24 gal./in. (-(1.227)KALMUT +(.0398) K A + (.287)KATpzr + (1.5)ATave) Leak Rate = 24 gal./in.(-(1.257)K +(.0398)K + (. 287 )V, +(1.5) ) INSTRUCTIONS: Determire A's between each 4 hour interval. Be sure to add all additions (A) listed for each interval. Draw a line under the data used calculation. 257 354 i e e
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