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Text

Transient Temp Study for HPSI Pump Room.
	ML17304A770
Person / Time
Site:	Palo Verde
Issue date:	04/04/1988
From:	Riley H; BECHTEL GROUP, INC.
To:	;
Shared Package
ML17304A744	List: ML17304A743; ML17304A755; ML17304A760; ML17304A761; ML17304A762; ML17304A763; ML17304A769; ML17304A770; ML17304A771; ML17304A774;
References
	13-MC-HA-A02, 13-MC-HA-A02-R00, 13-MC-HA-A2, 13-MC-HA-A2-R, NUDOCS 8811230028
	Download: ML17304A770 (146)
	v • d • e

OOCUHENT NVHSER Arizona Nuclear Power Project /3- HC - H 3 -pc+

TITLE/DESCRIPTION

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INTERNAL CONTROL NO.

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CALC. NO.

TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SUBJECT FILE NO.

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. P/ s-~Be I4 IL'Z 0 Table of Contents Pacae No.

I. Purpose 6

II. Design Criteria 7

8 III. Study Assumptions 9

IV. References 12 V. Summary of Results 14 VI. Room Heat-Up Computer Model I2 A. Model Description 15 I3 B. Required Input 17 C. Assumptions 18 D. Limitations 18 l6 E. Output 18 I7 VII. Study 19 18 A. Case A: Pump room with no HVAC and room door closed I9 1. Heat Loads 20 a~ Electric Motors Heat Loads 19 2I b. Lighting Heat Loads .21 22 c ~ Piping Heat Loads 22 23

d. Heat Dissipated by the HPSI Pump 24

e. Total Heat Loads 35

2. HPSI Pump Room Surface Area S Volume 36 26

3. Input Data 42 27

4. Results 43 28 B. Case B: With no HVAC and room door open 44 29 30

1. Air Flow Due to Temperature Difference 44 31

2. Heat Loads 46

3. Input Data 47

4. Results 47 34 35 36 LAO i998.1 7/85

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PROJECT JO8 Np 18601-183 CALC Np 13-MC-HA-A02 SUSJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET Np.

DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

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12 0 C. Case C: Verification of Average Room Temperature 48

1. Air Flow Due to Temperature Difference 48

2. Heat Loads 49

3. Input Data 49

4. Results 49 D.

Conclusions:

No HVAC and Room Door Open 51 VIII. Figures:

11

1. Classification of Heat Loads 52 12

2. HPSI Pump Room with no HVAC 53

('X.

13

3. HPSI Pump Room with no HVAC and Room Door Open 54 4

Appendices:

1. Computer Runs For:

A. HPSI Pump Room with no HVAC 17 18 B. HPSI Pump Room with no HVAC and Door Open 61 19 C. HPSI Pump Room with no HVAC and Door Open 67 20 (Alternate Run for verification of 21 average room temperature for Case B) 22 23 24 25 26 27 28 29 30 31 3$

36 LAO 9999.l 7/SS

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CALCULATIONSHEET PROJECT JOB NO 18601-183 CPLC NO 13-MC-HA-A02 SUEJECT TRANSIENT TE2PERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

. tQ i->W'E VDI-5 'Fo ~w bJ L 0 PURPOSE The design basis for cooling the HPSI pump eauipment rooms, when the pumps are in service, uses unit coolers and the Essential Chilled Water System for cooling. In the event that either the unit coolers or the Essential Chilled Water system fails when the HPSI pump runs, the room temperature will rise rapidly.

10 The purpose of this study is to determine the transient air 12 temperature for 24 hours2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months in the HPSI pump room for the 13 following two cases:

14 A) Fluid temperature in the pipes of 225 F with no HVAC s) Fluid temperature in the pipes of 225 F with no HVAC and 17 the room door open.

18 19 20 During post-Loca condition, the limiting containment sump 21 temperature is 225 F as shown in reference 19, figure 6.2.1-24.

22 23 Standard room heat-up (RNHTUP) computer program, ME204, Rev. A 24 is used to study the room ambient air heat-up by the equipment 2$ and other heat loads in the HPSI pump room.

26 27 The heat generated in the room is transferred to the room 28 ambient air, stored in the room enclosure concrete (heat sink) 29 and transferred to the air outside the room. The transient 30 temperature for the HPSI room ambient air is studied for a time 31 period of 24 hours2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months without any HVAC. In addition, the transient temperature is studied when there is no HVAC and the pump room door is open.

35 36 LAO 3991il 7/99

CALCULATIONSHEET PROJECT JO8 gp 18601-183 CALC. Np '3-MC-HA-A02 TRANSIENT TE2PERATURE STUDY FOR HPSI PAP ROOM SHEET NO.

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II. DESIGN CRITERIA:

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.

10 The systems involved in this study are the Safety Injection 12 (HPSI subsystem), Auxiliary Building HVAC (Normal and 13 Essential), and Essential Chilled Water. Their design criteria 14 are references 21, 22 and 23.

17 18 20 21 22 23 24 2$

27 28 29 30 31 36 I AO 9995,1 9/SS

CALCULATIONSHEET PROJECT JQB NQ 18601-183 CALC. NO. 13 MC-HA-A02 SUBJECT T~SIENT TEMPERATURE STUDY @OR PEPSI PRP ROOM 6 REV ii&/4

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2 III. STUDY ASSUMPTIONS1

1. Fluid temperature for the HPSI system in the HPSI pump room is 225 F. During post-Loca condition, the maximum containment sump temperature is 225 F as shown in reference 19, figure 6.2.1-24.

2. The initial temperature inside the HPSI room is 75 F. This 10 is based on the assumption that normal HVAC is available before the time period of this study. Temperature of 75 F 12 is the typical normal temperature in the auxiliary building 13 and is based on the operating experience.

3. The initial temperature outside the HPSI room is 75 F.

17 This is based on the assumption that normal HVAC is 18 available before the time period of this study. The 19 initial temperature of 75 F is the typical normal 20 temperature in the auxiliary building and is based on the 21 operating experience.

22 23 4. Essential or normal HVAC is not available during time 24 period of this study. This is the principle assumed 2S failure at the onset of this study as discussed in section 26 27 28 5. Initially, steady state temperature conditions exist in the 29 HPSI pump room and outside the pump room.

30 31 3S 36 LAO 5998.1 7/55

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CALCULATIONSHEET PRO JECT Jpe Np 18601-183 C>t C Np 13-MC-HA-A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NP.

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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 0.00667 hours 3.968254e-5 weeks 9.132e-6 months compared to the thermal capacity of the existing walls to absorb the heat, the additional. floor thickness 10 will not make any difference to the room ambient air temperature.

12 13 4

7. The walls, ceiling and floor are used as a heat sink. For details, refer to Section VI.C of this study.

16 17

8. The heat generated within the room is considered as being 18 constant. This is due to the fact that more than 90$ of

'I 9 the heat load, as shown in figure 1, is from the electric 20 motors. For details refer to Sections VI.D and VII.A.1.e 21 of this study.

22 23 9. Temperature at the inner surface of the insulation is equal to the temperature of the fluid in the pipe. This assumes 25 that the temperature of the outside pipe surface is the 26 same as the fluid temperature. It also assumes that the 27 temperature drop across the very small air gap between the 28 pipe and the inside surface of the insulation is zero.

29 This provides a conservative estimate of the piping heat 30 load for this study.

31

10. For calculation of heat dissipated by the pump, the pump modeled as a flat surface. This provides a conservative estimate compared to a cylindrical surface.

35 36 LAO 1%48 s TIAW

CALCULATIONSHEET PROJECT JO8 NO 18601-183 CANC NO 13-MC-HA-A02 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PEP ROON SHEET NO.

REV ORIGINATOR DATE DATE REV ORIGINATOR DATE CHECKER DATE

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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 HPSI pump room shares a common wall with the other HPSI pump room and with a CS pump room.

50 Operation of only one HPSI pump is required, but two are 52 assumed. The operating HPSI and CS pumps could be from 53 different trains so that these pump rooms may not be 54 adjacent to each other. This study uses a worst case scenario and assumes two common walls.

57 12. The dimensions of HPSI pump rooms A and B for all three 58 units are essentially identical. In addition, the electric 59 motors and pumps, equipment, lighting and piping sizes and 20 lengths are virtually the same for all of these room. This 25 study is performed for HPSI pump room A for Unit 1 and is 22 applicable to HPSI room A and B for all three units.

23 24

13. The shield wall in the pump room is considered a heat sink.

23 The shield wall is converted to an equivalent wall having 26 same thickness as the room walls. In doing this, the 27 equivalent surface area on one side of this wall is 28 modelled as a heat transmission pathway to the adjacent 29 30 spaces. The shield wall surface area and volume are 35 approximately 4S and 2.5% respectively of the pump room surface area and volume.

35 36 I AO 9999 I 7/95

CALCULATIONSHEET PROJECT JOB NP 18601-183 CALC NP 13-MC-HA-A02 SU8JECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

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D As can be seen from the results in Appendicies 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 ava3.lable for heat transfer.

Because the surface area and volume of the shield are a small percentage of the total, this w3.11 provide reasonably 10 acceptable results.

12 14. For the case when the room door is open, half of the room 13 opening is assumed for air flow into the room and the other half is assumed for the a3.r flow out of the room. ASHRAE Ref. 1, Chapter 19, Page 334, indicated that if there is 16 only one opening, or if one opening is extremely large 17 relative to the others, the neutral zone (where there is no

'I 8 pressure difference between inside an outside) will be at 19 20 or near the center of the opening. This reference supports the above assumption . In addition , 50$ effectiveness of 21 22 the opening (normal value 50% to 60%) 'for air flow is used.

23 For details, refer to section VII.B.1 24

15. Per assumpt3.on 4 above, the essential HVAC is not avaz.lable 26 during t3me period of th3.s study. For a conservative 27 approach, ACU fan will be assumed running, without chilled 28 water through the essential co3.ls. The heat load due to 29 this motor is minor as compared to the heat load from the 30 HPSI pump motor. 82% efficiency for the ACU fan motor is 31 assumed for calculation of room heat load. This is a typical motor efficiency for 5 hp motors as shown in reference 1, Chapter 22, table 30, page 417.

35 36 I AO )44' 7/AS

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CALCULATIONSHEET PROJECT Jp8 Np 18601-183 CALC Np 13-".1C-HA-A02 U8gECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NP.

REV ORICINATOR D A T 6' DATE REV ORICINATOR DATE CHECKER DATE

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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 6 20, table 1, page 357)

17. The lighting load in the HPSI pump room is assumed to be 2 Watts/FT . This is a typical lighting load for industrial 10 buildings as shown in the national electrical code 1987 handbook, reference 7.

12 13

18. This study is performed for a time period of 24 hours2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months . The computer model can provide details for a maximum of 720 steps (Refer Section VI.D). Therefore, each step or time 16 increment is 2 minutes.

17 18 19

19. The room walls are required to be divided into a number of 20 layers for computation of temperature distribution in the 2! concrete walls by the computer model. The required input 22 for the thickness of the first layer and the multiplication factor for thickness of other layers are selected as 0.01 24 ft (approx. 1/8") and 1.41 respectively. For details, see 25 sections VI.A and B.

26 27 28 30 31 34 35 36

CALCU LATION SH EET PROJECT JP8 NO 18601-183 CgLC Np 13-MC-HA-A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE IZ j ~</t g4 ~ N -A'g ) iOI-WE<

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20. For calculation of air flow due to temperature difference for the case of open door, the room average temperature is assumed to be 140 0 F. For support of this average temperature, see Section VII.C, verification of average room temperature.

21. For calculation of air flow due to temperature difference 10 for the case of open room door, the average temperature outside the room is assumed to be 90 F. It assumes that 12 doors in the corridor will be opened for enough air mixing

!3 to have the average temperature of 90 F. This approximates an average temperature after the pump room door has been open for a while. Note: the initial temperature was 75 F.

16 (Assumptions 2 6 3).

17 18 22. Concrete has the following properties:

I9 20 A. Density 144 lbs/f t (Ref 6) 21 B. Thermal conductivity 0.54 (Ref 6) 22 C. Specific heat 0.2 btu/lb- F (Ref 6) 23 24

23. The net pump room volume is required as input to the computer model. For calculation of net room volume, the 26 volume of the HVAC equipment in the HPSI pump room is 27 insignificant and is neglected.

28 29 30 31 36 LAO )998.1 9I99

C ALCULATIONSHEET PROJECT JO8 Np 18601-183 Np 13 MC HA A02 SU 8 JECT TRANS IENT TEMPERATURE STUDY FOR HPS I PUMP ROO SHEET Np.

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3 IV.

REFERENCES:

1. ASHRAE Handbook of Fundamentals, 1972.

2. Technical specif3.cation for thermal insulation materials and the application to piping and equipment, specification number 13-MM-301, Rev. 2.

3. Line designation list, 13-P-ZZG-014, Rev. 29.

10 4. Auxiliary building essential cooling System heat load calculation, calculation number 13-MC-HA-051, Rev. 1.

12 5. P & I diagram, safety injection and shutdown cooling 13 system, drawing number 13-M-SIP-001, Rev. 19.

14 6. Pr3.nc3ples of heat transfer, th3.rd edition, Frank Kreith, Intext Educational Publishers. table A-2, Physical Properties of Some Nonmetals, page 635.

7. The National Electrical Code 1987 Handbook, fourth 18 ed'.tion, General Lighting Loads by Occupancies, table 19 220-3 (b), page 100.

20

8. NAVCO Piping "Datalog", National Valve and 2'I Manufacturing Company, Pittsburg, PA. Ed3.tion No. 10.

9. Auxiliary building isometric, draws.ng number 23 13-P-SIF-201, Rev. 21.

24

10. Auxiliary builds.ng isometric, drawing number 13-P-SIF-203 Rev 23.

26

11. Auxiliary building plan at elevation 40'-0", drawing 2 I number 13-C-ZAS-110, Rev 16.

28 29

12. Auxiliary building plan at elevation 40 '-0", drawing 30 number 13-C-ZAS-112 Rev 4.

31

13. Aux'.liary building plan at elevate.on 51'-6", drawing number 13-C-ZAS-116 Rev 17.

14. Ingersoll-Rand pump drawing for HPSI pump, log N001-11.01-15-6 33 LAO 3998. I 1ISS

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CALCULATIONSHEET PROJECT JQQ NO 18601-183 NO 13-MC-HA-A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

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15. ingersoll-Rand Pump Manual, log N001-11.05-1, HPSI pump data sheet and pump curve.

16. Pump motor data sheets, log N001-11.05-7-2

17. Reliance Electric Co. drawing, log M721A-112-2

18. User's and Theoretical Manuals Verification Report, program RMHTUP-Room Heat Up, program number ME204 Rev.

10 A1, Bechtel Power Corporation, San Francisco Power Division.

12

19. Final, Safety Analysis Report, Palo Verde Nuclear 13 Generating Station, Ammendment 17.

14

20. Auxiliary Building Base Mat, Sections and Details, Drawing Number 13-C-ZAS-124, Rev. 13.

17

21. Detailed Design Criteria, Part III, System HA, HVAC-Auxiliary building, Rev 8.

18 19

22. Detailed Design Criteria, Part III, System SI, Safety 20 Injection and Shutdown Cooling System, Rev 5.

21

23. Detailed Design Criteria, Part III, System EC, 22 Essential Chilled Water System, Rev 3.

23 24 26 27 28 29 30 31 35 36 I AO 9999.I 7/OS

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CALCULATIONSHEET pRpJEcr SU8JECT REV ANPP ORIGINATOR

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SUMMARY

OF RESULTS:

The transient temperature summary for the HPSI pump room air for the cases 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 10 explained on page 51 the average of the results is felt to best 12 estimate the transient temperature profile when the room door is open.

14 No HVAC and Door Closed No HVAC and Room Door Open CASE A: CASE B: CASE C: Avg B 8 C Time Period ., 0F 0F 17 Tem F Tem ., Tem ., Tem ., F IS 0 min 75. 75 75 2 min 93.34 84.93 87.77 86.35 20 4 min 104.10 90.97 95.42 93.20 21 12 min 117.79 99.26 105.64 102.45 22 36 min 124.76 103.37 110.74 107. 06 23 1 hr 128.66 105.53 113.50 109.52 24 2 hr 135.64 109.36 118.40 113.88 26 4 hr 145.37 114.69 125.22 119.96 26 6 hr 152.80 118.75 130.43 124.59 27 8 hr 159.07 122;16 134.80 128.48 28 12 hr 169.57 127.88 142.14 135.01 29 24 hr 193.35 140.79 158.72 149.76 30 31 35 36 I AO 3999,l 7/85

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CALCULATIONSH EET .

PROJECT JO8 NO 18601-183 CP,LC NO 13-MC-HA-A02 SUBJECT I TRANSIENT TEMPERATURE STUDY FOR HPS PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE PS&/lu. s-aS-$ $ g-<Pi ).iO 13l

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8.

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 The temperature of room ambient air increases with time, due to the heat released from the equipment and other

!2 13 sources. 'he heat generated within the room is transferred 14 to the ambient room air, stored in the room enclosure (walls, ceiling, and floor) and transferred to the air outside the room.

17 18 The room walls are divided into a number of layers with 19 incremental thicknesses for numerical computation by the 20 computer program. ln this study, the value of imaginary 21 thickness of first layer of concrete wall is selected as 22 0.01 ft and the multiplication factor of imaginary 23 thickness of other layers is taken as 1.41. In other words,.

24 the first concrete layer thickness is 0.01 ft (approx.

2S 1/8"), the second layer thickness is 0.0141 ft (approx.

26 3/16"), third layer 0.01 X (1.41) ft, etc.

27 28 The transient room temperature is determined from the heat 29 balance equation, which balances the heat generated within 30 the room and the heat transferred to the ambient room air, 31 stored in the room enclosure and transferred to the outside air, as shown below:

3S 36 L AO 4994. I 7/45

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CALCULATIONSHEET PROJECT JO8 Np 18601-183 C/$ lLC NP 13-MC-HA A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

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Lz O ILI QA/ALL QdgutP @0M.7BI3)G Clif, Q,//Isla AtR 10 12 13 EQUIP = AMB AIR + WALL + OUTSIDE AIR 14 WHERE EQUIP Heat generated from equipment or any other source in the room, BTU/HR 18 19 AMB AIR Heat transferred to the ambient room 20 air, BTU/HR 21 22 WALL Heat stored in the room walls, ceiling 23 and floor, BTU/HR 24 OUTSIDE AIR Heat transferred to the outside air, 2

BTU/HR The room amb3.ent temperature and the wall temperature distribution are calculated at fixed time intervals. In addition, total heat stored in the ambient a3.r and in the concrete walls and heat transferred to the outs3.de air are prov3.ded for each time interval.

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L 0 B. Input Required for Computer Model:

The following information is required as input for transient temperature study in the HPSI pump room:

Initial room ambient temperature, degrees F

2. Initial outside ambient temperature, degrees F 10

3. Equipment and other heat generated in the room, BTU/HR Net room surface area, ft 12

5. Net room volume ft

!3 6. Thickness of room enclosure, ft 14 7. Density of room enclosure material, lbs/ft I

8. Thermal conductivity of room enclosure material, BTU/HR-ft-F 17 9. Specif ic heat of room enclosure material, BTU/lb-F 18 10. One period of time increment for calculation, min 19 11. Imaginary thickness of f irst layer of room enclosure, 20 ft 21 12. Multiplication factor of imaginary thickness of other 22 layers 23 24 25 26 27 28 29 30 38 36 I AO 9999.1 7/99

CALCULATIONSHEET PROJECT JpB Np 18601-183 CALC. Np 13 MC-HA-AO2 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOif SHEET NP.

Rav ORIGINATOR'ATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE PZe4 3->II-2 S'-&Pi > 13I-I4 cC IL E LI C. Assumptions for the Computer Model The room is simplified as an enclosed space bounded by the same thickness of walls, ceiling, and floors.

2. The gross room volume is corrected for the volume occupied by piping and equ3.pment.

3. The gross room surface area of the room enclosure 3.s corrected for the area occupied by equipment.

10 4. The enclosure walls, ceiling and floor are taken as a heat sink.

12 13 D. Computer Model Limitations 14

1. The room enclosure walls, ceo,ling and floor must be cons3dered as having the same thickness and of the 17 homogenous material.

18

2. The a3.r temperatures outside the room must be 19 considered as being the same and rema'.ning constant.

20

3. The heat generated within the room must be considered 21 as be3ng constant. No heat generated outside the room 22 can be cons@dered.

23 24

4. The program is limited to 720 time pere.od calculations.

25 26 E. Computer Model Output 27 28 The following information 3.s provided 3.n the computer model 29 output:

30 31 TAF Final room air temperature at each period, 0 F QAT Heat stored 3.n the ambient az.r, BTU QST Total heat stored in the concrete, BTU 34 QOT Heat transferred to the outside air, BTU 35 36 LAO 399$ .1 7/$ 5

CALCULATIONSHEET PROJECT JOB NO 18601-183 NO 13 MC-HA-AO2 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE S54 3-05 -8 5-6'a 8 3

4 VII. STUDY:

This s tudy is per formed for the fol lowing two cases:

A. Fluid temperature in the HPSI pipes of 225 F with no HVAC and room door closed.

10 B. Fluid temperature in the HPSI pipes of 225 F with no HVAC and room door open.

12 13 CASE A FLUID TEMPERATURE IN THE HPSI PIPES OF 225 F WITH NO HVAC AND 16 ROOM DOOR CLOSED:

17 18

1. Heat Loads:

19

a. Electric Motors Heat Load:

20 This heat load consists of the heat generated by the 21 HPSI pump motor and ACU fan motor.

22 23 24

1. HPSI Pump Electrical Motor Heat Load:

26 HPSI Pump design flow = 850 gpm (REF 15) 27 Pump design flow BHP = 885 hp (REF 15)

Motor efficiency, = 94.8" (REF 16) 28 P 29 30 31 36 4 A43 3996,I 1/65

CALCULATIONSHEET PROJECT JOB NO 18601-183 CALC NO 13-MC-HA-A02 SUBJECT TRANSIENT TElPERATURE STUDY FOR HPSI PU1'P ROOM SHEET NO.

Rav ORIGINATOR CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

-~~~Se/4.'ATE r .IO gv2c 6 AJ. P/ $ .~PS )Dl-W 0: U The pump and the motor are inside the HPSI pump room. The fluid is pumped to outside of the room.

Motor lleat load = BHP X 2545 X ~(1- )

(REF 1, note C, table 30, chap 22, page 417) 10 885 X 2545 X (1 0.948) BTUlHR 0.948 12 123,'545 BTU/HR 13 I

14 ii. ACU Fan Motor Heat Load:

The essential ACU fan may be running without essential chilled water thru the essential cooling coils (See 18 Assumption 15) 19 ACU fan nameplate hp = 5 (REF 17) 21 Motor efficiency = 82% (See Assumption 15) 22 23 24 The motor and the driver are both in the HPSI room and 26 the air stays inside the room (i.e. all the fan motor 26 energy remains in the room) .

28 29 30 3 'I 35 36 I AO 3999.I 7/45

CALCULATIONSHEET PROJECT JOB NO 18601-183 NO 1 3 MC HA-A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE L'

/~z~/~i - 2e-'g tp 9-~BI >Dl-4 IL z 0 bJ From ref 1, chap 22, table 30, page 417, eff 5 X 2545 0.82 10 15,518 BTU/HR 12 13 Total motor heat load = 123,545 + 15,518 14 139,063 BTU/HR 17

b. Lighting Heat Loads:

18 The heat load is due to the lighting in the HPSI pump 19 room.

20 21 HPSI pump room area = (20'-6") X (17'-3") (Ref 11) 2 22 20. 5 X 17. 25 FT .

23 353.63 FT 24 Typical lighting load for industrial buildings =

2 26 2 watts/FT (REF 7) 27 28 29 Room lighting load = (Room area, ft ) X (2 watts/ft ) X 3.41 BTU/HR-watt 30 353.63 X 2 X 3.41 BTU/HR 31 2412 BTU/HR 36 36 LAO 1999.1 1/99

ij CALCULATIONSHEET PROJECT JQ8 Np 18601-183 C<l C Np 13-MC-HA-A02 l

TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NP.

ORIGINATOR DATE DATE ORIGINATOR DATE CHECKER DATE I2

-'>d'-~"d'HECKER .IQ 5-zing'EV OI-big 4 C 0

c. Piping Heat Load:

When the HPSI pump is operating; design basis cooling is provided by an 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.

IO The HPSI pump initially supplies cooling water from the I2 refueling water tank. When that source is used, the I3 HPSI pump recirculates water from the containment sump 4

/ to remove decay heat in the core during the time period under study. It is assumed that the HPSI system is operating in both safety injection and long term I7 IS recirculation modes during this time period. The HPSI piping in this room is used for one of these two 20 operating modes. Therefore, all the HPSI piping in the room is used to calculate heat loads.

2I 22 23 24 25 26 27 28 29 30 3I 35 36 LAO 9998. I 7/SS

CALCULATIONSHEET PROJECT JOB NO 18601-183 CALC NO 13-MC-HA-AO2 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

e ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE I

)DI-LI g LE 0 0

This heat load is due to the HPSI pump suction and discharge piping in the HPSI pump room. All of the process piping in this room is insulated.

The following equation can be used to calculate the heat flow thru insulated piping:

10 12 13 14 17 18 19 qs = to ta 20 rs log rs + Rs 21 ro 22 K

23 24 (Ref 1, chap 20, eq 11, page 353) 29 26 27 Nhere qs = Rate of heat transfer per square foot 28 of outer surface of insulation, BTU 29 per (hour) (square foot) .

30 Temperature of inner surface of 31 insulation, degrees F 33 36 LAO 5994,1 7/55

J CALCULATIONSHEET PROJECT JOB NO 18601-183 CALC NO 13-MC-HA-A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE C iO

)nI-4l cC LZ0 Temperature of ambient air, degrees F Outer radius of insulation, inches ro Inner radius of insulation, inches k Thermal conductivity of insulation at mean temperature, BTU per (hour) (square foot) (of 10 per inch thickness)

Rs Surface resistance, (hour) (square foot) 12 (degrees F) per BTU.

13 4 For suction and discharge piping:

Fluid temperature or o = 225 F (See Assumption 1) l7 Ambient air temperature or a = 75 F (See Assumption 18 2) 19 20 Surface resistance, Rs= 0.25 (See Assumption 15) 21 22 Jacket emissivity of the calcium silicate insulation =

23 0.85 e 100 Degrees F (Ref 2) 24 26 Mean insulation temp = 225 + 75 = 150 F 28 29 Thermal conductivity of calcium silicate insulation at 30 150 0 F mean temperature, K =0.40 BTU per (hour) (square foot) 0 31 ( F temp difference per inch thickness) (REF 1, table 3B, chapter 20, page 364).

33 36 I AO 9999.1 9I95

CALCULATIONSHEET

,...PROJECT JO8 NO 18601-183 CAL'C NO 13-.fC-HA-A02 TRANSI NT TM'ERATURI'TUDY FOR HPSI PU. ROO.f SHEET NO n-l ORIGINATOR OATC CHCCKCR OATC RCV ORIGINATOR OATC CHCCK CR 0ATC cz 4'.. 4 S.~S-&y P JIM< HEAP Loh Gs (couT.)

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CV i ORIGINATOR OATC CHCCKCR OATC RCV i ORIGINATOR OATC CHC KCR OA ~ C

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CALCULATIONSHEET PROJECT JP8 NP 18601-183 CALc No 13-NC-HA-A02 TRA ISIENT T~ERATURE STUDY FOR HPSI PUMP ROON SHEET NO.

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DATE REV OR I GlN A TO R DATE CHECKER DATE

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CALCULATIONSHEET PROJECT JOg NO 18601-183 Cgl C NO 13-MC-HA-A02 Ug JECT TRAilS EENT T~ERATURE STUDY FOR HPS I PUMP ROON SHEET NO.

REV ORIOINATOR 'ATE CHECKER OATE REV ORICINATOR OATE CHECKER OATE f~~/f" gg pox p Sis cuazc z ~i> p HEA'T LoA D/

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CALCULATIONSHEET PROJECT JO8 Np 18601-183 cALc Np 13-MC-HA-A02 SUSJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET Np.

REV j~f)~'ATE ORIGINATOR 3-2$ '~"5 CHECKER DATE REV g-CPS'RIGINATOR DATE CHECKER DATE

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d. Heat Dissipated by the HPSl Pump:

10 I/vsQLQ TIOH 12 13 The pump walls are assumed to be flat surfaces (See Assumption 10).

16 The heat dissipated by the pump can be calculated from 17 18 the following equation for flat surface:

19 20 qs = to ta (REF 1,chap 20, page 353, 21 L+ Rs equation 10) 22 23 24 25 Where L= insulation thickness, inch 26 27 Per reference 2, the insulation used on the HPSX pump 28 is mineral wool and is 2" thick.

29 Therefore, L = 2" 30 31 At mean 150 F, the mean temp K = 0.285 (REF 2, exhibit F, section 2C, para F.2.1E)

Rs = 0.25 (For details, see Assumption 16) 35 36 an nnna ~ 7<ay

CA LC U LATI ON S H EET PRpJECT Jp8 gp 18601-183 CALC Np 13-~C-HA-A02 SU8JECT TRANSIENT TEMPERATURE STUDY FOR HPSI PU".P ROON SHEET VP.

REV O R I G IN A TO R DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

,4Q C>.h/+I -cg-N 4l CEu qs = 225 75 20.64 BTU/HR-FT 2 + 0 25 0.285 From ref 14, Surface area of HPSZ pump =

tt X 34 X 42.5 = 33.53 Ft 10 12 12 12 Heat dissipated by HPSZ pump 13 20.64 X 31.53 BTU/HR 651 BTU/HR 16

e. Total Heat Loads:

18 The following is. the sum of the heat loads in the HPSI 19 pump room:

20 21 HPSI pump and ACU fan 22 Electric motors heat load = 139,063 BTU/HR 23 Lighting heat load 2,412 BTU/HR 24 Piping heat load 5,986 BTU/HR 23 Heat dissipated by pump = 651 BTU/HR 26 27 Total Heat Load 148,112 BTU/HR 28 29 "I AO )994.1 3/9$

C CALCULATIONSHEET PROJECT Jp8 Np 18601-183 Np 13-MC HA A02 U B J ECT I TRANS ENT TEMPERATURE STUDY FOR HPS I PUMP ROOM SHEET Np.

REV ORIGINATOR DATE

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N CALCULATIONSHEET PROJECT JQ8 NQ 18601-183 CALC NO 13-MC-HA-A02 SUBJECT TRANSIENT T~ERATURE STUDY FOR HPSI P~a ROO.f SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE ji~<4, 3-wP 5

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CALCULATIONSHEET PROJECT JQQ PO 18601-183 gO 13 MC-HA A02 SUSJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV OR I GIN ATO R DATE CHECKER DATE

.iO 1 8m~//I )Ol-IiI Z 4 L 0

3. Input Data: Case A The following input data for the computer model is used:

Initial room ambient temp. = 75 0 F fAssumption 2]

2. Initial outside ambient temp. = 75 F [Assumption 3]

Equipment and other heat generated in the room = 148,112 3.'.

BTU/HR [See Section VII.A.1.e]

10 Net room surface area = 2232 FT 2 [See Section VII.A.2]

Net room volume = 9152 FT 2 [See Section VII.A.2]

12 6. Thickness of room enclosure = 2.75 FT [Ref 11]

13 7. Density of room inclosure material = 144 LBS/FT3 14 [Ref 6]

8. Thermal conductivity of room enclosure material 0.54 BTU/HR-FT- F [Ref 6]

17 9. Specific heat of room enclosure material = 0.2 BTU/LB- F 18 [Ref 6]

19 10; One period of increment for calculation = 2 min 20 fAssumption 18]

21 11 Imaginary thickness of f irst layer of concrete enclosure 22 0.01 FT [Assumption 19]'2.

23 Multiplication factor of imaginary thickness of other 24 layers = 1.41 [Assumption 19]

25 26 27 28 29 30 3 'I 34 36 I AO 3998,1 7/85

CALCULATIONSHEET PROJECT JO8 NO 18601-183 OP,I C NO 13-MC-HA-A02 SU8JECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE IL f'.m~/4 .)Q

> nI-bl z <

0: 0

4. Results: Case A The transient temperature for the HPSI pump room ambient 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 HPSI pump room will be as follows:

10 12 0 min 75 13 2 min 93.34 4 min 104.10 12 min 117. 79 16 36 min 124.76 17 1 hr 128.66 18 2 hr 135.64 19 145.37 20 6 hr 152.80 21 8 hr 159.07 22 12 hr 169.57 23 24 24 hr 193.35 25 26 27 28 29 30 31 LAO 5998<1 1/85

l CALCULATIONSHEET PRpJECT ~P JpB Np 18601-183 CALC Np 13-MC-HA-A02 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NP.

REV ORIGINATOR CHECKER DATE REY ORIGINATOR DATE CHECKER DATE L j's~e.4.'ATE IQ

)OI-<

14 I2 z0 VII.B CASE B FLUID TEMPERATURE IN THE HPSI PIPES OF 225 F WITH NO HVAC AND ROOM DOOR OPEN:

1. Air Flow Due to Temperature Difference:

When the temperature in a building or a room is different fro that outside, a pressure difference between the inside and th 10 outside occurs as a result of the difference in air density, i.e. due to the chimney effect.

12 13 The air flow due to the temperature difference is calculated 14 follows:

pc = 0.52ph (1 1) [Ref 1, ASHRAE Chapter 19, Page 334 17 To Ti equation 2]

Where pc pressure difference across room enclosure due to chimney effect, inches of water 20 p absolute pressure, psi 21 h .distance from neutral zone, feet 22 To absolute outside temperature, F absolute room temperature, 0 F 24

,26 27 LAO-5999.l 9/55

CALCULATIONSHEET PROJECT JOB Np 18601-183 CpLC Np 13-MC HA AO2 SUSJECy TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NP.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

).lD bJ DI-L' The door opening is 6'-6" X 3'-3" [Ref 13].

Therefore, h = 3'-3" (1/2 the height, assumption 14)

Assuming room temperature of 140 F and outside tempera.ture of 90 0 F, [Assumptions 20 and 21], the pressure difference, pc 0.52 X 14.7 X 3.25 x [ 1 1 ]

460+90 460+140 10 0.52 X 14 7 X 3.25 [ 1 1 ]

12 550 600 13

0. 0037641 inches of water 14 The flow velocity can be expressed equivalent to a velocity 17 head as:

I8 pv = 0.000482V 2 [Ref 1, chap 19, page 333, eq 1]

I9 20 Where pv = velocity head, inches water gauge 21 V = air velocity, miles per hour 22 Thus, 23 0.0037641 = 0.000482V 24 or V = 2.80 miles/hr.

25 26 Quantity of air flow through door opening:

27 Q EAV (Ref 1, chap 19, page 344,equation 6) 28 Where Q air flow, cfm 29 free area of the opening, f t 2 (1/2 height x 30 width, assumption 14) 31 air velocity, feet per minute = miles per hour X 88 effectiveness of opening (0.50 to 0.60 for 34 35 perpendicular flow) 36 LAO $ 998il 7/SS

l CALCULATIONSHEET PROJECT JO8 NO 18601-183 CA LC. NO 13-MC-HA-A02 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR g'HECKER DATE "

DATE REV ORIGINATOR DATE CHECKER DATE 0

SWlh -2f -Zd'-gP

~

>os-M z cf L V 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 8

10 11

2. Heat Loads with Door Open Case B

!2 f3 The heat load generated within the room is the same as in Case 14 A. Nith the door open there is energy transport from the room as a result of the air flow. This energy transport from the room is modelled as a constant over the 24 hour2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months period of 17 interest and is calculated as follows:

18 19 Air flow due to open door = 1301 CFM 20 21 Heat removed = 1.08 X CFM X (Temp Difference) BTU/HR [Ref 22 1, chap 19, page 343, Eq 5]

23 1.08 X 1301 X (140-90) 24 70,254 BTU/HR 25 Heat generated in the HPSI pump room = 148,112 BTU/HR (page 35) 27 28 Net heat load in the HPSI pump room = (148,112-70,254) BTU/HR 29 30 77,858 BTU/HR 31 36 1 AO $ 999.1 7199

CALCULATIONSHEET P ROJECT JOQ Np 18601-183 CALC Np 13-MC-HA-A02 SU8JECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET Np.

REV O R I G IN A TO R DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE BIO f~~(1/ .2d'-BP )

hipO I-

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L'

3. Input Data: Case B All input data for Case B is the same as for Case A on =page 42 except for item j) 3, Room heat load, which is 77,858 BTU/HR.

4. RESULTS: Case B The transient temperature for the HPSI pump room ambient air, obtained from the computer output, is shown in Figure 3. The transient temperature output, Appendix B, shows that, without 12 any HVAC and the pump room door open, the calculated 13 temperature in the pump room will be as follows:

Time Period Tem era ture 0 F 16 0 min 75 2 min 84.93 18 4 min 90.97 19 12 min 99.26 20 36 min 103.37 21 1 hr 105.53 22 2 hr 109.36 23 4 hr 114.69 24 25 6 hr 118.75 26 8 hr 122.16 2l 12 hr 127.88 28 24 hr 140.79 29 30 35 36 I AO S99d.1 7/85

I CALCULATIONSHEET PROJECT JOB NP 18601-183 CALC. NQ. 13 MC-HA-A02 SUBJECT T~SZENT TEMPERATURE STUDY pOR NpSZ p&p ROOM SHEET NQ.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

.IQ 5-Zd'-Pi 0DIcC bl E L 0 I

VII.C CASE C: Verification of Average HPSI Room Temperature:

The average room ambient temperature was assumed to be 140 F for case B. The computer output for the case B (Appendix B) shows that the room temperature is 128 F after 12 hours1.388889e-4 days 0.00333 hours 1.984127e-5 weeks 4.566e-6 months . 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 10 chimney effect was recalculated for 128 F.

1. Air Flow due to Temperature Difference: Case C.

13 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 128 F and outside 17 temp 90 0 F (same as before):

I8 19 pc = 0.52 x 14.7 x 3.25 x [ 1 1 1 20

[460+90 460+128]

21 22 0.52 x 14.7 x 3..25 [ 1 1 ]

23 24

[550 588]

2S 0.0029191 26 27 Calculating an equivalent air velocity and flow as before:

28 29 0.0029191 = 0.000482V 2 [Ref 13, chap 19, page 333, eq 1]

30 Air velocity, V = 2.46 miles/hour 31 Air flow, 9 = 0.5 x( 3.25 x 3.25) x (2.46 x 80) CFM 1143 CFM 36 36 LAO 5991,l 1/55

CALCULATIONSHEET PROJECT JpB Np 18601-183 CAI C Np 13-MC-HA-A02 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET Np.

REV ORIGINATOR DATE

~

4'ATE CHECKER REV ORIGINATOR DATE CHECKER DATE

~ iO

)DI-4l z 4 LL 0

2. Heat Load with the Door Open: CASE C Heat removed through the open door = 1.08 x 1143 (128-90}

1.08 X 1143 X 38 46,909 BTU/HR Net heat load with door open 148,112-46,909 101,203 BTU/HR 10

3. input Data: Case C 12 All input data for Case is the same as for Case A on page 42 13 except for item I 3, Room heat load, which is 101,203 BTU/HR.

14

4. RESULTS Case C Using this heat load, computer model is again run. The result

'18 of this computer run, Appendix C, is plotted on Figure 3. It 19 indicates that the temperature after 12 hours1.388889e-4 days 0.00333 hours 1.984127e-5 weeks 4.566e-6 months is 142 F and. th 24 hour2.777778e-4 days 0.00667 hours 3.968254e-5 weeks 9.132e-6 months temperature is 158.72 F.

20 21 22 The transient temperature for the HPSI pump room ambient air, 23 obtained from the computer output, is shown in Figure 3. The 24 transient temperature output, Appendix C, shows that, without any HVAC and the pump room door open, the calculated 26 27 temperature in the pump room will be as follows:

28 29 30 31 35 36

(

I 1

l

CALCULATIONSHEET JPg NP 18601 183 CA( C NP 13-MC-HA-A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO SO sent'v-sf-O'-R'ROJECT REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

.IQ gg p 9 >pk 14 0:

Zg 0

4. RESULTS CASE C (Continued)

Time Period Tem erature 0F 0 min 75 2 min 87.77 4 min 95.42 12 min 105.64 10 36 min 110.74 1 hr 113.50 12 2 hr 118.40 13 4 hr 125.22 14 6 hr 130.43

!

8 hr 134.80 12 hr 142.14

'17 24 hr 158.72 18 19 21 22 23 24 2$

26 27 28 29 30 31 34 35 36 I AO )998.1 7(SS

CALCULATIONSHEET P ROJECT Jps gp 18601-183 Cp,LC gp 13-MC-HA-A02 W~:

SU/ J EQ7 I TRANS ENT TEMPERATURE STUDY FOR HPS I PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE VX.D CONCLUSXONS: 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 10 underestimation of of the chimney effect.

12 Xn evaluating these results, it is concluded that the average 13 of the calculated transient room temperatures for Cases B R C 14 is a better approximation of the expected results. The average of the results of Cases B S C follows:

17 No HVAC and Room Door Open 18 CASE B: CASE C: Avg B Ec C 19 Time Period .

0F . F 0F

~Tem ~Tem ~Tem .

0 min 75 75 75 21 2 min 84.93 87.77 86.35 22 4 min 90.97 95.42 93.20 23 12 min 99.26 105.64 102.45 24 36 min 103.37 110.74 107.06 2S 1 hr 105.53 113.50 109.52 2 hr 109.36 118.40 113.88 27 28 4 hr 114.69 125.22 119.96 29 6 hr 118.75 130.43 124.59 30 8 hr 122.16 134.80 128.48 31 12 hr 127.88 142.14 135.01 24 hr 140.79 158.72 149.76 35 36 LAO 5995.1 7/85

i

~

CALCULATIONSHEET PROJECT JQB NQ 18601-183 CALC. WQ. 13-MC-HA-AO2 i

SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NQ.

R r. v ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE I2 0 ps~~g '->'-<<c~.4. p -Z>r-g I 0 CL ss iCW71 N OF VEA7 o HPSI PUIWP Rtc HEf.TuP 10 12 13

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21 PUNP 22 23 TOTAL HEPCAT LCIAD E,'TU,'HR 24 148. i THOUSht{D I

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l 3S 36 LAO 3998.1 7/$ 5

CALCULATIONSHEET PRPJECT ANPP JPQNP 18601-183 CALC. Np.

SuBJECTTRANS I ENT TEMPERATURE STUDY FOR HP S I ROOM SHEET Np.

ORIGINATOR CHECKER DATE REV ORIGINATOR DATE CHECKER DATE P<~tk'ATE 3 gg 6 S.e H F': PUMP OQH IAII H UAC' 200

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.'.ANP P 18601-183 13-MC-HA-A02 JOB NO. CALC. NO.

SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE t's eg:

eP~~ f'u~/ Room 200 WI Tl-I N HV uD PEnJ TOO 10

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REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE I's&tI ~-~~-<~ +.4/, Q ~.r.c-PP PzND(x INITIAI INTERNAL ROCK AMBIENT TEHPERATURE ~ DEGe fe'1

>7S INITIAL ADJACENt ROCH AMBIENT TEMPERATURE ~ DEG, Fel

>>75 EQUIPHENt HEAT GEHERAIED IN THE INTERNAL ROCH, 8'IU/HR>7

> IC 8112 MET INTERNAL ROQH SURFACE AREA, SQ, FT, 7

>>2232 NEt INTERNAL ROCH VOL(A(ED CU@FT ~ et 10 >9152 THICKNESS OF ROCH ENCLOSURE, Ft ~ 7

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>.54 SPECIFIC HEAT Of ROCH ENCLOSURE HATERIAL, STU/LB Fa7

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>2 16 IHAGINARY THICKNESS OF FIRST LAYER Of ROQH ENCLOSURE, FT, ~ 7

>.01 17 HULTIPLICATION fACtOR Of IMAGINARY THICKMESS OF OTHER LAYERS 7

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Il CALCV LATION SH EET PROJECT Jpg Np 18601-183 CALC. Np 13-MC-HA-A02 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET Np. +@

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE p~ ~i<.

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>Ol-4I ZO 1'I 12 Ts "~ ~ ~ ~ ~ ~ ~ T(H>1) 77.351 76.728 7d.121 7$ dr 1 7$ .26C 7S.OBC 7S.018 7$ ~ 002 7$ .000 7S.OOO 7$ . 000 7$ .000 rs.ooo rs.ooo rs.ooo 3 pfRlco ahr sese. asr. 9154. Cor. 0 HCI ~ 1.6529 MCO< .0000 TAF ~ 110.31 Tl 12 13 - ~~ ~ 1(kir) 78.573 77.76$ rd.91d 76.136 7$ .5CS 7S.194 7S.OC7 75.007 75.001 7S.OOO 75.000 75.000 rs.ooo rs.ooo rs.ooo d PER!CO CAT~ 6797 CST ~ 2282C. COT> 0, Hcl ~ I 74I19 Mc& .0000 TAFT II7.79 10 1'I ~ t2 ~ 13 ~ T(H+I) 81.471 80.432 79.21'I 77.903 76.688 7$ .769 7$ .250 7$ .051 75.006 75.000 7$ .000 7S.OOO 75.000 75.000 7S.OOO 12 13 12 PERICO ahri 7458. Csr ~ 5178C. OCT ~ 0. MCI ~ 1.7694 HCoi .0000 122,17 TAFT Tl 12 13 ~ " ~~~ ~ T(N>1) 8$ .259 BC.134 82.712 81.014 79.165 77.C16 76.080 75.332 75.061 7S.006 75.000 75.000 16 7S.OOO 75.000 7S.OOO 17 18 ps Rico ahr. rbcr. asr Blair. OCT ~ 0. HClil.7842 MCOa .0000 IA I 124. 76 18 11 ~ 12 ~ 13 ~ ~ "" 1(kir) 19 88.002 lb.b5C 85.366 83.518 81.37579.1CC 77.181 7S 841 7$ .208 7$ .028 7S.002 7S.OOO Zo 7S.OOO 7S.OOO 75.000 21 2C Pf RICO CAT 8159. CST '110326. oaf ~ 0. HCI~1.7963 H~ .0000 22 TAFT 126.85 11 12 13 ~~~~~ T(ktr) 23 90.270 89.110 87.585 85.6$ 2 83.334 80.791 lb.363 lb.C93 7S.C4d 75.078 7$ .007 7$ .000 7S.OOO 7S.OOO 7S.OOO i'. 30 Pf Rico fhf~ 128.66 CAT~ 8429 CST ~ 139678. COT ~ 0. HCI ~ 1.8066 HCO~ .0000 11 ~ T2 ~ 13 ~ -------~ - ~ - ~ -1(Ni))

27 92.248 91.080 89.532 br.scs 8$ .106 82.339 28 79.55C 77.229 75.768 7S ~ 160 7S.017 7S.001 75.000 75.000 75.000 25 30 36 Pf RICO ahri 8669. CST ~ 169058. Cori 0. HCI ~ 1.8159 HCO~ .0000 IAF ~ 130.28 31 Tl T2 13 .". . ~ ~ . ~ ~ " T(kti) 9C.026 92.8SS 91.288 d9.257 86.732 83.796 80.727 78.012 lb.152 7S.277 7S.036 7$ .002 rS.OOO 7$ .000 75.000 42 PfRICO CAT ~ 8889. OSri 198459. Cori 0. HCI ~ I.d2CC HCOi .0000 Thf> 131.77 3$

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CALCULATION SH EET PRPJECT JpB Np 18601-183 CALC Np 13-MC-HA-A02 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NP.

REV ORIGINATOR DATE CHECKER DATE REV ORIGIN ATOR DATE CHECKER DATE

.FO ps~~/4 0'3 I-0 6) 6J A'-~(l-S'S (EI L' Z EE O'

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CALCULATIONSHEET PROJECT JpB gp 18601-183 CaLC. Wp. 13-MC-HA-A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM ~

SHEET NP.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE ISA@,'-~(,-Q c<, ty. pj' Ice pER leo OAT 11333. asr 699568. aor. HCI%1.92CO HCO% .965C IAF% 14$ .53 11 12 13 ~~~~ "".-."1(Htr)

I TC. 17 112.9d 111+31 109.07 106.09 102.22 97.403 91.504 6$ .9CC 60.751 77.167 7$ .5'lr 75.064 75.003 7S.002 lsd PER I CO OAT% I ISCd. OST% 758596. OOI ~ C. HCI ~ 1.9331 HC0% .9659 TAFT 150.01 11 12 13 ~ ~~ ~ T(Htr)

IIS.50 IIC.60 '112.94 110.70 107.69 103.rd 98.894 93.'153 67.05d $ 1.525 77.594 7S.653 7S.058 75.005 75.002 10 16$ PERlco OAT. 11750. aST $ 17631. Ool ~ 7. HCI%1.9419 HC0% .9725 TAT ~ 1$ 1.CS 12 11 12 T3 ~ ~ ~ ~ ~ ~ ~ - ~ ----1(N+I) 117.3$ 116.17 11C.SI 112.26 109.24 105.30 13 100.34 94.C70 68.15C 62.305 78.021 7S.806 7$ .117 7$ .00$ 75.003 4 IIR 180 PERICO OAT ~ 119C6. OST ~ 876672. Ool ~ 10. HCI ~ 1.9504 HC0% .97dl TAFT '152.60 11 12 13 ~ ~ 1(Htr) 11$ .69 117.69 116.03 113.77 TI0.73 106.7d 10'1.74 95.755 89.2CO 83.098 78.Cdr 7$ .973 18 7$ .151 7S.OII 7S.OOS 19 192 PER I CO OAT ~ 12136. OST% 935720. Ool ~ 15. HCI ~ 1.9587 NCO .979d 20 9 'IAF ~ '154.13 lr 12 13 ----- . ~ - ~ --T(N+I)

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21 120.36 119.1S 117.C9 115.23 112.1d 108.1d 103.10 97.010 90.311 83.892 75.929 76.155 22 7S.191 7$ .015 7S.007 23 204 PER ICO OAT ~ 12319. OSI 994771. COT ~ 22'CI AT.9668 NC0% e9836 TAT% 155.C2 11 12 T3 ~ ~ ~ ~~~ l(H41) 2$

121.78 120 ~ 55 118.91 116.6C 113.5$ 109.$ $

IOC.CS 96.238 91.36$ 84.688 79.C04 76.350 26 7$ .23d 75.019 7S.009 27 28 21d PERlco aAI 12C96. asr 1053826. Oor 31. HCI ~ 1.97C7 HC0% .987C TAT% 156.67 29 11 12 13 ~ ~ ~ - ~ ~ ~ ~ - ~ ~ ~ -1(Nir) 123.1d 121.9$ 120.29 116.01 11C.9C 110.69 30 105.72 99.CCO 92.C12 BS.C85 79.893 76.559 rs.rer rs.ors rs.o1 2 31 22$ PER IOO IAF ~ 157.68 Il,T2 12C.SO 13 OAI ~

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123.30 OST%

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119.35 CS. HCI ~ 1.9d2C 116.27 NC0%

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f 6

CALCULATIONSHEET PROJECT JOB NO 18601-183 CALC NO 13-MC-HA-A02 TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGIN A TOR DATE CHECKER DATE

.IQ 0 g~64Z >O-IQI cC CC 0 2CO PER I CO QAT 12836. QSTi 11719C2. QOT ~ Sd. HCT ~ 1.9899 H~ .9951

'IAF ~ 159.07 ll 12 13 " ~ -T(H>I) I 12S.81 124.60 122.93 120.65 117.Sd 113.C7 108.21 101.77 94.457 87.077 80.900 77.012 7S.C07 lb.0C0 7S.018 26C PERICO OAT~ 131Sd. QSTi 129006'I. QOT~ 99. HCI~2.0045 HCOI1.0028 IAfi 161.35 ll,T2, T3 ~ ~ ~~ T(N+I )

128.33 127.12 125.CS 123.15 120.05115.92 110.S9 104.02 9d.CCO 88.661 81.9CO 77.S09 lb.55'I 75.061 lb.02b 10 288 PERICO OATS 13C65. QST~ 1408175. COTE 159. HC!~2.0186 HCO 1.0106 TAT ~ 163.53 11 12 T3 ~ ~ ~ T(H>I) 130.74 129.53 127.85 125.55 122.43 118.27 12 '112.88 106.18 98.388 90.234 83.005 78.04C lb.71b 7S.088 lb.0C0 13 312 PER ICO OAT< 137Sd. QST ~ 1526278. OOfi 245 ~ HCI>2.0322 H~I,0183 TAT ~ 16S.62 Tl 12 13 T(N>I) 16 133.0C 131.83 130,1S 127.85 12C.72 120.53 115.08 108.27 100.28 91.790 78.6'13 17 7$ .908 7S.122 lb.055 18 336 PERICO OAT ~ 14040. QST< 1644362. QOf 362. HCI~2.0454 H~1,0260 19 IAF ~ 167.63 fl 'l2 13 ~~~ ~ - ~~ "T(Ht1) 20 135.26 134.0$ 132.37 130.06 126.92 ~

122.71 117.21 110.30 102.13 93.330 85.185 79.211 7d.120 75 ~ 163 lb.073 IaaR 360 PER I CO QAT ~ IC310. QST 1762C19. OOfi 516. HCII2.0582 HCOII.0336 TAf~ 169.S7 11 T2 13 ~~~ ~~ T(Ntl) 24 137.CO 136.19 13C.SI 132.20 129. 04 124.81 119.27 '112.27 103.93 94.8$ 2 86. 292 79.836 2$ lb.09$

76.3SC 7$ .213 26 C32 PERICO OAT ~ 15068. QST 21163CC. OOT ~ 1279. HCI 2.0948 HCOIT.0560 27 TAF. ITS.04 28 Tl '12 13 ~ ~ ~ ~ T(Nif) 143.43 142.22 IC0.53 138.20 135.02 130.7C 29 12S.09 117.87 109.11 99.302 89.639 81.835 77.170 75.C13 lb.1d2 30 31 504 PERICO OAT ~ 15760. OSIS 246971C. COD 2653. HCI ~ 2.1292 HCOI 1.0773 TAT ~ 180.08 ll 12 13 " ~~~~ T(H>I)

IC8.97 IC7.76 ICd.07 IC3.73 IC0.53 136.20 130.46 123.07 113.98 10'8 92.987 83.973 lb.lCl 7S.69d lb.303 35 QSf 2822301. QOI ~ 4863 HCI 2.1dlb HCO'1.0976 576 PERICO QAT ~ 16COO. ~

36 IAfi 184.77

I h

CALCULATIONSHEET PROJECT Jpg Np CALC. Np 13-MC-HA-A02 18601-183'UBJECT TRANSIENT TEPERATURE STUDY FOR HPSI PUMP ROOM SHEET Np. >DIN-REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE jz>I. z->o4 , I

)I 0

4)

'll ~ T2,13 ~

~ ~ ~ ~ TIHtI) 154.13 152.91 151.22 ICS.SS TC5.66 141.30 135.C9 127.95 118.59 lor.ro 96.307 86.202 79.2CI 76.06$ 7S.CSS 648 PERI CO OAT ~ 16998. QST 3 I 73869. Ool 813$ NCI 2.1929 NCOII 1169 TAFQ 189.18 Tl T2 T3 ~~ ~~ TIHtl)

ISS.97 157.7$ 15deod 153+71 150.CS IC6.09 IC0.22 132.57 122.97 I'Il.dr 99.580 SS.C90 SO.CC9 7d.$ 17 75.647 Q9 ~C 720 PER ICO OAT 17560. OST 3524188. OOT 12691. NCI 2.2229 N~).1351 TAFH I93.35 10 Tl 12 '13 ~ TIHtl) 163.SC 162.33 160.63 IS8.28 155.0C 150.63 ICC.71 136.95 127.17 115.50 102.80 90.S14 81.7C9 77.048 7$ .865 12 13 17 18 20 21 22 23 24 26 27

4 t

CALCULATIONSHEET PROJECT JPg NO 18601-183 CALC. NO. 13-MC- A-A02 SUBJFCT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NO.

REV ORIGINATOR DATE DATE REV ORIGINATOR DATE CHECKER DATE 34.6-P'HECKER P~/Q PJn/ nC 8 INITIAL INTERNAL ROCH ANSIENT TEMPERATURE, DEQ. Fif

>7$

INITIAL ADJACENT ROCK AHRIENT TEMPERATURE, DEQ. Fil

>7$

EOUIPHENT NEAT GENERATED IN TNE INTERMAL ROCH, SIU/MR~7

>>77656 NET INTERNAL ROCH SURfACE AREA, SO. FT.>7

>>2232 10 MET INTERNAL ROCH VOLLNE, CU.FT.>>7

>9152 IMICKMESS Of ROCH ENCLOSURE, FT.>>7

>2 7S 12 DENSITY OF ROCH ENCLOSURE HATERIAL, LSS/CU.FTo>>7

>>ICC 13 THERMAL CONDUCTIVITY Of ROQH ENCLOSURE HAIERIAL, dlU/NR Fl F 7

>.SC SPECIFIC NEAT Of ROON ENCLOSURE MATERIAL, STU/LR FIT ONE PERICO Of TIHE INCREMENT fOR CALCULATION, HIM.>7 16 >2 IMAGINARY THICKNESS OF flRST LAYER Of ROOH ENCLOSURE, FT,>7 17 >>.Ol IKJLTIPLICATION FACTOR Of IHAQIMARY THICKNESS OF OTHER LAYERS 7 18 >1.4'I 20 ~ >> ~ >> ~ >> ~ >> ~ >> ~ >> ~ >> ~ >> ~ >>>> ~ >>>>>>>>>>>> ~ ~ >> ~ >> ~ >> ~ >>>>>> ~ >> ~ >>0>> ~ >> ~ >>>>>>>>>>>>>>>>>>>> ~ >>>>>> ~ >>>> ~ >>>>>>>>>> ~ >> ~

COPTRICNT 1976, 1979 RECMTEL POUER CORPORATION. ALL RIQMIS RESERVED, >>

21 ~>>~ ~ ~ >>~ ~ ~ 0 ~ >>~>>~>>~ ~ >> ~ >> ~ >> ~ >> ~ >>$ ~ I ~ 0 ~ ~ >>>> ~ >> ~ ~ >>1>> ~ ~ >> ~ 0 ~ 0$ ~ >> F 0 ' ~ 0>>>>>>>>>>00 '>>>>>>>>

22 23 24 25 HIMIRISER Of IHAQINARY LATER> IC 26 DXI,DXE,OX3, ~~ ~ DXIH) 1.00000 02 1.41000 02 '1.95610 02 2.60322 02 3.9525C 02 5.57305 02 27 7.65505 02 .11060 .15623 .22025 .31059 .C379C 28 .61749 .65053 29 3o +1']If> I PER I CO OAT ~ )622. OST ~ 973. OOI ~ 0. MCI~1.3923 NCOi .0000 i

'IAf 64.93 31 11,12 13 - ~ ~ *- ~ ~ ~ ---.-TIH>>1) 7S.533 7$ .363 75.214 7S. IOC 75.039 7S.011 7S.OO2 7$ .OOO 7S.OOO 7S.OOO 7S. 000 7S.OOO 7S.OOD 75.000 7S.OOO 34 Ool ~ 0. NCI ~ I.C79C NCO .0000 2 PER)CO OAT ~ 2569. Olla 2601.

35 IAfi 90.97 I I ~ 'll~ 13 ~ TIH>>I) lb.151 7$ .666 7S.563 75.307 7S.132 7S.042 36 1 AO SO'll 1 )/SS

CALCULATIONSHEET PROJECT JQB gp 18601-183 cAt c xo 13-MC-M-A02 SUgJECy TRANSIENT TEtPERATURE STUDY FOR HPSI PUMP ROOM SHEET Np.

REV OR I GIN A TO R DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE c~.4.

7$ .009 75.001 7$ .000 75.000 75.000 75.NO 7S.OOO 7S.OOO 75.000 3 PER I CO OAT< 3168. OST> 4dlb. Ooti 0. NCI ~ 1.5223 NCO .0000 TAF ~ 9C.61 11 ~ 12 ~ 13 ~ - ~ ----------t(Hil) 76.506 7d.39d 75.9dl 7$ .274 7S.097 7$ .024 75.003 7$ .000 7S.OOO 7S.OOO 7$ .000 7$ .000 75.000 d PER I CO OAT ~ 3896. OST 11672. COT~ 0. NCI ~ I.$ 656 IICO .0000 TAF ~ 99. 2d Tl 12 TJ ~ ~ ~~ T(H>1) lb.327 77.789 77.15d 7d. Cb4 75.bbl 7S.391 lo 7$ .127 7$ ,026 7$ .003 75.000 75.NO 7S. 000 75.000 75.000 7S.OOO 12 12 PER I CO OAT~ C313. OST~ 26528. OOI ~ 0. HCI ~ '1.5675 HCOi .0000

'TAF ~ 101.92 13 'Il 12 ~ '13 ~ ~ ~ T(Htt)

~

60.3C2 79. 7S2 79.005 78.121 77.157 76.2C8 75.$ 5d 75.170 7S.031 7$ . 003 7S.ON 7S.OOO 7S.OOO 7S.OOO 7S.OOO 16 ld PERICO OAT ~ CS39. OSt 42173. 0. NCI ~ 'l.5956 NCO .0000 17 TAFT IOJ.J7 TI,T2 '13 ~~~~~ ~ ~ T(H>1) 18 81.794 81.191 80.4'll 79.CC2 78.320 77.154 lb.131 7$ .C35 75.107 75.015 75.001 75.000 19 75.000 7S.OOO 7S.OOO 20 2C PERI CO OAT 471d. OST< S7564. GOT ~ 0. NCI ~ 1.6019 HCO .0000 21 TAT~ 104.SJ 1 I 12 13 ~ -- --------T(Hil)

~ ~

22 d2.991 52.382 81.S82 50.567 79.352 lb.020 76.7SI 7S.776 7S.232 7S.OCO 75.00C lb.0O0 23 7S.OOO 75.000 7S.OOO 24 I HR. 30

~ IAF PER IOO

~ IOS.S3 OAT ~ C673. OSt 72960. 001 ~ 0. HCI ~ 1.6073 NCO .0000 Tl>12,13 ~ ~~~ ~~ T(N>I) 26 52.605 81.56J 80.285 'lb.8!5 8C.03C 53.420 77.3ld lb.161 7S.399 75.083 7$ .000 27 7S.OOO 7$ .000 75.000 28 3d 5011. OST 86412. 001 ~ 0. HCI ~ I.dl21 NCO< .0000 29 PER I CO OAT TAT~ 106.C2 30 Tl ~ T2 ~ 13 ~ " ~ ~ ~ ~ ~ .~ AT(N>I) 64.971 5C.35C 83.532 62.466 81. ICI 79. 601 77.99! ld.572 75.600 7$ .1C4 75.019 75.001 7S.OOO 7S.OOO 75.000 C2 PER I CO OAT ~ 5136. - OSI 103857. NT ~ 0. NCI ~ 1.6165 NCO .0000 IAF ~ 107.24 Tl 12 13'-- ~ - ~ ~ - ~ ~ ----T(Hil) 8$ ~ 629 6S.210 54.381 8J. 296 51.937 60.32d 3$ TS.d27 7$ . 223 7$ .033 7$ . 002 lb.595 ld.99d 7S.OOO 75.000 75.000 36

Il "I

1

CALCULATIONSHEET PROJECT JOB NO 18601-183 CALC NP 13-MC-HA-A02 SU@ JECT REV ps~ g.

TRANSIENT TE1'PERATURE STUDY FOR HPS PUMP ROOM ORIGINATOR DATE z-('-J/.

CHECKER E'ATE I DATE REV ORIGINATOR SHEET NO.

CHECKER DATE 45 PERI CO OA'I 5252 OSTR 1193'll ~ OOT 0. HCI ~ '1.6206 Hm<<,0000 TAF ~ 107.99 1 I, 12, 13 ~ ~ r(H<< I )

66.00C 5$ .170

'b.d2S 84.073 82.683 6'I.0 IC 79.150 77.C26 7d.073 75.317 7S.053 7S.004 7S.OOO 7S.NO 7S.OOO 60 rERIco aht. 54e3. Ost Iso241. Oor 0. HCI ~ 1.6250 KCO .0000 IAfR 109.36 11,12,13>" ~ -- - - -.T(H>I)

~

85.07$ 57.CSI 86.609 55.492 SC.057 52.299 80.301 lb.289 76 606 7S.SC9 7S.'112 7S.012 75.001 7S.OOO 75.000 10

'I I 72PERlm ahri 5652. OSTR ISII92. OOT ~ 0. HCI ~ T.6347 HNE .0000 TAFT 110.60 12 11 12>13> ~ T(H<<1) d9.352 85.757 57.908 86.776 S5.305 53.453 13 51.361 79.140 77.17$ 75.52d 7S.197 75.025 7S.001 7S.OOO 7S.OOO 54 PER ICO OATR Sb25 OSTR 2'12160. OOTR 0. HCI ~ 1.6COS HCO .0000 16 TAFT 111.73 11,12 13 .~ ~ T(H>l) 17 90.582 89.955 59.101 57.95d 56.C64 SC.5d7 52.36$ 79.974 77.762 76.1C2 75.305 7$ .0C4

'I 8 75.003 7$ .NO 7$ <<NO I9 96IERICO ahri 5955. OSTR 243140. oats 0. HCI ~ 1.6466 HCOR .9C52 20 TAT% '112.75 Tl 12 13 - ~ -----------T(H<<T) 21 91.697 91.065 90.211 69.059 67.5CS 55.624 83.320 80.786 78.35S 7d.CSC 7$ .437 7S.072 22 75.006 75.000 75.000 23 105 PER!CO OAT ~ 6135. OST 27C130. Nl 0. KCI ~ 1.6520 HNE .9515 24 TAFT 113.76 11 T2 I3 ~~~~~~ T(H>l) 25 92.743 92.113 91.253 90.093 55.562 56.606 SC.233 51.5ld 75.955 le.546 7S.589 75.109 26 75.010 7S.OOO 7S.OOO 27 25 Cgj.tk 12o PER(Co ahr e277. asr 305129. Oor. 0. HCI ~ 1.6571 HCOE .95CS TAfR IIC.69 ll 12 13 " " ~ ~ ~ ~ ~ ~~~ T(H>'I) 93.73I 93.'101 92.238 91.071 89.526 57.5CO 30 5$ .105 52.344 79.557 77.225 7S.TS9 7S.ISC TS.016 7S.OOI 7$ .000 31 132 PERlm OAT. 6CII. Osl 33dl)5. Oor. 1. HCIR1.6619 HCOR .9577 IAfE 115.57 I I, t2, 13 ~ ~ ~ ------- ~ --T(H>1) 9C.671 9C.040 93.17C 92.002 90.CCS SS.C'33 5$ .949 53.092 50.152 ll.die 75.94d 7S.205 7$ .023 7$ .001 7$ .000 35 36

<<R<<1 1>>>> ~ > 1> ~ 1

ll

'

CALCULATIONSHEET PROJECT JpB Np 18601-183 caLc. No 13-MC-HA-A02 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PAP ROOM SHEET Np.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

+~a.o do

~c c k'// . I 0D)

L')

Wg<

0 ICC PERICO OAT> 6539. OST~ 3671C7. OOT ~ 1. HCI ~ I.bdbb HCO .9605 IAF IIS.CI ll T2 13 ~ T(Ht))

9$ .566 9C.936 9C ~ 069 92.892 91.32C d9.289 66.760 83.8)9 60.7C2 78.01S 76. 146 7S.271 7S.034 7S.002 7$ .001

'ISS pERlco OAT~ bddl osT< 396164, ool~ 2. HCI ~ '1.671'I HCO .9635 TAFH 117.22 7 I'I TZ l3 ." .-~ ~ ~~ ~ T(HtI)

R 96.426 9S.796 94.927 93.7CS 92.166 90m )13 8 67.5CC 64.S29 61.326 lb.423 7d.360 7S.3CZ 7S.OCd 7S.003 75.001 10 ldd pERIco OAT~ 6779. osT~ c29166. OOT ~ 3 ~ NCI ~ I.STSC HCO .9SSC TAF~ 116.00 11,12 T3 ~ ~~~~ ~ ~~ T(Ht))

97.25$ 96.623 95.752 94.567 92.980 90.908 12 66.30C 65.221 81.904 78.83C 7d.58C 7$ .C22 7$ .061 7S.004 7S.OOZ 13

$ H 4 160 PERIOO TAFT OAT<

lid.TS 6892. OST< CS0211. OOT ~ 5. NCI ~ I.S79d N~ .969C li 12 13 -"."".""T(H>I) 96.053 97.C20 9S.SC6 95.360 93.7SS 9'1.677 16 69.040 65.696 62.C74 79.2C9 76.616 75.510 17 7S.079 7$ .005 7S.003 18 192 pERIco OATi 7002. Osl ~ 491240. aol. 6. NCI>1.6836 H~,9724

)9 TAFK 119.47 Tl 12 13 ~ ~ ~~ ~ T(H>l) 20 96.62596.191 97.316 9S.127 9C.52592.C23 d9.756 66.556 63.037 77.061 75.605 7S.100 75.007 7S.003 22 204 pERIco OAT 7107. osT ~ 522271 ~ col 11. Hcl 1.667$ Nco .9755 23 TAFT 120.17 Tl 12 T3 "~ ~~~~~ ~ ~ T(H>I) 24 99.572 96.93d 96.064 96.870 95.262 93.14S 90.CS3 67,202 63.593 80.085 77.311 7$ .706 25 7S.123 75.010 7S.OOS 26 27 216 PER ICO OAT ~ 7210. OST~ 55330C. Oaf i IS. HCI ~ I.d91C HCoi .9785 TAF< 120.6$

28 11 T2 13 ~~ ~ ~ T(H>I) 100.30 99.6SC 98.766 97.592 95.978 93.850 29 91.132 67.834 64.1CI 60.503 77.567 7S.617 TS.1$ 0 7$ .013 75.006 30 31 226 PER ICO aAT 7310. OST ~ 564336. aOT ~ 22. HCI ~ 1.6951 NEO'9817 TAF ~ 121.52 TI,T2 13 ~ ~ T(Ntl) 101.00 100.37 99.C93 98.294 96.675 94.53d 91.795 66.C53 6C.S62 80.922 77.829 'S.933 7$ .160 7$ .017 75.006

>> 8HZ. ZCO PER ICO OAT ~ 7C07. Osl ~ 615373. OOI ~ 29. NCI ~ 1.6966 HCO .964d TAFFY 122.1d 36

\.AA 104 ~ ~ T II%

0 CALCU LATION S H EET PRPJECY JQB Np 18601-183 CALC. Np 13-MC-HA-A02 SUBJECT TRANSIENT TEPERATURE STUDY FOR HPSI PAP ROOM SHEET NP.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE P~c/l

'll 12 13 ~ ~~ ~~~ f(Nt))

101.69 101.06 100.18 98.977 97.35C 95.20C 92.CC2 89.060 d5.216 81.3CO 75.096 lb.05S 75.213 75.021 7S.010 264 PER I CO OAT ~ 7593. OST ~ bllCCd. OOT ~ 51 HCI ~ 1.7058 HCO .9911 TAF~ 123.CO Tl T2 13 ~ ~ T(NtI) 103.02 102.35 101.50 100.30 95.664 9d.C9S 93.696 90.239 86.2d3 82.173 75.643 7d.316 75.289 7$ .032 7S.015 28S PERICO OAT> llll. OSIS 739517. COT~ 82. HCI ~ 1.7126 HCO .9973 IAf~ 12C.59 fl 12 13 -------~ .----T(Hi))

10C.28 103.6C 102.76 101.56 99.916 97.731 9C.898 91.377 87.283 82.999 79.202 lb.597 75.377 7$ .046 7S.021 12 312 PERICO OAT 7941. Od'f 801S83.,001 ~ 127. HCI 1.7191 HCO 1.0036 TAF ~ 125 ~ 73 11,12,13, ~ .~ ~ ~~ " T<Nt))

105.C9 104 ~ 56 103.98 102.76 101.12 98.919 96.056 92.CTS 88.27S . 53.817 79.772 76.89d 7$ .47d 75.06C 75.029 336 PERICO OAT ~ 8104. OST 863639. OSIS IS7. HCI I ~ 725C HCO 1,0098 TAF~

11 T2 13 126.83

"" " ~ ~ - T(Ht1) 106.66 106.02 IOS,IC ,103.93 102.27 100.06 97.174 93.5CC 89.2CS 84.62d 80.3CS 77. 211 7$ .588 7S.OSS 7S.OSS IR H+ 360 PERICO OAT> 8262. OST- 925662. OOf ~ 267. HCI ~ I ~ 7315 HCOi).0160 TAF ~ 127.88 ll 12 13 ~ ~~~ ~ ~~~ t<N>I) 107.79 107.15 106.27 105.05 103.39 101.17 9d.25d 94.S79 90.196 S5.426 80.929 71.539 7S.710 75.111 75.050 C32 PER IOO OAT ~ 8703. OST 1111685. OOT ~ 663. Hcl ~ 1.74el Hco 1.03cl TAFT 130.86 11,12 13 --- ~ - ~ ~ ~ . ---T(Nil)

~

27 I¹C3 105.21

'110.9S 110.32 106.54 10C.2e 101.31 97.520 92.916 87.765 82.66S 78.589 28 76.139 7S.216 75.096 30 504 PERI(O OAT 9107. OST ~ 1297COS. Ool 1375. HCI ~ 1.76Cd HCO*I.OSIC IAF ~ 133.59 31 ll 12 13 " " ~~~ T(H>I) 113.67 113.23 112.3C 111.11 T¹CS 107.16 104.1C 100.26 95.478 90.015 5C.CCS 79.712 lb.6C9 7S.365 75.161 Slb PERICO OAT ~ 9481, OST ~ 146272C. OOT ~ 2519. HCI~1.7799 HCOi).0675 IAF ~ 136.14 35 II ~

'I 2

~ I3 ~ I( H i I )

116.55 115.94 115.05 113. 82 112. 13 109. 54 38

CALCULATIONSHEET PROJECT JpB Np 18601-183 CALC Np 13-MC-HA>>A02 SUBJECT TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET Np.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE pswg -A4~ @p @

~

>Ol-I4 I 0 IC I) 106.78 102.82 97.90'I 92.180 86.193 80.884 77.227 7S.55d 7S.2CC 6Cd PTRICO OAT~ 9832 'sr~ 1667518m Col~ 4211 'CI ~ 1.79C2 HC0*1.0833 TAFT 138.53 11 12 13 TIH+I) 119.12 lid.C8 '117.59 116.36 11C.66 112.35 109.27 10S.25 100.21 94.265 87.913 82.086 77.862 75.795 75 ~ 34S V H~720 PTRIco aAT. 10162. asr Idsrbro. Oor. 6566. HCI >1.8079 HOh1.0980 TAF ~ I CO. 79 11 12 13 ~~ ~~ ~ ~~~ .1(H+I) 121.53 120.89 120.00 118.76 117.06 IIC.74 10 111.63 107.55 102.CI 96.278 89.604 83.307 lb.SCS 76.073 7S.C62 12 13 16 17 18 I9 20 24 36 1 lh ttlg ~ 7 ~~

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CALCULATIONSHEET PROJECT JOB NO 18601-183 CALC NO 13-MC-HA-A02 SU 8 JECT TRANS TENT TEMPERATURE STUDY FOR HPS I PPi'P ROOM'EV SHEET NO. I-)

ORIGIN A TOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE I 0

)Ol-Ii) 8 NDIX C INITIAL INIERMAL ROOH AHSIENI TEMPERATURE, DEQ. f 2

>>7$

INITIAL ADJACENT ROON AHSIENT 1EHPERATURE, DEQ. F>2

>>7$

EOUIPHENT MEAt GENERATED IN THE INTERNAL ROCHe SIU/HRi2

>>101203 NET INTERIIAL ROCH SURFACE AREAe SOe fT ~ it

>>2232 10 NET INTERNAL ROON VOLIAIEe CU fT ~ >2

>>9152 THICKNESS Of RO(XI ENCLOSURE, ft.>2

>2.75 12 DENSITY Of ROOI ENCLOSURE MATERIAL, LBS/CUift.i2

>ICC 13 THERMAL CONDUCT)VIYY Of ROCH ENCLOSURE HATERIALe SIU/MR ft f>2

>.SC SPEClflC MEAT Of ROOH ENCLOSURE HAIERIAL, STU/LS f 2

> 2 CNE PERICO OF TINE )MCREHENT fOR CALCULA'IION, HINe~t IHAGINARZ THICKNESS OF f)RST LAYER Of ROCH ENCLOSURE, fT it

'I 7 >.01 WLTIPLICATIDN fACTOR OF IHAQINART THICKNESS OF DINER LAYERS 2 18 >I.CI T9 20 ~ e ~ 0 ~ e ~ >>>> ~ >>0> ~ > ~ > ~ > ~ >>> ~ > ~ ~ > ~ > ~ ~ > ~ > ~ > ~ >0>>>> ~ > ~ >> ~ > ~ >>> ~ >1>0> ~ > ~ >>>>>

21 i

~ ~ 0 ~ ~ ~ e ~ e ~ 0> ~ ~ e ~ 0 ~ 0 ~ e ~ 0 ~ ~ 0 bete>>> ~ ~ e ~ 0 ~ e ~ e ~ e ~ > ~ e ~ e ~ 0 ~ ~ > ~ 0$ ~ e ~ 0 ~ > ~ 0 ~ e> ~ >>

22 23 24 HeMIRISER Of IMAGINARY LAYER> 1C DXI,DXE,DX3, ~ ~ ~ ~ ~ ~ ~ ~ ~ 'DX(H) 1.00000 02 I.C1000 02 1.98810 02 2.60322 ~ 02 3.9525C 02 5.57306 02

.31059 .C379C

, 7.65605 02 ~ 11080 ~ IS623 .2202S F

.617C9 .65063 g Alai I PER ICO 67.77 OAT 206C. OST 1289, Ool 0. HCI ~ 'I.C371 HCOI .0000 TAFT 11 12 13 ~ ~" ~~~ ~ T(H>I) 7$ .706 75.CSO 7$ .283 75.136 7S.OS2 7$ .01C 7$ .003 7S.000 7S.OOO TS.OOO 7$ .000 75.000 TS.000 75.000 75.000 2 PER ICO OAT 330$ , OS( ~ 3CCI. 001 ~ 0. NCI ~ 1.53C2 HCOI .0000 TAF ~ 95.C2 3$

Il 12 13 ~ ."". ~~ "~ T(H>1) 36 76.582 lb.1CS 7S.7CS 7S.Cob 75.175 7$ .05S LAO 299M,I 2155

t PRPJECT ANPP JpB gp 18601-183 CA( C gp 13-MC-HA-A02 SUBJECT TRANSlENT TEMPERATURE STUDY FOR HPSI PUMP ROOM SHEET NP.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE

, I0

>Ol-0 L')

WgC 7$ .012 7S.002 7S.OOO 7S.OOO 7S.000 7$ .000 7$ .000 7$ .000 7$ .000 3 PER I CO OAT~ C020. OS'I ~ 6099. COT ~ 0. HCI ~ '1.$ 821 H~ .0000 TAFT 99.97 11 12 13 ~ ~ - ~ ~ - ~ ~ --- ~ AT(NiT) 77.38C 76.843 rd.277 7S.757 7S.362 7S.129 7$ .031 7$ .005 75.000 7S.OOO 7S.000 7S.OOO 7$ .000 7S.000 75.000 d PERICO OAI C903. 0$ 1 ~ 15337 OOT ~ 0. HCI ~ I.6329 H~ .0000 TAI. Ios.e(

Tl 12 13 ~ . ~ ~ "- "".T(N+I)

~

79.363 lb.bS9 77.833 76.951 rd.132 75.515 10 n.ler rs.o34 rs.ooc rs.ooo, n.ooo 7S 000 7$ . 000 75. 000 75. 000 12 12 PER I(0 OAT 5C06, OST ~ 35073. OOT ~ 0. HCI ~ 1.65C7 HCO .0000 TAFT I05.90 13 ~ ~ ~~~ - ~ ~ "T(NiT) 11 T2 13 81.970 81.Z02 80.233 79.0 77. BZO re.e33 7$ .728 7$ .224 7$ .041 7S.004 7$ . 000 7S.OOO 7$ .000 7$ .000 75.000 16 18 PER ICO OAT 5689. OST 550)0. OOT ~ 0. HCI ~ '1.6650 NCO<,0000 17 TAf~ '110.74

'll 12 13 ~~~ ~~~ ~ -".T(NII) 18 83.552 83.068 82.052 80.792 79.331 77.813 lb.C7b 7S.569 7S.140 7S,019 7S.OOI 7S.OOO 19 7$ .000 7$ .000 7$ .000 20 24 PER I CO OAT 5915. OST> 75043. OOT o. Hcl.l.erst Nco .oooo TAfI 112.22 11 12 13 ~~~~~ ~" -.T(Ntl) 22 85.405 5C.d13 83.S72 82. 253 BO.672 78,938 77.28C 76.013 75.303 75.053 75.005 75.000 23 75.000 75.000 7S.000

/HR so pERIco oAT ello. osl- 95057. OOT~ 0. He(~I.ebot Ncoi .0000 TAf~ 113.SO 11 12 ~ 13 ~ ~ ~ ~ ~ ~ ~

""" T(N41) 81.683 79.996 86.759 85.962 84.905 83.547 75.095 lb.51S 7$ .521 75.109 7S.OIZ 75.001 7S.OOO 7$ .000 7$ .000 36 PER I(0 OAT 6284. OST ~ I TS)$ 3. Ool ~ 0. HCI ~ 1.686$ N~ .0000 IAfi 114.64 Il IZ 13

~ ~ ~

~ ~ ~ .~~ ~~ --.T(Ntl) 57.9ld 87.17C 65.106 84 719 52.996 80.992 lb.b99 77.0C9 7S.783 75. 185 7$ .024 75.001 75.000 75.000 7S.000 C2 PER I CO OAT ~ 6CC2. OS ~I I35234. OOTi 0. NCI ~ 1.6922 NCor .0000 IAI~ 11$ .65 11 Tt ~ 13 ~ ~ ~ ~ ~ . ~ ~" T(N>T) d9.090 85.286 87.205 8S.800 BC.029 81.93C 3$ lb.0lb n.043 rs.oo3 79.682 77.600 ls ~ 000 7$ .000 7$ .000 I AO )99A

C.

CALCULATIONSHEET ANPP 18601-183 13-MC-HA-A02 P Rp JECT JpB gp CAI C gp TRANSIENT TEtPERATURE STUDY FOR HPSI PUMP ROOM SHEET NP. ~

REV ORIGINATOR DATE CHECKER DATE REV OR I GIN A TO R DATE CHECKER DATE 0 p~iic 4'.8z e 9-4:4 Cb Pf RICO OAT% dS86. QST% ISS327, COT% 0. HCI ~ I.d97S NCO% .0000 116.65 TAF%

11 ~ 12 ~ l3 ~

" ~~ ~~~ ~ T(H<I) 90.12C 69.317 88.232 66.807 6C.999 62.826 60.CC3 lb.160 7d.396 lb.C1C lb.070 7S.006 7S.OOO 7S.OOO 7S.000

~ a. p/< 60 Pf RICO QAT ~ 685C. QST% 195539. QOT 0. HCI ~ 1.7072 NCO .0000 TAFT 118.CO Tl 12 13 ~ ~ T(H%1) 92.008 91.198 90.102 68.650 86.764 64.C96 61.900 79.281 77.092 7$ .7ld 7S.146 75.015 7S.OOI lb.000 7$ .000 IO 72 Pf RICO QAT 7N2. QST 235779 QOT 0. NCI ~ 1.7160 HCO .0000 TAT% 119.96 12 ll 12 - ~ ~~~~ "T(HFI) 13 93.707 92.893 91.790 90.319 68.C I 0 86.037 13 83.276 80.369 77.831 76.076 lb.256 7S.032 14 lb.002 7S.OOO 7S.OOO 8C Pf RICO OAT% 7310. QST% 276040. QOT ~ 0. HCI ~ 1.7241 HC0% .0000 TAf% 12'I.C3 ll 12 13 "~ " " T(HtI)

~~~

17 95.265 9C,CSO 93.340 91.65C 89.913 67.471 8C.581 O'I.C72 78.595 76.C67 7S.396 7S.058 18 lb.004 7S.000 7$ .000 19 96 Pf RICO QAT 7512, QST 316316. OOI 0. NCI ~ 1.7317 NCO% .9C9d TAf% 122.77 Tl 12 13 ~ ~ ~~~ 'l(HFI) 21 96.71C 95.697 94.763 93.265 91.316 88.820 8S.823 82.527 79.370 76.931 lb.569 lb.NC 22 TS.006 75.000 TS.NO .

23 108 Pf R I CO QAT 7701 ~ QS'I 35660$ ~ QOT 0. NCI ~ I.7388 HC0% .9532 24 IAF ~ 124.03 25 11 12 13 ~ ~ ~ T(H+I) 96.074 97.255 96.137 94.629 92.638 90.Nd 26 d7.0N 63.SSC 60.150 77.403 7S.766 7S. IC2 lb.013 7S.OOO 7S.OOO 27 28 't~4 120 Pf RICO TAT% 12$

OAT%

.22 7879, QST% 39690$ . QOI% 0. HC1%1%7CSS NCO 9563 29 ll, I2,13,.-. ~ ~ ~ ~ ~ ~ - ~ ~ AT(HiI) 99.358 98.S39 97.C17 95.900 93.691 91.310 30 88.1C7 84.5SS 80.926 77.895 7$ .986 7S.200 7S.020 lb.001 lb.000 31 132 P(RICO QAT ~ 6046. QSI ~ C37215. COT% I~ HCI ~ 1.7520 HCO% .9593 TAFT 12d.3S Il,T2,13 ~ ~~~ ~ l(HtI) 100.58 99.7$ 9 96.634 97.110 95.06$ 92.C70 69.240 65.525 61.702 lb.CO4 Td.231'S.271 3$ 7$ .031 7S.001 7S.001 36 LAO $$$$ ,l 7/1$

SHEET ('ALCULATlON PROJECT JO8 Np 18601-183 Np 13 MC HA A02 SUBJECT REV ORIGINATOR j >Qg/ >~Md'ATE TRANSIENT TEMPERATURE STUDY FOR HPSI PUMP ROOM DATE CHECKER ck 4. /4 f DATE REV ORIGINATOR g.iP SHEET Np.

CHECKER DATE f 0 O'al-ai CC D ICC PER ICO QATi 8209. OSti C77$ 32. Qoli 1, HCI ~ I 75d2 HCoi .962C TAFi 127,43 Tl 12 '13 ~~~~ ~ - TINCT) 101.7S TAFFY 100.92 99.796 98.267 96.227 93.$ 83 90.295 86.471 d2.C69 78.92C 76.C92 7$ .352 FS.OCC 7S.002 7$ .001 156PERICO aAli 8363. aSti S17855. Qati 3 ~ HCIi1.76CI HCO .9655 12d.CF tl 12 f3 - ~ - ~ --- ~ - ~ ---TINif) 102.86 102.04 100.91 99.376 97.324 94.65C 91.31C 87.393 83.229 79.453 76.769 7S.CCS 75.060 75,003 FSI002 10 168 PERICO QAT SSII QST $ 58183 ~ Qol C. HCI ~ 1.7698 MCoi,9687 TAFi 129.47 Tl 12 13 ~ TIN>1) 103.94 103.12 101.98 100.CC 98.381 95.6S7 12 92.300 88.292 83.980 79.98S 77.061 7$ .5C9 f3 rs.obo n.oos n.oo2 4H+ 180 pERIco QAT 865c. QsT s98517. Qol 7. MCI ~ I FFSC HCoi,9720 TAFT 130.CS ll T2 13 ~ ~ ~ ~ ~ -~ . ~ ." TIN>I) 16 10C.98 104.15 105.02 101.C7 99.COI 96.686 93.258 89.'170 84.721 80. 527 7S.664 17 7S.IOS 7S.N)7 7S.003 16 192 pERIoo QAT 879'I. Qst 638854. QQT 10. Hcf '1.7808 Hco .9753 19 TAT ~ 131.35 1'I 12 l3 ~~~ ~ ~~ ~ TINF1) 20 105.98 105.15 104.02 102.C7 100.39 97.655 94.188 90.028 SS.C53 81.069 77.681 lb.7dd 7S.130 7S.0 I 0 lb.00S 22 204 PER!CO OAT ~ d92C. OSI 679194. Qof ~ 15. HCI ~ 1.7860 HCoi,9786 23 IAFi 132.25 TI 12 13 ----- ~ ~~~ ----TINCT) 24 106.95 106.13 IOC.99 103.CC 101.35 98.596 2$ 95. 094 90. 867 86. 175 S I . 613 78, 006 75,921 7$ .161 FS.0 IS 7S.006 26 27 216 PERICO QAfi 9053 ~ QST ~ 719537. Oot 21. HCI ~ 1.7911 MCO .9819 TAT ~ I33.13 28 Tl 12 13 ~ ~ ~ TINtl) 107.89 107.07 105.93 IOC.37 102.28 99.S11 29 9$ .9rr 91.689 86.888 82.158 78.339 76.064 7S.196 7$ .017 7S.008 30 228 PER I CO QATi 9178. QST i 759882. Qofi 29m HCI ~ I ~ 796 I HCoi .9S53 IAF 133.98 Il 12 13 "~ " "TINil) 108.81 107.99 106.8S 105.29 103. 18 100.40 96.8)d 92.C93 SF.S91 82 FOR 78. 680 re.21c 75.235 F5.022 75.010 35 p gg 2COPERICO QAT. 9300. OSti 800229. Qof ~ 39. HCI ~ 1.8010 HCoi .9887 36 TAFT I34.80 LAO )999.I 1/85

C;,

CALCULATI ON SH EET P RP JECT JpB Np 18601-183 Cp,l C Np 13-MC-HA-A02 S UBJECT TRANSIENT Ti2PERATURE STUDY FOR HPSI Pl&P ROOM STREET WP.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE 0 ) 0I-

. I C)

IOZC

()

'fl 12 13 ~ ~ ~ ~ ~ T(Hit) 109.70 108.88 107.74 106. Id IOC.07 101.27 97.680 93.282 88.28S 83. 245 79.027 lb.373 7$ .278 7$ .027 7$ .013 264 PER ICO QAT ~ 953C. QST> 880923. QOT~ 67. Hcl~l 8104 HCO .9955 lhfi 136.CO 1'I 12 13 ~ ~ ~ T(Nt1)

>>I.C2>>0.60 109.46 107.89 lbs.77 102.95 99.309 94.81S 89.6C6 SC.328 79.738 76.712 75.3rd 7$ .0C2 7$ .019 288 PER I CO QAT 97S7, 1ST< 961615, QOT ~ 108. HCI ~ I.8195 H~1.0024 TAT~ 137.92 10 11 T2 13 ~ T(Ntl)

>>3.07 >>2.2C >>1.10 109.53 107.40 10C.56 100.87 96.295 90.972 SS.C02 80.46$ 77. Olb TS.C90 7S.060 7S.027 12 13 312 PER ICO OAT< 99ll, OST ~ IOC2300. QOT~ idee HCI ~ Io8282 HQh1.0092 TAFT 139.38 Tl 12 13 ~~ ~ T(N>I)

>>4.6S>>3.82>>2.67>>1.10 108.96 106.10 102.38 97.725 92.264 86.C65 81.20S 77.C66 16 7$ .62o rs.083 rs.o)r 17 336 PER 100 QAT 10176. OST>>22970. Qot 2CS. HCI ~ 1.8366 Neo~I.oleo 18 TAFT IC0.79 Tl 12 13 "".- -T(NII)

~~ ~~

19 >>6.16>>$ .33>>4.19>>2.6'I >>0.46 107.59 103.83 99.>>1 93.526 87.517 81.955 77.87$

20 TS.lbs 75.>>'I 7S.050 21 22

/g /4+ 360 PER lao QAT 10373. OSf 1203623. QOT 350. HCI ~ I.SCCS Neo<I.0227 23 TAFT ll 12 13 ""

IC2.14

~ ~ ~ FAT(HII)

>>r.e3 >>e.do >>s.es >>C.ol >>1.91 109.02 lbs.24 100.46 94.758 88.557 82.710 78.302 24 75.1CS 75.065 75.924 25 432 PERICO QAT ~ 10926. QST ICCSCIS. QOT ~ 866. Hclil.Sebi HCO 1.0425 26 TAFT 14$ .96 11 12 13 ---- ~ . ~ ~ - ~ . ~ -T(Hit) 27 121.74 120.91 '>>9.76>>8.17>>d.oo>>3.07 28 I09.2>>04.28 98.29e 91.s98 84.997 79.667 lb.CS2 7S.281 75.125 29 30 504 PERICO QAT ~ >>432. QST ~ I686847. QOti 1797. HCI ~ 1.8898 HCOil.oeIS TAFT 149.47 31 ll T2 13 ---- ---- ~

~ ~~~ T(Ntt) 125 '3 124.70 123.5C 121.95 >>9.76>>6.81

>>2.89 I07.83 101.62 94.522 87.285 81.128

77. Ics ls.c7s 7s.208 Slb PER(CO Qhti 11900. QST ~ 1927747. QOti 3293. HCI<I.9103 HCO 1.0792 IAf< 152.74 3$

11,12 13 ."" " "~ T(N>I) 129,05 128.22 12r.ob 125.46 123.27 120.29 36 LAO 5999,1 7185

]1 k

N

C;:

i CALCULATlONSHEET:

PROJECT JOB NO 18601-183 CALC. NO 13-MC-HA-A02 f

SU 8 J CT TRANSIENT TEMPERATURE STUDY FOR HPS I PUMP ROOi 3 SHEET NO.

REV ORIGINATOR DATE CHECKER DATE REV ORIGINATOR DATE CHECKER DATE jgww< // 3-"<-ai $ 4<PE ) E)l-0 Ol I

IH O 116.32 111.17 104.77 97.336 d9.552 82.650 77.69d 7$ . 72d 7S.31d 646 PERICO OAT ~ 12336. OST 2167957. OOT 5507. HCI F 1.9296 H~1.0962 1AT~ IS$ .61 Tl 12 13 ~ ~~~ ~ ~ ~ T(HII) 132.36 131.53130.37 128.77 12d.56 123.5d 119.5S 'I1C.32 107.77 100.05 91.7d9 84.213 78.72T 76.034 75.446

~ 720 PER I CO OAT 12750. OST 2C07320 ~ OOT 6568. HCI ~ 1.9464 HCOel. 1122 1$ 6.72 TAT TI,T2,T3 " ~ ~~ ~ T(Htl) 135.C9 134.66 133.SO 131.b9 129.68 126.66 10 122.62 117.32 110 63 102.66 93.968 d$ .601 79.609 7d.397 7$ .597 12 13 16 17 18 19 20 21 22 23 24 2$

26 27 28 29 30 31 035 36 I AO )998. I 7/AS

r, 1

ML17304A770: Difference between revisions

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ML17304A770: Difference between revisions

Revision as of 09:48, 29 October 2019

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