ML17304A771
| ML17304A771 | |
| Person / Time | |
|---|---|
| Site: | Palo Verde  |
| Issue date: | 04/04/1988 |
| From: | Riley H BECHTEL GROUP, INC. |
| To: | |
| Shared Package | |
| ML17304A744 | List: |
| References | |
| 13-MC-HA-A05, 13-MC-HA-A05-R00, 13-MC-HA-A5, 13-MC-HA-A5-R, NUDOCS 8811230032 | |
| Download: ML17304A771 (157) | |
Text
~ ~
~
~ ~ t I
II
SJ1Cvpg
. ACj, /OQ 4
~ et g A J g ~fcv oE-AA
~J'Cur f'c V 4+$
la p
p PC4 g gpss~
gee
~~'" gs<p
~~'~
( g gCv
~@vs ~C C-
~ay C~
l<
~C~) ci IC J
( l-u) ~ g O'(~y al
> ~C ~ ) Ci-~)
7
%c
I I
(,. ~
J II I
C.b-c,~
l,p fcv 3
h/7 lg ~/J e M U
1
'I I It fG.a c....Q...+.
~.-K.--Q T'.
go
~
~
K 0
t i'
)
"t>
J II
.. w $ ~~ /.. ~o ~ ~
t q
r Q..-...~, c.as
.z.~ s 7S l~7 4>
gA
.-5cv.-=.--r v~e.o. z.q..
1 a.z~ 4 I -J7. r. a. f..t..D 1
)
'I
.. l'c>g
<to
.......,zg
- I <1-t >
El dV'.. P f- <~~
I
. Q~l<,iZpJ~~ 6(ZZ/gP
'I l
ANPP CALCULATION CHANGE NOTICE (CCN)
CALCULATION NO.
/8-Ac-MAGE REV.
CLASS AFFECTED SllEET NO(S CALCULATION TITLE
/~szznlc
~8w/. CfdBY N~
C, 5. Qng~ ~~
PAGE J
OF CCN NO.
CCN ISSUE DATE
~-El-SB AFFECTED PLANT CllANGES REFERENCE(S)
.UNITS AFFECTED I
UNIT 1 Kj UNIT 2 UNIT 3 Q
COilllON 0~
pic
- sea, DESCRIPTION OF CHANGE REASON FOR CBANGE Qygg7 g av'LuduK 5%%d'EdF k2/$ - lo a4
+km PS PW Azj&dn~.
>4'///$
7n~~~~l,ed- ~gyZy ~ aZ4clg ~,dg ccrc ORIGIN R
CD iZi4&sI/V CliECKER s/z7 yy v g.ld.R+
s z-g QA 8/A RS
I
~
Q
~ I
~ '
~
~
I'
~
II&&
KZK%
0
~
0 ~
0 0 0 0 0 I
0 0
0 000 0
~
0 0
~
0
~
0 0 ~
~
0
~
~ 0 0 0 0 0
~
0-
~
~
~
J
~
0
,Ij b
)I
P'AEL 0
~
I
~
0 ~
I I
~
~
0 0
0 ~
~ ~
~ ~
~
~ ~
~ ~
~
~ ~
0
~
0 0
~-
0
~-
0 0 0
INTERNALCONTROL NO.
l9'~ ol-N3 -cALC=eo3 CALCVLATIONCOVER SHEET SHET 1
PROJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM SUBJECT 18601 183 CALC. NO 13-MC-M-A05 FILE NO.
PROJECT QUAUTY CLASS DISCIPLINE D 0 0 C OOU ol O 0 g anal Q I c
~ C 0
D 0
~ C l5Cl 40 0 C0 tO a0 0 O Ia ns 0 cn ce D 0 I
C z ao 0 a
~
CO n)
Ol C) tD O P U 0
~ cn
~
COgl 0 0 KC m nl C O 0rngc aO0 W(Q N yj 0C C0 gg Q1 O OC ClO OU l
~
COMPUTER PROGRAM SCP YES NO PROGRAM NO. (S)
ME 204 VERSION/RELEASE NO.
,A1 RECORD OF ISSUES NO.
PESCRIPTlON TOTAI.
NO. OF SHEETS LEST SHEET GS CHtKP PATE 0
ORIGINAL ISSUE
-Ql-GG INFORMATION ENTERED IN THIS SPACE:
~
SHOw PROFESSIONAL ~ER STAMP F RECKAREp
~
ENTER REFERENCE TO ELUSION OF CHECKER'S ALTERNATE CAl.ClJ4kTlONS. F USED.
~
PROVCE ANY NOTES TO ASSIST CHECKlVG Ah APPROVAl
CALCULATIONSHEET 18601-183 PROJECT JOB NO.
SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS Pi&P ROON AL NO 13-hic-HA-A05 SHEET NO.
REV ORIGINATOR DATE t'~~/C g-Z7-8 CHECKER DATE
$-Zf.hF REV ORIGIN ATOR DATE CHECKER DATE I Q
)OI-4IE <
0: 0 Table of Contents 4 I.'I.
III.
IV.
V.
9 VI.
10 12 13 6 VII
'7 IS 19 20 21 22 23 24 25 26 27 28 29 30 31 Purpose Design Criteria Study Assumptions References Summary of Results Room Heat-Up Computer Model A.
Model Description B.
Required Input C.
Assumptions D.
Limitations E.
Output S tudy A.
Case A: Pump room with no HVAC and room door closed 1.
Heat Loads a.
Electric Motors Heat Loads b.
Lighting Heat Loads c.
Piping Heat Loads d.
Heat Dissipated by the CS Pump e.
Total Heat Loads 2.
CS Pump Room Surface Area
& Volume 3.
Input Data 4.
Results B.
Case B: With no HVAC and room door open 1.
Air Flow Due to Temperature Difference 2.
Heat Loads 3.
Input Data 4.
Results Pacae 6
13 15 18 19 19 19 20 22 23 33 34 35 42 43 46 47 47 34 35 36
I
PROJECT CALCULATIONSHEET 18601-183 13-MC-HA-A05 S-cV.PP REV ORIGINATOR TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM DATE SHEET NO.
CHECKER DATE L
. iQ
> O-
I4et C
U 10 12 13 C.
Case C: Verification of Average Room Temperature 1.
Air Flow due to Temperature Difference 2.
Heat Loads 3.
Input Data 4.
Results D.
==
Conclusions:==
No HVAC and Room Door Open.
VIII. Figures:
1.
Classification of Heat Loads 2.
CS Pump Room with no HVAC and Room Door Open 48 49 49 52 53 54 IX.
Appendices:
1.
Computer Runs For:
16 18 19 20 21 22 23 B.
C.
CS Pump Room with no HVAC CS Pump Room with no HVAC and Door Open CS Pump Room with no HVAC and Door Open (Alternate Run for verification of average room temperature for Case B) 55 61 67 25 26 27 28 29 30 3l
fl l
PROJECT CALCULATlONSH EET 18601-183 0
ORIGINATOR OR I G I N ATOR S-Zg-g SUBJECT TRANSIENT TL~PERATURE STUDY FOR CS PUMP RQQM t
REV DATE CHECKER DATE REV 0
DATE CHECKER DATE
.IQ
) OI-I4 c(
Z Q NO 13-MC-HA-A05 SHEET NO.
I 2 I.
PURPOSE The design basis for cooling the Containment Spray (CS) and Low Pressure Safety Injection (LPSI) pumps equipment
- rooms, when the pumps are in service, uses Essential Air Cooling Units (ACU) and the Essential Chilled Water System (ECWS) for cooling.
In the event that either the ACU or ECWS fails when the pump runs, the room temperature will rise rapidly.
10 12 13 14 The purpose of this study is to determine the transient air temperature for 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> in the CS/LPSI pump rooms (limiting case) for the following two cases.
The CS pump was selected as the limiting case.
The details for this selection are explained under Assumption 24.
17 10 19 20 21 22 23 7.4 25 26 27 28 30 31 A)
Fluid temperature in the pipes of 225 F with no HVAC B) 'Fluid temperature in the pipes of 225 F with no HVAC and the room door open.
Standard room heat-up (RMHTUP) computer program, ME204, Rev. Al is used to study the room ambient air heat-up by the equipment and other heat loads in the CS pump room.
The heat generated in the room is transferred to the room air, stored in the room enclosure concrete (heat sink) and transferred to the air outside the room.
The transient temperature for the CS room air is studied for a time period of 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> without any HVAC.
In addition, the transient temperature is studied when there is no HVAC and the pump room door is open
~
35 36 I AO 5998.1 7I55
PROJECT CALCULATIONSH EET 18 601-183 ALC NO 13-MC-A-A05 REV ORIGINATOR DATE CHECKER DATE PHs REV ORIGINATOR TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM DATE SHEET NO.
CHECKER DATE
. I O
>nl-hl z 4 L
0 DESIGN CRITERIA:
8 This is a study of the effect of certain equipment failures which are, strictly speaking, beyond the specific design basis for the affected systems.
The results will be used as input to a probabalistic risk assessment evaluation done by others.
'I 0 12 13 14 I
The systems involved in this study are the Safety Injection (CS subsystem),
Auxiliary Building HVAC (Normal and Essential),
and Essential Chilled Water.
Their design criteria are references 21, 22, and 23.
17 18 I9 20 35 LAO 9998.I 7/8$
4
CALCULATIONSHEET PROJECT JOB NO.
18601-183 TRANSIENT T~ERATURE STUDY FOR CS PUMP ROOM REV 3-~HE LC NO 13-MC-HA-A05
~
~
SHEET NO.
, IQ
>o+
lal2 c C
V III'TUDY ASSUMPTIONS2 Fluid temperature for the CS system in the CS pump room is 225 F.
During post-Loca conditions, the maximum containment sump temperature is 225 F as shown in reference 19, figure 6.2.1-24.
$ 2 2.
The initial temperature inside the CS room is 75 F.
This is based on the assumption that normal HVAC is available before the time period of this study.
Temperature of 75 F
is the typical normal temperature in the auxiliary building and is based on the operating experience.
l7 18 19 2i 22 25 26 27 2$
29 50 3.
The initial temperature outside the CS room is 75 F.
This is based on the assumption that normal HVAC is available before the time period of this study.
The initial temperature of 75 F is the typical normal temperature in 0
the auxiliary building and is based on the operating experience.
4.
Essential or normal HVAC is not available during time period of this study.
This is the principle failure assumed at the onset of this study as discussed in section I ~
5.
Initially, steady state temperature conditions exist in the CS pump room and outside the pump room.
LAO )II~,I I II
CALCULATlONSHEET 18 601-183 PROJECT JOB NO.
TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC NO 13-MC-HA-A05 REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE SHEET NO.
CHECKER DATE L'Q
)Dl-hl z <
L 0
10 6.
The room is simplified as an enclosed space bounded by the same thickness of walls, ceiling and floor.
All of the room walls actually are 2'-9" each.
In case of floor, no credit is taken for the thickness being more than the wall thickness of 2'-9".
Due to the low heat load generated in 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> compared to the capacity of the existing walls to absorb the heat, the additional floor thickness will not make any difference to the room ambient air temperature.
12 13 7.
The walls, ceiling and floor are used as a heat sink.
For details, refer to Section VI.C of this study.
16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 3l 8.
The heat generated within the room is considered as being constant.
This is due to the fact that more than 85% of the heat load, as shown in figure 1, is from the electric motors.
For details refer to Sections VI.D and VII.A.l.e of this study.
9.
Temperature at the inner surface of the insulation is equal to the temperature of the fluid in the pipe.
This assumes that the temperature of the outside pipe surface is the same as the fluid temperature.
It also assumes that the temperature drop across the very small air gap between the pipe and the inside surface of the insulation is zero.
This provides a conservative estimate of the piping heat load for this study.
- 10. For calculation of heat dissipated by the pump, the pump is modeled as a flat surface.
This will provide a
conservative estimate compared to a cylindrical surface.
35 36 LAO 1S98,1
>/85
PROJECT CALCULATIONSHEET 18 601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC NO 13-MC-A-A05 SHEET NO.
o I
ATOR DATE CHECKER DATE REV ORIGINATOR 9'-ZS-5 DATE CHECKER DATE 10 12 13 11.
When a wall is shared by two rooms, which may be heated at the same time, half of the wall surface area will be considered as a heat transmission pathway for each room.
This 'will provide half of the wall as a heat sink for each room.
Each CS pump room shares a common wall with a HPSI pump room and with a LPSI pump room.
The operating CS pump can be from a different train than the operating HPSI and/or LPSI pump so that the operating pump rooms may not be adjacent to each other.
This study uses a worst case scenario and assumes two common walls.
17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 12.
The dimensions of the CS pump rooms A and B for all three units are essentially identical.
In addition, the electric motors and pumps, equipment, lighting and piping sizes and lengths are virtually the same for all of these room.
This study is performe'd for CS pump room A for Unit 1 and is applicable to CS room A and B for all three units.
13.
The shield wall in,the pump room is considered a heat sink.
The shield wall is converted to an equivalent wall having same thickness as the room walls.
In doing this, the equivalent surface area on one side of this wall is modelled as a heat transmission pathway to adjacent spaces.
The shield wall surface area and volume are approximately 4% and 2.7S respectively of the pump room surface area and volume.
The small percentage surface area and volume of the shield will provide reasonably acceptable results.
35 36 I AO 9990.1 7/SS
PROJECT CALCULATIONSHEET JOB NO.
18601-183 TRAhSIENT TEHPERATURE STUDY FOR CS PIMP ROON 13-afC-HA-A05 SHEET NO.
REV O R IG IN ATO R OATE 3-2'HECKER DATE REV Cy. 0/ P1
-Zses ORIGINATOR OATE CHECKER OATE
. 1Q
)OI-wz IJ 8
IO As can be seen from the results in Appendixes A and B, very little heat is transmitted through the walls; most is stored in it.
This approach reasonably accounts for the shield wall mass, but slightly under estimates the rate at which heat is transferred into the shield wall because only one surface is assumed available for heat transfer.
Because the surface area and volume of the shield are a
small percentage of the total, this will provide reasonably acceptable results.
- 14. For the case when the room door is open, half of the room opening is assumed for air flow into the room and the other half is assumed for the air flow out of the room.
ASHRAE Ref.
1, Chapter 19, Page 334, indicated that if there is only one opening, or if one opening is extremely large relative to the others, the neutral zone (where there is no pre'ssure difference between inside an outside) will be at or near the center of the opening.
This reference supports the above assumption In addition 50< effectiveness of the opening (normal value 508 to 60<) for air flow is used.
For details, refer to section VII.B.1 15.
Per assumption 4 above, the essential HVAC is not available during time period of this study.
For a conservative
- approach, ACU fan will be assumed running, without chilled water through the essential coils.
The heat load due to this motor is minor as compared to the heat load from the CS pump motor.
81% efficiency of the ACU fan motor is assumed for calculation of room heat load.
This is a typical motor efficiency for 3 hp motors as shown in reference 1, chapter 22, table 30, page 417.
35 36 I AO 3999,1 I 55
REV ORIGINATOR DATE 3-V-8 CHECKER DATE REV ORIGINATOR C
CALCULATIONSH EET PROJECT JOB NO.
18601-183 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS P~~
RPPM DATE CALC. NO 13-MC-HA-A05 SHEET NO. 10 DATE CHECKER
,tQ O'O I-WL'I
- 16. Moving air is assumed in the room due to ACU fan rather than normal still air.
A conservative value of the surface resistance of 0.25, based on the assumed value of air velocity of 7 1/2 mph, is used.
(See Reference 1, chapter 20, table 1, page 357) 10 12 13 17.
The lighting load in the CS pump room is assumed to be 2
Watts/FT This is a typical lighting load for industrial 2
buildings as shown in the national electrical code 1987
- handbook, reference 7.
18 I9
- 18. This study is performed for a time period of 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />.
The computer model can provide details for a maximum of 720 steps (Refer Section VI.D).
Therefore, each step or time increment is 2 minutes.
20 21 22 23 24 25 26 27 28 29 30 31 19.
The room walls are required to be divided into a number of layers for computation of temperature distribution in the concrete walls by the computer model.
The required input for the thickness of the first layer and the multiplication'actor for thickness of other layers are selected as 0.01 ft,; (approx. 1/8") and 1.41 respectively.
For details, see sections VI.A and B.
35 36 LAO 3999.l 1/99
PROJECT CALCULATIONSHEET 18 601-183 CALC NO 13-MC-HA-A05 SUBJECy TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM SHEET NO.
REV ORIGINATOR Pr5e,g, DATE REV ORIGINATOR DATE Hue CHECKER R
,tQ
>OI-wz~
E II
- 20. For calculation of air flow due to temperature difference c
for the case of an open door, the room average temperature 0
is assumed to be 140 F.
For support of this average temperature, see Section VII.C, verification of average room temperature.
'I 0 12 13 16 17
- 21. For calculation of air flow due to temperature difference for the case of open room door, the average temperature outside the room is assumed to be 90 F. It assumes that 0
doors in the corridor will be opened for enough air mixing to have the average temperature of 90 F.
This approximates an average temperature after the door has been open for a while.
Note:
The initial temperature was 75 F.
(Assumptions 2 and 3) 19 20 21 22 23 24 25 26 27 28 29
- 22. Concrete has the following properties:
A.
Density 144 lbs/ft (Ref 6)
B.
Thermal conductivity 0.54 (Ref 6)
C.
Specific heat 0.2 btu/lb-F (Ref 6) 3l LAO 'ISO' 7 "A'
I
PROJECT CALCULATIONSH EET 18601-183 JOB NO.
CALC. NO.
3-MC-HA-A05 BJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
, IO O'O I-wzc I2 0
23.
The net pump room volume is required as input to the computer model.
For calculation of net room volume, the volume of the HVAC equipment in the HPSI pump room is insignificant and is neglected.
IO l2 I3 24.
As shown in section I, this study is to be performed for the limiting case for the CS pump room or LPSI pump room.
The pump motors for these two systems have the same nameplate ratings, but the operating BHP is higher for the CS pump than the LPSI pump.
I7 I8 I9 20 2I 22 23 26 27 28 29 30 31 Reviewing references 9,
10, and 20, there are insignificant, minor differences among the pipe layouts of these systems.
The lighting heat loads are practically the same.
CS pump room has a smaller area (20'-6" X 18'-0")
than the LPSI pump room area (22'-3" X 18'-0").
The height is the same for these rooms.
From the layout of the pump rooms (see page 38),
each CS pump room shares two walls, one with the HPSI pump room and the other with the LPSI pump room.
In the case of LPSI pump room, there is only one common wall with the CS.
Per assumption ll, the CS room has lower heat transmission surface area and lower heat sink volume compared to the LPSI pump room.
Prom above, it is concluded that CS pump room is the limiting case and this study will be performed for the CS pump room.
I AO 399dr1 7/9$
PROJECT CALCULATIONSHEET 18 601-183 13-MC-HA-A05 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM SHEET NO.
RIGINATOR DATE 3->84d'HECKER DATE REV ORIGINATOR DATE CHECKER DATE
, IO
>OI-wzcU IV.
REFERENCES:
1.
ASHRAE Handbook of Fundamentals, 1972.
2.
Technical specification for thermal insulation 10 12 13 16 17
'I 8
'I 9 20 21 3.
4 ~
5.
6.
7.
8.
materials and the application to piping and equipment, specif ication number 13-MM-301, Rev.
2.
Line designation list, 13-P-ZZG-014, Rev.
29.
Auxiliary building essential cooling system heat load calculation, calculation number 13-MC-HA-051, Rev.
1.
P
& I diagram, safety injection and shutdown cooling
- system, drawing number 13-M-SIP-001, Rev.
19.
Principles of heat transfer, third edition, Frank Kreith, Intext Educational Publishers.
table A-2, Physical Properties of Some Nonmetals, page 635.
The National Electrical Code 1987 Handbook, fourth edition, General Lighting Loads by Occupancies, table 220-3 (b), page 100.
NAVCO Piping "Datalog", National Valve and 22 23 24 25 26 27 29 30 31 35 Manufac turing Company, Pittsburg, PA. Edition No. 10.
9.
Auxiliary building isometric, drawing number 13-P-SIF-201, Rev. 21.
- 10. Auxiliary building isometric, drawing number 13-P-SIF-203 Rev 23.
- 11. Auxiliary building plan at elevation 40'-0", drawing number 13-C-ZAS-110, Rev 16.
- 12. Auxiliary building plan at elevation 40'-0", drawing number 13-C-ZAS-112 Rev 4.
- 13. Auxiliary building plan at elevation 51'-6", drawing number 13-C-ZAS-116 Rev 17.
- 14. General Arrangement, Containment Spray
- Pump, N001-11.01-36-6 36 LAO-9999 1 1l9$
I
PROJECT CALCULATIONSHEET 18601-183 JOB NO.
13-MC-HA-A05 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PEP ROOM SHEET NO.
REV ORIGINATOR PEA/C'ATE 3-af 4i CHECKER C,g. N DATE REV ORIGINATOR DATE CHECKER DATE
.IQ
) OI-MEg I2 0
10 12 13 17 I8
'I 9 20 21 22 23 24 25
- 15. Ingersoll-Rand Pump Manual, log N001-15.02-11, CS pump data sheet and pump curve.
16.
Pump motor data sheets, log N001-11.05-7-2
- 17. Reliance Electric Co. drawing, log M721A-109-2
- 18. User's and Theoretical Manuals Verification Report, program RMHTUP-Room Heat Up, program number ME204 Rev.
A1, Bechtel Power Corporation, San Francisco Power Division.
- 19. Final Safety, Analysis Report, Palo Verde Nuclear Generating
- Station, Amendment 17.
- 20. Auxiliary Building Isometric, Drawing Number 13-P-SIF-207, Rev. 22.
21.
De ta iled Des ign Criteria, Part III, Sys tern HA, HVAC-Auxiliary building, Rev.
8.
- 22. Detailed Design Criteria, Part III, System SI, Safety Injection and Shutdown Cooling System, Rev.
5.
- 23. Detailed Design Criteria, Part III, System EC, Essential Chilled Water System, Rev. 3.
- 24. Auxiliary Building Base Mat, Sections and Details, Drawing Numbers 13-C-ZAS-124, Rev.
13.
26 27 29 29 30 31 LAO 3998.1 7/SS
CALCULATIONSHEET 18601-183 PROJECT JOB NO.
TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE CHECKER
~-8989 6 8
/~1 DATE g-ct.P REV ORIGINATOR DATE CHECKER DATE L'IQ
>OI-14 Z 4 0:
0 2
V.
SUMMARY
OF RESULTS:
10 The transient temperature summary for the CS pump room air is shown below.
For case A, the temperature values can be used directly.
For cases B and C, having the door open results in air flow in and out of the room.
As explained in Section VII.D, the average of the results is felt to best estimate the transient temperature profile when the room door is open.
12 No HVAC and Closed Door No HVAC and Open Door 13 16 17 18 19 20 21 22 23 24 25 26 27 28 29 Time Period 0 min 2 min 4 min 12 min 36 min 2 hr 4 hr 6 hr 8 hr 12 hr 24 hr Case A
~Tem F
0
- 92. 13 102.05 114.44 120.75 124.31 130.68 139.56 146.34 152.05 161.62 183.29 84.06 89.49 96.83 100.45 102.36 105.77 110.50 114.10 117.14 122.22 133.68
- 87. 98 95.62 105.53 110.49 113.21 118.07 124.83 129.98 134.32 141.60 158.02 Case B
Case C
~Tem F
~Tem F
0 0
75 75 Avg BGC
~Tem F
75 86.02 92.56 101.18 105.47 107.79 111.92 117.67 122.04 125.73 131.91 145.85 35 36
PROJECT CALCULATIONSHEET 18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET No.
REV ORIGINATOR DATE 3-'7C'I6'HECKER DATE g +rp &
REV ORIGINATOR DATE CHECKER DATE
, IQ 0 Dl-hl z C0 VI.
ROOM HEAT-UP COMPUTER MODEL A.
Model
Description:
(Ref 18)
The room heat-up computer program, RMHTUP, program number ME204, version A1, can be used to study the room ambient air heat-up by the equipment heat or any other heat sources in the room.
10 12 13 The temperature of room ambient air increases with time, due to the heat released from the equipment and other sources.
The heat generated within the room is transferred to the ambient room air, stored in the room enclosure (walls, ceiling, and floor) and transferred to the air outside the room.
17 18 19 20 21 22 23 24 25 26 27 28 29 30 3l The room walls are divided into a number of layers with incremental thicknesses for numerical computation by the computer program.
In this study, the value of imaginary thickness of first layer of concrete wall is selected as 0.01 ft and the multiplication factor of imaginary thickness of other layers is taken as 1.41. In other words, the first concrete layer thickness is 0.01 ft (approx.
1/8"), the second layer thickness is 0.0141 ft (approx.
3/16"), third layer 0.01 X (1.41) ft, etc.
The transient room temperature is determined from the heat balance
- equation, which balances the heat generated within the room and the heat transferred to the ambient room air, stored in the room enclosure and transferred to the outside
- air, as shown below:
36 LAO S99S
~ I llSS
PROJECT C
CALCULATIONSH EET 18601-183 13-MC-HA-A05 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM
->g -Q $,
.pg g-cZ$
SHEET NO.
CHECKER DATE
~ iO
)O1-LLIZ 4 L2 0
QMIALL 0 AMS AIR,.
@OATS(Dr A1q 10 12 13 r
EQU1P
=
AMB AIR +
WALL +
OUTSIDE AIR 16 17 18 20 21 22 WHERE:
QEQUIP
=
Heat generated from equipment or any other source in the room, BTU/HR AMB AIR =
Heat transferred to the room air, BTU/HR 23 25 WALL Heat stored in the room walls, ceiling and floor, BTU/HR 26 27 28 29 30 31 QOUTSIDE AIR = Heat transferred to the outside air, BTU/HR The room ambient temperature and the wall temperature distribution are calculated at fixed time intervals.
In addition, total heat stored in the ambient air and in the concrete walls and heat transferred to the outside air are provided for each time interval.
36 LAO )999l ll89
lj r
CALCULATlONSHEET JEC~
TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM GAL NO SHEET NO.
REV ORIGINATOR PA./L DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
~ 10
) DI-hJ E <
C 0
B.
Input Required for. Computer Model:
The following information is required as input for transient temperature study in the CS pump room:
IO I2 I3 I7 2.
3.
4 ~
6.
7 ~
8.
Initial room ambient temperature, degrees F
Initial outside ambient temperature, degrees F
Equipment and other heat generated in the room, BTU/HR Net room surface area, ft Net room volume, ft Thickness of room enclosure, ft Density of room enclosure material, lbs/ft Thermal conductivity of room enclosure material, BTU/HR-ft-F I8 I9 20 2I 22 23 24 25 26 27 28 29 30 31 9.
Specific heat of room enclosure material, BTU/lb-F 10.
One period of time increment for calculation, min
- 11. Imaginary thickness of first layer of room enclosure, ft
- 12. Multiplication factor of imaginary thickness of other layers 35 l
36 LAO i998.1 71$ S
'l
'l
CALCULATIONSHEET 18 601-183 PROJECT JOB NO.
TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC NO 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE CHECKER DATE g.eI-N REV ORIGINATOR DATE CHECKER DATE R
, IO
>DI-wz<
R 0
C.
Assumptions for the Computer Model 10 12 13 2.
3.
4 ~
The room is simplified as an enclosed space bounded by the same thickness of walls, ceiling, and floors.
The gross room volume is corrected for the volume occupied by piping and equipment.
The gross room surface area of the room enclosure is corrected for the area occupied by equipment.
The enclosure walls, ceiling and floor are taken as a
heat sink.
D.
Computer Model Limitations 16 17 18 1.
The room enclosure walls, ceiling and floor must be considered as having the same thickness and of the homogenous material.
19 21 22 23 2.
3.
The air temperatures outside. the room must be considered as being the same and remaining constant.
The heat generated within the room must be considered as being constant.
No heat generated outside the room can be considered.
24 25 26 27 28 29 4.
The program is limited to 720 time period calculations.
E.
Computer Model Output The following information is provided in the computer model output:
31 35 36 I-+O 9990
~ I 7/IS TAF QAT QST QOT Final room air temperature at each period, F
Heat stored in the ambient air, BTU Total heat stored in the concrete, BTU Heat transferred to the outside air, BTU=
PROJECT CALCULATIONSHEET 18601-183 13-MC-HA-AO5 REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM DATE SHEFT NO.
2 0 DATE CHECKER
, I 0 o
L 0
VII.
STUDY:
This study is performed for the following two cases:
10 A.
B.
Fluid temperature in the CS pipes of 225 F with no HVAC and room door closed.
Fluid temperature in the CS pipes of 225 F with no HVAC and room door open.
12 13 16 17 I8 1 ~
19 20 21 22 CASE A r
FLUID TEMPERATURE IN THE CS PIPES OF 225 F WITH NO HVAC AND ROOM DOOR CLOSED:
Heat Loads:
a.
Electric Motors Heat Load:
This heat load consists of the heat generated by the CS pump motor and ACU fan motor.
23 24 26 27 28 29 30 31
- 3. ~
CS Pump Electrical Motor Heat Load CS Pump design flow
= 3890 gpm (REF 15)
Pump design flow BHP
= 630 hp (REF 15)
Motor efficiency, ~
= 93.4<
(REF 16) 35 36 LAO 9994.1 9/>>
CALCULATIONSHEET 18601-183 PROJECT JOB NO.
TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE IZ
, IO
) OI-4IE 4 C
0 The pump and the motor are'nside the CS pump room.
The fluid is pumped to outside of the room.
10 12 13 Motor heat load
= BHP x 2545 x ~(l-
)
77 (REF 1, note C, table 30, chap 22, page 417) 630 x 2545 x (1
0.934)
BTU/HR 0.934 113,299 BTU/HR ii. ACU Fan Motor Heat Load:
17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 The essential ACU fan may be running without essential chilled water thru the essential cooling coils (See Assumption 15)
ACU nameplate fan hp
=
3 hp (REF 17)
Motor efficiency
= 81<
(See Assumption 15)
The motor and the load are both in the CS room and. the air and all the motor energy stays inside the room (i.e. all the fan motor energy stays inside the room).
34 3S 36 1 AO )995,1 PIB5
t I
I o
PROJECT CALCULATIONSHEET 18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-AO5 SHEET NO.
EV ORIGINATOR DATE CHECKER p Q.p/
DATE g.pg-PP REV ORIGINATOR DATE CHECKER DATE From ref 1, chap 22, table 30, page
- 417, Heat gain from fan motor 10 12 13 3
X 2545 0.81 9,426 BTU/HR Total motor heat load
= 113,299
+ 9,426
= 122,725 BTU/HR V
16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 b.
Lighting Heat Loads:
The heat load is due to the lighting in the CS pump room.
CS pump room area
=
(20 '-6") x (18 '-0")
(Ref 11) 20.5 x 18 FT 369 FT Typical lighting load for industrial buildings
=
2 watts/FT (REF 7)
Room lighting load
=
(Room area, ft
)
X (2 watts/ft
)
X 3.41 BTU/HR-watt 369 X 2 X 3.41 BTU/HR 2517 BTU/HR 35 36 LAO-)S9e,i 7/S5
f
P ROJECT CALCULATIONSHEET JOB NO.
18601-183 NO 1 3 MC HA A05 SUBJFCT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM SHEET NO.
REV ORIGINATOR PSST.i'4 DATE CHECKER DATE 5 N.B REV ORIGINATOR DATE CHECKER DATE
,IQ
)OI-biz<0 IO c.
Piping Heat Load:
When the CS pump is operating, design basis cooling is provided by the essential Air Cooling Unit (ACU).
Essential chilled water is recirculated through the ACU chilled water cooling coils.
In the event that either the essential ACU or the Essential Chilled Water System fails, the pump room temperature will rise rapidly.
12 13 17 18 I9 20 2'I 22 23 24 The CS pump initially supplies cooling water from the refueling water tank.
When that source is used, the CS pump recirculates water from the containment sump to remove decay heat from the core during the time period under study.
In addition, the CS will operate continuously during this time period.
Essentially all CS piping in this room is in use.
Therefore, all the piping is included for calculation of heat loads.
/
26 27 28 29 30 31 LAO 5998il 7I55
I,
CALCULATIONSHEET ANPP 18601-183 PROJECT TRANSIENT TE1'PERATURE STUDY FOR CS PR'P ROON 1 3 HC HA A05 SHEET NO.-
REV ORIGINATOR P>~~- fi 'ATE "r-ZPV CHECKER DATE REV ORIGINATOR DATE g-IPP CHECKER DATE
. I Q
)OI-ZO This heat load is due to the CS pump suction and discharge piping in the CS pump room.
All of the process piping in this room is insulated.
The following equation can be used to calculate the heat flow through insulated piping:
12 13 14 qs
=
to-ta rs loge rs ro
+ Rs 17 (Ref 1, chap 20, eq 11, page 353) 19 20 21 22 23 24 25 26 27 28 29 30 31 Where:
qs t
ta ro
=
k Rs Rate of heat transfer per square foot of outer surface of insulation, BTU per (hour)
(square foot).
Temperature:
inner surface of insulation, degrees F
Temperature of ambient air, degrees F
Outer radius of insulation, inches inner radius of insulation, inches Thermal conductivity of insulation at mean temperature, BTU per (hour)
(square foot)
(of per inch thickness)
Surface resistance, (hour)
(square foot)
(degrees F) per BTU.
34 35 36 LAO 3998.I 7/SS
l I
f~
0 t
~l
CALCULATIONSHEET 18601-183 PROJECT JOB NO.
SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE
-M-8 CHECKER DATE g-o-aV REV ORIGINATOR DATE CHECKER DATE
.IQ 4l z <
12 0
For suction and discharge piping:
Fluid temperature o
= 225 F
(See Assumption 1) t o
Ambient air temperature a
= 75 F
(See Assumption 2)
Surface resistance, Rs= 0.25 (See Assumption 15) 10 Jacket emissivity of the calcium silicate insulation
=
0.85 8 100 Degrees F (Ref 2) 12 13 Mean insulation temp
= 225
+ 75
= 150 F
2 17 18 19 20 21 22 23 24 25 Thermal conductivity of calcium silicate insulation at 0
150 F mean temperature, K =0.40 BTU per (hour)
'(square foot)
(
F temp difference per inch thickness)
(REF 1, table 3B, chapter 20, page 364).
27 29 30 l
36 LAO 3991.I 7/8$
CALCULATIONSHEET ANPP 18 601-183 P ROJECT JOB NO.
(:
TRANSIENT TEMPERATURE STUDY FOR OS PUMP ROOM'ALCNO SHEET NO.
ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
,SO
)Oi-hl z 4 L
0
'PIF'tNe i-/eA7 LOAgs (cow~)
7HE PIPIIN$
HEA7 LOADS
>Cr'>>~>><L I-Y rd<
7 i~<
POJ5(P IZC V'IdJI Pgg/~ (,
7/I C, JISM@>I>lR5'~
j IP>P>sJ'C 10 12 13 54
{
17 58 19 20 21 22 23 24 29 26 27 28 29 30 31 I UIt 1P DOC, TION PIP/I'1 4 7 H~
Put/P
~UC7-IOII/
PIPInfCP
/P/
~/IP g~
Pg~P gOOa1 CaeSIS7 S a 8 VII'OLL@AgIzJi",
Jt/a.
/'
7ALQ09 Ara25
/ iDS'ZA $ 067
I/
t gfE 31 Li>JZ
~IZQ
=
/ I scH 40 ZrJ55LI /j 7/o>t/
7I/I+ (A/C=
= k S' YP<
QF L>Jsii-4/l 7'I ON
= c-4L c. I vs 1
slL, 1+$ 7/""
fggF 3j PtPF O.a, CQGF iSj Z~J5~L L.>'17IOI/
4). I)
=
1P-1 +(2 yP.q)
C.
I>>E Nq I PS3:A t Oog
~
IpscpCOc11 Is I(slT~
I>J 7>dg slZp o/vc sIIoe>t/
>1 r~oui=
6 1"I/c o7HcR sHowa
>3< Lo~ I IP
=IZE
=
/6 SCH Za t Rer-~7
(
32
~>>5<I. L>1<Ini/ 7//iCi;i/~ss fRf/ Q]
/PC 01"
=~S~5,L>17iOAI
= (gL.Cion//./
SILiCA fE 36 LAO 3988.5 7/8$
i
CALCULATIONSHEET ANPP 18601-183 PROJECT RAN I NT RA o
P ROOM CALC. NO.
SHEET NO.
ORIGINATOR fg.g DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE BIO III cC
>ply-Z Q
/'/PC o g
=
/8
<A/Su.L//I 7iO~l 5
~ 3,
=
~8'
(>> ~'<)
10 12 13 14
(
17 18 Foz Iy
- PIPB, y
/'I p'n'og Eau.hY/ an!
s'HomA/
0 N q
~ S L(~)
q S 7
Q 9o II g 5 7'0 i~a c~~
19 20 21 22 23 24 29 26 9g Stu.
/t HC -e7'2 0 Q.-TF <
sag rgcg
~ RE./L o r-'e~u.<A 7 /onJ rT II IP Z I I:.r /LIIIEAI/F I I 2.
I/, I/7 P7.~/ MINI'-AQ I-7 28 29 30 31 I.
32 7+7 I(/IIII.IIIIIIIi'+7 g Cf, 3g
+7/.I.j I/R-36 LAO 3998
~ I 7/8$
V
CALCULATIONSHEET ANPP 18601-183 PROJECT C
SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC. NO. ~~ +
SHEET NO.
REV ORIGINATOR CHECKER DATE REV
-2g.fr" ORIGINATOR DATE CHECKER DATE
.IQ
)gl-I/IZ cC L
0 Fog lg pter'z 23
~S 2
rs',
//
/go~
/I g
~ 0 i ~oA'1 E6'UA 7IOrJ BOAS'lid
/ /~4F-4 It 10 12 13 I/I
(
17 18 19 20 21 22 23 24 25 26 27 2$
7Z<
Moo
+O.
Ogo O
S 6 87u.y><<
0 (YE+
SttRFrICE p 4ggg gr-grJsggrt-g x /
/ 7 //.>>>'EAg F7
/2.
g.>/2. /:r//./~Z>/>/. > r ko's6 x 6'~-
/3pu/////
L>>/z>/8 X7-S
/q 9 '
7 A37u// //// - L>>/I>/f(
F 7 29 30 31 32 35 L*0 3998.I 1/85
CALCULATIONSHEET ANPP 18601-183 PROJECT C:.
SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC.NO./ 4~A4 / OE SHEET NO.
e"'RIGINATOR DATE CHECKER 3->HI gg, DATE g-Za'-&
REV ORIGINATOR DATE CHECKER DATE
.10 OD}
blL 0
L/n/2 6'o.
Heg7 Loan/
pip>
Q pip+
$ /u&JR F7 5/2F l~rP/
BTM-Ffg Liu r T HEAT LOA2) 87'A./HR.
IF'sr ALOoq gg3Xx Q
=
3/7 10 12
!3 14 I PSEUD l 00$
/Q" I PSrAL O67 I
37
/2~ '7 7 Ctg 3S tz3 7P) 37
=
9S 7P qq zs'>Ps
= 2/8'9 17 18 19 20 21 22 23 24
/)p/f/T gg/i l> / g~~
//C7////J P/Pti/Ci
=
7 ~
"/////I JOAN.
p/pC L,E>/ 7'<
SEE Ri fi4'8,',ErJ CE 26 27 28 29 30 31 7 LIE 6 xis7lfJC, 2 ivs<i g i) 7i0f/
V-gtiC~rie~s Pap PiPw Cj c QlllPPICN7 PJIf 5 SEgg(7p g Pgg 31, sF c7.<<fJ D,s
~ g iJ//+1 7/J gi.i r
35 36 LAO-5555.1 7/55
i i,
CALCULATIONSHEET PROJECT ANPP JOB NO. 18 601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC. NO. /g 4C gI gO-SHEET NO.
REV ORIGINATOR n
DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
.IQ
>nI-blL 0
ggP QIISC/I/II/C>/=
P/VIIII'>
10 12 13 54 57
'I 9 20 8U~~/
PIS <h's18< E P~t
+ IA 782 Cs'ERIL/
gOOhl A<>ls'7s
>8 7/IF f=o dZ p~grJ Cq"
'I.
Lied eo.
I p~InLo7$ net IIstnL o gz: C R 3$.
II l IIII/-
SX Z8
=
IO SC/d 9 O
+NSMZ87Iol/ 7h'/g;~p
~~g 2
TREF Zj
<yPE o/=
ZnrSCCL.87IOra
= CC)L,C/W'ly/qrg7.g F'/PE O. D.
=
/O 7S f Rdd id/
zesisLnTioe
- o. T)
=
io 7& I LZ, x 2)
I
/0'"
21
'~oR
/O I'll'Z
/Y 7S'-
7'3 7z 22 o
0
=
IO 7J
=
~'~7K 24 29 26 27 28 29 30 3 'I 32 36 I AO 5998
~ I 7/85 05-<7S(TIE.
Sgg/A C e'/PE.A a/c Z/I/Su.& 7/ 0>
FT /LgernR FT
/2.
- p. gg Fp / ju/Ft>l/
~"T zq. gg F 'z< FoT~z
'I< I9 ~'"/<<'<-'
CALCULATIONSHEET ANPP 18601-183 PROJECT R
ROOM
/
CALC. NO.
SHEET NO.
REV ORIGINATOR DATE CHECKER DATE
~/pe Joj)
REV ORIGINATOR DATE CHECKER DATE 6,
I iA/E
/I/O, 1P~ZALOOO:
/I l IAIF-5/Z.E
=
< 'C// gg Z///SIJLA7/owl 7FJICk'A'c. SS
=
2 ZNS<//l 7/0 n/
7 p'pE
=
CfllgC./gn/ s'/L/gg yg Qj/= 3Q PIPZ O. Z/
10 12
~<<IJ.//t7'/ow Cl.gi
=
P Z7z+ (2~>3
/9 4
~ 37J-13 14
(
FoR Z
P/PE,
=-'
'yo 3 /67$
2-I/
37S
=
I <<7<
17 js 19 20 21 22 Es
- 2. 25 7~
3 /979 g~J 3 /97
/ /97$
0'g
/8 //R 67u/u9.- ir 23 24 25 27 28 29 30 31 32 8 IJ784 suCFAcz 88m/7l o/
XWS<<</l 7r owl 0
X 4 S~S
/-777//Z/~xi)E C T
/Z
/, g7 R7i/9/eZAR R7 I/7 PB" / /'7 47c<///R
/.,iJri1R R7 3// 66 9/ /u/uR - LinieAR. F'7 33 36 L AO-$998 ~ 1 7/85
CALCULATIONSHEET PROJECT ANPP JOB NO. 18601-183 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC. NO.
SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE 6QP/
.1O
) OI-Wg+
IL 0
t //JE, No P(PE SIZE 8~7-z.oap/
~ p/pF
/IN&Ã Fl S~
lq&l7 Lo83 gV<
/IIIR.
=-
I PzzAL o7) 77 es /9 qs'/g x 77=
7B 30 10 t Psz~LoSz.
/0 2d 9- '/9 gS'/P/IZW =
12 13 IA
/
I P~X/I Lab'o 3o F4 3o g4' va
=
J 3 Q.7 I7 18 I9 20 21 22 23 24 h'EA7 l oA3 /-Og 9/sCl/Age'E PZPlNf = /I />>
HEAL 7 l0A3 /0R,>U<7/Onl 1 lf llIl'C, 7orAc Pipz~~r yvaw7 Coat
= iB,sqzar<</eg
+ pok P/P~
/-EiJ4 ills sEE
<~FE<E~<~~
/0 it<~ <0 33 LAO 3998.1 7/95
CALCULATIONSHEET ANPP 18601-183 PROJECT TRANSIENT TEMPERATURE STUDY FOR CS P&P ROOM CALC NO 13-MC-M-A05 SHEET NO.
REV ORIGINATOR PSSe./4. 'ATE CHECKER C~,S DATE REV ORIGINATOR Hd'-N DATE CHECKER DATE
,1Q
)DI-4l z 4 C
0 d.
Hea t Diss ipa ted by the CS Pump:
10 12 13 14
'I 7 19 20 22 23 24 The pump walls are assumed to be flat surfaces (See Assumption 10).
The heat dissipated by the pump can be calculated from the following equation for flat surface:
qs
=
to.ta (REF 1, chap 20, page
- 353, L+ Rs equation 10)
K Where L= insulation thickness, inch Per reference 2,
the insulation used on the CS pump is mineral wool and is 2" thick.
Therefore, L = 2"
- However, the pump insulation has been replaced with the reflective insulation for Unit 1.
CS pumps for Units 2
and 3 still have mineral wool insulation.
The thermal conductivity of reflective insulation is almost the same as that of calcium silicate.
At 150 F mean temperature, value of K for the 0
reflective insulation
= 0.40 BTU per (hour)
(square foot)
(
F temp difference per inch thickness) 35 36 LAO 3998.1 7/8$
At 150 F mean temp, value of K for the mineral wool 0
0.285 BTU per (hour)
(square foot)
(
F temp difference per inch thickness)
(REF 2, exhibit F, section 2C, para F.2.1E)
R
= 0.25 (For details, see Assumption 16).
PROJECT CALCULATIONSHEET 18 601-183 JOB NO.
SUBJFC7 TRANSTENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC NO 13-MC-HA-A05 gL, SHEET NO.
DATE 3-~r-rf CHECKER DATE REV Cy. 4/ /0 7-d'8-g ORIGINATOR DATE CHECKER DATE I2 I Q
>DI-big<
C 0
The conservative value of the insulation thermal conductivity for mineral wool versus reflective insulation is used.
This value is K = 0.40, BTU per (hour)
(square foot)
(
F temp difference per inch thickness).
0 10 gs
=
225
75 2'
0.25 0.40 28.57 BTU/HR-FT2 12 13 From ref 14, Surface area'f CS pump
=
2 x 19.75 x 7
+
14 x 13.88-7 12 12 12 12 9.26ft
+
8.625 x 25-19 12 12 18 19 20 21 22 23 24 26 27 28 29 30 31 Heat dissipated by CS pump 28.57 X 9.26 BTU/HR 265 BTU/HR e.
Total Heat Loads:
The following is the sum of the heat loads in the CS pump room:
CS pump and ACU fan electric motors heat load
= 122,725 BTU/HR Lighting heat load 2,517 BTU/HR Piping heat load 18,592 BTU/HR Heat-dissipated by pump
=
265 BTU/HR Total Heat Load 144 099 BTU/HR LAO 299dil 2ld5
0
CALCULATIONSH EET P ROJECT ANPP JOB NO. 18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC.NO. ~
SHEET NO.
ORIGINATOR DATE
-~s-8 CHECKER Cw.fi 4 DATE REV ORIGINATOR DATE CHECKER DATE
. IQ
)nI-bl g 4 L
0 CS UH 00iIiI S'uJ"FACE RE!I 8
{IOLU)I '/E 0)J l" 5 Puidi'c)art ugJ-Acr ARcg; 10 12 13
'14 18 pUAf R.ocJr)
Slw)grIJsl0iIJ5 LxAJx IV Zo'-t."
~ /z'" ~ ~-7'-s" EII<<II"~"3 I
/
pIJrap R,oooo 8'As 8
~orIMo>>J ~"i-~ (
r/
I
'/
1A/I7H HP>z t'uilp Root/ 'it
""u ~
co~<>iI/
~wee (i8-a x z7-3g Al(7p L,p5T pugp ROOM JI g
O)=
7')F
~ C/~~~oiI) ~iIL L
/0 IiKEA JrJ 7(yP C S i UA'i'Oorg 20 21 24 2S i I ~
i) i 8 77l<iI'i fo/'P BEr)7 7iPiJg/~~)sstd!I).
fReF gssywP7/o rJ If/
JEZCFORS 7H~
SuRFWC/.
8 gal JC'Og PgE.Ay mrliIISJ FQ
/S QS
/OL LPA/4';
r/
0/ALL St(AF$ CE r/)@pi)
/ g g g 27 3
+ 2O-G 2 -3 26 2/
26 29 30 rl I/
>o-4 x a.7'-3 ld'-o
/$ 7) F7
/
tr
/rg
/I
~ 20-a/ +
/
/I x 27-3
/
I/
I JO-S
+
~ -O) 31 C.E-IL!n /I SuRFJI CE 8/PE))
/
//
I r/
g-O 32 3t:g e7 I
rr
/I su+i-"i)cE
]3Ig F/7
~a -4
- y. i 6'o 3$
36 LAO-3999.1 9/8$
I lI A
l
CALCULATI ON S HEET ANPP 18601-183 PROJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC.NO. !9 gC /AA )Oh SHEET NO.
e'RIGINATOR DATE CHECKER DATE REV g'Za'-Pd'RIGINATOR DATE CHECKER DATE goop 5MRFA cE 23l2 F 1' 10 12 13 7/./ERE I
g Sit IFL 0 AlALl lwJ roc iiooi4
~ 7f/
BISEnlsxoes lg -4 x g-3 y 2-4
[RSf IIj gg g
II I/
u'oLuHz of seiE'zy
~sf LL =
~S4 Erg<I vALzev 14
/
17
'18 19 20 saiaCS WOrsL.
S~<1 g~
2-7S I 3
/=7 2 90$
21 23 24 25 26 27 28 29 30 31 32 F LOON ggF zi gC C,upi'~
/3y 7 HC CS PU/-II
=
Q F. g >
I
~cF:
i~/'<gg r'>f Cg
/~ED'I
~ oR HE/i v 7/dzirl<+)ls'srD ~~
P.90J -. 9 35 LAO 3998.1 3/8$
L'
PROJECT CALCULATIONSHEET 18601-183 SUBJECT TRANSIE.tT T~ERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
7 O
P~e(g ECKER s-es-m 6 O' DATE 9-cSPP REV ORICINATOR DATE CHECKER DATE
.iQ nl-wz C
U Z)00~ 3-3 IIC 4"(Tying 10 cs Puv)P 8'oo+I 3-C~ g SHIE I.JI ah~<+~
HPsZPu+IP A gaowt HPs Z PU+~i '8 70067 12 I3 SIIIf,fQ klALL 0-C 16 18 19 20 21 22 LPsZ Pu>IP A Z<<<
SHIELD ~ALL 25 27 28 29 30 3l M
Doog 3'-3"g 6'-g" 7 lo LA/oQ7 oF f'U~P g go~~
(I WZg OAJ RE~
~'~
8 '~3 LAO )%% ~.I 7/ ~ S
CALCULATIONSHEET ANPP 18601-183 PROJECT JOB NO.
(
TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CAt C.NO.i~+~ +~ ~+~
SHEET NO.
ORIGINATOR DATE CHECKER DATE 9-za'-l REV ORIGINATOR DATE CHECKER DATE
~ oO
)nI-Iol g <
L 0
L.
CS owl Zoo~
~>LU+~~
Purl gooier uozuzz z~
6 '~ ig'Q
)( 2,7 3
10 lOOS-X S7~
gzi/fp'l3g 12 13 14 7 78'~a~/2 UOL.ul.)E VaL. ur-ye EuD +
/El AWFU 7o i~Vl<P+ SOC+iDAI DlSC j/lIfggg P +P 17 18 19 20 21 22 23 24 ygLgI/p
- g
~ ~'~~ ~
- + Z 8
X l3'/~- 7i n.
"I
)
/2
~
7T t'8>~)
z (ow->9) 5 '7& F7 parV<ax) l3l57 Q) +PL lI]C>
0 pgoTog Yo6088
=
l~
oo y
7 y g Xd'(93El-~
lz g~
/W 27 28 29 30 31 32 i +HIt ~ Pl0 fo/
JrdLUME = ~ 7d+'++
l3/
yz 7 8',
lT 7
S4/
l37f7~
35 36 LAO 3998
~ 1 I/88
CALCULATlONS HEET ANPP 18601-183 PROJECT TRANSl NT TEHPERATUR FOR S
PUMP ROOM CALC. Xo.
SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
'-'->E 6, li),]sf rg gj FoZLo4JirrC, P/.'o usga S'iI~
PtfzrJQ uog/J~E 7 f4-E g s
/UAJP goop:
(REF
/AG'sx z6 2.'1 3g g( ~~g p~)
10 LINE rtlo fPszA Loop Pli Z Eiz E, 2 /1/'Sg// g7/gA/
0.$
Pip<
LErJ/ rH.
12 13 14 i Psz//Loop
( (oases L yI/'7 37'7 18 19 20 i/ S~H Lo7ol (0
77'2 23 f / 52') L Of2.
f 0 t
pug //t L 0 f~
4 37s-
'6 I AO 3998.I 1/85
CALCULATIONSHEET ANPP 18601-183 PROJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC. NO. i~
SHEET NO.
REV ORIGINATOR DATE x
CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
. I 0
)DI-hip cC 12 II t/
/I UoLOHE d//=
/ Par8 L oo'7 i~
1T (sy i (yx.ps/
FT~
~ 7
~ /g F7~
I/
VOLuRE-0/-
/ P>Z rl LOO)-
/II'0 x/QX g 37 F7 12 13 Ia Uo Lu&E log
~ 7Z F7~
//
/ p$jg g 7f /
/f/L/4)
I @++Ad 0 I2-- /o ii x fiI'7-~i x
( 77+ ag) 8 r 17 18 19 20 21 22 23 2a 25 UOLur.>F d/
c/g FT 27 28 29 30 31 32 35 36 LAO 3998,1 7/SS
4
CALCULATIONSHEET PROJECT JOB NO 18601-183 U JECT CALC. NO, i~
SHEET MO. +/
REV ORIGINATOR DATE 3-V5'HECKER C>,8 iA DATE REV ORIGINATOR DATE
-Zo'-d'HECKER DATE
.IP
) I3 I-bl z 4 L'
CS PuRP gOOW Vo~~~i~ =
SHIE LD A/8LL UOL.VI"/~
pUgt cf-Qo7og SCT pl PIN g Yd 6 U/-18 g a o s's-p 7 s I-5a e pap e 3 oJ t<<~
t ge>I 3 UoCUZ-/E
=
/3'7 Q 7 ~
tSe.c. +)a%
z.4 z F7 Qs~~p~<p <<
IO I2 I3 I4 PUAP <OoA Uoz vwgZ
/oops (z~g A<37 y z G3)
't~qg e7-~
'I7 j8 I9 20 21 22 23 24 25 26 21 28 29 30 31 32 35 LAO 3998.1 7/85
p
PROJECT CALCULATIONSHEET JOB NO 18601 183 TRANSIENT TE>iPERATURE STUDY FOR CS PU?'P ROON 13-??C-HA-A05 SHEET NO.
+~
REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE f's~/4'&-fg
. Qj.g g-EP-Pz
.IQ
> D-
II4 C
U 3.
Input Data:
Case A
10 12 13 16 17
'I 8 19 20 21 22 23 24 25 26 27 28 29 30 3I The following input data for the computer model is used:
1.
Initial room ambient temp.
= 75 F
[Assumption 2]
2.
Initial outside ambient temp.
= 75 F
[Assumption 3]
3.
Equipment and other heat generated in the room
= 144,099 BTU/HR [See Section VII.A.1.e]
4.
Net room surface area
= 2396 FT
[See Section VII.A.2]
2 5.
Net room volume
= 9399 FT
[See Section VII.A.2]
2 6.
Thickness of room enclosure
= 2.75 FT [Ref 11]
7.
Density of room enclosure material
= 144 LBS/FT
[Ref 6]
3 8.
Thermal conductivity of room enclosure material 0.54 BTU/HR-FT-F
[Ref 6]
9.
Specific heat of room enclosure material
= 0.2 BTU/LB-F
[Ref 6]
10.
One period of increment for calculation
=
2 min
[Assumption 18]
11 Imaginary thickness of first layer of concrete enclosure 0.01 FT [Assumption 19]
- 12. Multiplication factor of imaginary thickness of other layers
= 1.41
[Assumption 19]
34 35 36
PROJECT CALCULATlONSHEET 18601-183 JQB NQ.
TRANSIEttT TE>PERATURE STUDY FOR CS PE'P ROOM 1 3 MC HA A05 SHEET NQ.
REV ORIGINATOR DATE CHECKER
-a-p DATE REV S-7f P ORIGINATOR DATE CHECKER DATE
~ tO
) aI-Id E <
C-U
- 4. Results:
Case A:
10 The transient temperature for the CS pump room air obtained from the computer output, is shown in Figure 2.
The transient temperature
- output, Appendix A, shows that without any HVAC and the door closed, the calculated temperature in the pump room will be as follows:
13 18 19 Time Period 0 min 2 min 4 min 12 min 36 min 1 hr 2 hr 6 hr 8 hr 12 hr 24 hr 75 92.13 102.05 114.44 120.75 124.31 130.68 139.56 146.34 152.05 161.62 183.29 L+0 )O'10 1
I dS
ANPP PROJECT CALCULATIONSHEFT 18601-183 13-MC-HA-A05 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS Pl&P ROOM SHEET NO.
REV ORIGINATOR
/~JZI.,/t-DATE CHECKER OATE 3'-4'-4'EV ORIGINATOR O ATE CHECKER OATE
.iO
)OI-wz<
L LI VII.B.
CASE B
FLUID TEMPERATURE IN THE CS PIPES OF 225 F WITH NO HVAC AND ROOM DOOR OPEN:
1.
Air Flow Due to Temperature Difference:
IO 12 I3 When the temperature in a building or a room is different from that outside,a pressure difference between inside and outside occurs as a result of difference in air density, i.e.
due to the chimney effect.
16 The air flow due to the temperature difference is calculated as follows:
pc
= 0.52ph (1
1)
[Ref 1, ASHRAE Chapter 19, Page
- 334, To Ti equation 2)
Where p
h To Ti pressure difference across room enclosure due to chimney effect, inches of water absolute pressure, psi distance from neutral zone, feet absolute outside temperature, F
absolute room temperature, F
0 LAO 3999 I
I 8$
i
PROJECT CALCU LATINO N S HEET 18601-183 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS Fbi'P ROON CALC NO 13-.fC-HA-A05 SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
.IQ
)OI-ILlz<
L O
The door opening is 6'-6" X 3 '-3" [Ref 13].
Therefore, h
= 3'-3" (1/'2 height: Assumption 14) ssuming room temperature of 140 F and outside temperature of 90 F,
[Assumptions 20 and 21]
IO Pressure difference, pc 0.52 X 14.7 X 3.25
[ 1
1
]
460+90 460+140 13 0.52 X 14.7 X.3.25
[ 1
1
]
550 600 I
0.0037641 inches of water IS 19
[Ref 1, chap 19, page
- 333, eq 1]
The flow velocity can be expressed equivalent to a velocity head as:
pv
= 0.000482V Where pv
=
velocity head, inches water gauge V
=
air velocity, miles per hour Thus setting pc
= pv 0.0037641
= 0.000482V or V = 2. 80 miles/hr.
Quantity of air flow through door opening:
Q
= EAV (Ref 1, chap 19, page 344, equation 6)
Where Q
= air flow, cfm A = free area of the opening, ft V = air velocity, feet per minute
= miles per hour X 88 E
= effectiveness of opening (0.50 to 0.60 for perpendicular flow) 4+0
>999 7
7 9S
j
CALCULATIONSHEET PROJECT JOB NO.
18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR fD~//.
DATE
"-~(f-Zd CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
. tQ
)OI-bl 0:
0 Half of the door opening is assumed for flow into the room and the other half for flow out of the room
[See Assumption 14)
In addition, E
= 0.50 is used Therefore, Q
= 0.5 x (3.25 x 3.25) x (2.80 x 88) 1301 CFM 10 12 13 17 I8 19 20 21 22 23 24 25 26 27 28 29 30 31 2.
Heat Loads with Door Open Case B
t Air flow due to open door
= 1301 CFM Heat removed
= 1.08 X CFM X (Temp Difference)
BTU/HR
[Ref 1, chap 19, page
- 343, Eg 5]
1.08 X 1301 X (140-90) 70,254 BTU/HR Heat generated in the CS pump room
= 144,099 BTU/HR Net heat load in the CS pump room (144,099-70,254)
BTU/HR 73,845 BTU/HR LAO 5995.1 9195
]
PROJECT CALCULATIONSHEET 18 601-183 SU8JECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET HO.
~ 7 REV ORIGINATOR ps
.a'.
DATE gf g CHECKER c~.4r //
9'-cz-PP DATE REV ORIGINATOR DATE CHECKER DATE
~ 10
~D C
O
- 3. Input Data:
Case B
All input data for Case B is the same as for Case A except for item N3, Room heat load, which is 73,845 BTU/HR.
4.
RESULTS:
Case B
10 12 13 14 The transient temperature for the CS room ambient air, obtained from the computer output, is shown in figure 3.
The transient temperature
- output, Appendix B, shows that, without any HVAC and the pump room door open, temperature in the pump room will be as follows:
17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 Time Period 0 min 2 min 4 min 12 min 36 min 1 hr 2 hr 4 hr 6 hr 8 hr 12 hr 24 hr Tem erature F
0 75 84.06 89.49 96.83 100.45 102.36 105.77 110.50 114.10 117.14 122.22 133.68 35 36 LAO 9998.1 7/9$
l 4
PROJECT CALCULATI ON 9 HEET 18 601-183 ORIGINATOR CHECK ER TRANSIENT TEMPERATURE STUDY FOR CS PAP ROOai e
REV ORIGINATOR DATE DATE REV 0
84 DATE 13-MC-HA-A05 SHEET NO.
CHECKER DATE VII.C Case C:
Verification of Average Room Temperature:
IO 12 13 Average room temperature was assumed to be 140 F for case B.
0 The computer output for the case B (Appendix B) shows that the room temperature is 122 Degrees F after 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br />.
It is apparent that the average heat removed by the chimney effect is slightly over estimated and that the final temperature may be slightly underestimated.
To establish an upper limit, the chimney effect was recalculated for 122 F.
1.
Air flow due to Temperature Difference:
Case C
17 Ie I9 20 2l 22 23 25 Using the methodology used in case B, the pressure difference, air flow and corresponding heat load are recalculated, due to temperature difference, with room temperature 122 F and outside temp 90 F
(same as before):
0 0
Pressure difference, p
= 0.52 X 14.7 X 3.25
[
1
1
[460+90 4eo+122]
0.52 X 14.7 X 3.25'
[
1 1
]
[550 582]
0.0024835 0.0024835
= 0.000482V
[Ref 13, chap 19, page
- 333, 2
eq 1]
Air velocity, Air flow, V = 2.27 miles/hour Q
= 0.5 X (3.25 X 3.25)
X (2.27 X 88) 1055 CFM 35 36 LAO 3')98 I
I 8$
P l
Y
PROJECT CALCULATIONSHEET 18601-183 TRANSIE'NT TE"PERATURE STUDY FOR CS PU1'P ROO,t
~
~
REV ORIGINATOR DATE DATE CHECKER REV ORIGINATOR g-le/
DATE CHECKER DATE C
LC NO 13-HC-HA-A05 CALC. NO.
SHEET HO.
R I 0 2.
Heat Load with the Door Open:
Case C
Heat removed due to open door 1.08 X 1055 (122-90) 36,461 BTU/HR Net Heat load with door open
= 144,099 36,461
= 107,638 BTU/HR 10 3.
Input Data:
Case C
All input data for Case C is the same as for Case A except for item 03, Room heat load, which is 107,638 BTU/HR.
12 13 4.
RESULTS:
Case C;
16 18 19 20 Using this heat load, computer model is again run.
The result of this computer run, Appendix C, is plotted on Figure 3. It indicates that.the temperature after 12 hours1.388889e-4 days <br />0.00333 hours <br />1.984127e-5 weeks <br />4.566e-6 months <br /> is 142 F and the 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> temperature is 158 F
I $ (h)Q rI I(,
~ h pS.'C.f,h <- 6'iT -4, I'
hr
+ gIB Ih" $5,hh~i h,
h I
~r l)rQ h
'i hler hfj h
~,
hh%rr
~
~
~
r~r (C I
3hI
CALCULATIONSHEET P ROJECT JOB NO.
18 601-183 TRANSIENT TB'PERATURE STUDY FOR CS PIMP ROON 13-NC-HA-A05 SHEET NO.
0 ATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE o
j'S>.l'~, '~8.85 6 4 '~
s4-88
)OI-ILIz <
O RESULTS:
Case C
(continued)
IO The transient temperature for the CS pump room air, obtained from the computer output, is shown in Figure 3.
The transient temperature
- output, Appendix C,
shows that, without any HVAC and the pump room door open, the calculated temperature in the pump room will be as follows:
I2 13 I4 IS I9 20 2I 22 23 24 25 26 22 28 29 30 31 Time Period 0 min 2 min 4 min 12 min 36 min 1 hr 2 hr 4 hr 6 hr 8 hr 12 hr 24 hr Tem erature F
75 87.98 95.62 105.53 110.49 113.21 118.07 124.83 129.98 134.32 141.60 158.02 34 35 36 LAO 999d.l I/dd
l'
PROJECT CALCULATIONSHEET 18601-183 SUBJECT
~RANSTEVT TEMPERATURE STUD~
FOR CS PU1'P R00 13-etc-HA-A05 SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV OR I GIN ATOR DATE CHECKER DATE VII.D CONCLUSIONS:
No HVAC with Pump Room Door Open:
Reviewing the results for Case B,, it is concluded. that the temperature at each step beyond eight to twelve hours is slightly underestimated because the chimney effect is slightly overestimated.
Similarly for Case C, the temperature in this time interval is slightly overestimated due to the slight underestimation of the chimney effect.
In evaluating.these results, it is concluded that the average of the calculated transient room temperatures for Case B and C
is a better approximation of the expected results.
The average of the results of.Cases B and C follows:
Time Period 0 min 2 min 4 min
- 12. min 36 min 1 hr 2 hr 4 hr 6 hr 8 hr 12 hr 24 hr Case B:
~Tem F
75 84.06 89.49
- 96. 83 100.45 102.36 105.77 110.50 114.10 117.14 122.22 133.68 No HVAC and Room Door Open Case C:
~Tem F
0 75
- 87. 98 95.62 105.53 110.49 113.21 118.07 124.83 129.98 134.32 141.60 158.02 Avg B
& C
~Tem F
0 75 86.02 92.56 101.18 105.47 107. 79 111.92 117. 67 122.04 125.73 131.91 145.85
e PROJECT CALCULATIONSHEET 18601-183 SUBJECT TRANSIENT TEii!FERATURE STUDY FOR CS FUMF ROOM CALC NO 13 Mc HA A05 SHEET NO.
REV ORIGINATOR r]1'j DATE
)j'HECKER
&,O'4'ATE REV ORIGINATOR
.c3-99 DATE CHECKER DATE 0
I
)DI-IrlZ <
L O
. s zicATsou OF IAEA7 LOAD>
10 Il r
12 13 II 14 I
17 18 19 21 22 23 24 25 26 27 28 29 30 31 CS PUf'1P Rl'1 HEATUP TOTAL HEAT LOAD BTU"'HR 144. i THOU'="FIND F iG uk'.
8%. 5
)
s.'LECTRIC I"IGTGRS
- 12. 98.
PIPING 1.75.
POOH LIBHTINB
- 8. i8::
PUMP 35 36 I AO 3999.1 7I99
PROJECT CALCULATIONSHEET Np 18601 183 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC. NP 13 MC HA A05 SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE 0
I) 131-hl z C(
C II F00 cs PuRP P,op~)
hl/7H II/0
/d t/8 C 10 12 13 14 18 19 20 21 22 23 24 26 27 28 29 30 31
/po 4
/go 0
~ /70
~~ (40 p /So
/$ 0
/30
/ao
//0 O
--0
-< /oo 9o 80 75' N
Q 4
8 to
/2 lg lb la Po
/83-zVS 34 35 36
~
7/A III 7lmd PV I-rgugS
/ ICpgl+E
1'f tl
PROJECT CALCULATIONSHEET 18601-183 TRANSXENT TEMPERATURE STUDY FOR CS PUMP ROOM CALC. NO 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR ah.tt-DATE
>>F -2 CHECKER F<.di'/4 DATE
-Zg@b REV ORIGINATOR DATE CHECKER DATE 0
I) gI-wzg L'
CS UIvtP ROMANI Wt7H h/o VAC 8 OPEiv DooR.
pro 10 12 13 16 18 19 20 2'I 22 23 24 25 i7o
/6o
/So
/4o
/30 I20
/10
/Oa
/I vs@/lgs 0/ CAsss + &C~
CAsE. C
~,pG
~.<
cASE 9 ISQ.gg 8
/$5;8$ F 13& 68 8 27 28 29 30 31 go Qo 7S' 8
lo lk lg
/6 lg PO aZ 49 34 35 36 7 ln)E. Av l-/OQRS l-/ Cy L//('Q
P ROJECT REV C
CALCULATIONSHEET 18601-183 TRANS XENT TEMPERATURE STUDY FOR CS PUMP ROOM ORIGINATOR DATE
~-~f -d>
CHECKER DATE S@~s ORIGINATOR DATE REV CHECKER DATE
.10
>(31-I>IL U
13-MC-HA-A05 SHEET NO.
pp&/S/x' 10 12 13 14 17 18 INITIAL IN'IERNAL ROON AHSIENT TEHPERATURE, DEG.
F$ 7
>75 INITIAL ADJACENT RDOH AHSIENT TEHPERATURE, DEG. f$7
>7S fOUIPHENI HfAT GENERATED IN INE INIERNAL ROCH, 81U/NR$)
>> ICC099 NET INTERNAL ROQH SURfACE AREA, SO. fl.*)
>2396 NET INTERNAL ROCH VOL(R(E> CU.F).$)
>9)99 THICKNESS Of ROCH ENCLOSURE, fT.$)
>2.7S DENSIIT Of ROON fNCLOSURE HATERIAL, LSS/CU.F1.$ )
>ICC THERMAL CONDUCTIVITT Of ROOH ENCLOSURE HAIERIAL, STU/NR'FT f )
>.54 SPEC)f)C NEAT Of ROOH ENCLOSURE HAIERIAL, STU/LS F$)
>.2 ONE PERICO Of TIHE INCROIENI FOR CALCULATION> HIN.$7 IHAGINARY THICKNESS Of flRST LAYER Of ROON ENCLOSURE> fl~ ~I
>.01 WLTIPLICATION fACTOR OF IHAGINARY THICKNESS OF DINER LAYERS>7
>I.CI
'I 9 20 2'I
~ $ ~ $ ~ $ ~ $ ~ $ ~ ~ $ ~ $ ~ ~ $ ~ $ ~ $ ~ $
~ $ ~ ~ $ ~ $ ~ $$ ~ $ ~ ~ $ ~ $ ~ ~ $$ ~ $ ~ ~ $
~ $ ~ $ ~ $ ~ $ ~ $ ~ $ ~ ~ ~ >A > A $$
'OPIRIGNI 1976, 1979 SECH)EL POUER CORPORATION. ALL RIGNIS RESERVED ~
~ ~ > ~ ~ $ ~ ~ ~ ~ ~ $ ~ ~ ~ ~ $ ~ ~ ~ ~ ~ $ ~ ~ ~ ~
$ ~ $ ~ ~ ~ $ ~ ~ $ ~ ~ $ ~ ~ ~ ~ $ ~ ~ ~ $ ~ $ ~
$ ~ ~ $ ~ $ ~ ~ $ $ ~ $ ~ ~ $ ~ $ ~ $ ~
22 23 24 26 27 28 H>N(A(BER Of IHAGINARY LATER> IC DXI,DX2,DX),
"DX(H) 1.00000.02 I.C1000 02 1.98810 02 2.80322
~ 02 3.95254.02 5.5730S.02 7.85805.02
.11080
.15623
.2202S
.31059
.C379C
.61749
.65083 29 30 75.192 75.000 QQJ/~
I PERICO OAT~
2873.
QSI ~
1930.
DOT~
TAF $
92.13 11,'l2,13 "~
~ ~. ~ ~
~ ~ T(H>1) 75.98S 75.670 75.395 75.004 75.000 7S.000 75.000 75.000 75.000 0.
NOIR I.C967 NC0$.0000 75.073 75.020 7S.000 75.000 36 2 PER ICO OAT ~
CC84.
OS1$
5122.
001 ~
IAF ~ 102.05 11,12,13." """"
~ I(H>1) 11.163 76.591 75.563 75.017 0.
NCI ~ 1.6060 NC0$.0000 LAO )998<<1
)ISS
(I
P ROJECT CALCULATIONSH EET.
18601-183 "
'UBJECT TRANSIENT TEMPERATURE STUDY FOR CS PRE'OOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE Q~2P i+i CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
.FO
) (31-NI E IC L
()
rs.ole rs.oo2 rs.ooo n.ooo n.ooo rs.ooo rs.ooo rs.ooo rs.ooo 7S.178 7$.000 3 PER ICO OAT S388.
OST 9021.
Ool
- 0. HCI~ 1.6588 HCO
.0000 TAf> 107.71 11 12 T3
~ ~ - ~---------T(Ho))
lb.2lS 77.S35 rd.75d 76.0CC 75.C99 7$.043 7S.006 75.001 75.000 75.000 7$.000 7S.000 7$.000 10 0.
NCI ~ 1.713'I HCO~.0000 77.651
'6.5C3 7S.704 7S.OOO 7S.OOO 7S.OOO 6 PERICO OAT>
6CC9.
OSSA 22370.
COTE TAFT IIC.CC 11,12,13 "~ "
" T{HtI) 80.897 79.953 lb.84'I 7$.229 7S.047 7$.006 75.000 75.000 7S.OOO 12 13 12 PER ICO OAT~
7066.
OS I~
50573.
OOT ~
IAF< 118.CO 11 12 13 """
T{Ht1) 8C.320 83.300 82.010 80.C69 7S.98C 7S.303 75.056 7$.005 7$.000 7$.000 7$.000 78.789 75.000
- 77. 200
- 75. 000 0.
NCI ~ 1.7380 NCoi.0000 17 18 19 20 21 22 23 24 ld PER ICO OAT 7C30.
051 '9027.
~
~ ~.T(HFI) 86.803 8$.762 8C.C12 re.984 rs.res n.189 75.000 75.000 75.000 82.736 rs.ore 84.669 7$.0lI 2C PER ICO OAT 772$.
OST ~
107S52.
OOT ~
TAT~ 122.66 Il 12 13
~ ~
~ ~ ~
~ ~ ~ ~ ~ ~ T(H>T) db.d56 87.80C 86.C22 lb.05S 76.358 7$.C08 75.000 75.000 7S.000
- 0. HCI<1.7SIS HCOI.0000 80.792 78.767 7S.002 75.000 0 ~
HCI ~ '1.7622 NCO*.0000 82.567 80.259 7S.006 75.000 25 26 27 28 0.
HCI ~I.VIS NCO*.0000
/ jIg 30 PER ICO OAI 7980.
QST 13dllb.
Ool ~
TAT~ 124.31 11 T2 13 """
"T(HFI)
~
~
~
90.6C8 89.589 88.185 86.381 84.172 81.662 79.13S V.025 75.698 75.1C6 75.016 75.001 7$.000 75.000 75.000 29 30 31 32
- 0. NCI>1.7799 HCO<.0000 36 PER I CO OAT~
8207.
OSI>
16C708.
00'I ~
IAf~ 125. 79 11,12 TS "".~" ""T(H>I) 92.258 91.194 89.Vb 87.93$
8S.6C$
82.983 80.199 77.735 76.047 7$.252 75.033 7S.002 7$.000 7$.000 7S.OOO 35 36 0.
HCI ~ 1.787$
NCoi.0000 42 PERIOO OAT.
8414.
OST ~
193320.
001 ~
IAF ~ 127.15 11,12 13
~
~ ~
~ ~ ~ ~
~ ~ T(HiI) 93.734 92,666 91,23$
d9.366 87.01$
8C.231 81.237 78.468 76.C)9 7S.389 7$.05d 7$.00C 7$ ~ 000
- 75. 000 7S ~ 000 LAO 5995. I 7/55
PROJECT CALCULATIONSHEET 18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV O R I G I N AT,O R DATE CHECKER DATE 2g g. p 5-PZ4P 0
- 1) E) I-Ql z <
CC 4) 0.
HCI ~1.79C7 HCOI.0000 90.700 68.299 SS.C'll 75.553 75.093 75.008 CS PER IOQ QAT~
6606.
QSfi 221947.
Oaf~
TAfi 128.CO TI 12 13 - ~ -----------TIHif) t
~
~
95.104 9C.033 92.593 82.2ce 79.210 re.des 75.000 75.000 75.000 IO 93.143 7S.955 60 PERI CO QAT~
8953.
QST 279237.
QOT ~
TAfi I30.68 Il T2 T3." ""..TIN+I) 97.600 9d.52C 95.070 84.179 80.699 77.787 7S.001 75.000 75.000
- 0. NCli1.8077 HCoi.0000
- 90. 665 dl.629 7S.196 75.020 12 13 0.
HCI ~I.S19d Naacp
.9472 89.670 75.043 95.35C 92.821 lb.C36
'5.3C2 72 PERIOQ QAT 9265 QSf 336562 ~
Qal TAf~ 132.73
'll 12 13
~
TIHtf)
- 99. 651
- 98. 771
- 97. 307 86.004 62.168 7S.769 75.003 75.000 75.000 16 17 18 97.390 76.979 SC PERICO QAf 9550.
QSI 393914.
aalu TAf~ 134.61 Tl 12 13
~ ~. ~-. ~ ~-----TIHif) 101.92 IOO.S3 99.362 67.73S 83.605 79.782 7S.005 75.000 75.000
- 0. HCII1.8306 NCO>.9C97 9C.613 91.572 7S.530 75.077 19 20
- 99. 286 77.570 96 PER ICO QAT~
981C.
OS I~
C51287.
Oafi TAf~ 136.3d Tl 12 13
~
~
TIHt1) 103.64 102.75 101.27 89.362 85.005 80.612 7S.OIO
'5.000 7S.OOO 9d.673 75.757 93.360 7S.126
- 0. HCI ~I.dead HCOi.952C 10S PERICO OAT~
10061.
OSf 508678.
001 ~
TAI0 138.00 Il 12 13 "
""""TIH>I) 105. 64 104. 55 103. 07 101.07 90.955 86.367 81.846 78.196
- 75. 017 7S. 001 7S. 000 0.
NCI ~ I.SSOS HCOI.955C 98.c2e Os.os2 76.020 7S.189 1.
HCI ~ 1.6597 NCOI.958C Q HR, 120 PER ICO QAf 10293.
QSI 566082.
QOI TAfi 139.56 11,12,13,"'"
~"""TIH>1) 107.3C 106.26 104.77" 102.75 100.09 96.66I 92.C63 87.692 82.879 7S.850 lb.315 75.267 7S.027 75.001 7S.001 104.36 79.525 132 pERIco aAT.
Ioslc.
Qsl 623498.
Qol IAf~ IC1.03 fl,l2,13, ~". ~ ~ ~ ~
- IIHtf) lad.96 107.87 106.38 93.914 88.981 63.906 75.0CI 7S.002 7S.OOI 101.67 76.637 96.200 7S. 360
- 1. HCII1.8684 NCO>.9616 I AO )996.1 7IRS
II
PROJECT
(,
CALCULATIONSHEET 18 601-183 JOB NO.
SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PIMP ROOM REV DATE DATE REV ORIGINATOR CHECKER ORIGINATOR DATE CHECKER DATE
~
$ 0
>Ol-ILI 2R EC CC
()
CALC NO 3-MC-A-A05 SHEET NO.
ICC PER ICO QAT~
1072C.
QST ~
680923.
QOI ~
TAIR IC2.CC II 'l2 T3 "". -
"T(H>$)
110.SI 1(N.C2 107.92 105.89 95.312 90.236 84.924 80.21S 7$.058 75.003 7S.001 103.1'9 76.984 99.676 75.C69
- 2. HCIEl.drd9 KCOE.96C8
$ 56 PER ICO QAIR 1092$.
OST ~
738357 QOT~
TAfR IC3.79 Tl I2 13 """"
T(H>$ )
1$ 1.99 110.90 109.CO 107.36 9d.b63 91.C59 85.931 80.917 7S.080 75.005 7S.002 4.
KCI~ 1.8850 NCOR.9682 104.6C 101.10 77.352 75.593 10 12 13 108.78 81.627'68 PER ICO QAT 11'118.
OST 795799.
QOT TAfE 145.08
'll 12 T3 -------------T(HEI) 113.CI 112.32 110.82 Or.972 92.es2 86.927 7S.106 7$.007 75.003 7
KCI~ 1.8929 HCOE 9716 106.04 102.C7 77.7CO 7S.731 16 17 110. IC 82.343 g HR, 180 PERICO OATS 11304.
OSIS 8532C7.
QOTE TAFT IC6.3C ll 12 T3 " ".~. ~ ~. AT(HEI)
IIC.79 113.70 112.19 99.2C2 93.817 87.911 7$.137 '$.010 75 ~ 004
- 10. NCIEIR9005 NCOE.97SI 107.39 103.79 7S.IC4 75.882 18 19 20 21 22 192 PER I CO QAT IICd).
OST ~
910699.
QOt IAfE IC7.55 Tl 12 T3 T(HEI) 116.12 115.03 113.52 111.C7 100.CS 9C.9$ 5 88.882 d3.062 7S. 173
- 75. 0$ 3 7$. 006 15.
NCI ~ 1.9079 NCOE.9787 108.70 105.0S 78.563 76.047 23 24 26 27 28 29 30 216 PER ICO QAT 11825.
QS I~ 1025616.
001 fAI~ IC9.86 Tl 12 T3
~-------~ ----T(HEI) 118.66 117.5d 116.0S 113.99 111.21 107.54 102. 85
- 97. 157
- 90. 786
- 84. S07
- 79. 437 76.41C 7$.260 75.023 7S.OI0 31.
NCI ~ 1.9221 NCOE.9860 22.
HCI ~ 1.9151 KCO
.9823 20C PERICO QATR
$ 1657.
OS'68156.
QOT ~
TAN IC8.72 11 f2 T3
~ ~ "~
~
~ AT(H>l) 117.CI 116.31 IIC.SI 112.75 109.97 106.32 101.6S 96.068 89.840 83.784 78.99C 7d.225 7S.21C 75.01d 75.00S 3$
42.
KCI~ 1.9290 KCOE.9897 228 PERICO QATE
$ 1988.
OSIR 1083077.
QOT ~
TAIR 150.97 11, I2,13 - ~. ~ -- ~ - ~.---T(HEI)
$ 19.88 118.78 117.27 115.20 112.41
$ 08.72 103.99
- 98. 225 91 ~ 719
- 85. 229
- 79. 889 lb.dl C l5.312 75.029 7S.013 35 C HR. 2CO PERICO QAT~
12147.
QST IICOSCO.
QOT ~
36 TAT~
1$ 2.05 56.
HCI ~ 1.9357 NCOE.993C I AO 3994,I TINS
t
PROJECT
,C CALCULATIONSHEET 18601-183 REV CHECKER ORIGINATOR ORIGINATOR See-H TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM REV DATE DATE DATE CHECKER DATE 0
I
>(31-W (C
O 0
13-Mc-HA-A05 SHEET HO.
11 12 13 T(NE1)
~
~
~
121.06 119.9d 118.CS 105.'ll 99.271 92.639 7S.369 75.037 7S.0'Ir 116.38 85.950 113.58 80.350 109.87 rd.82s 26C PER ICO OATi 12C52.
OSfi 1255C67.
Qofi IAI~ ISC.13
'll 12 T3
~
~
~ ~
~T(HEl) 97.
HCI ~ 1.9487 HCoi1.0009 123.34 122.25 120.73 107.27 101.30 9C.CCC 75.500 rs.ose rs.o2s 118.65 87.386 115 84 112.'lo 81.292 77.27S 10 12 288 PER ICO QAT~
127C2.
QS'fi 1370391.
IAfi 156.11 Tl 12 13
" T(H>1)
~
~
~
12$.52 124.CS 122.91 109.34 103.27 96.203 7$.651 7S.080 75.03d aof ~
120.82 88.811 lid.oo 82.258 IIC.23 77.760 ISd.
HCI ~ 1.9612 HCOi1.0084 13 16 312 pERIoo OAT 13020.
asti lc85301.
IAf~ 158.02 11 12 13 f(H>I)
~
~
~
127.61 126.52 125.00 I'11.34, 105.16
. 97.918 rs.d24 7S.111 7S.OSO Qof ~
122.91 90.222 120.07 83.2CO 116.27 78.276 239.
HCI ~ 1.9733 HCoi1.0159 17 IB 19 20 336 pERIco QAT 13287.
Qs'f 160019c.
TAfi 159.85 11 12 13. ~""."".~T(HEI) 129.63 128.53 127.01 113.2d 107.00 99.S91 rb.old 7$.1C8 75.066 QQT ~
12C.91
- 91. 617 122.06 84.23C 118.25 78.818 353 ~ HCI ~ 1.9851 HCoi1.0233 21 120R360 PERICO OA'f~
13543.
OST ~ 1715059.
IAI~ 161.62 11 T2 13
~.""~"."~ T(HEI) 131.57 130.C7 128.94 llS.13 108.79 101.23 76.227 7$.193 7S.086 2S oafi 126.85 92.996 123.99 85.237 120.15 79.38C 503.
HCIi1.9964 HCOi1.0307 26 27 28 29 c32 p(RIco CAN lc262.
Qsf 2059clr.
TAfi Ibb.df Tl 12 13
~""
~ "T(NEI) 137.03 135.93 134.CO 120.40 113.86 105.92 76.968 75.374 7$.165 QQT ~
132. 29 97.030 129.41
- 88. 270 125.52 81.197 12CC ~ HCIS2.0289 HCoi'1.0524 30 31 504 PERTCO OAli 14918.
QSI ~ 240323$.
TAT~ 171.20 fl 12 13
~
AT(Nif)
~
~
~
142.0$
140.95 139.42 12$.27 118.57 110.33 77.8C8 7$.631 7$ ~ 27$
aali 137.30 100.91 134.40
- 91. 306 130.C8 83.134 2S79.
HCIi2.059C HCOS1.0730 35 36 576 PERICO QATi 15525.
Qsfi 27C6290.
Qofi C72$. HCli2.0882 HCOS1.0927 IAfi 17$.C7 II ~ f2 ~ 13 ~
T(Nil)
IC6 ~ 72 IC5.62 ICC.08 IC1.96 13'9 ~ 05 135.09 LAO 5995,T 7/85
PROJECT ORIGINATOR
,s n V
SUBJECT TRANSIENT REV DATE
>'Z-8 CHECKER DATE REV ORIGINATOR CALCULATIONSHEET 18601-183 TEMPERATURE STUDY FOR CS PUMP ROOM DATE CHECKER DATE 0
- 1) OI-Ol g 4 CC 4) 13-ifC-HA-A05 T
SHEET NO.
129.83 78.645 123.00 7S.9eS I'IC.SI 104.bC 9C.31C 85.155 7S.C17 846 PC RICO OAT~
18092.
OST ~ 306835C.
OOI TAIS 179.C9 11 12 13 -------------T(Hil)
IS1.11 150.00 N6o47 Nb.3C 13C.12 127.18 118.C9 108.2C 79.9CO 78.375 75.S68 143.C2 97.281 139. CC 87.229 7902. HCI>2.1157 M~1 1113
'Itff4720PERICO OAT lbb2d.
OST 3C29204.
OOT-IAI~ 183.29 ll 12 13 " "
T(HtI) 155.2b ISC.IS 152.d2 150.C6 136.18 131.15 122.26 111.71 81.118 78.657 75.78e 147.55 100.20 IC3.55 89.335 12325 ~ HCI>2. TC2I HCOiI ~ 1289 18 I9 31 35 36 LAO )999.1 7/89
.C CALCULATIONSHEET
\\
PROJECT 18601-183 ORIGINATOR CHECKER REV ORIGINATOR TRANSIENT TEMPERATURE STUDY FOR CS PAP ROOM REV DATE DATE s Zgzi DATE CHECKER DATE
,1Q
)OI-1>J g
>C IK LJ 13-MC-HA-A05 SHEET NO.
APPs~six 8 10 12 13 18 INITIAL INIfRMAL ROON AHSIEN'I TEMPERATURE> DEG. F<7
>>75 INITIALADJACENt ROCH AHSIENt TEMPERATURE, DEG.
F>7
>7$
EOUIPHENT NEAT GENERATEO IN THE INTERNAL ROOH, SIU/NR>1
>>73845 NET INTERNAL ROCH SURFACE AREA, SO. Ft.>T
>2396 Nft INTERNAL ROCH VOLTAIC CU.ft, ~'1
>9399 THICKNESS OF ROCH fNCLOSURE ~ FT.
1
>2.7$
DENSIIT Of ROCH ENCLOSURE MATERIAL, LSS/CU.fl.>1
>1C4 THERMAL COMDUCTIVIIT OF ROCH ENCLOSURE MATERIAL, BTU/NR ft fi)
>>,SC SPEClfIC NEAT OF ROCH ENCLOSURE MATERIAL, STU/LS f>7
>.2 ONE PERIOD Of TINE INCREHENt fOR CALCULA'IICH> HIN.>1
>2 IHAGINART THICKNESS Of fIRST LATER Of ROCH ENCLOSURES ft. 1
<<.Ol IRILTIPLICATIOMfACTOR Of IHAGINART THICKNESS Of DINER LATERS>1
<<I.CT
'I 9 20
~ > ~ > ~ > ~ ~ ~ > ~ > ~ ~ > ~ > ~ > ~ > ~ > ~ ~ ~ > ~ ~ > ~ > ~ > ~ > ~ > ~ > ~ > ~ >> ~ > ~ > ~ > ~ ~ I ~
> ~ >> ~ > ~ ~ >> ~ > ~ >>> ~
COPTRICNT 1976, 1979 SECNIEL POMER CORPORATICM ~ ALL RIGHTS RESERVED.
~
~ > ~ > ~ > ~ > ~ > ~ ~ > ~ > ~ ~ > ~ > ~ > ~ ~ > ~ > ~ > ~ > ~ > ~ ~ > ~ > ~ > ~ > ~ > ~ > ~ > ~ > ~ ~ ~ ~
>> ~ > ~ ~ > ~ > ~ > ~ ~ > ~ > ~ >
H>MLR1SER Of IHAGINART LATER> IC DXI DX2>OX)~
OXIH) 1.00000 02 I.C1000 02 1.98810 02 2.80322 ~ 02 3.95254 02 5.57308 02 7.65805.02
.11060
.'15623
.22028
.31059
.C3794
.617C9
.65083 9C3.
OOT ~
0.
NCI ~ 1.3771 KCO>.0000 75.035 75.000 75.010
- 75. 000
- 75. 000
~Pl I/'i I Pf RICO OAI~
IS18.
OST ~
TAf~
8C.06 II,T2,13,
~ ~. ~ ~ "~ ~ ~. ~ ~ TIH>1) 75.C81 7S.327 7S.193 75.002 75.000 75.000 7$.000 7S.000 7$.000 2 PER ICO OAI~
2CIS.
OS I~
2508.
OOT ~
IAS ~
SP.CP I),12>t)> ~
~. ~"~ ~ ~ ~ ~ "TIH>l) 76.060 7$.779 7S F 506 7$.276 0.
NCI ~ I.C595 NCO>.0000 7S.119 7$.038 LAO 5995,1 1/85
PROJECT CALCULATIONSHEET 18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PEP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE CHECKER DATE g-(Pti REV ORIGINATOR DATE CHECKER DATE
.1Q
) o)-
'I OIZ~
(C
()
7S.OOB 7$.001 75.000 7$.000 7$.000 7$.000 TS.QOO 7S.QOO 7S.OOO 75.513
- 75. 000 3 PERICO QAT 29CS.
QST CC'39.
Qof TAFT 92.74 fl f2 13
~
~ ~ T(H>l) 7d.blS 76.2C9 7S.86S 7S.021 75.003 75.000 75.000 75.000 75 F 000
- 0. HCI~I.4996 K~,oooo 7$.2CS 75.087 7S.OOO 7S.OOO IO lb.322 75.000 d PERICO OATS 3608.
Qsfi 11160.
aalu'AT<
9d.83 I'I 12 13 "-"--"""f(H>I) 77.9$ d 77.CBO lb.920 75.113 75.023 l5.003 75.000 75.000 75.000 0.
KCI~ I.SC20 KCO~.0000 7$.765 7S.3C9 75.000 75.000 12
'13
- 77. 768 75.003 12 PER ICO QAT 3984.
QSf 25S53.
QOI ~
TAT~
99.17 Tl 12 13 """
~ " T(H>I) 79.713 79.211 78.553 7$.C94 7S.152 7$.02d 7$. 000
- 75. 000 7S. 000 0.
KCI~ I.SSBB HC(N.0000 lb.91C lb.105 7S,OOO 7S.OOO 17 18 19 78.934 7S.013 18 PER ICO QAT C190.
QST ~ '"
Calid.
QOT ~
TAT~ IOO.CS Tl 12 13 ""
T(H>I) 81.01C BO.CBI 79.791 lb.003 7S.386 7S.095 7S.QOO 75.000 7S.OOO
- 0. KCI>1.5660 KCN.0000 77.9C I 76.910 75.001 7$.000 20 21 22 23 54720 2C PER!CO OAT~
C35C.
QST~
TAF~ IOI.CB Tl T2 13 "" "
T(H>l) 82.070 81.531 80.824 76.5SI 75.688 7S.206 7$.000 75.000 7S.OOO Qof ~
79.92d 7$.036 0.
HCI ~ 1.5716 KCOI.0000 78.853 77.67$
75.003 75.000 24 i HR. 30 PERlco QAI cc9d.
Qsf ~
69346.
TAT~ 102.36 Tl 12 13 " -~" "" T(Ht1)
~
N
~
82.991 82.CC9 81.730 27 77.104 76.029 7$ ~ 35C 7$.000 75.000 7S.OOO 28 QOT ~
50.507 75.074
- 0. HCI*T~ 5763 KCO>.0000 79.677 78.39C 75.008 7$.000 29 30 31 0.
HCI ~ '1.5506 KCOI.0000 Sd PER ICO OATS
- C622, QSI ~
83'988.
Qof>
fAF 103.16 11 12 T3
~. ~"."~". ~ T(H11) 83.818 83.273 52.$ 47 81.604 BO.C33 79.071 77.649 76.392 7$.532 75.125 7S.016 7S.OOI 75.000 7$.000 7S.OOO 35 36 C2 PERICO OATa C737.
QST 986C'I.
Oaf~
TAFT 103.85 fl,f2,13, ~ ~"-".~ ~
~ 1(H>I) 84.$ 76 BC.O29 83.29d ld. 181 76.7dl 7$ ~ 732 7S 197 7$ ~ 000 7S.OOO 7S.OOO 0.
KCI ~ 1.554$
KCOI.0000 81.13d 79.712 7S.029 7S.002 1 AO-)994.1 7/RS
l
P ROJECT CALCULATIONSHEET 18601-183 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PEP ROOM CALC. NP 13-MC-M-A05 SHEET NO.
REV ORIGINATOR DATE p Q.-J'HECKER DATE REV ORIGINATOR DATE CHECKER DATE 0
- 1) OI-hlg <
D Cd Pf RICO OAti CSCC.
OST ~
IIS)02.
TAF ~ 10C.SS 11 T2 13 T(Hit) 65.279 SC.730 83.993 lb.69d 77.1Cl 7S.950 75.000 7$.000 lb.O00 Ooti 83.024 75.261 81.795 7S. 047 80.320 7S.OOC
- 0. HCI>T.SSSO HCOi.0000
'I 0 60 PERICO OAT~
5037.
OSt IC26C5.
TAFT 105.77
'll 12 13 "
~ ~ "
T(Htt) 86.$ 60 86.009 85.264 79.689 77.909
'b.C2 I 7$. 000
- 75. 000 7S ~ 000 OOfi SC.277 75.C86 0.
HCI ~ 1.594d HCoi.0000 8'I.CSC 7S. 010 12 13 72 Pf RICO OAT~
5211.
OST ~
172007.
'IAF* 106.86 tl fZ l3 "T(H>I) 67.714 87.16'I 66.CII 80.625 7S.662 7d.92C 7S.001 75.000 lb.000 oofy
- 85. 411 7$.73Z 8C.114 7$.17C 82.501 7S.022 0.
HCI ~1.6005 HCOi.0000
'I 6 17 18 84 PERICO OAT~
5370.
OS'01384.
TAFT 107.87 TI, 12,13 "~
~
~
~
"T(NtI) 86.774 88.220 dl.C65 S1.512 79.398 77.CC3 7S.003 75.000 7S.000 Ool ~
86.CSS
- 76. 010 85.135
- 75. 270 83.Cld 75.039 0.
HCI ~1.6059 HCoi.9476 I9 20 21 22 23 24 96 PER ICO OAti 5517.
OSti 230773.
TAT~ 108. 80 Tl 12 T3 " "
.T(Htt) 89.7S9 89.203 88.CCb 62 ~ 35d 80.116 77.970 75.005 7$.000 75.000 108 PER ICO OAT~
5655.
OST ~
260171.
TAf~ 109.67 li 12 t3 T(Hit) 90.683 90.127 69.366 83.162 60.81C 78.500 7$.009 75.000 7$.000 67.C27 lb.31Z OOli 88.34i 76.633 0.
HCI ~ 1.6109 HCO~.9501
- 86. 069 SC. 393 7S.366 75.064 0.
HCI ~I.d156 HCoi.9525 66.968
- 65. 260 75.521 75.09d 4HQIZO Pf RICO OAti 57SS.
OSti 289577.
TAFT 110.50 Tl TZ,T3 --
~ ~ --------T(Hi1) 91.S56 90.999 90.236 83.935 81.493 79.029 75.014 rs.ool rs.ooo OOT 89.205 re.968
- 0. HCIi1.6201 HCO<.95C9 Sl.SCO 66.06$
75.671 75.136 3$
90.028
- 77. 313 132 PER ICO OAT~
S908.
OST ~
318969.
OOT.
IAf~ 111.28 TI,IZ,I3.
~.
~
T(N>I) 92 ~ 386 91.d28 91.064 SC.679 62.153 79.555 7$.021 7$.001 7$.000
- 66. 651 7S.S)d
- 66. 674 7S. ISC 1.
HCI ~ 1.62CC HCoi.957$
36 LAO )998.1 TIRS
PROJECT CALCULATIONSHEET 18601-183 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM REV DATE DATE REV ORIGINATOR CHECKER ORIGINATOR S c741 DATE CHECKER DATE
. IO
) Ol-4l (2
0 NO 13-MC-HA>>A05 SHEET NO.
ICC PER ICO OAT%
6026.
QST%
3CSC06.
TAT% 112.03 Tl l2 13 ---."""~ --T(H+I) 93.179 92.620 91.85C 85.395 82.796 80.077 75.030 75.002 75.001 QOf%
- 90. SIC 77.667 89.428 re.014 87.630 75.239 I ~
HCI ~ 1.6285 NC0%.9602 156 PERICO OATS 6138.
QST 377829.
TAf% 112.75 Tl 12 13.".-.
T(H+I) 93.938 93.380 92.612 86.088 83.C23 80.593 7$.0CI 75.002 75.001 QOI%
- 91. $68 78.026 90.174 76.202 88.35d 7$.303 2.
HCI ~1.632C HCO%.9629
'I 0 12 168 PERICO OAT%
62C6.
OSIER C07255.
TAFT 113.CC Tl f2 13 "
" "- T(H<l) 9C.669 94.110 93.3CI 86.759 84.034 81.103 7$.054 7S.003 75.002 QOf ~
92.294 78.390
- 90. 892 lb. C0 I
- 89. 061 75.373 3 ~ NCI ~ 1.6362 HC0%.9656 14 17 qljg leo PER!CO QAT 6351.
QSI 43668$.
TAT~ IIC. 10 11,12,13 " "
" T(H>1) 95.374 94.815 94.044
- 87. 410
- 84. 631 81; 607 75.070 75.005 75.002 QOT ~
92.994 7S.756
- 91. 585 76.608 89.740 7$.CSI 5.
HCI ~ 1.6398 HC0%.9685 18 19 20 21 93.671 79.125 192 PER ICO QAT 6451.
QST ~
46511d.
QOf ~
lif% IIC. 75 11 12 13 T(Htl) 96.0se 9$.496 94.724 8S.OC2 85.21C 82.105 75 ~ 08S 7S.007 7S.003 S.
HCI ~ 1.643C HC0%.9713 92.257 90.398 76.822 7$.535 22 23 24 25 26 20C PER ICO QAT~
65CS.
QST C95553.
QOT ~
11.
HCI ~ 1.6C68 NCO
.9742
'IAf% 115.37 ll T2 13 "" -" "T(Htf) 96.716 96.156 95.383 94.328 92.90S 91.03S ee.e58 es.res 82.$ 96 79.49s 77.043 7$.626 7S.109 7S.009 7S.OOC 27 28 29 30 2'Ib PERICO OAT%
66C3.
OSf%
52C989.
TAFT 115.98 11 12 13 ""~"" " T(Htf) 97.357 96.797 96.023 89.258 86.3C3 83.080 7$.133 75.012 75.005 QOT ~
94.966 79.865 15.
HCI ~ 1.6502 HCO%.9772 93.5CO 91.660
- 77. 270 7S. 723 31 22S PERICO QA'I'73C. OS'54C27.
IAf~ 116.56 11,12, 13
~ - ~ -- ~ ~ --- ~ - ~ 'f(H%1) 97.981 97.C20 96.646 89.843 86.890 83.55S 7$.159 75.015 75.007 QOf ~
95.586
- 80. 235 9C.156 77.501 92.265 7$.825 21.
HCI ~ 1.6534 HC0%.9801 36
~iiI/240 PER ICO Qil~
6824.
QSI ~
583865.
Qol ~
28.
HC1%1.6566 HC0%.9831 IAf~ 117. 14 I AO 399$,1 7/RS
ORIGINATOR DATE REV 8-9'-&
C
(,
~
CALCULATIONSHEET 18601-183 PROJECT JOB NO.
SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM REV DATE CHECKER ORIGINATOR VJ-AP DATE CHECKER DATE
, IO
)n)-
ILIA<
L
()
NO 13-MC-HA-A05 SHEET NO.
Tl 12 13
~
~" T(NII) 9S.SSS 98.027 97.252 96.190 94.75d 92.856 90.415 dl.C26 84.030
~
80.604 77.737 7S.933 7$. 189
- 75. 019 7$. 009 95.913 93.997 7S.220 76.16C 264 PERI(0 OAf 6995.
OS'I 6C2743.
OOT~
C9.
HCI ~ 1.6628 HCO
.9S91 IAF~ 118.24 ll 12 13.
~
~
~ T(Nt))
99.7SS 99.196 98.C20 97.35S 91.523 M.C68 SC.955 81.3CO 7$.25$
75.02S 7S.013 IO 12 2M PERICO OAT 7159.
OCT ~
701620.
TAT~ 119.30 11 12 13 ---------~ - FAT(Nif) 100.M 100.31 99.536 92.585 89.C74 M.856 75.333 7S.041 7$.019, OOT ~
98.468 82.070 97.019
- 78. 71$
95.089 lb.C12 79.
HCI ~).6687 HCOI.9952 13 312 PER I CO OAT 7316.
OCT ~
760492.
OOT ~
121.
HCI ~ 1.6743 HCO 1.0012 TAf~ 120.31 fl T2,13, ~ ~
~ ~
T(Ntf) 16 101.95 101.38 100.61 93.608 90.CCb 86.735 7S.421
S.OS6 7S.O26 99.5)d 82.793 9e.odl
- 79. 21d 96.138 ld.bib 17
'I 8
'I 9 20 336 PER I CO OAT~
7C66.
OST 819354.
Ool 17S.
HCI~ 1.6798 HCO 1.0071 IAFI 121.2d 11 12 T3 "" '(N>I) 102.98 102.C2 101.64 100.56 99.103 97.148 9C.596 91.388 87.592 83.508 79.727 lb.95C 7$.520 75.07S 7$.03C 21 22 23 24 25 360 PER ICO OAT IAIDO 122.22 ll f2 13 -------------T(Ni1) 103.97 103.CT 102.63 9$.552 92.303 SS.C30 7$.628 75.098 7S.OCC 101.55 100.09 98.125 84.21C 80.2CI 77.2CC 7dll.
Oll~
S78204.
Oof~
25C.
HCI ~ 1.6852 HCOII.0131 26 27 C32 PER I CO OAT~
8017.
OCT ~ IOSC63C.
Ool ~
IAII 12C.86 II 12 13 - ~ -----------T(Nif) 106.77 106.21 105.C3 104.35 98.253 94.901 90.83C 86.2SI lb.007 75.191 75.0SS 629. HCI~).7002 HCOi1.0304 102.87 IOO.M 81.795 78.172 30 31 50C PERICO OAT~
8390.
0$ 1~ 123079C.
TAf~ 12l. 29 II 12 13 ------ ~ - ~ ~ ~ --T(Ni))
109.3C 108.78 108.00 100.7$
97.318 93.096 76.4$ 8 75.322 7$.1C2 Oofi 1303.
HCI ~ 1.71C2 HC031.0470 106.91 IOS.CS 103.C2 SS.269 83.350 79.165 35 36
'ld PER)co OAI.
873$.
Osf 14odslc.
IAIDO 129.5$
11 12 13, ~
~ ~
~
AT(N>I)
II).74
'111.17 110'9 Oof+
2386.
HCI ~I ~ 7273 HCO 1.062S 109.30 107.81 105.78 LAO )998,I 7/8$
PP ROJECT
.C CALCULATIONSHEET 18 601-183 ORIGINATOR DATE ORIGINATOR gr )P-TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM REV DATE CHECKER REV ZZ8'l DATE CHECKER DATE 0
IOI-14 Z cC IC-U 13-MC-HA-A05 SHEET NO.
103.08 76.969 99.S&$
95.237 90.182 84.891 80.200 7S.493 75.2 1d 1$ 1.55 92.024 648 PTRICO OAT 9058.
OSIS 1581857.
00$
TAT~ 131.67 Tl 12 13 "
~
~ "" T(NiI) 113.99 113.42 112.64 105. 28 101. 73
- 97. 274 77.530 7$.702 7S.305
$ 10. 05 86.411 108. 01
- 81. 262 3988.
HCI ~ $.7398 HCO 1.0777 IO 113.67 93.803
+8420 PTRICO OAT 93d2 ~
OST ~ 1756532.
001 ~
IAF~ 133.M Il T2
$3
~
~ TINCT) 116. 11 115.55114.76 107.37 103.77 99.221 lb.133 7S.948 75.410 112.16 87.906
'110.11 82.342 6216.
HCI ~ 1.7S16 HCO 1.091&
12 13 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 35 36 LAO 3998.1 7/99
II
PROJECT CALCULATIONSHEET 18601-183 SUBJECT TRANSIENT TEMPERATURE'STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE
-N-Pi CHECKER DATE
) Q
>o)-
Wzg CC L) perisix C
7 10 12 13 14 6
17 18 19 INITIAL INTERNAL ROCH AHSIENT TENPERATURE, DEC.
F>Y
>>7$
INITIALADJACENT ROCH AHSIENT YEHPERATURE ~ DEG. f 1
>>7$
EOUIPNENT HEAT CfNERATED IN THE INTERNAL ROCH, BTU/NR~Y
>107636 NEI INTERNAL ROCH SURfACE AREA, SO. fl. 1
>>239d NET INIERNAL ROQH VOLUHE~ CU.fl.i)
>>9399 THICKNESS Of ROCH ENCLOSURE, fT ~ l
>>2,75 OENSIIT Of ROCH ENCLOSURE HAIERIAL, LBS/CU.FT.<2
>> ICC
'INERHAL CONDUCTIVITY Of ROCH ENCLOSURE HAIERIAL, BIU/NR FY fit
>>. 54 SPECIFIC NEAT Of ROCH ENCLOSURE HA'IERIAL, BIU/LB f>Y ONE PERIOD Of TINE INCREHENT fOR CALCULAIION, HIN.IT IHAGINARY THICKNESS OF flRST LAYER OF ROON ENCLOSURE, FT
~'I
>>.Ol HULTIPLICATION fACTOR Of IHACINARY THICKNESS Of OTHER I.ATERS 7
>>1.41 20 21 22
~ >> ~ >> ~ >> ~ >>0 ~ >> ~I~ ~ 0 ~ 0 ~ 0 ~ ~ >>>> ~I~ >> ~ 0 ~ ~I~ >> ~ >> ~ 0 ~I~ >>1 ~ P ~ 0$ ~ ~ 4 ~ 0$ ~I~ 0 ~ >> ~ 0 ~I~ >> ~ P ~I~
COPYRICNI 1976, 1979 BECNIEL PQIER CORPORATION. ALL RICNIS RESERVED.
~ >> ~ >> ~ ~ >> ~ ~ ~ ~ ~ ~ > 0 ~ ~ 0 ~ ~ ~ >> ~ ~ ~I~ 0 ~ 0 ~I~ ~ 0 ~ ~ 0 ~ ~ 0 ~I~ ~I~ 0 ~ 0 ~ 0 ~ 0 ~ 0 0 0 ~ '>> ~ >> ~ 0 ~ ~I~I~ ~I 23 24 26 27 28 29 H<NIAISER Of IHAGINARY LAYER> 14 DXI)DX2~ DX3)
DXIH) 1.00000 02 I.C1000 02 1.98810 02 2.80322 02 3.952$ C ~ 02 5.57308 02 7.85805 ~ 02
.11080
.15623
.2202S
.31059
.C379C
.617C9
.65083 I PER!CO OAT~
2)77.
OST ~
I TAFT 67.98 Il 12 13 ". ~ ~ "
~ ~ TIH>>I)
~
~
~
75.720 7S.C89 75.288 75.003 75.000 75.000 7$.000
- 75. 000 7S. 000 75.1CO 75.000 TS.053 75.01C TS.OCO 75.000 30 Cll. OOTR, 0.
NCI ~ I.CC03 NCOR 00000 31 35 36
- 0. HCI ~ 1.$ 366 HCOi.0000 2 PER ICO OAT~
3C28 OST ~
3747.
OOI TAFT 95,62 II ~ 'I 2 )I3
~ ~
I( H J I)
Td.SS) lb.164 75.75$
7$.412 7$.178 7$.056
~
'LAG-3999,I 7/SS
PROJECT SUBJECT
(
CALCULATIONSH EET 18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR i~44;l-.'ATE CHECKER 4(lj P DATE REV ORIGINATOR DATE CHECKER DATE 0
, l) C) I-CC
()
7$.012 7$.002 75 ~ 000 75.000 7S.OOO 7$.000 rs.ooo rs.ooo rs.ooo 7S.765 75.000 3 PERICO QAT~
4148.
QST 6615.
QOT TAfi 100.08 il 12 13 " "~ "
T(H>1) 77.404 rd.560 rd.289 75.032 7S.OOS 75.000 7S.OOO 7S.000 7$.000 0.
HCI~ 1.5833 HCOE.0000 7S.366 7S.130 rs.ooo rs.ooo IO rd.95d 75.000 6 PER(CO QAT~
5019.
QST ~
16508.
OOTN TAT~ 105.53 Tl 12 13 -
~ ~
~ T(H>1) 79.362 lb.661 77.&37 75.168 75.03575.004 7S.OOO 75.000 7S.OOO 76.137 7S. 000
- 75. 5 Id
- 75. 000 0.
HCI ~ 1.6318 HCOE.0000 12 13 14 79.062 7$.004 12 PERICO QATN ssld.
QSTN 37S37.
QOTN TAFT 108.68 Tl 12 13 "".""".T(N>l) 81.933 81.172 80.210 7$.728 7$.224 75.041 75,000 75.000 7$.000
- 0. HCINI.6526 HCOE.0000 77.812 76>630 7S.OOO 7$.000
'I 7 IS I9 20 21 22 23 24 25 I ~li 26 27 28 18 PERICO QAT 5803.
QST 58778.
QOI ~
IAF~ 110.49 Tl Tt 13 """"""T(H>l) 83.793 83.016 82.009 76.473 7$.567 75.140 7S. 000 7$. 000
- 75. 000 So.rsd 75.019 24 PER ICO QAT~
6033.
QST ~
80075.
QOTE TAFE 111.95 Tl T2 T3 - ~---------~ AT(N>1) 85.330 84.544 d3.513 77.273 76.009 75.302 rs.ooo rs.ooo rs.ooo 82.204 7S.053 83.485 7S.108 30 PERICO OATS 6231.
QSI ~
101404.
Qof ~
IAF~
113. 2'I Tl 12 13 " "
~ "
T(N>l)
- 86. 670
- 85. 879
- 54. 831 7S.079 76.507 75.519 75.000 7S.000 7S.OOO 79.309 77.800 7S.001 7S,OOO 0.
HCI ~ 1.6707 HCOE.0000 80.636 75.005 78.915 7$.000 0.
SCIL
'1.6776 HCOE.0000 81 835 79 963
- 75. 012
- 75. 001
- 0. HCI ~ 1.6627 HCOE.0000 29 30 31 36 PERICO QAT 6407.
OSIS 122754.
Qol ~
TAT~ 114.34 TI>T2 T3
~
~
"".T(H>l) 87.874 87.080 86.020 lb.873 77.037 75.779 7S.000 75.000 75.000 84.646 7S.187
- 0. HCIEI.6838 HCOE.0000 d2.937 80.950 7S.024 7$.001 3$
36 0.
HCI ~ 1.689S HCO>.0000 85.716 83.960 SI.&83 7S. 289 7S ~ 043
- 75. 003 42 PER ICO QAI 6568.
QST ~
144120.
QOT ~
TAT~ 115.35 11, 12, 13
~ T(N>1) 58.977
&S. ISO 87.112 79.649 77.583 76.071 rs.ooo rs.ooo rs.ooo I AO 5999.I 7/95
PROJECT CALCULATIONSHEET 18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR Ig/~ /S~
DATE CHECKER DATE grPgrP REV ORIGINATOR DATE CHECKER DATE
,IQ
>Dl-hlg <
(C
()
lb. 713 7S.412 Cd PERICO OATS brlr.
1ST~
165C98.
QOfi IAF~ 116.33 fl 12 13
" T(H>I) 90.001 89.201 88.126 80.C03
- 78. 13S 76.3d9 75.000 75.000 7S.000 0.
HCI ~ '1.69C8 HCOi.0000 b4.920 62.769 75.069 7S.006 10 88.$ 36 7S.711 60 PERICO QA'I 698$.
QST ~
208280.
QOT<
TAFQ 118.07 11 12 13
~
f(Htl) 91.867 91.063 89.977 dl.dCb 79.2C9 77.077 75.001 7S.000 7S.OOO 86.689 7S. IC6 SC.C22
- 75. 015 0.
SCIL 1.70CC HCO~.0000 12 13 72 PERICO QAT 7230.
OS'51090.
TATI 119.63 Tl I2 13 "
~ ~ ~ ~ ~ ~ ~ ~ ~ ~T(N>l) 93.549 92.7C3 91.649 83.210 60.3C7 77.SIO 7S. 002 75,000 7$. 000 0.
HCI ~1.7I31 NCOi.9460 90.191:
8$.299 85.9C7 76.070 7S.254 7S.032 16 17 18 64 PERICO QAf~
7C52.
OS'93922.
TAF~ 121.07 ll 'f2 13
~ ~
T(H>1) 95.093 94.28$
93.185 SC.503 61.420 78.567 7$.004 75.000 75.000 91.712 re.cre 0.
HCI ~ 1.7211 HCO~.9C89 89.787 87.366 75.395 7S.OSS 19 20 2'I 22 9e PERIQO QAI 7656.
OS'36769.
TAT~ 122.40 11 12 13
~ ------------T(Hil) 96.528 95.718 9C.613 6$.733 82.C66 79.33d 7$.006 7$.000 7$.000 OOT ~
93.129 76.916 91.178 rs.ses 8$.703 75.09C 0.
HCI ~ 1.7286 HCO>.9515 23 24 2$
26 108 PER ICO OAT>
7SSO.
QST ~
379629.
IAF0 123.65 Il,T2,13, ~ ~
~
~
~
~ T(NtI) 97.674 97.063 95.954 86.909 83.C63 d0.108 75.013 7S.000 7S.000 001 ~
94.C60 92.C67 75.761 69.967 7$.1CI 0.
HCI ~ 1.7356 NCOI.95CT 27 H4 120 PE RICO QAT~
6032.
QST ~
C22501.
TAFT 124.63 Tl T2 13
~ ~ ~ ~
T(Htf) 99.1C6 98.33C 97.222 30 8$.03$
SC.473 S0.879 75.020 7S.OOI 75.000 31 QOf ~
95.720 77.872 0.
NCI ~ 1.7423 HCO>.9569 93.729 91.170 75.980 7S.199 35 132 PERICO QATAR 6204.
OS'65361.
TAFT 12$.95 Tl 12 13 " "
""f(H>I) 100.3d 99.SC'3 98.C28 69.119 SS.C36 81.6Cb 7$.030 7$.00'I 7$.001 QO'I ~
96.916 78.3rd 94.91'I 76.221 92.319 7S. 269 1.
NCI ~ 1.7C87 HCO*.9597 36
PROJECT CALCULATIONSHEET 18 601-183 13-MC-HA-A05 SUBJECT TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM SHEET NO.
REV ORIGINATOR DATE
~-~d'M CHECKER DATE REV ORIGINATOR DATE CHECKER DATE
.iO
) Ol-ILIE cC (C
()
ICC PERICO QAT>>
8368.
QST>>
508270.
OOI>>
'IAF>> 127.02 fl T2 13
~ ~
~
~
T(H>>I) 101. $ 1 100. 70
- 99. 580
- 98. 064 90.163 86.373 82.407 7S.892 75.043 75.002 lb.001 96.043 76.480 93.C22 7S.350 2.
HCI ~ 1.7$ CS HCO>>.9627 97.129 94.483 76.755 7S.CC2 156 PERICO OAT~
852C.
OS'51165.
QOT ~
3.
HCI 1.7606 HCO>>.9657 TAF>> 128.04 Tl ~ f2 ~ T3i T(H>>I) 102.62 101.80 100.68 99.163 91.173 87.287 83.1$ 9 79.C16 7S.059 75.004 75.002 10 12 13 100.22 79.9C6 168 PERICO QAT~
8675.
QSf>>
59C06C ~
QOT>>
fAF~ 129.03 ll 12 13
~ ~ - ~ ~ - ~------T(H>>I) 103.68 102.87 101.7$
92.150 88.)78 83.903 7S.079 lb.005 7S.002
- 5. HCI'1.7663 HCO'9689 98.176 95.506 77.044 75.545 16 S.
HCI ~ 1.7718 HCO>>.9721 101.2C 99.1d7 96.497 SO.CS I 77.3Cd 7S.SSS 180 PER ICO QAT~
- 8820, OST>>
636969.
QO'f>>
TAFT 129.98 Tl T2 T3 "
"f(N>>1) 104.71 103.90 102,77 93.099 89.0CS 84.63d 7$.102 7S.007 7S.003 18 19 20 21 22 102.23
- 81. 018 192 PER ICO QAT~
8960.
QST>>
679878.
QOT ~
TAT~ 130.90 fl 12 13 -------------T(N+I) 10$.70 104.89 103.76 94.021 89.898 85.363 75.129 7S.QIO 75.005 11 ~ HCI ~ 1.7772 HCO>>.9753 100.17 97.4$ 6 77.659 lb.7Sl 23 25 26 27 29 30 216 PER ICO QAT~
9227.
QSI 765704.
QOT ~
23.
HCI 1.7874 HCO
.9819 TAF>> 132.66 ll T2 13 -
~
T(N>>I) 107.60 106.7S 10S.bb 102.0C 99.29C 95.793 91.5CS 86.785 lb.3'll 76.055 7S.19C lb.017 7$.008 IOC. 'll 82.096 204 PER(CO QAT~
9096.
QSf 722790.
QOT ~
16, HCI ~ 1.7823 HCO
.9786 TAF>> 131.79 Il 12 13 -
~ ~ ~ ~ ~ ~ ~
~ T(H>>1) 106.67 IQS.SS 104.72 103.19 101.11 98.388 9C.918 90.729 86.079 81.557 77.981 7$,91C 75.160 7S.013 7S.006 31 105.02 82.636 228 PER ICO QAT~
935$ ~
QST ~
808621 ~
QOf TAT~ 133.50 fl f2 '13
. ~"T(N>I) 108.SI 107.69 106.56 96.64d 92.3CO 87,C82 75.233 75.022 75.010 31, HCI ~ 1.7923 HCO>>,9853 102.93 100.18 lb.649 76.204 35 36 240 PER(CO QAT ~
9C79.
QST ~
851538.
COT ~
C2 ~
HCI ~ 1.7971 HCO>>.9887 TAN 134.32 LAO 3999.1 3/55
PROJECT CALCULATIONSHEET 18601-183 TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM 13-MC-HA-A05 SHEET NO.
REV ORIGINATOR DATE
~2Pig CHECKER C,k DATE REV ORIGINATOR DATE
-CSP/
CHECKER DATE I'I T2 13 "
~
~ ~ ~ ~T(N+I) 109.39 108.56 107.45 97.CSO 93.122 65.170 75.27S 75.027 7S.012 IOS.90
- 53. 174.
103. 8'I
- 78. 993 101. OC
. 76.362 26C PERICO OAT 97lr.
OST 93737$.
TAFT 1$5.90 11,'f2,13 """
~ T(N>T) 111.10 110.28 109.1$
99.09C 9C.641 69.518 rs.srs 7$.041 rs.o19 Oof ~
107.60 64.247 105.49 79.697 102.70 re.e98
- 72. Hcl ~I.dobe Hco
.9955 10 12 285 PERICO OAT~
994C.
OST~ 1023209.
TAT$ 137.4I Tl 12 13
~
~
~ ~
~
~ ~T(N>I) 112.73 111.91 110.78 100.6C 9d. 106 90.831 r5.486 rs.oeo rs.o2r Oofi 109.22 65.311 107.1'I SO.CIS IOC. 29 77.060
'116.
HCI ~ 1.815C HC0~1.0023 13 16 312 PER ICO OAT 10162.
OST T109033.
TAfi 1$8.86 11 T2 13
~ ~ ~ ~ ~ ~ ~ ~ ~
T(H>l)
IIC.29 113.C7 112.34 102.13 97.52C 92.112 7S.bls 7S.082 75.037 OOT~
178.
HCI ~I.d2CO HCO~T.0091 I10.77 105.65 105.82 86.365 81.152 77.CCS 17 18 19 20 33d PER(CO OAT 10371.
OSTi 1194643.
TATR IC0,25 fl 12 13 -. ~ ~ ~ ~ ~ ~ ~ ~ ~ ~
..T(N>l) 115.79 IIC.97 11$.84 10$.57 98.897 9$.$62 75.758 7S. 110 7S.OSO 112.27 67.C07 110.1C 51.894 107.29 77.850 OOT>
262.
HCI ~ 1.832C HCoaf.0158 113.72 88.C37 21 7 2 ~4360 PER I CO OAT~
10572.
OST 1280634.
Ool 22 TAf~ 141.60 II l2 1$
~ ~
~ > ~
~
~ T(N>1) 23 117.2C 116.42, 115.26 104.97 100.23 9C.563 24 7S.916 75.1CC 75.06C 374'CI~ 1.6405 HC041.022$
111.5d 105.72 82.643 78.273 26 2'7 28 29 30 31 191C.
HCI ~ 1.8850 HC0~1.0610 50C PER ICO OAT~
11650.
OST 179C636.
OOT ~
IAf~ IC6.86 Tl>'12>ls, ~"'
~ ~"~ T(N>1) 12$.07 12C.25 123.11 112.54 107.5C 101.39 77.12d 7S.471 75.207 121.53
'119.36 116.C3
- 94. 348
- 87. 176
- 61. 07C 924.
HCI ~ 1.5635 HCO>1.0422 432 PERICO OAT 11135.
OSIS 1537831.
OOT TAf~ T45.$ 6 Il T2 13
~
~
'f(N>l) 121.32 120.50 119.3d 117.79 115.63112.73 108.90 104.02 98.088 91.CSO 64.909 79.626
- 76. C69
- 75. 279 7S.12C 3$
36 576 PER I CO OATa 12128.
OST ~ 205087S.
OOI 3506.
HCI ~ 1.9053 HCO 1.0785 fAf~ 152.10 fl,l2,1$,
~ ~ ~ ~ "
~. ~ T(N>1) 126 F 56 127.74 126.59 125.01 122.6$
119.65 4 5
>>>>0
~
9
~ ~ \\
PROJECT
(,.
CALCULATIONSHEET 18601-183 JOB NO.
ORIGINATOR DATE ORIGINATOR
>>~ -s~
5.(o -RP TRANSIENT TEMPERATURE STUDY FOR CS PUMP ROOM REV DATE CHECKER REV j
DATE CHECKER DATE 0
I) OI-HI 12 LI 13-MC-HA-A05 SHEET NO.
I IS.95 77.871 110.85 75.720 104.51 97.'136 89.C23 82.583
- 75. 313 648RTRICo mr.
1257c.
osr 2306380.
ool TAT~ TSS.Ic TI,T2,13 - ~ ~ ~ ---------T(H+I) 131.8C 131.02 129.87 128.28 119.15
'113.97 107.C8 99.822 78.689 76.025 7S.CC2 5862.
HCI~T.9245 HCOII.0957 126.10 123.12 91.639 84.'132.
10 g'f/IR.72o 9(RIco mr 12994.
osr-2560984.
oor ~
TAT~ 158.02 I'I 12 13
~----------.-T(Hir) 134.9C 13C.12 132.97 131.37 122. 19 116. 9C 110. 31 102. C I 79.568 lb.385 75.592 129. 18
- 93. 817 126.19 85.705 9140.
HCI ~1.9429 HC04T ~ 1117 12 13 16 17 18
'I 9 20 21 22 23 24 25 26 27 28 29 30 310 35 36 LAO 39984r r/RS