ML20199K666
| ML20199K666 | |
| Person / Time | |
|---|---|
| Site: | LaSalle  |
| Issue date: | 05/07/1986 |
| From: | Field R, Kong S COMMONWEALTH EDISON CO. |
| To: | |
| Shared Package | |
| ML20199K523 | List: |
| References | |
| CON-6695-80 3C7-1184-001, 3C7-1184-001-R01, 3C7-1184-1, 3C7-1184-1-R1, NUDOCS 9712010179 | |
| Download: ML20199K666 (127) | |
Text
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ATTACHMENT H CAu ULATION NO. 3C7-1184-001, Rev.1, Dated May 7,1986 ECCS ROOM LEAK DETECTION SETPOINTG (Note that the " Mezzanine Area" as referred to in the attached calculations is the same as the holdup pipe area for RWCU) l l
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i 9712010179 971124 PDR ADOCK 05000373 i i P PDR_
- _ - _. . - - - -._ - - . . _ = _ - . - . _ _ - . _ _ _ _ - _ -
ECCS ROOM LEAK DETECTION SETPOINTS . No.
- 8 Dato ' March 1, 1985 Commonwealth Edison Company Safety Helated yes LaSalle - Units 1 & 2 Project No(s). 6695-80 O Page No. i ,
\ Project File No. 6695-80 WIN-0340 .
CALCULATION RE_ VISION
SUMMARY
SHEET _
APPROVED REVISED PREPARED REVIEWED REVISION BY/DATE PAGE NOS.
NO. BY/DATE BY/DATE <
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i Calc.' No. 3C7-ll84-001 l
Revision: 1 l Page 2 l Project No. 6695-80 ,
ABSTRACT The room temperature for each of the ECCS equipment rooms (RHh Pump '
Room A, RHR Pump Rooms B & C and RCIC Pump Room) due to high energy fluid leakage within the room was calculated. The differential ;
temperatures for the air side of the are*a fan-cooler (VY) and for-the HVAC flow (VR) in each room were also determined. Calculations 1 were performed for summer and for winter conditions and both for simultaneous VR and VY system operation and for VR system operation only.
The results are provided to determine setpoints for the leak detec-tion system.
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- Cole..No. 3C7-1184-001
- Revision: 1 Page: 3 ;
Projection No. 6695 O TABLE OF CONTEN Q PAGE SECTION 2
ABSTRACT'
- 3 TABLE OF CONTENTS 1 ,
S LIST OF FIGURES
- 6 1.0 EXCEPTIONS TO VERIFIED DATA i 7
2.0 INTRODUCTION
8 3.0 COMPUTER PROGRAMS 9
4.0 METHOD OF ANALYSIS 1 9
4.1 Room Temperature 4.2 Differential Temperature Across Water and Air Side of Fan-Cooler 13 4.3 Condensate Flow in Fan-Cooler 13 5.0 ASSUMPTIONS AND INFORMATION 14 15 1 6.0 RESULTS AND DISCUSSION 7.0 REFERENCE 16 REVIEW METHOD SHEET 24 1
APPENDIX A* - HAND CALCULATIONS 1
O
- The in ' Appendix the Safeguards is filed Systems with the Section original report Central File.and is kept 1
, . _ . . . . . ~ . . . . . . . . . , _ _ , . . , , , . , , , , ,, - . . , , . , - - _ , . . . , - y- , . , , . , - - , . .
f Calc. No. 3C7-1184-001
- R3 vision: 1 ,
Page: 4 Project No. 6695-80 1 *
(This page is intentionally left blank) i a
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, , Cole. No. 3C7-1184-001 Revision: 1 -
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Page:
Project No. 6695-80 l
LIST OF FIGURES l
Page I Figure 1 - Model Schematic 17 Figure 2 - RHR-A Room Temperature Versus Leakage Rate 18 Fig tre 3 - RHR-BC Room Temperature Versus Leakage Rate 19 20 1 Figure 4 .9CIC Room Temperature Versus Leakage Rate Figure 5 - RHR A Pump Room Differential Temperatures 21 Figure 6 - RHh b*: Pump Room Differential Temperatures 22 Figure 7 - RCIC Pump Room Differential Temperatures 23 O
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- m. - -, ..-,. , ----r-.--,---- g---- . ,- -- --- -.i-.-- - - -~ . . - - - . -
- _ _ . . . . _- - . .- = _ - - . -__ - .
Calc. No. 3C7-1184-001
<* Rsvision: O '
Page 4 Project No. 6695 80 0 .
1.0 EXCEPTIONS TO VERIFIED DATA All information used in this design calculation was obtained from HVACD and is therefore considered by NSLD to be approved data except for the followings No exceptions,.
Cole. No, 3C7-1184-001
,, Reviolona 1 Page: 7 '
Project No. 6695-80
2.0 INTRODUCTION
The leak detection system (LDS) for detecting reactor coolant leakage from ECC systems is comprised of a number of independent subsystems, each of which is intended to detect certain classes of high energy fluid leaks. One of the ,
subsystems is a collection of temperature sensors used to ;
detect leakage by means of high indication of room air i temperature and/or high indication of the differential temperature of VY system air entering and leaving the area '
fan-cooler. The function of the system is to detect leaks 1 (both steam and liquid) and to indicate when the leaking system ;
should be isolated.
'lva purpose of this calculation is to Jetermine the room ,
temperature in the ECCS equipment rooms (RHR Pump Room A, ,
/~' RHR Pump Room B & C, and RCIC Pump Room) due to high energy fluid leakage within the room. The calculations were performed l
for two cases: for simultaneous operation of the f an-cooler 1 (VY system) and reactor building venti 11ation (VR system) and for VR system operation only. The differential. tempera-ture across the air and water sides and the condensate flow rate of the area fan cooler in each room are also determined.
Results of this calculation will be used to determine set-points on temperature readings to trigger control room annunciators signaling detected leaks.
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Calc No. 3C7-1184-001
. . Rovision: O '
Page:.8 Project No. 6695- 80 0 4 3.0 COMPUTER PROGRAMS No computer programa were used in this analysis.
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Calc. No. 3C7-1184-001
.* R vicion: 1 ,
Page: 9
,- y Project No. 6695-80 t i
%.J 4.0 METHOD OF ANALYSIS 4.1 Room Temperature The steady-state temperature for each room due to high energy fluid leakage was calculated by applying the laws 1 of mass and energy conservation. Figure 1 shows schematically the mass and energy flows into and out of each room.
At steady state the mass and energy balance equations are m3+mw yy + m2 "2 * "1"4 + "2"4 , and (1) q,+mhg g + ghy+mh 2 2 " *1 4h + m h24 (2) where
- ( = mass of fluid leakage, l'\ 1 (g my = mass of " dry" ventilating air (VR),
m2 = mass of " dry" fan-cooler air (VY),
w y = humidity ratio of ventilating air cntering room, w 2 = humidity ratio of fan cooler air entering room, w 4 = humidity ratio of air in room, q, = heat added to room from internal sources such as hot piping an_i operating electrical equipment, etc.,
h 3 = enthalpy of leakage fluid, by = enthalpy of moist ventilating air per unit mass of dry air entering room, h2 = enthalpy of moist fan cooler air per unit mass of dry air entering room, and h 4 = enthalpy of moist air per unit mass of dry air
-in room.
For operation of the VR system only, m2 is zero, and the n i unknowns in Equations (1) and (2) are h 4 and w 4 v'hich can be 1 f,
solved for directly.
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calc. No. 3C7-1184-001 l Revision: 1 . .
Page 10 Project No. 6695-80 4.1 Room Temperature (cont'd)
For operation of both the VR and VY syCtems, the unknowns in !
Equations (1) and (2) are m 2 , h2 , h 4, w2
""d "4 Therefore i three additional equations are needed to solve for h4 and w4 . l An energy balance for the fan-cooler yields the following equation mh2 4 =yp m c at, + m2 h 2 + "2 I"4 ~ "2) h e
I3) where i
g = mass flow of cooling water, c = specific heat of cooling water, p
At, = temperature rise of cooling water, and li = mean enthalpy of condensate.
The last_ term [m 2 I"4 ~ "2) h c) represents the heat removal by the condensate stream leaving the fe.n-cooler. 1 The mass of " dry" fan cooler air, m is given by' 2
m2 " 0 1 /V 4 where Q1 - = volumetric flow of fan cooler air, and v = volume of moist f an cooler air per unit ma::s 4
of dry air.
The volume, v , is related to h 4 4 and w 4 by de 2emo-dynamic properties of moist-air, i.e.,
m2 " O /f (h ,w )
l 4 4 (4)
' Cole. No. 3C7-ll84-001
- R0vicion: 1 ,
Pages 11 Project No. 6695-80 .
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4.1 Room Temperature (Cont'd)
The fifth equation can be obtained from the performance data of the f an cooler which specifies the outlet air condition.
In this calculation, it is assumed that the air leaving the f an cooler is. saturated, therefore (5) 1 w = f(h 2 f saturated air) 2 This assumption is conservative for calculating the room temperature since it minimizes the room air temperature rise for a given leakage rate.
4 In Eq. (3), the temperature rise of the cooling water is required. 1 It is assumed to be the difference of the dew point temperature of th.
incoming air, tdp,4, and the inlet water temperature, t,,g, i.e.,
i i
() A t, = (tdp,4 ~t w,1)
This assumption is conservative for calculating the room temperature. In some cases, this assumption would result in the enthalpy of the air leaving the f an cooler to be less than *the enthalpy of saturated air at a temperatur<
equal to the inlet cooling water temperature. For these cases, the air leaving the f an cooler is assumed to be 'at the temperature of the inlet cooling water and not saturated. The humidity ratio of the air leaving the fan cooler is therefore w 2 = f( h2 ,ty,1) (6) 1 The term Ke -in Eq. (3) can be expressed as-a function of h4 and h , therefore, Eqs. (1) through (5) or (6) can be solved 2
simultaneously for the five unknowns. The temperature of the room, t 4, can be obtained by using the thermodynamic
( relationship between t4, h4 and w 4.
cole. No. 3C7-1184-001 t
- Rovision 0 '
i Page 12 l Project No. 6695-80 i
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4.1- Room Temperature (Cont'd) l Because a manual-iterative process is used to sc1ve !
1 Eqs. (1) through (5) , the last term in- Eq. (3) is j eliminated to reduce the computational effort. This is not conservative, however, the effect on the results is small.*
In the cases where the f an cooler coil is dry, Eqs. (3) ;
and (5) are replaced by the following four equations **
(7)
(mc p ),(t 4 -t2 ) " 'I"*p min (t4-tyg)
I w =w 2 (8) 4 h = f(w ,t ) (9) j 4 4 4 h2 " fI"2,t 2) (10)
O where t (mcp ), = heat-capacity of air ,
(mcp ) , = heat capacity of cooling water, .
-(mc p ) min = the smaller of (mc p ) , and (mc p ) ,,
c = effectiveness of heat exchanger, w ,w = humidity ratio of fan cooler air, 4 2 t
4
= temperature of air entering fan cooler, and .
t 2
= temperature of air leaving fan cooler.
- For example, for the case of 25 gpm steam leak in the RHR pump rooms B &:C-during the summer season, the elimination of:the ,
condensate term results in a room. temperature of 182'F which is 24 !
higher. Because all the other assumptions are conservative, the error should be less than 2'F. For smaller leak rates, the error -
is smaller.
- There are two additional equations because of the two additional i
O unknowns, t 2 and t 4 l >
,___,._,__-..__-._-._______,,.,_.-_.._...m - - . _ - _ _ . . . . - . . _ . _ . _ _ _ _ _ _ _ . . _
i Ccic. No. 3C7-1184-001 i
- Revision: 1 .
Page: 13 Project No. 6695-80
\
4.2 Differential Temperature Across Water and Air side of Fan Cooler The differential temperature across the water and air side
. of the f an cooler are respectively
(
A t, =
t,,, - tw,1, and -
A t, =t -t I12I 4 2 For a " wet" coil, it was assumed that t, g a tdp,4' Although, this assumption is conservative for calculating t 4, it is, however, not conservative for At, and at, when 1
used for specifying setpoints and therefore, a reduction factor is recommended, e.g.,
et w,setpoint = 0.9 at y, and At a,setpoint = 0.9 At 3
For dry coils, at , and at, are calculated by At, =c (mcp ) min (t4 t,1) /(mc p)w, and I13I '
=c (mc p ) min (t4-ty,1)/(mc p) ,
At a (14)
A reduction factor is not required since for a dry coil the 1 at y,o is calculated using the coil effectiveness which is known.
4.3 Condensate Flow in Fan Cooler The condensate flow in the fan-cooler is given by 1
mc " "2 I"4 ~ "2) (15)
A reduction factor of 0.9 is recommended based on reasoning given in Section 4.2.
\
Calc. No. 3C7-1184-001
,e R vision: 1
- Pages 14 l Project No. 6695-80 t U .
j 5.0 ASSUMPTIONS AND INFORMATION
- 1. Each room is assumed to be a homogeneous volume. ,
t
- 2. Normal HVAC (VR) is in operation during the duration of fluid leakage.
- 3. No heat is transferred to the walli of the rooms.
l
- 4. For each room, information for the internal heat load, HVAC air flow conditions, and fan cooler conditions t are taken from Reference 1. ,
- 5. Only steam leaks are considered for the RHR rooms since processing of high temperature 1.iquid by the RHR j system occurs for only a short period (2 hours2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br />) after shutdown (Reference 2) . (Steam enthalpy = 1194 Btu /lb ,) 1
- 6. For wet coils, the temperature of the outlet cooling water is assumed to be equal to the dewpoint of the incom! g air.
- 7. The heat removal by the condensate in the fan cooler is not considered. Justification for this assumption, y la documented in Appendix A.
- 8. The air leaving the fan cooler is saturated. An exception to this assumption is given in Section 4.
- 9. .The effectiveness of the dry fan cooler coil is taken y as a constant.
The conservatism of assumptions (6), (7) and (8) are l discussed.in Section 4.
_ _ ~ _ _ . . _ _ _ _
, , Calc. No. 3C7-1184-001 -
Revision: 1 Page 15 Project No. 6695-80 V(~~l .
6.0 RESULTS AND DISCUSSION Reom Air Temperatures Room air temperatures for various leakage rates and for summer and winter conditions are presented graphically in Figures 2 through 4. Included are curves for two operating conditions:
simultaneous operation of the VR and VY systems and opera-tion of the VR system only. The curves shnw a significant rise in room air temperature with increasing leakage rates under all conditions analysed. For example, for a leakage rate of 25 gpm, the room air temperature exceeds 160'F for all ECCS rooms and operating conditions analysed.
Differential Air Temperatures Differential air temperatures for VR and VY system flows are 1
(} present in Figures 5 through 7. These plots depict the dif-forential temperatures versus leakagt rate for summer and winter conditions for simultaneous VR and VY system operation.
As indicated on the graphs, differential temperature for VR system flow is strongly dependent and monotonically increasing with leakage rate for all ECCS rooms and conditions. On the other hand, differential temperature for VY system flow is not strongly dependent on the leakage rate beyond a rate of about 2 gpm. It also has a different functional dependence for summer and winter conditions. Thus, it is concluded that the differential temperature of VR system flow is a much more reliable indicator of steam leakage than that of VY system flow.
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,, Cc1c. No. 3C7-1184-001-
- l Revision: 1 i Page: 16 l Project No. 6695-80 7.0 REFERENCE
- 1. Design Information Transmittal DIT-LS-HVAC-00ll-3, [
D. J. Benton (HVACD) to R. M. Field and
. P.-L. Kong (NSLD), November 22, 1985. !
i e
- 2. Notes of zesting held in Sargent & Lundy offices on 1 !
August 8,1985, Project No. . 6695-80, !
t D. J. Benton, signed August 20, 1985. ,
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Calc. No. 3C7-1184-001 ,
,. Rovision: 1 !
Page 17 l Project No. 6695-80_ l a l J
l FIGURE 1 :
Model Schematic !
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Entering 1,eaving
- MVAC air _ _
HVAC air i
-- i m,h,w y y y m,h,w y 4 4 l Room air- .
at 1 Air from Fan Cooler t,h 4 4 and w 4 Air to Pan Cooler j i
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Internal Fluid
, Heat Load, Lenkage 9, m,h,3 y l~
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Colc. No. 3C7-1184-001 LEAKAGE RATE, LB/ MIN RGvicion: 1 ,
. Pcgo: -10 Project No. 6695-80 .
- i 100 200 300 400 500 0 --
r- 3 220 , , i-t 200 < - .
- /
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Q .
4 160 .-
JW 140 -
Oi w * '
RHR PUMP ROOM A h
- Steam condensing Mode l p 120 -
A Winter, with VR and VY flows f
M h b Junener, with VR and VY flows f
@ Winter, with VR flow only l 100 .. .
y Summer, with VR flow only i
t 80
[Q
(.;
a 60 .
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i i i l 1 i 20 30 40 50 60
.( 0 10 LEAKAGE RATE, GPM*
FIGURE 2 RHR-A ROOM TEMPERATURE VERSUS LEAKAGE RATE Based on water density of 62.4 lb/cu.ft, dw+r q-yw- .y- y e- , e negr>- y yr wy- m og m -
y -r w,e--w- 9 y e--y 9 *w--r ---+- m ---s -y-
calc. No. 3C7-1184-001 ;
I
,j'"[h LEAKAGE RATE, LB/ MIN Pt.;ect No. 6695-80 ,
200 300 400 500 ;
- 0 100 i e 220 i i e i
. . .s j l 200 -
180 -
160 -
$ 140 -
oi m
'RilR PUMP ROOM - B & C
- Steam condensing tiode 120 -
- G Winter, with VR and VY flows g
d Summer, with VR and VY flows O Winter, with VR flow only 100 - .
V Summer, with VR flow only 80 6 0 (' -
f I i 1 f
O 0 10 20 30 40 50 60 LEAKAGE RATE, GPM*
F.TGURE 3: RilR-BC ROOT 1 TEMPERATURE VS. LEAKAGE RATE "Basid on water density of 62.4 lb/cu.ft.
, .- .,-, .,.-,.--._~,,.-.,a., ..-w , , - - - - --,-.m.. - - - . , , - - . , , -
_ _ _ _ _ _ . _ _ . . _ _ . . . - _ _ _ _ _ _ _ . . .- __ _ . _ _ - - - _ -_._ _ ._ ~ ._ ._ __ . . _ _ _ _ _ .
Calc. No. ?;7-1184-001 LEAKAGE RATE, LB/ MIN R; vision: 1 .
- Paa s 20 s
- O~ o 30 y g0 220 - - - - - - -
- I .
200 ' -
, s
. l 180 -
- 1 160 .-
tu e
140 -
g RCIC P' UMP RODN_
h3 .
g 120 - - @ Winter, with VR and VY flows i d Summer, with VR and VY flows a .
O Winter, with VR flow only
' y Summer, with VR flow only 100 4
80 -
60 ,
8 g
i e 60 I a 30 40 - 50 O 0 10 20 LEAKAGE RATE, GPM*
FIGURE 4: RCIC ROOM TE!!PERATURE VERSUS LEAKAGE RATE Based on water density of 62.4 lb/cu.ft.
1'ife wg -*
4 -r -- z- ---4 g = - ,y+ 4c y y a--y ,-e-w-p-9%,q ,vww vywww e
.. .- .- . - _ - . _ _ = _ _ - . - ~ _ - - - .. . _ - - . . -
~
5bribion: '5"' f LEAKAGE RATE, LB/MI!T Pag 3: 21 ,
200'
- 300 Ob NO , f 0 100 i i !
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I 140 -
s 120,._ AT of VR air 10(
w 80 _ ,
RHR-A PUMP ROOM Steam condensing Mode l @ .
@ Winter,'with VR and VY flows so 60 _
d Sunumer, with VR and VY flows k
R N 1 40 - s
' g 4 _ __ _.e- -G
$ . g -d 5 A' 2L. . 8 6T of VY air s
0
(' 's i , l I I 40 gu 50 10 20 q 0
'd LEAKAGE RATE,,GPM
- l FIGURE'5: RilR-A PUMP ROOM DIFFERENTIAL TEMPERATURES
- Based on water density of 62.4 lb/cu. ft.
Cole. ho. 3C~/-AA6e-ova nuvAo A vis 2 PCg3: T. Projcet No. 6695-80 LEAKAGE RATE, LB/ MIN 500 ;
200
- 300 400 0 100
- i i i '
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e 140 a
I 120 - AT of VR air 100 _
$ 80 .
RHR-BC PUMP ROOM g Steam Condensing Mode
@-Winter,withVRand'VYflows y
g 60 _
8 Susmeer, with VR and VY flows .
p .
~
g 40 _
E .
's% g_ _.e_.____ 4-o
-O
_._Ar 4 20 _
,d AT of W air 2
[
0 -
, i ,
-( e i 20 i
30 40 50 0 10-LEAKAGE RATE, GPM*
FIGURE 6: RHR-BC PUMP ROOM-DIFFERENTIAL TEMPERATURES
- Based on water density of 62.4 lb/cu.ft. ,
ny..- . ..,___._.,,,..._,,_m.,m....,,..,,.-.m.y,. . , . _ , , , , _ . - , . . , _ . . . , .
, . . . . _ . .~.%.y,,. --.m . c , - . , ,,
oss . .. . .. ...s ...
Revioicnt 1 L POgat 23' LEAKAGE RATE. LB/ MIN Projcet.No. 6695-80 500 0 100 200 300 400 .
i i i i
140 .
t i
120 _.
i AT of VR air .
100 _ ,
s t
80 _ .
I' RCIC PUMP ROOM bQ W @ Winter,with VR and VY flows 3
60 - :
g Susumer,wlth VR and VY flows h
1
- 40 -
Os j
o
' g _ _ y __
4
--e -O 20 -
,-g" AT of VY air 0 .
1 I I I i 10 20 30 40 50 LEAKAGE RATE, GPM
- FIGURE 7: RCIC PUMP ROOM DIFFERENTIAL TSMPERATURES
' Based on water density of 62.4 lb/cu.ft.
1
.,>w. .--r .. . , , . . -. o ,. ,z,.. . , . , . , , . . - - - , c.- . ,e ,,-+-- - - . , , - .
..m:.w,- =, -
. s Calc. No. 3C7-ll84-001 '
Revision 1 REVIEW METHOD SHEET Page 24 (FINAL PAGE) fm Proj.No. 6695-80
!vl .
This calculation has been reviewed by me according to the method (s) checked below.
- 1. Computer Aided Calculations a Review to ottermine inat the como .ter pergramt si nas oten vaiiaatea and oocumentea, is suit oie to tne proolem oeing annivrea, ano snat sna caieviation contains ait necessary information for reconstruction at a later cate, o Revte, to ootermine snat ene input asia as specif tea f or program execution is consist-ant with the design input, correctly Oeftnes the ProDiem for the computer algorithm Itattations of the and 1s SU*f1Clently accurate to produce results within any numertcal program, e.
C Review to verify that the resulta ootained from the program are Correct and within stated assumptisnt and limitations of the program and are consistent with the input.
O Review vaitdation CoCumentation for temporary Changas to listed. or Oevelopmental, or untoue single application programs, to assure that methods used aceovately valtoate tne program f or the intenced application, o
Review of cope input only, since the computer program has sufficient history of use at Sargent & Lunoy in stmtlar calculations, f
Review arttnmetic necessary to prepare code input cata.
1 g other:
A U 2. Hand Preparad Design Calculations Detailed review of the ortginal calcdlattons.
a o Revtew by an alternate, simplified, or approximate method of calculation.
c Review of a representative sample of repetitive calculations.
. R.vtew of tne caicuistir , a,a,nst a e,s iar caicuist,oe prov,ous,y performe . ]
- 3. Revisions a Ecttorist enanges only.
O ElimtnStton of unapprovec input data without altering calculateo results.
- X '""kl.4 6 4 .4 Jan.1. GALL ,
- 4. Other jh
%- _W / k
\ "~'~"fg ppa 7, o= w 5 g/[~f m.,oRurivicu-,c:,,,,esg~ g
* * . Calc . 1;o. 3C7-ll84-001 - '
Revision: 1 Page: Al Project No.. 6695-80 O # Prepared _ by \ l W- Date Y ~ O' O Prepared by MM phte Y- 8 'dd Reviewed by M _Date 8/(([ Approved by M 9. _ Date // fey 7, /#7 8 6 v - v y APPENDIX A_ HAND CALCULATIONS O Commonwealth Edison Company LaSalle - Units 1 & 2 Project No. 6695-80. Project File No. 6695-80 (WIN-0340)
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fs.,e'm>(Q-4>)fe ] lab 51, ]80345. 2fAf}p. 35C819 426423, j = m, (9 -ws ) Ju -J6.62- 6 'lSCd. } -0.04A -o.041 - 0.011 e - noo N/A 77) z.s z -o.011 f,y(p,ap,.)/g),Ib/.a, m,. = m3(m - w o 0.00 S 8. ;l )04,A0 15).oA 2.04.8 9 290.!A 357 ]f 24.56 35.82. 42,81 mt'(Il/s)(7.48/Qp n d.00 6',18 12 52.- 18.I1 sty ue- t+ - t, ~5 2.c 30, 55 80, 1 05. 130 J A o, 3S.66 36,7'i 38,21 A te, ,.c ' & - tz, )5.98 6,,5, $4.8$ 36.0J
- a. 9. :o )). 89 13.81 15 43 16.25 mc = Es. (4 )
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mt, IL/wn 20.86 4],7 93.4 155,1 165. 8 115,1 O h . el S.oo Jo.f; ]5,00 2.0.00 2D9] O Ms.,ym*(mt,IL/.e) Z. 50
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, m,.,y=x(mt,IL/.,,)
; 74s/p b u - (v m,w, )/m, 0.0118 s.15z '1 0.3r3t 0.4535 0.6038 0.754 4 0.904 7 8
b &(gs m 4s m.4,,)/m, 110.3 8 ]U.8} 378 8) SS7.8) 736 !2. 'lI6.t5 1015.:A Jo).A t ]2t.ob 16z.z? ]13.z.2- 168.65 zoo.5) so1.86 G =o(('4-1oso.sm o.4 r 4 ) u4)/ i e ts, w c
- 4f - t; 31.42. SZ.06 S t.1) )03.Zz Jf8.6f p 130.5) 13166 FK M co i W 4 50.00b, h.4
- 20*88> b4 * 'l A. 'l ~f ,
. -. A ta , WA C. #Y* '
c.u reEccs Room LEAK DE" REC-T10d Cow N.3Cl-I l 04 ~ 000 SARGENTfaLUNDY ,g7 ggy ... f o,,,
'TcT c / s.i ,_n eiw w.a-s v-n wiw % A4 2 .i F.rd4t_.
O c' - c ec- <".e'" - n.m L A Se lle, - l(,,,t, f 4 2 no w 6, o , Am w 6, o n.i. w.. (o 6 9 5 - 8 0 e. # w.. . An Rczc PVmf A00 h (C w T M pMLT A i C A!Lut AT10h! SHEE T - VR OPERAT10hl oNL.Y Pump Room : RcIC- ,3&ASoH:Summ6K _ Pau na a cus : Wx877*ER JUMM&K C, " 70. 10 A . C'F) a), = 0.002 6 0.0J 8 (/bn//b V' ) 3. A JA.61 (ft'//h 4.,' * ]1.63 44.95 Q= 3918. 254,46 (8t%/)/Am) Gfm (as/v,)=m',- ./b~/mm p= 335, B0,/hiri
; %.* ]l11, 8tw//Jm o,. - 4 z.4 4z. A (/J~/ft')
E cAss 1 case 2- casa s cAss.A case 5 c^se L cass -9 83A Jt5. ] 166, 5 ? AB. 4 0 lW m u, t h /u,,, 2.0.86 41.9 6,00 15.00 26,00 C trh,ym*(tsh,IL/,,) 7. f0 10.00 Z.D. 00 j x218/(o u h ed4 - (ma m,w, )/m, 0.1000 0.18 19 0,3459 0.50'16 0.693f 0.8373 0,018 8 b f-(gs m Js sm.4,)/m, ]4 3,89 L4).43 d36.56 01,1A 826,40 1022.53 %Z9 t 4= (4-toto.s uk)/ 132.90 150.6'l 176.6t. 191.60 z0956 217.43 l0l.54 (o.z4ro.4rs) s ta, m e s t4- t, z8. 90 46.61 12.8z. 90. 6 0 103.56 JJ3.43 S.54
084 DJEFE '
,. NSLD Calc. No. 3C7-ll84-001 , :
Date: ~ March 1, 1985 ' l ( Revision: 0 Page: 1 l SAFETY RELATED: Yes , M M Date
#' ,l Prepared by \
- Reviewed by /1); ka [ 4 Date Ab2U/53" Approved by )f'. $ . 4 #91 __ Date JtF ///4.te/ / /9f's ,
v v . ECCS ROOM LEAK DETECTION SETPOINTS
/
lO 2 n Commonwealth Edison Company LaSalle - Units 1 & 2 Project No. 6695-80 Project File No. 6695-80 7
)
Cole. No. 3C7-1184-001
.e R3vicion: O .
Page: 4 Project No. 6695-80 O %) < LIST OF TABLES I PAGE 1 Table 1 - Results for RHR Pump Room A 17 l Table 2 - Results for RiiR Pump Rooms B & C 18 4 Table 3 - Results for RCIC Pump Room 19 4
Calc. No. 3C7-1184-001
.
- Revision: 0 /
Page .5 Project llo. 6695-80 , o i LIST OF FIGURES Page_ 20 l riguro 1 - Modol' Schematic ,, l 1 O e i O .
--gv w-,-w,,-m-en,-n-w.,w-.-e,y -y,-,-- ,.,y m s.--g,- wer,- o ----
Ccic. No. 3C7-1184-001
.. R3 vision: O '
Pages.9 Project No. 6695-80 ,fq h , 4.0 METilOD OF ANALYSIS 4.1 Room Temperature The steady-state temperature for each room due to high energy fluid leakage was calculated by applying the laws of mass and energy conservation. Figure 1 shows schematically the mass and energy flows into and'out of each room At steady state the mass and energy balance equations are mg + mywy + m 2 W2 " "1 W4 + "2 W4 III and q, A ght+mhyy+mh2 2 * "l 4 h+ m h24 (2) where g = mass of fluid leakage m y = mass of " dry" ventilating air m2 = mass of " dry" fan coolcr air w y = humidity ratio of ventilating air entering room w 2 = humidity ratio of fan cooler air entering room w = humidity ratio of air in rooni 4 q, = heat added to room from internal sources such as hot piping and operating electrical equipment, etc. h = enthalpy of leakage fluid 3 by = enthalpy of moist ventilating air per unit maso of dry air entering room h2 = enthalpy of moist fan cooler air per unit mass of dry air entering room h4 = enthalpy of moist air per unit mass of dry air in rcom. The unknowns in Eqs. (1) and (2) are m 2 , h2 , h ,4 w2 and w4 i, therefore, three additional equations are needed to solve for h 4 and w 4 i
- . - . - . - - . . _ . - . - - - _ _ . . - - . - . . _ - - - . . _ ~ . . . - . . . . - . .
I Calc. No. 3C7-1184-001 *
,. Ravicion: 0 Pages.10 '
Project No. 6695-80 4.1 Room Temperature (Cont'd) An energy balance for the fan cooler yields the following equation mh2 4 = m,c (3) p at,+ m h2 2 + "2 I"4 - "2) h e where - g = mass flow of cooling water, c = specific heat of cooling water, p At y = temperature rise of cooling water, i and - Ti = mean enthalpy of condensate. c l represents the heat removal The last term [m2 I"4 ~ "2) c
. by condensation of the water vapor in the heat exchanger.
The mass of " dry" fan cooler air, m 2 is given by m2 ". 0 17 V4 where 03 = volumetric flow of fan cooler air ' and v4 = volume of moist fan cooler air per unit mass of dry air. The volume, v4, is related to h4 and w 4 by the thermo-dynamic properties of moist-air, i.e., i
= O y/f (h ,w ) (4) m2 4 4 O ,
i l I3 } l _ . . _ --,-.....,,.,_..,._.,,.,.__...,,.-,,.,-.,_s.
. .-.._.,.-..._s, . , _ . _ . _ . , , . . _ , _ , - . _ _ , _ ___...._..._.-.---,i.-.
_ _ . _ _ _ . _ _ ~_._ . _ _ ._- _ . l Calc. No. 3C7-ll84-001
** Revision: 0 ,
Pages 13 Project No. 6695-80 p 4.2 Differential Temperature Across Water and Air Side of Pan Cooler
-The differential temperature across the water and air side of the fan cooler are respectively- !
l (11) l At, = t,jo - ty,g , and At =t -t y (12)
, 4 For a "wt " coil, it was assumed that t , =t 3p,4.
Although, this assumption is conservative for calculating t 4, it is, however, not conservative if At,and At,were ; to be used for specifying the setpoints for these ditferential temperatures. Therefore, a reduction factor is used, i.e., At w,setpoint = 0.9 At, At a,setpoint = 0.9 at, For dry coils, a reduction factor is not required and At, ?nd At, are calculated by (13) At, =c (mc p ) min (t4-t y 1)/(mcp)g. (mc (14) p ) min (t4 - t,,y)/(mcp) , At =c 4.3L C'j ensate Flow in' Fan Cooler The condensate flow in fan cooler is given by
* (15)
.m c ' '
- 2 (" 4 - *2)
O The basis for using a reduction factor of 0.9 is identical to that given Section 4.2.
~
O . s' .. TABLE 1 ^ Results for RHR Pump Room A Cooling Water Fan Condensate Room Temperature Cooler Flow
' Leak Rate, Percent Tentperature, Rise, Air ,
Leak: Rate, Side At gpm r gpm Flashed . 'F 'F Season Type-104 1 3.6- 0* Summer - 0 - 130 17 16 2 Summer Steam 5 100 i 188 59 25 7 Summer Steam 25 100 i f f 4.6 19 0* i f Summer Water 5 14 121.5 129 12.6 18 1.1 1 Summer Water 25 14
- i
- 0 - 75 6.7 25 0*
t
- Winter -
t t t t steam 5 100 104-108 l . Winter * - 161 93 31.5 11.6 Winter Steam 25 100 ! 70.8 7.6 21.4 0.3 5 14 Winter Water mmwn Winter Water 25 14 73.5 22.6 24 2.3 o$$$
- u. s r o
- @'~ W.
o r ; ! n -Jeoz :s o i i 2 . . o [
. ou <
, n, t
j Fan cooler.is cycling. e to M. [
.m w ;
- Fan cooler coil'is dry. I ' GD CD- A f a o 8 i
o o tj i W ; l f. l: i l
- , . . _ . _ . .. . - . _ - _ , . . - _ . - . - _ _ . ~ _ . _ _ - . . ._
O 8 t TABLE 2 , t Results for RHR Pump Rooms B & C r f Cooling Water Fan Condensate ! l Cooler Flow , l Leak Room Temperature Percent Temperature, Rise, Air Rate, i
. Leak Rate, gpm Flashed 'F 'F Side at gpa [
Season Type- ' 0* i 0 - 104 1 -3.7 }l Summer - f 4 5' 100 127.5 16 14 2 [ Sumer Steam ; { 21 8.2 Summer Steam 25 100 182 57 I Water 5 14 117.5 4.7 16 0* Summer Water 25 14 125.5 11.7 15 1.2 , Sumer . ! 1 0 - 75 8.4 26 0* . Winter - t t t t t 5 100 104-108 ; , Winter Steam- r q Steam 25 100 151.5 88 25 13 t t Winter ! Water 5 14 <65 <10.5 <16 0.4 ' [ Winter :
- f. *oown Mmae Water 25 14 69.5 20 20 2.3 oc<w Winter utro '
e.g. o r et w o z , eDo [ z -- t
- o j l
. ow t e O Ii i o e
- w j
! Fan cooler is cycling. = t , m .,.
- Fan cooler coil is dry. o i o o
k W l i ' f
- i
f , t t i l -i l: . TABLE 3 ; l Results for RCIC Pump Roosa - 4 l i , 1 l Cooling Water Fan Condensate ! Leak - Room Tempeirature Cooler Flow ! I: Rise, Air Rate,
- j. Leak' Rate, Percent Temperature, Type gpu Flashed 'F 'F Side at gpm j Season 0 104 1 3.6' 0*
Summer d
-. i i Summer Steam 5 100 126.5 14 15 l.7 !
t Summer . Steam 25 100 175 51 21 8.1 f I 0* Winter - 0 - 75 8 25.5 ,. ! l . f l' 21 21 2 .7. f Winter Steam 5 100 70 Winter Steam 25 100 134 77 27 12.5 l- - ! 3 i [ (' , mmwn 4 nues 4 oc<w r
- uern !
- e-a.
n.- 2 agoz
- ~*
1
- Fan' cooler coil is dry. $eDo
. ou O
h m a , q m a j w w
- u. 129 W l , e i 2 &
o a i' o o v
.i 1; .
j.
. _ . . . _ . _ _ . _ _ _ _. __ _ _ _ _____ _ _-_____ _______ ~ ___
Calc. No. 3C7-1184-001 REVIEW METHOD SHEET
- Revision 0
- Page - 21 (FINAL. PAGE)
Proj.No. 6695-80 This calculation i.ts been reviewed by ine according to the method (s) chee'ked below.
. ' . Computer Aided Calculations Review to ootermine that the computer program (s) has been voltosted and oocumented. is suttante to tne prooles oeing analynea, ano that tne caleviation contains oli necessary l Information for reconstruction at a later oste.
O Revtew to ootermine that the input oats as specified f or program esecution is consist- l ent with the oesign input. correctly oef tnes the proolem f or the comouter algortthm and is sufficiently accurate to produce results within any numerical limitations of the program. c Review to verify that the results octatnea f rom the program are correct anc within stated assumptions and Itaitations of the program ano are consistent with the input. a Review valtoatton cocumentation for temporary changes to lasted, or oevelopmental, or untoue single application programs, to assure that motheos used sceoustely valioste the program for the intenced application.
- Review of cooe input only. since the computer program has sufficient history of use at sargent & Luncy in similar calculations. .
f Review sestnmetic necessary to pr. pare coo, input osta. 9 other:
- 2. Hand Prepared Design Calculationo aX oetsii.a r.vi.. of sne originsi calcaistions.
o Review ey an alternate, simplifiea. or appro imate metnoa of caicuistion, e Review of a representative sample of repetitive calculations. - O Review of the calculotton against a stattar calculation previously performed.
- 3. Revisions a tat torial enanges only.
b tiimination of unapprovea input cats witnout altering calculated results, c Other:
- 4. Other
**~
hhhg g **~ hal8l@$~ VAM* F ORM. REVIEW
- 1 0 /19/05
(
, - _ . . ~ - . _ _ _ ._ , , - , - . - . .. .. - .-
I
,e * ,
Calc."No. 3C7-1134-001 Revision: O O Page: Al Project No. 6695-80
- 1 Prepared by '
M N Date #!*
, Reviewed by lL)) L*Lo T C Date Ald2/85~ ,
Date # f M /, / f / f Approved by M Q. ler v v .
)
i APPENDIX A jjAND CALCUI.ATIONS O . I l r 1 (. I O
_ . _ - . . . - - . _ . . . _- .- _ - .-_ _ _ . .. ~.... ._ - - ~ . - . . . - . _ . - C.ien For Ceit. No. #$ $ l' iib 5 *00l WSEMUNDY < ,,, c) o,, , seenweepene. , , , c-=-- so ..,_ n.. I N...s .... n *, e- ., O t ci i h .e by c.a _ Rwiewed by D.te hopect A m . M by Dew h.). No, h O 'f8*[ 3 f quip. No. , g. i MJ.s. o ' e. n . q J s.c
't w r r.<. ,.,. <a.Gr, t /3 0 c$
% D....;. : .'.aG
/5
! [',yte [ #
M )* l R v:n P n Ram la 6 C. A27 RCic (%.; Rxx-I Pf w k E 4 . Y Di 94 I n [ . . . . , _ . . _ . - , , _ . _ . _ - , , . _ . . - . _ . _ . . - - _ _ , . . . _ , . _ _ , . . ~ . , , - , , - - . ~ , - . - _ - - , - . _ . . . . _ _ , . . __
ceia For c.ic.N..IC7~//l#'#;'/ '
,, ,,. O o, SARRENTkLUNDY ,
EAcSo sesmy-n ei.e wen-a. icy-nwi.e P s /1 4 et ci n , 6, _ o. nw e by 0.te Pr.,.ct r,.i. n.. W/5 -l' O r.u, n.. A,,r e 6, om RHR. f u % (G
^
G,' /2 I All u.h, ,, , V,,, / e lnd sit (t/w r.
^) S G,$ c or s n ,
f = n s (s.g , 1 ' scr F
=7 .)g # ll9+ ; . Vj :. .o t c'. 4 - > G ' N . 3 e, u, ~ .<. a..- -
f
- ilo;n. , t: M4 F
.4 b l5. 7 ' ! 5.C
~7 3
ff
?>)
& ,.:. W. .
k n 21re ,< be 'e 7 ,. ' :5775) l: i 47'o b .' t L .' ? / ,: !<
.s 44 l 33.9 G. :
- J 3 5()
Ll, '. f
' A' ) en. CN D.f
) /: :t Q: t[000 c -{,,-
8 8 lWct'(~ t Q / E O <,<j , b tw; c to J w ./ tso,s
, xy d,) <
it
. z.
.- ; jf. : ..,
.Qs 4h c a c-:
t ii, = ys , f 52 : w .. a i s; : i,s . : ' .2 v .- T,
_ _ _ ~ _ _ _ _ _ . . . . _ . _ _ - . ._ I
~ C.lcs For c.\e. uo. 3C 7- IV4 ~00l SARGENThLUNDY n.v. o o.. .
c"c^= s.v.iv-n.wi.e Non_s.i.iv.n.i.i.e P / 7 or 7 Cient Pr.p.t.d by , D.t. R. vow.d by Date Propoet, Pro). No. bbf6~[O E quip. No. Approv.d by D.te RHlt 5 tus Lnle (5y ) Py 1% A ) Sa m m ; b)' 15 0 , lDc.,' J D f:; A 4 */20,=2 to ' 120.5 * k 'c lol.0 79 7 ; IbYg i 7o :
+ 4
%. = 7: . 6 ro,'i.,
- A;= +5.5, ra,co oit, V,
- .. 1).
mi 4 boo /v, : 46 00/t+4 * ?tf.4
& m2
- 18000,lV;
- Il000ltb.7b ' 1073.8 D%) = 150 f ;
- 1243.3 o 4 + '% N u
,9 7 ) {l, l19.3 ~100) = f$,0b
= -
l20 40
=V v)2 = 0.0b3 f f It 2 = l12 )
N D niS
- m, + mu s 3I9$ '1073.E
- llf5.z WA.+n1Jw ? 17 9 (+3 5)
- 1073.t(17.04) --
22,w p
.f) ,
n i <" s /3 13.2-
.a
,3- , m, 0, r nu vh . 31f.+ (0.ca) - to7u 'o stny; . gog3 g
;O M> /3l ;-
E nu (Q- 4, j - y E s, e l 313. 2-(tw.40 - 25.n) - +71b = 4. 37b ' 'O,
,u ' ny (% - e,) A u = 1373 2 (0.0717- o.c;; 45) it V
= 4,3 7+ x r o' 13 U g, .
Y)' ' ~ hvi , ,o o - o. o f, (; , e ne m3(%-e,) { 4.1r y u _ - - ,
ce,e. ua. BC l-1184 '%l' Celes. For SARGENThLUNDY
- am 0 o.= ._
~
Non-Safety-Related of
"$Yc. Selety-Related Pete Y
Cient ' Reywwed by. Deu hek " Apar*
- 6v Pro). No. 66 f5-80 e..ip. No. -
RH R P , R A > S"" i #"" * ' " J') 7 sk = 0. 9 (by - thi )
=
o.7( n13 - too)
=
17.4 g - y, (v4 - vA) x o. f
=
9 l073. 8 (o.o717 - 0.0b'11)
=
IS,[7 IVu x hh i = 2.0 em
. O! ?
d __
!w 8
E V
l c us vor ~ ^ - c.a. uo. X 7- ll84 *MI SARGENT%LUNDY . . ,,, O o,,, c ' "c - = s.i.i,- n.wi.d non-s.t.ty-n.wi.e P Af or g i o. ci.ni Pr. ,.e by R.vi.w.d by D te Proj.ct P'oj. No. bbf8"80 E quip. No. Approv.d by 0.te RH(Q (' Re., A i lum.~<3 S.Ga.c l u !< ('z sgr > P~.r D: tw ist, t . t u s ~ t y~ as.s, 4 +w 6s _,_. - u4 0. 3 9622, vg
- 26.71
_C i;6 ' 95*, f
- 502, O Ai
- 455^i S'j 'l 0 ti, t/, = i+. 4 m,=44oo/v,~=< boo /w4: B /93 _
l8 m, = i200o,/ v[ f IPoss/=6.7 / 7 f 73. 7 ms: I5'O ( 7.48 /bS3= l2 43. 3 0 .A t = d4 ^ $ a(to-ts,;) g
. m.is ' ;,'} co(iu.s- ico) = s77.e i l: w :0, : '.30032 ' ( Q= j;c) +
d b #j
- M1 j " nk = 3 /f k # hf 3. ,# : f f 3,3 M , , ,v, L
- = ai u (4s.s> ,s7: tcarzet) = 2 70.s i n J. 3 m, 19;..s-m, w, + m, s ~. 3 i? ' (o. oir ) 473.9 (0. 3co n) " ,,
NA
~
8 Uh
- m, 7y. 3 U
g
- M y 'J *j '"" f g
= 9p. 2 (+18.u - 8o.2 i,) - +7 7f : 2 2 zoi4 p, m, (s - m p 4 - 113.3(c.nbe 0.zoysayom 22/474 O 9: = p.y.< y ...o . v. m A
n m, % - a.,) l.kh = ae.I y
c.ia r., cei,. no'30 7- / //f.03/ SARGENThLUNDY Rev. O Date . owneenene. Pege A / O of
""*** Solety-Related Non-Safety-Related Propered by oste cient Revowed by Date hopet Proi. No. hhf$~[O Equip No. Approved bV Dete_
RHR Pny Rom A &~ .a i . snw us. 8 (a s -, .) v i i a
& = 0. f i f - L,; }
=
- o. 9 16 5. 5 - i co )
59 h2 g 60 9 D1c= - k]z ) X 0. f l
=
6731 (0. 3ff & a 3 co3:.)x o. f Q Y 58 2 lb,L. x ez 7O GO.y pn1
\ . +
e4 9 8 a 8 . E h O
Celcs. For Cele. No.E 7* ' b ' # '#! 8ARGENTELUNDY >* ,,, O o,,, , 1
..es es '
C " 'C ^ " - Cafety-Related Non-Sofety-Related Pese A // of I operse by Date Cient Reviewed by Date Propect Dete Prol. No. 6675-8') revie. No. A,oreved by i I,,.../ be le
/ .
j), : ll 0. _4f U!. .
$.g' ES
- l f ? :5. 7 r (7 = s c,7 0, ' 'I$l7(5a A ,e : 160. I , Lgg,,
- f 70. 3 , J 7, , ' II 50. 4-f t
0 4. ; = A 2. 3/57 180.l+X(9775)
>'* C 14 f an,n1 'h M v,' & <
~: . . . -
i 1 r
': )
a 7rm AuA 3 ha /< i ,
,- .c -
i
= .
~ 'i, g ?,F" 7.+tx iv? (
n o e ~r ma a ' jn.Li r ew ny X (g...-) Q ' 746 x Qf-) , E;/=
'1 ms L .
($' '
-nv
Celes. For Cele. No. [07' //[4
- U /
SARGENTfaLUNDY . n,, O o,,, e..e se. . C " 'C ^
- Selety-Related Non-Sofety-Related Page//2 et Propered by Date Cient Revoured by Date Preject Pro). No. 66/5 1 E,ui,. No. Approved by Date RHR P~7 R~~ A >
%g WrZr Ln k (5y )
Paz e) % 121. 5, %' 37.r.* -in ' 7e ,4 ' Sv ? tdf* 0.o ? f zo , V4 ' 15.f 5 D t ti. ' f5, i m , =64,6 00jv; * = 50 E' If.h4 * ),
- 4 I 5, id,
- C. 018 9m z e
// 65. D ma= : /8000/(v'96:/742)'/2#l ISO l
>h c e < + a), . -
% ic - i;'
t< - it Q l 3 ,9,73 z,.t , Q-, ,.. =. .G ' .. , 7 ~ .' ) tz = Q - E (C 4 - tm ) = 121.5 - 0. 70( lb' b- tm
= / O 2.15 }
{ LOU tD+ = 0. 03420 i .A,= 0.2403 (e t % ( io(, o. c 4
~
') 4 5' te )
k ' O. : 4 03 ( !O2. :=)t (0.034d)(s o b o.5 + 0.4 5 x !O2.
= ~
62.37 s Q h1 9= m, + m z = }$84. 5 Q ,
- fo .
=
n,1, - m L Df + (m - tilt '6 2 n ) - 3 8. : e
* 'y'3 n ,. I+E4 5 ' & w >J . + n a uJ u
- t ? a (0.012 ) ' trb: ; 0 034 2u)
= =
U)? . n., l. e-
, 0. 0 3 072.
L., C * '"!{b4~A 3 ~"3 j 3
=
IStd. 5 (67.21 - St : :-) - 7.?E 3 = 5,7s / 10 s . ,, .7 o, .4 r O ff,e
- WS 4
- U5 .] L. ' lI!h. I 0 ~ I ? O ~ D O.YO~/L ll50!
= 5 ff .< y
,;f] : f
- fs**;-- , .9 p - O, p 5
,s ,
. . . . . - - . - .. .. - . ~ . _ . . . _ . . . . ._ . . . - . . _ . . . - . . - . - . . _ . . . _ . . . . -
Celes. For Calc.No. 3C 7*//M'# #l N S E ILUNDT 2 .e
,,. r ; o,,, ,
l messensasses. t*- C*C^* -
- e'ety-Related ll Non-Sofety. Related Page / 3 of l Propered by Date -
Cient Revened by Date ' Pree - Approved by Date Pro!. No. b b f 6*'8 U E quip. No. lY (( H Wis, 0 b) Su hn <>K l WEf DO {Sy ] u t= ny fub- %)(y (lt }- 4. V ~y (m ),)asta ' E fi>,7)~ l t - % ) Cp , = o,210 3 r o.4 c w z :
- 0. 2 c 4 Otb5 s ta ' o, p ,,g)(0.:cs) x (121,5 - I 00) = 4, b
/nc O
, 4 4 -. 11 - / 2/. 5- /o2./r = / f,.4 O w 3
~
- N 8
e E-h C
Cale No, ?C]~ HN' % $ SARGENTkLUNDY Celes. For
* ,,, o o,,, ,
.. .se .
Page A / 4 of C " 'C ^ #* Safety-Related Non-Safety-Related . {~}
%J Cient Prepared by Date _ . ,
Reviewed by Date Project Approved by Date _ _ _ E quip. No. Pro). No. bhf 6 ~[O RRR %,7 R u A
%C4/ Z~([leLw,.72 .
(begcWG.) .
% G.,.t Dan Na 28svJ+0+s93
(
% = 17? 3 0 x o. of n - tbf7
%i' 1%yr - [6 I 7/24 2) =
l2'l o.2 5 Q~ O C =
/
V p Gnc,,),a
% )<
Iso- to 94 "
?
S~ [n'G b )~ [sta )) ( %150 ., --105 t o,, , )O"?O h 5 E 1 (
C.lcs. F.t - C.lc. N.. /' iib *2N SARGENTkLUNDY
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SARGENTkLUNDY Rev - Dem , eeemassemens Pe A > f or c -c ^ = s.iety_nei.i.d Non-s.iety-nei.ied. Ov Cient Propered by D.te Reviewed by Date Project Proj. No. bd f["N Equip. No. Approved by Date
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l69 :: 0 C I C NSLD
,. Cole. No. 3C7-1184-001 Date: May 7, 1986 <*
Revision: 1 Page 1 O SAFETY RELATED: Yes
~
Prepared by k 4M d Date l Preparod by M / _ f Date I"O'OS f Reviewed by e , el Date 8'~ {~ Approved by [. ,1. _..
~
__ Date ///A+ 7,/984 r 7 ECCS ROOM LEAK DETECTION SETPOINTS O b t Commonwealth Edison Company LaSalle - Units 1 & 2 Project No. 6695-80 Project File No. 6695-80 l-0 WIN-0340
, . ,,w., y -,.-.wy ..y-r _ . - . - ~ _ , - ~ . ,r,,w eg-v 7
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