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Rev 0 to Calculation V75100.NSP97.00501, Determination of Containment Overpressure Required for Adequate NPSH of Low Pressure ECCS Pumps
	ML20141B934
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Site:	Monticello
Issue date:	06/18/1997
From:	Sparacino J; DUKE ENGINEERING & SERVICES
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ML20141B908	List: ML20141B902; ML20141B911; ML20141B918; ML20141B927; ML20141B934;
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	V75100.NSP97.00, V75100.NSP97.00501, NUDOCS 9706240209
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l FORM DPR-3.2A PAGE 1 OF 1 4

REVISION 1 g' EE5 DukeDagineeriquervica 1

CERTIFICATION OF ENGINEERING CALCULATION PROJECT: Containment Overoressure Reauired for Adeauate NPSH for ECCS. l LOCATION: Monticello Nuclear Generatina Station TITLE OF CALCULATION: Determination of Containment Overoressure Reauired for Adeauste NPSH

-of the Low Pressure ECCS Pumos.

CALCULATION NO.: V75100.NSP97,00501 ORIGINALLY CONSISTING OF:

PAGES THROUGH TOTAL ATTACHMENTS 5 (A. B. C. D. & El '

TOTAL MICROFICHE ATTACHMENTS NONE THESE ENGINEERING CALCULATION COVER QA CONDITION 1 ITEMS. IN ACCORDANCE WITH ESTABLISHED PROCEDURES. THE QUALITY HAS BEEN ASSURED AND 1 CERTIFY THAT THE ABOVE CALCULATIO HAS BEEN ORIGINATED, VERIFIED, AND APPROVED AS NOTED BELOW:

ORIGINATED BY: 3 . s o ela DATE: b //f 7 VERIFIED BY: I. = DATE: d//f/97 APPROVED BY: u 4# DATE: /f 7

> ISSUED FOR QA RECORD STO GE: DATE:

RECEIVED FOR QA RECORD STORAGE: DATE:

MICROFICHE ATTACHMENT LIST: 0 YES O NO SEE FORM DPR-3.2D CALCULAILD PAGES (VOL) ATIACHMLNIS (VOL) V01OMES ORIG VER APPR ISSUE REY. DATF NO. REVISED DELEILD ADDED REVISED t'ELET[D ADDED DLLF',LL ADDED DATE BAIL DATE REC *D DATE O

9706240209 970619 PDR ADDCK 05000263 h i d 6i P PDR

E&S 9

kN Mermnwigsmces j PROJECT: Required Containment Ove. pressure for NPSH FILE NO: V75100.NSP97.00501 l LOCATION: Monticello Nuclear Generating Station CALC.NO V75100.NSP97.00501 j

Calculation Verification Checklist Calculation

Title:

Determination of Containment Overpressure Required for Adequate

. NPSH of the Low Pressure ECCS Pumps, j Revision: 0

1) Were inputs correctly selected and incorporated ? h/N/NA I Are assumptions adequately described and reasonable?

2) h/N/NA

3) Are the appropriate quality and quality assurance requirements specified? @/N/NA

4) Are the applicable codes, standards and regulatory requirements identified and met? hN/NA

5) Have applicable construction and operating experience been considered? Y / N /h

6) Have the design interface requirements been satisfied? @/N/NA ;

l 7) Was an appropriate design method used? hN/NA 1 l 8) is the output reasonable compared to inputs? @ N/NA I

9) Are specified parts, equipment, and processes suitable for the required application? hlN/NA )

10) Are the specified materials compatible with design environmental conditions? Y/N h

11) Have adequate maintenance features and requirements been specified? Y/N @

, 12) Are accessibility and other design provisions adequate? Y/N @

13) Has adequate accessibility been provided to perform the in-service inspection? Y/N h !

14) Has the design properly considered radiation exposure? Y/N/@

15) Are the acceptance criteria incorporated in the design documents sufficient to allow Y/N/b verification?

16) Have adequate pre-operational and subsequent periodic test requirements been Y/N/h specified?

17) Are adequate handling, storage, cleaning and shipping requirements specified? Y/N/

18) Are adequate identification requirements specified? Y/N/$h

19) Are requirements for record preparation review, approval, retention, etc., adequately specified?

Y/N h Verified by/Date:

C- b initials:

[ Verifier REVISION O PAGE 2 PREPARED BY / DATE gl()f g / p CHECKED BY / DATE f// fjjgj47 of /57

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e oems taetngmanngumca PROJECT: Required Containment Overpressure for NPSH FILE NO: V75100.NSP97.00501 LOCATION: Monticello Nuclear Generating Station CALC.NO V75100.NSP97.00501 Design Verification Sheet Client / Project Northern States Power - Monticello Nuclear Generatina Station Reauired Containment Overoressure for Adeauate ECCS NPSH Title of Calculation Determination of Containment Overpressure Reauired for Adeauate NPSH of the Low Pressure ECCS Pumps. i Calculation No. V75100.NSP97.00501 Rev.No. O Design Verification Method: @ Design Review 0 Alternate Calculation O Qualification Testing )

Results of Design Review Ac com u sa'n /RfetvC) l i

l k,& c/n/v

/ Verifier Date REVISION O PAGE 3 PREPARED BY / DATE _fhJ %/S9 CHECKED BY / DATE //J. (,/f 9/4? of /57

) DE&S Naperville, Illinois PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc Not V75100.NSP97.00501 CLIENT Monticello Nuclear Station REFF.RENCE TABLE OF CONTENTS .

Descriotion Pace No. - q Section ,

1.0 Objective 5 2.0 QA Requirements 5 3.0 Methodology 5 4.0 Applicable Codes and Standards 7 .

5.0 Design input 8 6.0 Applicable FSAR Criteria 12 7.0 Assumptions 12 8.0 References 13 9.0 Statement of Suitability 13 4 14 l 10.0 Calculations 11.0 Summary and Conclusions 15 List Of Attachments page 16 A. NPSH AND OVER PRESSURE RESULTS FOR EACH CASE.

page 25 B. FLO-SERIES MODEL PIPING AND NETWORK INPUT AND OUTPUT FOR CASE #1.

page 59 C. FLO-SERIES MODEL PIPING AND NETWORK INPUT AND OUTPUT FOR CASE #2. l D. FLO-SERIES MODEL PIPING AND NETWORK INPUT AND OUTPUT FOR CASE #3. l page 126 E. FLO-SERIES MODEL PIPING AND NETWORK INPUT AND OUTPUT FOR CASE #4. l PAGE 4 REVISION O PREPARED BY/DATE $p yggp OF /5T CHECKED BY/DATE M//'ln/4; I i J

i 1

' l l DE&S !

Naperville, Illinois PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc Not V75100.NSP97.00501 CLIENT Monticello Nuclear Station l REFERENCE 1.0 OBJECTIVE The purpose of this calculation is to determine the containment over pressure that would be required to achieve an adequate Net Positive Suction Head (NPSH) for the '

Core Spray (CS) and Residual Heat Removal (RHR) pumps during different phases :

and scenarios of the Design Basis Accident (DBA), Loss of Cooling Accident (LOCA).

2.0 QA REQUIREMEN IS This calculation covers QA condition 1 items (Nuclear Safety Related).

1 3.0 METHODOLOGY l 3.1 introduction This analysis will use FLO-SERIES software, version 5.01, to run the model of the .

CS and RHR piping systems which was created in DE&S calculation V75100.NSP97.00500," Low Pressure Emergency Core Cooling System (ECCS) g,4 Run Out Flows". Specific data, which is representative of particular Torus and plant conditions will be input into this model in order to achieve pump and system output '

data required for NPSH determinations.

3.2 FLO-SERIES modeling 3.2.1 The FLO-SERIES software methodology uses Bemoulli's equation in determining the system pressures at the node points. When performing the pressure calculation at a node in the system, the fluid velocity value is unknown at that node so it is not factored into the pressure calculation. FLO-SERIES explains this assumption by stating that the fluid velocities in a process system are designed to be fairly constant and therefore the velocity terms will cancel each other ot? in the equation.

This assumption can not be applied in this model. Regardless of changes in fluid velocities within the system, the pressures being calculated need to be corrected for velocity head. In order to determine the correct NPSHA for each pump, the correct pressure at that pump suction must be used. In order to obtain the correct suction pressure for each pump, a cosction must be added which takes into account the effect of velocity head. This conaction consists of adding a fixed resistance REVISION o PAGE 5 PREPARED BY/DATE %gg OF /f7 CHECKED BY/DATE (

\

DE&S Naperville, Illinois PROJECT Monticello Nuclear Station File No: V75100.NsP97.00501 OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station REFERENCE coefficient of 1. This resistance coefficient is used in calculating the head loss and .

is directly related to the velocity in the pipe. This head loss is equal the velocity term in Bemoulli's equation. The correction is placed in the model piping just .

upstream of each pump suction node and corrects the pressure at each pump

suction node by taking velocity into account as a head loss. In the model, this .

correction for the velocity term in Bemoutli's equation is identified as, " Fixed K vel l corctn". This methodology was used in DE&S calculation V609.000.00001 rev. 2, 8.3 l

" Low Pressure Emergency Core Cooling Systems (ECCS) Net Positive Suction i Head (NPSH)".

3.2.2 The "A" suction strainer was chosen to be modeled as the blocked strainer due to the i '

I results of the DE&S calculation V75100.NSP97.00500," Determination of CS and 8.4 RHR system run out flows", which shows that the "A" suction strainer passes the largest amount of flow.

3.2.3 To produce the CS and RHR pump flows specified by each case, a control valve was simulated in the modelline ups. The control valve was set to the specific pump flow for each case. In order to produce the pump run out flows specified in case #1, the model line up does not contain any control valves, which allows the CS and RHR ,

pumps to pump as much flow as the piping system and pump design will allow.

These run out flows are less than the flows determined by DE&S calculation 8.4 V75100.NSP97.00500," Determination of CS and RHR system run out flows". The ,

decrease in pump run out flows is due to the 15% increase in pipe friction loss due to !

aging of the piping as discussed in section 7.3.

3.3 FLO-SERIES results The FLO-SERIES model of the Torus ring header and ECCS piping allows the ,

specified initial Torus conditions, such as pressure and temperature, as well as pump j flows, to be input into the model with the purpose of receiving the outputs needed for the NPSH calculations. The specific FLO-SERIES outputs required for the NPSH calculations are fluid velocity and pressure at the suction of the particular pump.

REVISION o PAGE 6 PREPARED BY/DATE [/Of f/[g OF /O CHECKED BY/DATE

DE&S Naperville, Illinois PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station REFERENCE 3.4 NPSH Calculations :

Given the inputs of fluid velocity and pressure at the pump suction, the NPSH

available to any of the RHR or CS loops (A or B) is calculated using the following equation.

2 87 NPSHA = Hbly - Hva/y + Ps/y + Z + Vs /2g where:

?

NPSHA = net positive suction head available, ft.

Hb = atmospheric pressure,2053.44 lb/ft 2, jg,g Hva = vapor pressure at the specified fluid temp, Ib/ft 2, Ps = pressure of the fluid at the suction of the pump,Ib/ft2, y = specific wei0ht of fluid at pumping temperature, Ib/ft = (1/ specific volume).

Vs = average velocity of the fluid at the suction of the pump, ft/s.

Z = vertical distance between center line of pump and indication of Ps, = 0.0 ft. i

g = 32.2 ft/s2, 3.5 NPSH Details .

Attachment A contains spread sheets which details the NPSH calculations for the CS l

and RHR systems in each case. NPSHA is calculated for each operating pump, at +

the specified time interval and associated temperature, for each case. The pump +

suction pressure and velocity that is determined from the FLO-SERIES results is -

used in the above equation, along with the specific weight and vapor pressure for i that specified temperature, to calculate the NPSHA. The NPSHA is then subtracted '

s from the NPSHR, and that result is the required containment pressure that is needed to satisfy NPSHR.

4.0 APPLICABLE CODES AND STANDARDS This calculation of NPSHA for the low pressure ECCS pumps does not reference .

i.

any codes or standards.

1 1 REVISION O PAGE 'l PREPARED BY/DATE Qg OF /[Y CHECKED BY/DATE

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4

I l DE&S f Naperville, Illinois PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station REFERENCE 5.0 DESIGN INPUT 5.1 Case #1: '

Short Term phase of the DBA LOCA - O to 600 sec (10 minutes).

. Double ended guillotine break of the "B" Reactor Recirculation discharge ' 8.6 piping.

e Failure of the LPCI loop select logic.

. 100 % blockage of the "A" ECCS ring header suction strainer. :

. Head loss of the remaining suction strainers is 1 ft @ 10,000 gpm.

. All CS and LPCI pumps running at run out flows.

. Suppression pool temperatures for the specific time intervals listed .

below, that are listed in Case 1 of reference 8.2. .

PARAMETElS VALUE Atmospheric Pressure 14.26 psia 8.6 Primary Containment Pressure O psig . 8.6 Reactor Pressure O psig : 8.6 Suppression Pool Water Level 908'-9.3" 8.6 "A" CS Pump Flow run out 8.6 "B" CS Pump Flow run out 8.6 "A" RHR Pump Flow run out ; 8.6 "B" RHR Pump Flow run out 8.6 "C" RHR Pump Flow run out 8.6 "D" RHR Pump Flow run out : 8.6 CS NPSHR 33 ft 8.9 RHR NPSHR 27 ft 8.10 Time Temperature Specific Weiaht Vaoor Pressure 86.3 sec 131.8 'F 61.5195 lb/ft' 335.8368 lb/ft* , 8.6, 8.8 2

148.8 sec 137.9 F 61.4119 lb/ft 394.0948 lb/ft 8.6, 8.8 2

212.2 sec 141.6 F 61.3459 lb/ft' 433.4947 lb/ft 8.6, 8.8 2

274.7 sec 143.5 F 61.3121 lb/ft' 454.9824 lb/ft 8.6, 8.8 2

337.2 sec 145.1 F 61.2839 lb/ft' 473.7556 lb/ft 8.6, 8.8 2

399.7 sec 146.4 F 61.2482 lb/ft' 489.5280 lb/ft ' 8.6, 8.8 2

462.2 sec 147.5 F 61.2389 lb/ft' 503.2008 lb/ft 8.6, 8.8 524.7 sec 148.3 F 61.2239 lb/ft* 513.3398 lb/ft* 8.6, 8.8 2

587.2 see 149.1 F 61.2085 lb/ft' 523.6430 lb/ft 8.6, 8.8 599.7 sec 149.3 F 61.2040 lb/ft' 526.2667 lb/ft* . 8.6, 8.8 REVISION O PAGE 8 PREPARED BY/DATE Q g7 OF /6'T CHECKED BY/DATE 4

! DE&S

! Naperville, Illinois

. PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501

. OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station 4

REFERENCE I 1

5.2 Case #2:

Long Term phase of the DBA LOCA greater than 600 sec (10 minutes) .

i

. Double ended guillotine break of the "B" Reactor Racirculation discharge l 8'6 piping. -

. Loss of off-site power. ; j

. Failure of one Diesel G snerator. :

. 100 % blockage of the "A" ECCS ring header suction strainer.: i

. . Head loss of the remaining suction strainers is i ft @ 10,000 gpm. l

. Suppression pool temperatures for the specific time intervals listed ,

I below, that are listed in Case 2 of reference 8.1. :

PARAMETERS VALUE -

l

] Atmospheric Pressure 14.26 psia 8.6 l

Primary Containment Pressure O psig 8.6 i Reactor Pressure O psig: 8.6 1 3 Suppression Pool Water Level 908'-9.3" ,

8.6 l "A" CS Pump Flow 0 gpm : 8.6 "B" CS Pump Flow 2800 gpm (delivered to the core) ,

8.6 "A" RHR Pump Flow 0gpm i 8.6 i "B" RHR Pump Flow 4000 gpm : 8.6 "C" RHR Pump Flow 0gpm 8.6 l "D" RHR Pump Flow 0gpm 8.6 CS NPSHR 29 A 8.9 RHR NPSHR 26 ft 8.10 llme Temperature Specific Weiaht Vapor Pressure l 742.8 sec 152.7 "F 61.1378 lb/ft' 572.3140 lb/ft' : 8.6, 8.8 l 2

2280.1 sec 164.0 F 60.9125 lb/ft' 750.5856 lb/ft 8.6, 8.8 I 2 '

6017.6 see 176.0 F 60.6575 lb/ft' 989.1360 lb/ft 8.6, 8.8 2

15,039.1 sec 188.0 "F 60.3901 lb/ft' 1288.3680 lb/ft 8.6, 8.8 2

21,538.3 sec 192.0 F 60.2954 lb/ft' 1403.5680 lb/ft 8.6, 8.8 2

30,035.6 see 194.0 F 60.2482 lb/ft' 1464.1920 lb/ft 8.6, 8.8 2

33,534.8 sec 194.2 F 60.2439 lb/ft' 1470.4400 lb/ft 8.6, 8.8 2

46,528.1 see 193.0 F 60.2736 lb/ft' 1433.6640 lb/ft 8.6, 8.8 2

, 52,027.3 sec 192.0 F 60.2954 lb/ft' 1403.5680 lb/ft . 8.6, 8.8 2

71,151.1 sec 187.0 F 60.4120 lb/ft' 1260.8640 lb/ft

8.6, 8.8 E

REVISION O PAGE 9 PREPARED BY/DATE (p ggg OF lp l CHECKED BY/DATE

i 4

i DE&S NapervDie, Illinois

\

i PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 i OWNER Northern Stat 4s Powsc Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station l

l '

! REFERENCE 5.3 Case #3: :

Long Term phase of the DBA LOCA - greater than 600 sec (10 minutes).

8.6

. e Double ended guillotine break of the "B" Reactor Recirculation discharge i

piping. l l . Failure of the LPCI injection valve. l i

. Loss of off-site power.

i . 100 % blockage of the "A" ECCS ring header suction strainer. .

l

. Head loss of the remaining suction strainers is 1 ft @ 10,000 gpm. j

e Suppassion pool temperatures for the specific time intervals listed below. that are listed in Case 2 of reference 8.2.

)

PARAMETERS VALUE !

Atmospheric Pressure 14.26 psia ; 8.6 l 1 Primary Containment Pressure O psig -

8.6 Reactor Pressure 0 psig 8.6 l i Suppression Pool Water Level 908'-9.3" 8.6 l "A" CS Pump Flow 2800 gpm (delivered to the core) ,

8.6 l l

l "B" CS Pump Flow 2800 gpm (delivered to the core) -

8.6 "A" RHR Pump Flow 0gpm 8.6 "B" RHR Pump Flow 4000 Opm -

8.6 i "C" RHR Pump Flow 4000 gpm -

8.6 "D" RHR Pump Flow 0gpm . 8.6 CS NPSHR 29 ft , 8.9 RHR NPSHR 26 ft : 8.10 i

E

~ Time Temperaq Specific Weicht Vapor Pressure 742.7 sec 150.2 "F 61.1845 lb/ft' 537.6960 lb/ft* 8.6, 8.8 2

2349.0 sec 159.8 F 60.9979 lb/ft* 679.5360 lb/ft 8.6, 8.8 3 4007.0 sec 164.5 F 60.9013 lb/ft' 759.4920 lb/ft* ; 8.6, 8.8 2

5324.0 sec 167.1 F 60.8472 lb/ft' 807.0077 lb/ft ! 8.6,8.8 2

6299.5 see 168.0 "F 60,8273 lb/ft' 824.0112 lb/ft 8.6, 6.8 7612.5 see 168.4 F 60.8199 lod 831.7238 lb/ft* ' 8.6, 8.8 8925.5 sec 168.7 F 60.8145 ibin' 837.5083 lb/ft* l 8.6, 8.8 3 2 14,579.2 sec 166.3 F 60.8650 lb/0 792.1354 lb/ft 8.6, 8.8

2 28,055.0 see 158.4 F 01.0262 lb/ft 657.1555 lb/ft l 8.6, 8.8 41,793.7 sec 151.3 F 61.1639 lb/ft 552.9499 lb/ft' 8.6, 8.8 i

i i

i f REVISION O PACE 10 PREPARED BY/DATE ///Ji gh OF

/,fy CHECKED BY/DATE

DE&S ;

Naperville, Illinois l

PROJECT Monticello Nuclear Station File Not v75100.NSP97.00501 OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station REFERENCE l

5.4 Case #4:

Long Term phase of the DBA LOCA - greater than 600 sec (10 minutes) .

. Double ended guillotine break of the "B" Reactor Recirculation discharge j 8.6 1 piping.

i e Failure of the LPCl injection valve. .

. 100 % blockage of the "A" ECCS ring head 3r suction strainer. .

. Head loss of the remaining suction strainers is 1 ft @ 10,000 gpm.

. Suppression pool temperatures for the specific time intervals listed below, that are listed in Case 4 of reference 8.2.

l PARAMETERS VALUE Atmospheric Pressure 14.26 psia 8.6 Primary Containment Pressure O psig -

8.6 Reactor Pressure O psig 8.6 Suppression Pool Water Level 908'-9.3" : 8.6 "A" CS Pump Flow 2800 gpm (delivered to the core) 8.6 "B" CS Pump Flow 2800 gpm (delivered to the core) ' 8.6 "A" RHR Pump Flow 4000 gpm 8.6 "B" RHR Pump Flow 4000 gpm 8.6 "C" RHR Pump Flow 4000 gpm 8.6 "D" RHR Pump Flow 4000 gpm 8.6 CS NPSHR 29 ft 8.6, 8.9 RHR NPSHR 26 ft 8.6,8.10 Time Temperature Specific Weicht Vaoor Pressure 724.0 sec 150.5 "F 61.1789 lb/ft' 542.1456 lb/ft' 8.6,8.8 2

1647.3 see 156.0 F 61.0724 lb/ft 620.1792 lb/ft 8.6, 8.8 2

3213.8 sec 159.9 F 60.9961 lb/ft' 681.1488 lb/ft 8.6, 8.8 2

4621.6 see 162.0 F 60.9533 lb/ft' 715.9968 lb/ft 8.6, 8.8 2

5094.8 sec 162.2 F 60.9489 lb/ft' 719.4211 lb/ft . 8.6, 8.8 6475.3 see 162.0 F 60.9533 lb/ft' 715.9968 lb/ft* 8.6, 8.8 2

7894.8 sec 161.0 F 60.9719 lb/ft 699.2064 lb/ft . 8.6, 8.8 3 2 c618.6 sec 159.9 F 60.9961 lb/ft 681.1488 lb/ft 8.6, 8.8 2

11,N9.8 sec 157.7 F 61.0407 lb/ft' 646.1928 lb/ft 8.6, 8.8 2

21,124.8 sec 149.3 F 61.2040 lb/ft' 526.2667 lb/ft 8.6, 8.8 REVISION O PAGE 11 PREPARED BY/DATE //$ (dj$/$7 OF CHECKED BY/DATE 6

DE&S Naperville, Illinois i

l PROJECT Monticello Nuclear Station File No: V75100 NSP97.00501 OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 l CLIENT Monticello Nuclear Station i

REFERENCE 6.0 APPLICABLE FSAR CRITERIA

" Emergency Core Cooling S UFSAR section 6.2, overall description o f the CS and RHR systems. ystems (ECCS)", contains the j l

7.0 ASSUMPTIONS 7.1 The head loss of the ECCS ring header suction strainers a-d the associated Ram's l head was modeled as a 1 foot head loss at 10,000 gpm. The calculated head loss is 8.5 l shown in DE&S calculation V751.NSP97.00502 rev. O, " Head Loss Through ECCS Suction Strainer Assembly".

7.2 CS and RHR system losses are not changed by the change in fluid temperature.

The pump suction pressures which are used in calculating the NPSHAs for each case, do not change enough over the change in suppression pool temperature to significantly change the resultant NPSH, therefore the pump suction pressure used in the NPSHA calculations remains as a constant for each case. The pump suction pressurc that is used in the calculation of the NPSHA, is taken at the lowest -

temperature for that case. As the suppression pool temperature increases, there will -

be less head losses in the piping system, and therefc re a larger suction pressure will result. By using the pump suction pressure at the lowest temperature for that case, -

the result of the NPSHA will be conservative. -

7.3 To model the effects that aging has on the friction factor of a pipe, the lengths of each pipe in the FLO-SERIES model were increased by 15%. The increase in pipe length by 15% will increase the head loss of the particular pipe by 15%, thus -

simulating a 15% increase of the pipe friction factor.

REVISION O PAGE 12 PREPARED BY/DATE %$ Q7 OF

/%

CHECKED BY/DATE i

l DE&S Naperville, Illinois PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station

)

l REFERENCE

8.0 REFERENCES

8.1 Letter GLN 97-019, from P. T. Tran of General Electric Company, to S. J. Hammer 1 of Northem States Power Company, Monticello Nuclear Generating Station, dated May 9,1997, subject: " Revised Analysis of Suppression PoolTemperature and Wetwell Pressure for Limiting Long-term LOCA event for NPSH (Task 6.0)."

8.2 Letter GLN-97-022, from P. T. Tran of General Electric Company, to S. J. Hammer of Northem States Power Company, Monticello Nuclear Gtnerating Station, dated May 30,1997, subject: " Additional Analysis of LOCA Suppression Pool Temperature and Wetwell Pressure for Evaluating NPSH (Task 6.0)."

l 8.3 DE&S calculation V609.000.00001 rev. 2, " Low Pressure Emergency Core Cooling l Systems (ECCS) Net Positive Suction Head (NPSH)".

8.4 DE&S c:siculation V751.NSP97.00500 rev. O, " Low Pressure Emergency Core Cooling Systems (ECCS) Run Out Flows". l l

8.5 DE&S calculation V751.NSP97.00502 rev. O, " Head Loss Through ECCS Suction Strainer Assembly".

8.6 Fax from Pat Tobin of Norther States Power Company, tn Joe Sparacino of DE&S,

Subject:

Inputs for Containment Pressurer/NPSH Evaluation Rev.1, Dated June 15, 1997.

8.7 Pump Handbook,2nd edition,1986, Igor J. Karassik. ,

8.8 ASME Steam Tables, sixth edition, The American Society of Mechanical Engineers.

8.9 Monticeito Station Drawing No. NX-7833-17,18,23, & 24, "CS Pump Curves and Data Tables".

8.10 Monticello Station Drawing No. NX-7905-51,52,53,54,55,56,58, & 59,"RHR Pump Curves and Data Tables".

9.0 STATEMENT OF SUITABILITY This calculation does not involve any materials, parts, equipment, or processes which require a suitability review.

REVISION o PAGE 13 PREPARED BY/DATE p;())6/[h OF /67 CHECKED BY/DATE p

,- - . _ . . .. -. - - .. - . _ . . .. - .. . . _ . .-=_

I l DE&S Naperville, Illinois PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 l

OWNER Northern States Power Co. Calc Not V75100.NSP97.00501 CLIENT Monticello Nuclear Station l

REFERENCE 10.0 CALCULATIONS 10.1 FLO-SERIES modeling The nodal diagram, piping inputs and line up outputs for the low pressure ECCS piping model is contained in attachments B, C, D, and E. The resultant suction pressures and velocities for each pump, in each case defined in the inputs section, 5.0, are listed in Table 10.1 below, in each of the model runs, the High Pressure Core Injection (HPCI) system, and Reactor Core Isolation Cooling (RCIC) system have been isolated from the ring header.

10.2 Table 10.1, shown below, lists the pressure and velocity at the suction of each pump for each case. These pressures and velocities are used to calculate the NPSHA as shown in attachment A.

PUMP PRESSURE VELOCITY Case #1 "A" CS -1.153 psig 12.29 ft/sec "B" CS -1.380 psig 12.0:, Usec "A" RHR -0.109 psig 9.956 ft/sec "B" RHR -0.941 psig 10.07 ft/sec "C" RHR -0.543 psig 10.08 ft/sec "D" RHR -0.555 psig 10.11 ft/sec Case #2 "B" CS 2.108 psig 8.688 ft/sec "B" RHR 2. 399 psig 9.315 ft/sec Case #3 "A" CS 1.938 psig 8.706 ft/sec "B" CS 1.857 psig 8.088 ft/sec "B" RHR 2.127 psig 9.315 ft/sec "C" RHR 2.222 psig 9.315 ft/sec Case #4 "A" CS 1.511 psig 8.706 ft/sec "B" CS 1.177 psig 8.687 ft/sec "A" RHR 0.683 psig 9.279 ft/sec "B" RHR 0.047 psig 9.297 ft/sec "C" RHR 0.327 psig 9.351 ft/sec "D" RHR 0.376 psig 9.332 ft/sec TABLE 10.1 REVISION O PAGE 14 PREPARED BY/DATE g OF /f'?

CHECKED BY/DATE /

DE&S Naperville, Illinois 4

PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station 4

REFERENCE 11.0

SUMMARY

AND CONCLUSIONS 5 11.1 Results: The results of the FLO-SERIES model runs for each case are attached to

, this calculation in each of attachments B, C, D, and E. The pump suction pressure and velocity output results of the models are listed in Table 10.1 for each case. The required containment over pressure results for each pump, which is the difference between the NPSHR and the NPSHA, are ,

listed in Attachment A for each case according to time (elapsed time after l

.. the break of the Reactor Recirculation line) and Suppression Pool temperature. The details of the NPSHA calculations for the different

temperatures in each of the 4 cases are also shown in Attachment A.

l.

11.2

Conclusion:

The over all containment over pressure required for each case, and ,

the pump that it is required for, is listed in Table 11.1 below. These i

pressures were determined by using the largest required containment pressure for each case.

4 CASE REQUIRED OVER SYSTEM PRESSURE PUMP 1 3.9161 psig "B" CS 2 5.6801 psig "B" CS 3 1.4887 psig "B" CS 4 1.3689 psig "B" CS TABLE 11.1 REVISION o PAGE 15 PREPARED BY/DATE % b/ g OF jh CHECKED BY/DATE g

DE&S Naperville, Illinois f

1 j PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc No: v75100.NSP97.00501 l CLIENT Monticello Nuclear Station REFERENCE fl 4

I ATTACHMENT A 4

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NPSH AND OVER PRESSURE RESULTS FOR EACH CASE.

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Requred Spec #c Pressure W) Pressure (Hb) Pump Sucten Velocay v'72(32 7)) Conquement Temperature (T) Weight (Sw)(ItWR) (IbMP) Hva/$w (M ) (:bNt2) HblSw (R ) Pressure (psan) (ft/sec) (R ) NPSHA(9) NPSHR (ft ) System Pump Pressure (psma)

Trne (sec)

() 86 3 131 8 61 $195 335 8368 5 4590 2053 44 2053 44 33 3787 33 3787 1153

-138 12 29 12 05

-0 3534

-0 9755 27 5662 26 9441 33 33

A" CS "B" CS 2 35M 2 6234 Q 86 3 131 8 615195 335 8368 5 4590

-t153 12 29 -0 3582 26 8616 33 *A" CS 2 /457 O t48 8 137 9 64 4119 394 0949 6 4172 2053 44 33 4372 148 8 137 9 61 4119 394 0949 6 4172 2053 44 33 4372 -1 38 12 05 -0 9812 26 0388 33 T CS 3 0156 2 22 1416 61 3459 433 4947 7 0664 2053 44 33 4731 -1153 12 29 -0 36t t 26 0456 33 "A'CS 3 0126 y

= 212 2 141 6 61 3459 433 4947 7 0664 2053 44 33 4731 1 38 12 05 -0 9846 25 4221 33 T CS 3 2828 2747 143 5 61 3121 454 9824 7 4208 205344 33 e"" -t153 12 29 -0 3626 25 7083 33 "A" CS 3 1588 274 7 143 5 61 3121 454 9824 74208 20$3 44 33 (31 -1 38 1205 -09864 25 0844 33 T CS 3 4290 g

a 337 2 145 1 61 2639 413 1556 7 1305 2053 44 33 5070 -t153 12 29 -0 3638 25 4127 33 "A" CS 3 2868 O 337 2 145t 61 2839 413 7556 7 7305 2053 44 33 5070 -1 38 12 05 -0 9879 24 7888 33 T CS 3 5572

- 3997 146 4 64 2482 489 5280 7 9925 2053 44 33 5265 -1153 12 29 -0 3654 25 1688 33 'A'CS 3 3926 Z 3997 146 4 61 2482 489 5280 ?9925 2053 44 33 5265 -1 38 12 05 4 9898 24 5442 33 T CS 3 8631 O 462 2 1475 61 2369 503 2006 6 2170 2053 44 33 5316 .i153 1219 -0 3658 24 9486 33 "A" CS 3 4878 462 2 147 5 61 2389 503 2008 8 2170 2053 44 33 5316 -138 12 05 4 9903 24 3243 33 T C6' 37583 y 524 7 148 3 61 2239 513 3396 63846 2053 44 33 5399 -1153 12 29 -0 3865

-0 9911 24 7887 33 33 "A" CS T CS 3 5511 3 8277 O 524 7 148 3 61 2239 5 0 3398 8 3846 2053 44 33 5399 -1 38 12 05 24 1641 !

O 587 2 149 1 61 2005 523 6430 8 5551 2053 44 33 5483 -t153 12 29 4 3672 24 6261 33 'A" CS 3 6276 O 587 2 1491 61 2005 523 6433 8 5551 2053 44 33 5483 -1 38 12 05 -0 99t9 24 0013 33 T CS 38982 !

" 593 7 149 3 61 2040 526 2667 85986 2053 44 33 5507 -1153 12 29 -0 3674 24 5848 33 "A" CS 3 6455 599 7 149 3 61 2040 526 2667 8 5986 20$3 44 33 $507 -1 38 12 05 -0 9921 23 9000 33 T CS 3 916 I M

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CONTAINMENT PRESSURE REQUIRED FOR ADEQUATE RHR NPSH DURING THE SHORT TERM PHASE OF THE DBA LOCA Vapor Atmosphefee (PstSw + Requered Spec 6c Pressure (Hva) Pressure (Hb) Pump Sucten Velocay V'72(32 2)) Consummere f Twne (sec) Temperature (*F) Wecht (9w)(ItA') (IbNt ) HvaSa(it) 9tA2) Hbtsw (it ) Pressure (pse) (fttsee) (ft) NPSHA (it ) NPSHR (It ) System Pump Prosauro (pse) r O 86 3 131 8 615t95 335 8368 5 4590 2053 44 33 3787 -0109 9 956 1 2640 29 2037 27 "A" RHR -0 9546 ?

N 86 3 131 8 61$195 335 8368 5 4590 2053 44 33 3787 4 904t to 07 -05416 27 3780 27 TR@ -01638 E

86 3 131 8 61 5195 335 8368 5 4590 2053 44 33 3767 -0543 10 08 0 3067 28 2264 27 C RHR -0 5313 86 3 131 8 61$195 335 8368 5 4590 2053 44 33 3787 -0555 to 11 0 2880 28 2077 27 "D" Ree -05232 148 8 137 9 61 4119 394 0949 6 4172 2053 44 33 4372 e 109 9 956 12836 28 3035 27 "A" RFWI -0 5647 N 148 8 137 9 61 4119 394 0949 64172 2053 44 33 4372 -0 9041 to07 -0 5453 26 4746 27 T RtWR 02276 148 8 137 9 61 4119 394 0949 6 4172 2053 44 33 4372 -0543 to 08 0 3045 27 3244 27 C RHR -0 1405 148 8 137 9 614119 394 0949 6 4172 2053 44 33 4372 -0 5% to t1 0 2858 27 3057 27 C R 4t -0 1324 a 212 2 1416 61 3459 433 4947 7 0664 2053 44 33 4731 -0109 9 956 12833 278800 27 "A" RF54 -0 2989 r O 212 2 1416 61 3459 433 4947 7 0664 2053 44 33 4731 -0 9041 to07 -0 5476 25 0581 27 T RHR 04942

.O 212 2 141 6 61 3458 433 4947 70664 2053 44 33 4731 4 543 10 06 0 3031 26 7099 27 "C" R@ 0 1257 !

Z 212 2 141 6 61 3459 433 4947 7 0664 2053 44 33 4731 -0555 10 11 0 2844 26 0911 27 "O" Rt44 0t338

M 274 7 143 5 69 3121 454 9824 7 4208 2053 44 33 4916 -0109 9 956 12832 27 3540 27 *N Rt44 -0 1534 h

9 2747 274 7 143 5 143 5 61 3121 613t21 454 9824 454 9824 74208 74208 2053 44 2053 44 33 4916 33 4916

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-0 543 10 07 10 00

-0 5488 0 3024 25 5220 26 3733 27 27 T RHR "C" RtWI 06402 02715 O 274 7 143 5 61 3121 454 9824 7 4208 2053 44 33 4916 -0 5% to 11 0 2036 26 3545 27 "O"RHR 02796 i O 337 2 145 1 61 2839 473 7556 7 1305 2053 44 33 5070 -0109 9 956 12830 27 0585 27 "N RHR -00258 O 337 2 1451 61 2639 473 7556 7 7305 2053 44 33 5070 -0 9041 to 07 -05498 25 2267 27 T RHR 07882 a 337 2 145 1 61 2830 473 7556 77305 2053 44 33 5070 -0543 to 08 0 3018 26 0783 27 C RHR 03993 337 2 1451 61 2839 473 7556 77303 2053 44 33 5070 4 555 10 11 0 2830 26 0588 27 "D" R>5t 04074 I 3997 146 4 61 2482 489 5200 79925 2C53 44 33 5265 -0 109 9 956 42829 26 8189 27 "N R&54 0 0793 3997 146 4 61 2482 489 5280 7 9925 2053 44 33 5265 -0 9041 to 07 4 5510 24 9830 77 T RHR 08738

> 399 7 146 4 61 2482 4895200 7 9925 2053 44 33 5265 0543 1C08 0 3011 25 4351 27 "C" RHR 05046 3997 146 4 61 2482 489 5280 7 9925 2053 44 33 5265 -0 5% to 11 0 2823 25 8163 27 "D" R&5t 05128 g 462 2 147 5 61 2389 '

503 2006 62170 2053 44 33 5316 -0109 9 956 12829 26 5975 27 "NRHR 01144 g 462 2 147 5 61 2389 74 3 2006 8 2170 2053 44 33 5316 -09041 to07 -0 5513 24 7833 27 T RHR 09889 g 462 2 1475 61 238's "C3 2000 8 2170 2053 44 33 5316 4 543 to 08 0 3000 25 6155 a7 "C" RHR 05998 g 462 2 147 5 612389 503 2006 8 2170 2053 44 33 5316 45% to 11 0 2821 25 5987 27 "D" RHR 0 8079 gy 5247 1ad 3 64 2239 513 3398 8 3846 205344 33 5399 -0109 9 956 12828 26 4380 27 "N M4t~ 02435 Z 524 7 146 3 61 2239 513 3398 83846 2053 44 33 5399 -09041 10 07 -0 5519 24 8034 27 Y RHR 10>2

-1 524 7 1483 63 2239 513 339t> 83846 2053 44 33 5399 4 543 to 08 0 3008 25 4558 27 "C" RHR 0 868 I 524 7 148 3 61 2239 513 3398 83846 2053 44 33 5399 -0 5% 10 11 0 2818 25 4370 27 "D" RHR 0 677 I ,

587 2 149t 61 2005 523 6430 85551 2053 44 33 5483 -0109 9 956 42827 26 2759 27 *N RHR 03 I -

587 2 1491 61 2005 523 6430 85%1 2053 44 33 5483 -09041 to 07 -05524 24 4408 27 T RHR 11086 587 2 1491 61 2005 523 6430 8 5551 2053 44 33 5483 -0543 10 08 0 3003 25 2935 27 "C" RtW4 0 7393 587 2 1491 61 2085 523 6430 85551 2053 44 33 5483 -0 5% to11 0 2814 25 2747 27 "D" RHR 0 7474 +

599 7 149 3 61 2040 526 2667 45986 2053 44 3' 5507 -O 109 9 956 12827 26 2349 27 "N R&#4 03314 599 7 149 3 61 2040 526 2867 85986 2053 44 33 5507 -0 9041 10 07 4 5525 24 3998 27 T RF54 11265 599 7 149 3 61 2040 526 2667 85986 2053 44 33 5507 4 543 10 08 03002 25 2524 27 "C" RHR 07571 g"O 599 7 i49 3 61 2040 526 2867 8598n 2053 44 33 5507 -0 5% to 1i 02813 25 2335 27 "D"RHR 07652 w ,

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TH.E LONG TERM PHASE OF THE DBA LOCA

,ymp Specinc Vapor Atmospherenc Suction (PS/Sw

Requred Weight Pressure Pressure (Hb) HbfSw Pressure Velocdy V'/2(32 2)) Containment Twne (sec) Temperature (*F) (Sa) (fb#t') (Hva) (Ib#t') Hva/Sw (t } ('bM?) (ft ) (psg) (M/sec) (ft ) NPSHA (ft ) NPSHR (It ) System Puig Pressure (paq) L O 742 8 152 7 61 1378 572 3140 9 3611 2053 44 33 5871 2 108 8 688 6 1371 30 3632 29 ? CS 4 5905 t C 2280 1 164 60 9125 750 5856 12 3224 2053 44 33 7113 2108 8 688 6 1555 27 5444 29 7 CS 06305 Q 6017 6 176 60 6575 989 1360 16 3069 2053 44 33 8530 2 108 8688 6 1764 23 7225 29 7 CS 2 2862 g 15039 1 188 60 3901 1288 3680 21 3341 2053 44 34 0029 2108 8 688 6 1986 18 8674 29 7 CS 4 3894 ty, 21538 3 192 60 2954 1403 5680 23 2782 2053 44 34 0563 2 108 8 688 6 2065 16 9846 29 7 CS 52051 30035 6 194 60 2482 1464 1920 24 3027 2053 44 34 0830 2 108 8688 6 2104 15 9908 29 T CS 5 6356 h

On 33534 8 46528 1 194 2 193 80 2439 60 2136 1470 4400 1433 6640 14 4081 23 7859 2053 44 2053 44 34 0855 34 0686 2 108 2 108 8 688 8 688 6 2108 6 2083 15 8881 16 4910 29 29

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T CS CS 56801 5 4189

=* 52027 3 192 6u2954 1403 5680 23 2782 2053 44 34 0563 2 108 8 688 6 2065 16 9846 29 T CS 5 2051 8

71151 1 187 60 4120 1260 8640 20 8711 2053 44 33 9906 2 108 8 688 6 1968 19 3163 29 T CS 4 1950 z '

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Speedic Vapor Atmospherec Sucten (Ps/S*

Requred Weght Pressure Pressure (Hb) Hbisw Pressure Velocdy 8 V /2(32 2))

f Contammert O Tune (sec) Temperature (*F) (Sw) Ob!!t') (Hva) (IbMt') Hva/Sw (ft ) (IbMl2) (ft ) (psg) _ (ft/sec) (ft ) NDSHA @ ) NPSHR (It ) System Pump Pressure (paag)

C 742 8 1527 61 1318 572 3140 9 3611 2053 44 33 5871 2 399 9 315 6 9918 31 2238 26 T RHR -2 2630 Q 2280 1 164 60 9125 750 5856 12 3224 20'.3 44 33 7113 2 399 9 315 70187 28 4077 26 T RHR 10430 g 6017 6 176 60 6575 989 1360 16 3069 2053 44 33 8530 2 399 9 315 7 0425 24 5887 26 T RHR 06114 y 15039 1 188 60 3901 1288 3600 21 3341 2053 44 34 0029 2 399 9 315 70678 19 7366

26 ? RHR 2 7133 21538 3 192 60 2954 1403 5680 23 2782 2053 44 34 0563 2 399 9 315 7 0767 17 8549 26 7 RHR 3 5285 m

30035 6 33534 8 194 94 2 60 2482 60 2439 1464 1920 1470 4400 24 3027 24 4081 2053 44 2053 44 34 0830 34 0855 2 399 2 399 9 315 9 315 7 0812 7 0816 16 8616 16 7590 26 26 T RHR 3 9588 a ? RHR 4 0032 46528 1 193 60 2736 1433 6640 23 7859 2053 44 34 0686 2 399 9 315 7 0788 17 3615 26 TRm 3 7422 8 52027 3 192 60 2954 1403 5680 23 2782 2053 44 34 0563 2 393 9 315 7 0767 17 8549 26 T RHR 3 5285 g 71151 1 187 60 4120 1260 8640 20 $711 2053 44 33 9906 2 399 9 315 70657 20 1852 26 T RHR 2 5190 '

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Case 3 CONTAINMENT PRESSURE REQUIRED FOR ADEQUATE CORE SPRAY NPSH DURING THE LONG TERM PHASE OF THE DBA LOCA rwnp w-Speedic Vapor Atmospheret Sucten (P579w

Requwed Weght (Sw) Pressure Pressure (Hb) Pressure Velocity V't2(32 2)) Contamment Temperature (*F) (IbNt) (Hva)(IbNt') Hva/Sw m ) (IbNt?) HbtSw m ) (psag) (ft/sec) m) NPSHAm) NPSHR ('t ) System Pump Pressure (pass)

Twne (sec)

O T42 7 150 2 61 1845 531 6960 87881 2053 44 33 5614 1 938 8 706 67381 30 $114 29 *A* CS 4 6547 1 742 7 150 2 61 1845 f 37 6960 87881 2053 44 33 5614 t857 8 688 5 5426 30 3159 29 T CS 0 5701 Q 2349 159 6 60 9979 679 5360 11 1403 2033 44 33 6641 1 938 8706 67520 28 2758 29 -A CS 0 3137 g 2349 159 8 60 9979 679 5360 tt1403 2053 44 33 8641 1 857 8 688 5 5560 26 0797 29 T CS 0 3987 -

8,p 4007 164 5 80 9013 759 4920 124109 2053 44 33 7175 1 938 8 706 5 1593 27 0059 29 A- CS 08638 4007 164 5 60 9013 759 4920 12 4709 2053 44 33 71 FS 1 857 8 688 5 5629 26 8095 29 T CS O9488 h

m 5324 5324 1671 16F t 60 64T2 60 8472 807 007F 807007F 13 2628 13 2628 2053 44 2053 44 33 7475 33 7475 1936 1 857 8 706 8 688 57634 55860 26 2400 26 0514 29 29 A- CS T CS 11922 1 2773 d

62995 168 60 8273 824 0112 13 5467 2053 44 337586 1 938 8 106 67649 25 9767 29 -A- CS t3097 6299 5 168 60 8273 824 0112 13 5467 2053 44 33 7586 1 857 8 688 5 5683 25 7801 29 T CS 13949

h 1612 5 1684 60 8199 631 7238 13 6752 2053 44 337627 t 938 8 706 5 7654 25 8529 29 A CS 13633 h 7612 5 168 4 808199 631 F238 13 6752 2053 44 2053 44 33762F 331657 1 857 1 936 8 688 8 706 55688 57659 25 8562 25 7800 29 29 T CS

A*CS 14485 14036 1 89255 1687 60 8143 637 5083 13 F116 89255 1687 606t43 637 5083 13 7716 2053 44 33 765F 1 857 8 688 5 5802 25 5634 29 T CS 14887

14579 2 166 3 80 8650 792 t354 13 0146 2053 44 33 F376 1 938 8 106 57620 26 4850 29 A CS I0895 t4579 2 166 3 158 4 60 8650 61 0262 792 1354 657 1555 13 0146 10 7684 2053 44 205344 33 7376 33 6485 1 857 t936 8 688 8 706 5 5655 5 7499 262885 28 6300 29 29 T CS

A- CS 1+F46 O1603 20055

$ 20055 158 4 61 0262 6571555 to 7684 2053 44 33 6485 33 5727 1 857 1 938 6 686 8 706 5 5539 57396 28 4340 30 2719 29 29 T CS A%S O2452 4 5510 41793 7 151 3 61 1639 552 9499 9 0405 2053 44 41793 7 151 3 61 1639 552 9499 9 0405 2053 44 33 5727 1 857 8 688 55441 30 0763 29 T CS -0 4663 ,

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Case 3 CONTAINMENT PRESSURE REQUIRED FOR ADEQUATE RHR NPSH DURING THE LONG TERM PHASE OF THE DBA LOCA nrep we Spec @c Vapor Atrnosphetene Suchon (Ps73w + Requred weight (Sw) Presswe Pressure (Hb) Pressure Vebc4y V'72(32 2)) Co h O Twne (sec) Temperature (T) (ItAi (Hva) (IbNt') HvafSw M ) (IbNt2) Hbr9w M ) (psm) M7sec) M) NPSHA M ) NPSHR M ) System Pump Pressure (pse)

E 742 7 150 2 61 1845 537 6960 8 7881 2053 44 335614 2 127 9 315 6 3533 31 1266 26 T RHR -2 2209 Q T42 7 150 2 61 1645 537 6960 67881 2053 44 335614 2 222 9 315 6 5769 31 3502 26 VRW -2 3177 g 2349 1594 60 9979 679 5360 11 1403 2053 44 33 6N1 2127 9 315 6 3686 28 8924 26 tR@ -1 2530 y 2349 1598 60 9979 679 5360 11 1403 2053 44 33 6641 2 222 9 315 6 5929 29 1167 26 V RHR -1 3501 4007 164 5 60 9013 759 4920 t2 4709 2053 44 337175 2 127 9 315 6 3766 27 6232 26 t RHR 4 7032 h

Ot 4007 5324 164 5 1671 60 9013 60 6472 759 4920 807 0077 12 4709 13 2626 2053 44 2053 44 33 7175 33 7475 2 222 2 127 9 315 9 315 6 8012 6 3811 27 8478 26 8857 26 26 V Rt44 T RHR 08005 4 3750

$ 5324 62995 167 1 168 60 8472 60 8273 807 0077 8240t12 13 2626 135467 2053 44 2053 44 33 7475 33 7586 2 222 2 127 9 315 9 315 66059 6 3827 27 0905 26 5945 26 26 V RHR T RHR

-0 4724

-0 2576

O g 6299 5 168 60 8273 824 0112 13 5467 20$3 44 33 7586 2 222 9 315 6 6076 26 8194 26 V RHR 4 3550 (t) 76125 168 4 608199 831 7236 13 6752 2053 44 33 7627 2 127 9 315 6 3833 26 4708 26 T RHR -02039 1 7612 5 168 4 60 8199 831 7238 13 6752 2053 44 33 7627 2 222 9 315 6 6083 26 6957 26 V RHR -0 3014

$ 89255 8925 5 168 7 168 7 608143 60 8143 837 5083 837 5083 137716 137716 2053 44 2053 44 33 1657 33 7657 2 127 2 222 9 315 9 315 6 3638 6 6087 26 3700 26 8029 26 26 t RHR V RHR

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O 14579 2 166 3 60 8650 792 1354 13 0146 2053 44 33 1376 2 127 9 315 6 3796 27 1026 26 T RHR -0 4776 14579 2 166 3 60 8650 192 1354 13 0146 2053 44 33 7376 2 222 9 315 66044 27 3273 26 V RHR -0 5750

.O' a 280$5 1584 61 0262 657 1555 10 7664 2053 44 33 6485 2 127 9 315 63663 29 2464 26 T RHR -14063 20055 1584 61 0262 6571555 to 7664 2053 44 33 6485 2 222 9 315 65905 29 4705 26 V RHR -15034 41793 7 15t3 61 1639 552 9499 9 0405 2053 44 33 5727 2127 9 315 6 3550 30 8673 26 t RHR -2 1172 41793 7 151 3 61 1639 552 9499 9 0405 2053 44 33 5727 2 222 9 315 65787 39 1109 26 V RHR -2 214%

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Spec 6c Vapor Atmosphereec Pump Sucten Requeed Weght (Sw) Presswe Pressure (Hb) Pressure V'72(32 2)) Contamment 8

Trne (sect Temperature (*F) (M )

8 (Wa)(M ) Wa/%v@) (ItA2) Hb/Sw M ) (pse) Veiocity (fUsec) m) NPSHA M) NPSHR (ft ) System Pump Pressure (paq)

O g 724 1505 61 1789 542 1456 5%6 2053 44 33 5645 1 511 8 706 4 1335 29 4363 29 *A*CS 4 1890 g 724 150 5 61 1789 542 1456 4- t 2053 44 33 5645 t 177 8 687 3 9422 28 6450 29 T CS O1538

% 1647 3 156 0 61 0124~ 620 1792 101xa 2053 44 33 6230 t 511 8 706 4 7397 28 2079 29 *A*CS O 3432 2 1647 3 1560 ~6iM24 620 1792 to 154d 20$3 44 33 6230 1 177 8 687 3 9470 27 4152 29 T CS O6865

N 3213 8 159 9 60 9961 681 1488 11 1671 2053 44 33 6651 1 511 8706 4 7441 27 2421 29 *A"CS O7615 32138 159 9 60 9961 681 1488 11 1671 2053 44 33 6651 1 177 8 687 3 9505 26 4485 29 T CS 11053

, 4621 6 1620 60 9533 715 99b8 in 7466 20$3 44 33 6887 1 Sit 8106 4 7466 26 6887 29 "A"CS 10013 ;

.,a 4621 6 1620 60 9533 715 9968 11 7466 2053 44 33 6887 1 177 6687 3 9524 25 8945 29 ~B* CS 13453 O 50948 162 2 60 9489 719 4211 11 8037 2053 44 33 6912 1 511 8 706 4 7469 26 6344 29 "A'CS 10248 N $094 8 162 2 60 9489 719 4211 11 8037 2053 44 33 6912 1 til 8 687 3 9526 25 8401 29 'B CS 1 3689 ,

6415 3 162 0 60 9533 715 9968 11 7466 2053 44 33 6887 1 511 8 706 4 7466 26 6887 29 *A CS 1 0013

? CS 13453 '

y 6475 3 1620 60 9533 715 9968 11 7466 2053 44 33 6887 1 171 8 687 3 9524 25 8945 29 e 18948 1610 60 9719 699 2064 11 4617 2053 44 33 6785 1 511 8706 4 1455 26 9563 29 "A" CS O8853

.N 7894 8 1610 60 9719 699 2064 11 4677 2053 44 33 6785 1 177 8 687 3 9516 26 1624 29 T CS 12293 (M

9618 6 9618E 159 9 159 9 60 9961 60 9961 681 1488 681 1488 11 1671 11 1671 2053 44 2053 44 33 6651 33 6651 1 511 1 177 8 106 8 687 4 7441 3 9505 27 2421 26 4485 29 29 "A CS T CS O7615 11053 3 11749 8 157 7 61 0407 646 1926 10 5863 2053 44 33 6405 1 511 8 706 4 1415 27 1957 29 *A' CS O5217 11749 8 1577 61 0407 646 1928 to5863 2053 44 33 6405 1 117 8 687 3 9484 27 0027 29 T CS O8652 i 21124 8 149 3 61 2040 526 2667 8 5986 2053 44 335501 1 511 8706 4 1320 29 6842 29 *A CS -02964 !

21124 8 149 3 61 2040 526 2667 8 5986 2053 44 33 5507 1 177 8 687 3 9410 28 8932 29 T CS O0463 M

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Case 4 I I i l i l l l I i l I i CONTAINMENT PRESSURE REQUIRED FOR ADEQUATE RHR NPSH DURING THE LONG TERM PHASE OF THE DBA LOCA Sg:ec#c Vapor Atmospherec Pump Suctori (Ps/Sw + Requeed Weght (Sw) Pressure Pressure (Hb) Pressure v't2(32 2)) Cortawnert Tune (sec) Temperature (T) 3 ObM ) (Hva) Ob/f) Hva/Sw M ) ObM2) Hb/Sw M ) (psc) Veloc4y @/see) @) NPSHA M ) NPSHR @) System Pump Pressure (psc) g 724 150 5 61 1789 542 1456 8 8616 2053 44 33 5645 0688 9 279 2 9563 27 6592 26 "WRHR 4 7188 g, 724 150 5 61 1789 542 1456 8 8616 2053 44 33 5645 0 047 9 297 1 4528 26 1556 26 T RHR 4 0674

~~

724 150 5 61 1789 542 1456 8 8616 2053 44 33 5645 0 327 9 351 2 1775 26 8303 26 "C" RHR -03%7 724 150 5 61 1789 542 1456 8 0616 2053 44 33 5645 0 376 9 332 2 2373 26 9401 26 *O"RHR -04073 2 1641 3 156 0 61 0124 620 1792 10 1548 2053 44 33 6230 0 688 9 279 2 9592 26 4214 26 rRHR 4 1851 N 1647 3 156 0 61 0724 620 1792 10 1548 2053 44 33 6230 0 047 9 297 1 4530 24 9212 26 7 RHR 04673 eC 1647 3 156 0 61 0724 620 1792 10 1543 2053 44 33 6230 0 327 9 351 2 1288 25 5970 26 V RHR 01746 y.a 1647 3 3213 8 156 0 1$9 9 61 0724 60 9961 620t792 681 1488 to 1548 11 1611 2053 44 20$3 44 33 6230 33 6651 0 376 0688 9 332 9 229 2 2388 2 9612 25 7070 2$ 4592 26 26 "O'RHR

WRHR 01269 0 2343 O 32138 159 9 60 9961 681 1488 11 1671 2053 44 33 6651 0 047 9 297 1 4531 23 9511 26 7 RHR 06876

.O 3213 8 159 9 60 9969 681 1488 11 1611 2053 44 33 665t O 327 9 351 2 1298 24 6218 26 C RHR 05944 3213 8 159 9 60 9961 681 1488 11 1671 2053 44 33 6651 0376 9 332 2 2399 24 7380 26 "O"RHR 0 5467 g 4621 6 1620 60 9533 715 9968 111466 2053 44 33 6887 0688 9 279 2 9623 24 9044 26 *W RHR 04746 to 4621 6 1620 60 9533 715 9968 11 7466 205344 33 6887 0 047 9 297 14532 23 3953 26 T RHR 11284

.N 4621 6 1620 60 9533 715 9968 11 7466 20$3 44 33 6887 0 327 9 351 2 1303 24 0724 26 "C" RHR 0 83*O O 4621 6 162 0 60 9533 715 9968 11 7466 2053 44 33 6881 03/6 9 332 2 2406 24 1827 26 W RHR 0 7813 Us 50948 162 2 60 9489 719 4211 118037 20$3 44 33 6912 0688 9 279 2 9624 24 8500 26 *A" RHR 04982 O $094 8 162 2 60 9489 719 4211 11 8037 2053 44 33 6912 0 047 9 297 1 4532 23 3407 26 *B"RHR 11520 5094 8 162 2 60 9489 719 4211 11 8037 2053 44 33 6912 0 327 9 351 2 1304 24 0179 26 "C" RHR 08587 50948 162 2 60 9489 719 4211 11 8037 2053 44 33 6912 0 376 9 332 2 2406 24 1281 26 "D'RHR 08109 6415 3 162 0 60 9533 715 9968 11 7466 20$3 44 33 6881 0 688 9 279 2 9623 24 9044 26 C HHR 04146

> 64 ?$ 3 1620 60 9533 715 9968 11 7466 2053 44 33 6887 0 047 9 297 14532 23 3953 26 T RHR 11284 6415 3 1620 60 9533 715 9968 11 7466 2053 44 33 6887 0 327 9 351 2 1303 24 0724 26 *C"RHR 0 8350 y 6475 3 1620 60 9533 715 9968 11 7466 2053 44 33 6887 0 316 9 332 2 2406 24 1827 26 "D'RHR 07873 0 7894 8 1610 60 9719 699 2064 11 4611 20$3 44 33 6785 0688 9 279 2 9618 25 1726 26 *C RHR 03584 T 78948 1610 60 9719 699 2064 11 4677 20$3 44 33 6185 0 047 9 297 1 4531 23 6639 26 8"RHR 1 0120 E 7894 8 1610 60 9719 699 2064 11 4617 2053 44 33 6785 0 327 9 351 2 1301 24 3409 26 "C" RHR 07187 ITI 7894 8 161 0 60 9719 699 2064 11 4677 2053 44 33 6785 0 376 9 332 2 2403 24 4511 26 "D'RHR 067to Z 9618 6 159 9 60 9961 681 1488 11 1611 20$3 44 33 6651 0688 9 219 2 9612 25 4592 26 'N HHR 0 2343 d % 18 6 159 9 60 9961 681 1488 11 1671 2053 44 33 6651 0 047 9 297 1 4531 23 9511 26 8" RHR 08876 9618 6 159 9 60 9961 681 1468 11 1671 2053 44 33 6651 0 327 9 351 2 1298 24 6218 26 *C" RHR 05944 h 9618 6 159 9 60 9961 681 1488 11 1671 2053 44 33 6651 0 316 9 332 2 2399 24 7380 26 "O-RHR 05467 11749 8 151 7 61 0407 646 1928 to $663 2053 44 33 6405 0688 92/9 2 9600 26 0142 26 *C RHR 4 0u62 11749 8 1577 61 0407 646 1928 10 5863 2053 44 33 6405 0 047 9 297 1 4530 24 5073 26 v RHR 06467 11749 8 157 7 61 0407 646 1928 10 5863 2053 44 33 6405 0 327 9 351 2 1292 25 1834 26 *C'RHR 0 3537 11749 8 157 7 61 0407 646 1928 10 5863 2053 44 33 6405 0 376 9332 2 2393 25 2935 26 V RHR 03061 T 21124 8 149 3 61 2040 526 2661 8 $986 2053 44 33 5501 0 688 9 219 2 9557 27 9019 26 rRHR -O8265 h 21124 8 149 3 61 2040 526 2667 85966 2053 44 33 5507 0 047 9 297 1 4527 26 4049 26 T RHR -0 1754

$ 21124 8 211248 149 3 149 3 61 2040 61 2040 526 2667 526 2667 8 5986 85986 2053 44 2053 44 33 5507 33 5507 0 327 0376 9 351 9 332 2 1211 2 2369 27 0793 27 1891 26 26

'C" RHR O"RHR 44676

-05151 R

o

-=

\

Page 2

! DE&S Naperville, Illinois j PROJECT Monticello Nuclear F,tation File No: V75100.NSP97.00501 .

Calc Not V75100.NSP97.00501 l

, OWNER Northern States Power Co.

CLIENT Monticello Nuclear Station

\

l REFERENCE l

1

! ATTACHMENT B i

j FLO-SERIES MODEL PIPING AND NETWORK INPUT AND OUTPUT FOR CASE #1.

l l

I l

l PAGE 25 REVISION O PREPARED BY/DATE /Q 646/77 OF /[T CHECKED BY/DATE /

TB g g TA TD qp gp TC B A D 8:_ H4e g4f H_52, _ H5 4 H51 j(4Qg H6a _ 33 H4a2, 9 SB 10 11 SC 12 ,

46a1

_ HP.tN RC.tN yp -

" I B.CS IN B RH.IN A.RH.tN A.CSIN ,H6b2 g

d >

[hU@ -h W NW[ k :" NN S* (>

E 7 6 5 4 SA 3 2 120 191ESD 17 16 '

g 'A 14 2 B.CS.T ~ ' _CS0018 i -:: A.CS.T p HP001

$ RH001 RC001 g 1. CS0038 g 1

CS003A 9.[S.SUCT A.CS.SUDI gg ,

RC.T q, HP.T q p :g g HP002 RH001A A.RH.T RC002 o B.RH.T q r ' e o

RH003). C.tN A.tN

.$.a 1tHOO3B '

D IN B.IN -*O RHg RC.SUCT hp a> o*-

, RH0048 p RH004A 4

,3 _ _

O B.SUC C.SUC I

E m

Z RHOO5B _.

RH005A g

CDStB O.SUC A.SUC CS01A CRHR

^"""

s @ """ g/) ( \

A.CS

% ScS e

Q RH0060 RH006B RH006C RH003A Company: Duke Engineering & Services 06/11/97 4:56 pm Project: Linelist: OVRPRES1 by: Joseph D. Spsracin0 ACSoSCo Lineup:

Canmet$tAS A D8S flo w rate: gpm CSo48 ,

C. DIS 4p DDIS pressure: pSig

"" 8^

Version: PIPE-FWGer 5.01 RH007A CSO2A level & grade: ft

BRHRj A.CS RHOO60 RHOO68 RHOO6C RHOO5A BCSDSCG e CSD4A CSD4B j, '

Il > >^ '

RHOO6DA, D. DIS RHOO7CADtSTEEltHOO7A CSD2 D.DISA qlHOOZ w RHOO78 iQ p_" ACSD2

, SD2B BDISTEE ,

1HOO8A q, g

RHRHXS2 q,- RHRHXS1q)

ACSO4 Z RHRHXE 5;HXBYPSB RHRHX/. THXBYPSA 4p P qpBCSD4 yp*BCSD2 RHRHXDB W' RHRHXDAk g RXO18 1XO1A

,o CSD78 RHRHXDDjp RHRHXDCj p qpACSD5 (A RXO1D 1XO1C ,

7 CSD5B ACSD9 CROSSTIE RECtRCB q) __. _ ": RECIRCA CSD6A

'O jpBCSD7 4XO2g RXO2A MO2013h p qp MO2012 CSD3A hb ACW6

-:SO3B RXO2O RXO2C

> o CDS7A

<pBCSD5 g 4> ik g> REC 1RC2 RECIRC1 j,

BCSD3 ACSO3 ,

yyACSD7 E

m CSD6B CSDBA D

,o, j,BCSD6 j,ACSDB e

e O

J R

4 S

Company: Duke Engineering & Services 06/11/97 4:57 pm Project: Linelist: OVRPREst by: Joseph D. Sparacino Lineup:

Comments: flow rate: gpm pressure: psig Version: PIPE-FLO ver 5.01 level & grade: ft l

Ccmp ny: Duka Enginesring & SirvicIs 06/12/97 8:17 tm Pr:JIct: Syst:m: OVRPRES1 by: JosIph D. Spir:cino riv: 06/12/97 8:16 am SYSTEM REPORT Created: 11/04/9611:56 am Pipes: 93

~

Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.131.8'F. and 0 psig cont. press. Containment overpressure cales.

SYSTEM NODES NODE ELEVATION PIPELINES IN PIPELINES OUT ]

ft l

.1 90225 H11 H1 10 90225 H52 H5 11 902.25 H5 H51 12 902.25 H6a2 H6a 13 902.25 H6a H6a1 14 902.25 H6b2 H6b 15 902.25 H6b H6bi 16 902.25 H72 H7 17 902.25 H7 H71 18 902.25 H82 H8 19 90225 H8 H81 2 902.25 H2 H22 ;

1 20 90225 Hi H12 3 902.25 H21 H2 l

4 902.25 H3 H32 5 902.25 H31 H3 j i

6 902.25 H4b H4b2 7 902.25 H4bi H4b 8 90225 H4a H4a2 9 902.25 H4a1 H4a A.CS.IN 902.25 H6bi CS001A H72 A.CS.SUCT 897.833 CS003A CSD1A A.CS.T 899.916 CS001A CS003A A. DIS 897.833 RH006A RH007A Calc / No. V76100.NSP97.00501 ATTACHMENT l Pagedof /57 PIPE-FLO ver 5.01 pg 1

SYSTEM NODES 06/12/97 8:17 Cm NODE ELEVATION PIPELINES IN PIPELINES OUT ft l '

A.lN 897.583 RH002A RH005A A.RH.lN 902.25 H12 RH001A H81 1

i A.RH.T 897.583 RH001A RH003A A.SUC 897.833 RH005A RH006A ACSD2 931.917 CSD2A CSD9A ACSD3 981.188 CSD3A ,

1 ACSD4 900.156 CSD4A CSD5A J

ACSD5 900.74 CSD5A CSD6A i ACSD6 925.875 CSD6A CDS7A i

ACSD7 928 CDS7A CSD8A !

ACSD8 927 CSD8A ACSD9 971.25 CSD9A CSD3A ACSDSCG 899.635 CSD1A CSD2A CSD4A i

ADISTEE 901.083 RH007A RH008A

, RH007C .

B.CS.IN 902.25 H4b2 CS001B

~

H31 B.CS.SUCT 897.833 CS003B CDS1B B.CS.T 899.885 CS001B CS003B B.D;S 899.5 RH006B RH0078 B.IN 897.583 RH003B RH002B RH004B B.RH.lN 902.25 H22 H11 RH001B B.RH.T 897.583 RH001B RH003B B.SUC 897.833 RH004B RH006B BCSD2 927.833 CSD2B CSD7B BCSD3 980.38 CSD3B BCSD4 899.896 CSD4B CSDSB BCSDS 901.688 CSDSB CSDGB BCSD6 930.333 CSD6B Calc / No. V75100.NSP97.00501 ATTACHMENT _d Page M of /N PIPE-FLO ver 5.01 pg 2

. ____ =. .. _ _._.. _ _ _ _ . . _ . . _ . _ _ . _ . _ .. _ _ _ _._. _ _ . . _ _ - _ . _ _ _ . . _ .

SYSTEM NODES 06/12/97 8:17 Cm NODE. ELEVATION PIPELINES IN PIPELINES OUT 5

ft 4

BCSD7 978.5 CSD78 CSD3B j

BCSDSCG 899.583 CDS1B CSD2B CSD4B BDISTEE 908 RH007J RH008B RH0070 J C. DIS 897.833 RH006C RH007C C.IN 897.583 RH003A RH002A RH004A l C.SUC 897.833 RH004A RH006C D. DIS 899.5 RH006D - RH006DA D.DISA 908 RH006DA RH007D i

D.lN 897.583 RH0028 RH005B D.SUC 897.833 RH005B RH006D i

2 HP.IN 902.25 H4a2 H4bi HP001 HP.SUCT 901.615 HP002 HP.T 901.615 HP001 HP002 l M02013 940.91 RXO2B RX02D l MO2012 940.917 RXO2A RX02C

]

RC.IN 902.25 H6a1 H6b2

RC001 j RC.SUCT 899.042 RC002 i- RC.T 902.25 RC001 RC002 i

i RECIRC1 ' 951.75 RX02C RECIRC2 951.75 RXO2D

RECIRCA 930.168 CROSSTIE RX02A

! RX01C l RECIRCB 930.167 RX01D CROSSTIE RX028 i

RHRHXDA 916.333 RHRHXA RX01A RHXBYPSA l

) RHRHXDB 915.49 RHRHXB RX01B j RHXBYPSB RHRHXDC 916.336 RX01A RX01C I

d Calc / No. V75100.NSP97.00501 ATTACHMENT b Page 30 of 159 PIPE-FLO ver 5.01 p9 3

... -.. .. .~ ..

l SYSTEM NODES 06/12/97 8:17 am NODE ELEVATION PIPELINES IN PIPELINES OUT ft RHRHXDD 921.33 RX01B RX01D l RHRHXS1 909.406 RH008A RHRHXA RHXBYPSA l

RHRHXS2 908 RH008B RHRHXB RHXBYPSB SA 902.25 A H21 )

H32 SB 902.25 B H4a1 H52 SC 902.25 C H6a2 H51 SD 902.25 D H82 H71 TA 904.316 A TB 904.316 B TC 904.316 C TD 904.316 D 1

l Calc / No. V75100.NSP97.00501 ATTACHMENT S Page 3( or /51 PIPE-FLO ver 5.0i pg 4

- . . _ . . . - ..-. - . - . . . ..---- ..-.- . ~ . - .. - . - -. - ~ - ~. -_

l SYSTEM PIPES 06/12/97 8:17 am l

! PIPELINE . SPEC FROM_ NODE TO_ NODE PUMP / COMP l

l A 31 TA SA B 31 TB SB C TC SC 31

)

CDS1B 16 B.CS.SUCT BCSDSCG BCS l CDS7A 35 ACSD6 ACSD7 j

, CROSSTIE 21 RECIRCB RECIRCA CS001A 16 A.CS.IN A.CS.T l

CS001B 16 B.CS.IN B.CS.T CS003A 16 A.CS.T A.CS.SUCT CS0038 16 B.CS.T B.CS.SUCT CSD1A 16 A.CS.SUCT ACSDSCG A.CS CSD2A 16 ACSDSCG ACSD2 q CSD2B 16 BCSDSCG BCSD2 CSD3A 35 ACSO9 ACSD3 CSD3B 35 BCSD7 BCSD3 CSD4A 16 ACSDSCG ACSD4 l CSD4B 16 BCSDSCG BCSD4 CSD5A 35 ACSD4 ACSDS CSD5B 35 BCSD4 BCSDS l CSD6A 16 ACSDS ACSD6 )

CSD6B 16 BCSD5 BCSD6 CSD78 16 BCSD2 BCSD7 CSD8A 16 ACSD7 ACSD8 CSD9A 16 ACSD2 ACSD9 0 31 TD SD '

Hi 26 1 20 H11 31 B.RH.lN 1 H12 31 20 A.RH.IN H2 M 3 2 H21- 31 SA 3 H22 31 2 B.RH.lN H3 26 5 4 H31 31 B.CS.IN 5 H32 31 4 SA H4a 26 9 8 H4a1 31 SB 9 H4a2 31 8 HP.IN H4b 26 7 6 H4b1 31 HP.IN 7 H4b2 31 6 B.CS.IN H5 26 10 11 HS1 31 11 SC Calc / No. V76100.NSP97.00601 ATTACHMENT _ 6 Page 32of /S'l PIPE-FLO ver 5.01 pg 5

SYSTEM PIPES 06/12/97 8:17 cm i ,

i PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP i

l H52 31 SB 10 H6a 26 12 13 H6a1 31 13 RC.IN H6a2 31 SC 12 26 14 15 l H6b H6bi 31 15 A.CS.IN H6b2 31 RC.lN 14 H7 26 16 17 H71 31 17 SD H72 31 A.CS.IN 16 H8 26 18 19 H81 31 19 A.RH.lN !

H82 31 SD 18 HP001 21 HP.lN HP.T HP002 21 HP.T HP.SUCT RC001 16 RC.IN RC.T RC002 16 RC.T RC.SUCT j RH001A 26 A.RH.IN A.RH.T RH001B 26 B.RH.IN B.RH.T RH002A 26 C.lN A.lN RH002B 26 B.lN D.IN RH003A 26 A.RH.T C.lN RH003B 26 B.RH.T B.lN RH004A 21 C.lN C.SUC RH004B 21 B.lN B.SUC RH005A 21 A.IN A.SUC .

RH005B 21 D.lN D.SUC RH006A 16 A.SUC A. DIS ARHR RH0068 16 B.SUC B. DIS BRHR RH006C 16 C.SUC C. DIS CRHR RH006D 16 D.SUC D. DIS DRHR RH006DA 16 0. DIS D.DISA RH007A 16 A. DIS ADISTEE RH007B 16 B. DIS BDISTEE RH007C 16 C. DIS ADISTEE RH007D 21 D.DISA BDISTEE RH008A 21 ADISTEE RHRHXS1 RH008B 21 BDISTEE RHRHXS2 RHRHXA 21 RHRHXS1 RHRHXDA RHRHXB 21 RHRHXS2 RHRHXDB RHXBYPSA 21 RHRHXS1 RHRHXDA RHXBYPSB 21 RHRHXS2 RHRHXDB Calc / No. V76100.NSP97.00501 ATTACHMENT b Page 33of.lf_1

( PIPE-FLO ver 5.01 pg 6 i

._ _ _ _ . _ _ . ___ _. . _ _ - - . ~ _ _ _ . _ . - _ . .. __ _ .

SYSTEM PIPES 06/12/97 8:17 am PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP RX01A 21 RHRHXDA RHRHXDC RX01B 21 RHRHXDB RHRHXDD RX01C 21 RHRHXDC RECIRCA RX01D 21 RHRHXDD RECIRCB RX02A 21 RECIRCA MO2012 RX02B 21 RECIRCB M02013 RXO2C 35 MO2012 RECIRC1 RX02D 35 M02013 RECIRC2 RXO1A 16 .

l Calc / No. V76100.NSP97.00601 ATTACHMENT S Page 34 of jf_T PIPE-FLO ver 5.01 P9 7

. . . . - . . -. . . . . - . - . . - - . . ~ - . . . . . - - = . . . . . - .

SYSTEM COMPONENTS 06/12/97 8:17 am PUMP / COMP PERFORMANCE DATA A.CS gpm: 0 2179 3990 5040 5755 ft: 850.3 795.5 664 536.2 411.7 egn: 850.3 - 4.49715e-006 Q ^ 2.12033 ARHR gpm: 0 3365 4000 4250 4540 ft: 810.3 498.9 350 280 171.8 egn: 810.3 - 1.3787e-006 Q ^ 2.36763 l l

BCS gpm; O 1948 3080 4875 5600 I ft: 844 770.1 719.4 535.2 418.1 egn: 844 - 0.000218414 Q ^ 1.66917 BRHR gpm: 0 3656 4000 4250 4408 l ft: 813.8 436 350 280 230 l

eqn: 813.8 - 2.04305e-006 Q ^ 2.32005 CRHR gpm: 0 3540 4000 4250 4440 ft: 763.9 461.1 360 290 235.4 eqn: 763.9 - 5.58043e-007 Q ^ 2.46066 DRHR gpm: 0 3542 4000 4250 4425 ft: 810.1 463 350 285 227 eqn: 810.1 - 2.16007e-006 Q ^ 2.31196 Calc / No. V75100.NSP97.00501 ATTACHMENT l PageMofM PIPE-FLO ver 5.01 pg 8

Ctmpiny: Duka Enginnring & Strvic:s 06/12/97 8:17 cm ProjIct: Systim: OVRPRES1 by: Joseph D. Spiracino r;v: 06/12/97 8:16 cm PIPELIST REPORT Created: 11/04/9611:56 am Pipes: 93 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 NSP RHR ar.d CS piping model, SP Temp.131.8'F. and 0 psig cont. press. Containment overpressure cales.

SPECIFICATIONS SPECIFICATION PIPE MATERIAL FLUID VALVE TABLE DESIGN LIMITS Sch / Roughness Temp / Pres Vel / Pres 16 LB30 Steel Water Standard 0 - 12 ft/sec rev 06/12/97 8:15 am Sch 40 131.8 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 21 LB31 Steel Water Standard 0 - 12 ft/sec rey: 06/12/97 8:15 am Sch 30 131.8 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 26 LB32 Steel Water Standard 0 - 12 ft/see rev: 06/12/97 8:16 am Sch 20 131.8 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 31 LB34 Steel W ater Standard 0 - 12 ft/see rev: 06/12/97 8:16 am Sch 60 131.8 *F 0 - 200 psi g 0.0018 in 0 psig Size for: 8 ft/sec 35 LB34a Steel Water Standard 0 - 12 ft/sec rev:06/12/97 8:16 am Sch 80 131.8 'F 0 - 200 psi g 0.0018 in 0 psig Size for: 8 ft/see Calc / No. V75100.NSP97.00501 ATTACHMENT O Page 3b:of M PIPE-FLO ver 5.01 pg 1

_ .- -- - . _ . . - - _ - - - ~ . -

PIPELIST 06/12/97 8:17 Km PIPELINE SPEC MATERIAL LENGTH FLUID VALVES Size / Sch ft Temp / Pres TotaLK A 31 Steel 3.6777 Water 1.163 l 20 in / 60 131.8 'F / 0 psi g B 31 Steel 3.6777 Water 0.4469 20in / 60 131.8 'F / 0 psi g l C 31 Steel 3.6777 Water 1.163 20 in / 60 131.8 'F / 0 psi g i

CDS1B 16 Steel 3.45 Water 0.2689 10 in / 40 131.8 'F / 0 psi g CDS7A 35 Steel 7,73835 Water 0.478 2 in / 80 131.8 'F / 0 psi g CROSSTIE 21 Steel 49.0188 Water 1.403 14 in / 30 131.8 'F / 0 psi g CS001A 16 Steel 41.8129 Water 2.285 i 12 in / 40 131.8 'F / 0 psi g i CS001B 16 Steel 42.5259 Water 1.695 12 in / 40 131.8 'F / 0 psi g CS003A 16 Steel 10.7215 Water 1.779 12 in / 40 131.8 'F / 0 psi g CS003B 16 Steel 27.109 Water 2.018 12 in / 40 131.8 'F / 0 psi g CSD1A 16 Steel 3.7973 Water 0.2689 10 in / 40 131.8 'F / 0 psi g CSD2A 16 Steel 108.553 Water 60.59 10 in / 40 131.8 'F / 0 psi g CSD2B 16 Steel 108.723 Water 59.14 10 in / 40 131.8 'F / 0 psi g CSD3A 35 Steel 57.0055 Water 19.08 8 in / 80 131.8 'F / 0 psi g CSD3B 35 Steel 55.4392 Water 19.08 8 in / 80 131.8 'F / 0 psi g CSD4A 16 Steel 2.22525 Water 1.664 2.5 in / 40 131.8 'F / 0 psi g CSD4B 16 Steel 2.7485 Water 1.93 2.5 in / 40 131.8 'F / 0 psi g CSDSA 35 Steel 0.67045 Water 6.654 2 in / 80 131.8 'F / 0 psi g CSD5B 35 Steel 2.0608 Water 6.654 2 in / 80 131.8 'F / 0 psi g i CSD6A 16 Steel 38.6803 Water 152.5 2.5 in / 40 131.8 'F / 0 psi g CSD6B 16 Steel 101.051 Water 155.4 2.5 in / 40 131.8 'F / 0 psi g CSD78 16 Steel 97.3901 Water 1.995 10 in / 40 131.8 'F / 0 psi g CSD8A 16 Steel 45.7585 Water 2.453 2.5 in / 40 131.8 'F / 0 psi g CSD9A 16 Steel 75.8885 Water 1.53 10 in / 40 131.8 'F / 0 psi g Calc / No. V76100.NSP97.00501 ATTACHMENT 6 Page '37 of iw PIPE-FLO ver 5.01 pg 2

I PIPELIST 06/12/97 8:17 Em PIPELINE SPEC MATERIAL LENGTH FLUID VALVES Size / Sch ft Temp / Pres Total-K D 31 Steel 3.6777 Water 1.163 l 20 in / 60 131.8 'F / 0 psi g 1 H1 26 Steel 52.2054 Water 0.144 i 20 la / 20 131.8 'F / 0 psi g 31 Steel 1.9171 Water 0.2536 H11 {

20 in / 60 131.8 'F / 0 psi g i H12 31 Steel 1.9171 Water 0.00366 20 in / 60 131.8 'F / 0 psi g H2 26 Steel 24.1868 Water 0.072 20 in / 20 131.8 *F / 0 psi g H21 31 Steel 1.9171 Water 0.00366 20 in / 60 131.8 'F / 0 psi g H22 31 Steel 1.9171 Water 0.01484 20 in / 60 131.8 *F / 0 psi g H3 26 Steel 24.3777 Water 0.072 20 in / 20 131.8 'F / 0 psi g H31 31 Steel 1.4375 Water 0.2425 20 in / 60 131.8 'F / 0 psi g H32 31 Steel 1.9171 Water 0.2536 20 in / 60 131.8 'F / 0 psi g H4a 26 Steel 31.4675 Water 0.072 20 in / 20 131.8 'F / 0 psi s, H4a1 31 Steel 1.9171 Water 0.7201 20 in / 60 131.8 'F / 0 psi g H4a2 31 Steel 1.725 Water 0.01484 20 in / 60 131.8 'F / 0 psi g H4b 26 Steel 45.6907 Water 0.144 20 in / 20 131.8 *F / 0 psi g H4bi 31 Steel 1.725 Water 0.2425 20 in / 60 131.8 'F / 0 ps! g H4b2 31 Steet 1.725 Water 0.01484 20 in / 60 131.8 'F / 0 psi g H5 26 Steel 108.244 Water 0.288 20 in / 20 131.8 *F / 0 psi g H51 31 Steel 1.9171 Water 0.2536 20 in / 60 131.8 'F / 0 psi g H52 31 Steel 1.9171 Water 0.7201 20 in / 60 131.8 'F / 0 psi g >

KGa 26 Steel 15.1777 Water 0.072 20 in / 20 131.8 'F / 0 psi g H6a1 31 Steet 1.725 Water 0.01484 20 in / 60 131.8 'F / 0 psi g H6a2 31 Steel 1.9171 Water 0.0036G 20 in / 60 131.8 'F / 0 psi g H6b 26 Steel 61.7884 Water 0.144 20 in / 20 131.8 'F / 0 psi g H6b1 31 Steel 1.725 Water 0.01484 20 in / 60 131.8 'F / 0 psi g Calc / No. V78100.NSP97.00601 ATTACHMENT 6 Page 33,of B I

P!PE-FLO ver 5.01 P9 3

. . - . . . . - . . - . _ - . - . . . ,.... . - . . . . . - - - ..-. ~ ~ ~ . - . . _

PIPELIST 06/12/97 8:17 tm PIPELINE SPEC MATERIAL LENGTH FLUID VALVES

Size / Sch ft Temp / Pres Total-K H6b2 31 Steet 1.725 Water 0.2425 20 in / 60 131.8 *F / 0 psi g L

l H7 26 Steel 24.3777 Water 0.072 l 20 in / 20 131.8 *F / 0 psi g 4 l H71 31 Steel 1.9171 Water 0.2536 i 20 in / 60 131.8 'F / 0 psi g H72 31 Steel 1.725 Water 0.2425 20 in / 60 131.8 'F / 0 psi g H8 26 Steel 24.1868 Water 0.072 20 in / 20 131.8 *F / 0 psi g H81 31 Steel 1.9171 Water 0.01484 20 in / 60 131.8 'F / 0 psi g H82 31 Steel 1.9171 Water 0.00366 20 in / 60 131.8 'F / 0 psi g HP001 21 Steel 67.5027 Water 3.127 l 14 in / 30 131.8 'F / 0 psi g )

HP002 21 Steel 9.3679 Water. 1.356 l l

14 in / 30 131.8 'F / 0 psi g l

RC001 16 Steel 22.7965 Water 4.054 l 6 in / 40 131.8 'F / 0 pel g RC002 16 Steel 56.5179 Water 1.298 6 in / 40 131.8 'F / 0 psi g RH001A 26 Steel 62.1357 Water 2.161 20 in / 20 131.8 'F / 0 psi g RH0018 26 Steel 55.6198 Water 2.09 l 20 in / 20 131.8 'F / 0 psi g i RH002A 26 Steel 5.75 Water 0.7101 20 in / 20 131.8 'F / 0 psi g RH002B 26 Steel 5.3671 Water 0.7101 20 in / 20 131.8 'F / 0 psi g RH003A 26 Steel 7.1093 Water 0.2367 l' 20 in / 20 131.8 'F / 0 psi g RH003B 26 Steel 7.6671 Water 0.7101 20 in / 20 131.8 *F / 0 psi g RH004A 21 Steel 14.758 Water 2.63 l 14 in / 30 131.8 'F / 0 poi g RH004B 21 Steel 14.95 Water 2.63 14 in / 30 131.8 'F / 0 psi g RH005A 21 Steel 14.758 Water 1.867 j 14 in / 30 131.8 'F / 0 psi g

]

RH005B 21 Steet 14.95 Water 1.867 I 14 in / 30 131.8 'F / 0 psi g RH006A ' 16 Steel 1.15 Water 0.2977 12 in / 40 131.8 'F / 0 psi g l RH006B 16 Steel 3.0671 Water 0.5573 l 12 in / 40 131.8 'F / 0 psi g j RH006C ' 16 Steel 1.15 Water 0.2977 l 12 in / 40 131.8 'F / 0 psi g Calc / h. V75100.NSP97.00501 ATTACHMENT b PageM of.1.f*J I 1

PIPE-FLO ver 5.01 pg 4

PIPELIST 06/12/97 8:17 gm '

1 PIPELINE SPEC MATERI.M LENGTH FLUID VALVES ft Temp / Pres Total-K Size / S4 RH006D 16 Steel 3.06671 Water 0.5573 12 in / 40 131.8 'F / 0 psi g RH006DA 16 Steel 20.7 Water 1.76 10 in / 40 131.8 'F / 0 psi g RH007A 16 Steel 17.6094 Water 2.534 10 in / 40 131.8 'F / 0 psi g RH0078 16 Steel 19.2625 Water 2.298 10 in / 40 131.8 'F / 0 psi g RH007C 16 Steel 19.7656 Water 3.065

- 10 in / 40 131.8 'F / 0 psi g j RH007D 21 Steet 4.025 Water 0.2543 14 in / 30 131.8 'F / 0 psi g RH008A 21 Steet 11.7875 Water 0.5086 14 in / 30 131.8 'F / 0 psi g

, TH008B 21 Steel 2.875 W ater 0.2543

- 14 in / 30 131.8 *F / 0 psi g RdRHXA 21 Steel 28.4145 W ater 5.436

, 14 in / 30 131.8 'F / 0 psi g RHRHXB 21 Steet 54.8343 Water 6.316 l

14 in / 30 131.8 'F / 0 psi g )

l RHXBYPSA 21 Steel 29.4849 Water 5.85 14 in / 30 131.8 'F / 0 psi g

~

RHXBYPSB 21 Steel 15.4172 Water 5.341 14 in / 30 131.8 'F / 0 psi g i RX01A 21 Steel 6.3849 Water 0.763 14 in / 30 131.8 *F / 0 psi g RX01B 21 Steel 20.748 Water 1.272 1 14 in / 30 131.8 'F / 0 psi g RX01C 21 Steel 83.5906 W ater 3.24 14 in / 30 131.8 'F / 0 psi g RX01D 21 Steel 73.7917 W ater 3.24 14 in / 30 131.8 'F / 0 psi g RX02A 21 Steel 12.3625 W ater 4.454 16 in / 30 131.8 'F / 0 psi g RX02B 21 Steet 12.3625 Water 4.207 16 in / 30 131.8 'F / 0 psi g RXO2C 35 Steet 102.769 Water 3.252 16 in / 80 131.8 'F / 0 psi g RX02D 35 Steel 97.9537 Water 3.184 16 in / 80 131.8 'F / 0 psi g RXO1A 16 Steel 6.3849 Water 0.7645 14 in / 40 131.8 'F / 0 psi g Calc / No. V75100.NSP97.00501 ATTACHMENT b Page 4Oof /5 9 PIPE-FLO ver 5.01 pg 5

..- - . - _. -= - - . . . . ... - = - - . .

Comptny: Duks Enginuring & SIrvicts 06/12/97 8:17 cm I PrcjIct: SystIm: OVRPRES1 l by: Jos;ph D. Spiricino rsv: 06/12/97 8:16 am ;

MATERIALS REPORT )

p Created: 11/04/9611:56 am Pipes: 93 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.131.8'F. and 0 psig cont. press. Containment overpressure cales.

l PlPE MATERIALS LIST ,

I

PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft A 31 Steel 3.6777 1-Fixed K strainer 20 in / 60 1-Tee Fiow Thru Branch B 31 Steel 3.6777 1-Fixed K STRAINER j 20 in / 60 C 31 Steel 3.6777 1-Fixed K STRAINER )

20 in / 60 1 Tee Flow Thru Branch I i

~

CDS1B 16 Steel 3.45 1-Elbow Short - r/d 1 @ 90' 10 in / 40 CDS7A 35 Steel 7.73835 1-Elbow Short - r/d 1 @ 90*

2 in / 80 1-Reducer Enlargement 2 X 2.5 I

, i CROSSTIE 21 Steel 49.0188 3-Elbow Short - r/d 1 @ 90' i

14 in / 30 1-Tee Flow Thru Run i 1-Reducer Contraction 16 X 14 1-Reducer Enlargement 14 X 16 !

2-Gate Wedge Disc l

CS001A 16 Steel 41.8129 4-Elbow Short - r/d 1 @ 90*

12 in / 40 1-Gate Wedge Disc 1-Gate Double Disc 1-Tee Flow Thru Run 1-Tee Flow Thru Branch 4

CS001B 16 Steel 42.5259 1-Elbow Short - r/d 1 @ 90' 12 in / 40 1-Elbow Short - r/d 1 @ 45' 1-Tee Flow Thru Run 1-Gate Wedge Disc 1-Gate Double Disc 1-Tee Flow Thru Branch CS003A 16 Steel 10.7215 3-Elbow Short - r/d 1 @ 90' 12 in / 40 1-Fixed K vel coretn CS003B 16 Oteel 27.109 1-Elbow Short - r/d 1 @ 90' 12 in / 40 4-Elbow Short - r/d 1 @ 45*

1-Fixed K vel coretn CSD1A 16 Steel 3.7973 1. Elbow Short - r/d 1 @ 90' 10 in / 40 Calc / No. V76100.NSP97.00501 ATTACHMENT b Page 4I of /f'T PIPE-FLO ver 5.01 pg 1

PIPE MATERIALS LIST 06/12/97 8:17 am PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS

Size / Sch ft i CSD2A 16 Steel 108.553 1-Tee Flow Thru Run 10 in / 40 1-Swing Check Vertical

5-Elbow Short - r/d 1 @ 90' 8-Elbow Short - r/d 1 @ 45' 1-Fixed K Flow Element 1-Fixed K Res. Orifice

i j I

CSD2B 16 Steel 108.723 4-Elbow Short - r/d 1 @ 90' )

j 10 in / 40 1-Swing Check Vertical

. 2-Elbow Short - r/d 1 @ 45'

1 Tee Flow Thru Run i 1-Fixed K Res. Orifice 1-Fixed K Flow Element 4

4

. CSD3A 35 Steel 57.0055 3-Gate Wedge Disc 8 in / 80 1-Swing Check Angled i

6-Elbow Short - r/d 1 @ 90' 1-Fixed K Spargers CSD3B 35 Steet 55.4392 3-Gate Wedge Disc 8 in / 80 1 Swing Check Angled 6-Elbow Short - r/d 1 @ 90*

1-Fixed K Sparger CSD4A 16 Steel 2.22525 1-Elbow Short - r/d 1 @ 45' 2.5 in / 40 1-Tee Flow Thru Branch 1 l

1-Reducer Contraction 2.5 X 2 CSD4B' 16 Steel 2.7485 2-Elbow Short - r/d 1 @ 45' 2.5 in / 40 1 Tee Flow Thru Branch 1-Reducer Contraction 2.5 X 2 CSDSA 35 Steel 0.67045 1-Globe Valve 2 in / 80 1-Reducer Enlargement 2 X 2.5 g CSDSB 35 Steel 2.0608 1-Globe Valve 2 in / 80 1-Reducer Enlargement 2 X 2.5 CSD6A 16 Steel 38.6803 1-Elbow Short - r/d 1 @ 45' 2.5 in / 40 2-Elbow Short - r/d 1 @ 90' 1-Reducer Contraction 2.5 X 2 1-Fixed K Orifice Min.

CSD6B 16 Steel 101.051 10-Elbow Short- r/d 1 @ 90*

2.5 in / 40 2-Elbow Short - r/d 1 @ 45* ,

1-Fixed K Orifice Min.

l CSD7B 16 Steel 97.3901 1-Reducer Contraction 10 X 8 10 in / 40 4-Elbow Short - r/d 1 @ 90' 1-Elbow Short - r/d 1 @ 45* j l

Calc / No. V75100.NSP97.00501 ATTACHMENT O Page 4o7of M PIPE-FLO ver 5.01 pg 2 j

PIPE MATERIALS LIST 06/12/97 8:17 am PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS I Size / Sch ft 1-Tee Flow Thru Run 1

CSD8A 16 Steel 45.7585 6-Elbow Short - r/d 1 @ 90' 2.5 in / 40 1-Elbow Short - r/d 1 @ 45'

CSD9A 16 Steel 75.8885 1 Reducer Contraction 10 X 8 4 10 in / 40 1-Tee Flow Thru Run l 3-Elbow Short - r/d 1 @ 90'

, D 31 Steel 3.6777 1-Fixed K strainer 20 in / 60 1-Tee Flow Thru Branch l

4 H1 26 Steel 52.2054 2-Fixed K 22.5 mitre l 20 in / 20

! H11 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 1-Tee Flow Thru Run

't H12 31 Steel 1.0171 1-Fixed K enlargement 20 in / 6C' 4 H2 26 Steel 24.1868 1-Fixed K 22.5 mitre 4

20 in / 20 j i

l H21 31 Steel 1.9171 1 Fixed K enlargement 20 in / 60 l

H22 31 Steet 1.9171 1-Fixed K contraction i 20 in / 60 H3 26 Steel 24.3777 1 Fixed K 22.5 mitre 20 in / 20 I

H31 31 Steet 1.4375 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Run H32 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 1-Tee Flow Thru Run H4a 26 Steel 31.4675 1-Fixed K 22.5 mitre 20 in / 20 H4a1 31 Steel 1.9171 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Branch H4a2 31 Steel 1.725 1-Fixed K contraction 20 in / 60 H4b 26 Steel 45.6907 2-Fixed K 22.5 mitre 20 in / 20 H4bi 31 Steet 1.725 1-Fixed K enlargement Calc / No. V75100.NSP97.00501 ATTACHMENT @ Page3 of./f7 PIPE-FLO ver 5.01 pg 3

PIPE MATERIALS LIST 06/12/97 8:17 cm PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft 20 in / 60 1-Tee Flow Thru Run H4b2 31 Steel 1.725 1-Fixed K contraction 20 in / 60 HS 26 Steel 108.244 4-Fixed K 22.5 mitre 20 in / 20 H51 31 Steel 1.9171 1-Tee Flow Thru Run 20 in / 60 1-Fixed K contraction H52 31 Steel 1.9171 1 Tee Flow Thru Branch 20 in / 60 1-Fixed K enlargement H6a 26 Steel 15.1777 1-Fixed K 22.5 mitre 20 in / 20 H6a1 31 Steel 1.725 1-Fixed K contraction 20 in / 60 H6a2 31 Steel 1.9171 1-Fixed K enlargement 20 in / 60 H6b 26 Steel 61.7884 2-Fixed K 22.5 mitre 20 in / 20 H6b1 31 Steel 1.725 1-Fixed K contraction 20 in / 60 H6b2 31 Steet 1.725 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Run H7 26 Steel 24.3777 1-Fixed K 22.5 mitre 20 in / 20 H71 31 Steel 1.9171 1-Tee Flow Thru Run 20 in / 60 1-Fixed K contraction H72 31 Steel 1.725 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Run j

I H8 26 Steel 24.1868 1-Fixed K 22.5 mitre )

i 20 in / 20 H81 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 ,

1 H82 31 Steel 1.9171 1-Fixed K enlargement !

HP001 21 S eel 67.5027 1-Elbow Long - r/d 1.5 @ 22.5' 14 in / 30 2-Gate Wedge Disc !

1-Swing Check Angled i 3-Elbow Long - r/d 1.5 @ 90*

Calc / No. V75100.NSP97.00501 ATTACHMENT b Page N of /6 PIPE-FLO ver 5.01 pg 4

PIPE MATERIALS LIST 06/12/97 8:17 Crn PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft 1-Tee Flow Thru Run 1-Tee Flow Thru Branch HP002 21 Steet 9.3679 1-Elbow Short - r/d 1 @ 90*

14 in / 30 1-Gate Wedge Disc 1-Fixed K vel coretn 1 RC001 16 Steel 22.7965 1-Elbow Long - r/d 1.5 @ 67.5*

6 in / 40 1-Elbow Long - r/d 1.5 @ 45' 1-Elbow Long - r/d 1.5 @ 90*

2-Gate Wedge Disc 1-Swing Check Angled

, 2-Tee Flow Thru Branch RC002 16 Steel 56.5179 1-Elbow Short - r/d 1 @ 90*

6 in / 40 1-Fixed K vel coretn j

i RH001A 26 Steel 62.1357 2-Elbow Short - r/d 1 @ 90*

20 in / 20 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Elbow Short - r/d 1 @ 45*

1-Tee Flow Thru Branch 4

RH001B 26 Steet 55.6198 1-Elbow Long - r/d 1.5 @ 90*

20 in / 20 1-Elbow Short-r/d 1 @ 90*

1-Gate Wedge Disc 1-Tee Flow Thru Branch

. 1 Elbow Short- r/d 1 @ 45' 1-Tee Flow Thru Branch l RH002A 26 Steel 5.75 1-Tee Flow Thru Branch 20 in / 20

< RH002B 26 Steel 5.3671 1-Tee Flow Thru Branch 1

20 in / 20 RH003A 26 Steel 7.1093 1-Tee Flow Thru Run 20 in / 20 RH003B 26 Steel 7.6671 1-Tee Flow Thru Branch 20 in / 20 RH004A 21 Steet 14.758 1-Tee Flow Thru Branch 14 in / 30 1-Reducer Contraction 20 X 14 1-Gate Wedge Disc 2-Elbow Short - r/d 1 @ 90*

1-Fixed K vel coretn RH004B 21 Steel 14.95 1-Reducer Contraction 20 X 14 4

14 in / 30 2-Elbow Short - r/d 1 @ 90*

1-Gate Wedge Disc 1-Tee FlowThru Branch 1-Fixed K vel coretn Calc / No. V75100.NSP97.00501 ATTACHMENT 6 Page 6 of /5.9 PIPE-FLO ver 5.01 pg 5

PIPE MATERIALS LIST 06/12/97 8:17 am PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft RH005A 21 Steel 14.758 1-Reducer Contraction 20 X 14 14 in / 30 1-Gate Wedge Disc 2-Elbow Short - r/d 1 @ 90*

1-Fixed K vel coretn RH005B 21 Steel 14.95 1-Reducer Contraction 20 X 14 14 in / 30 2-Elbow Short - r/d 1 @ 90' 1 Gate Wedge Disc 1-Fixed K vel coretn RH006A 16 Steel 1.15 1 Reducer Contraction 12 X 10 12 in / 40 RH006B 16 Steel 3.0671 1-Elbow Short - r/d 1 @ 90' 12 in / 40 1-Reducer Contraction 12 X 10

' RH006C 16 Steel 1.15 1-Reducer Contraction 12 X 10 12 in / 40 RH006D 16 Steel 3.06671 1-Elbow Short- r/d 1 @ 90' 12 in / 40 1-Reducer Contraction 12 X 10 RH006DA 16 Steel 20.7 3-Elbow Short - r/d 1 @ 90' 10 in / 40 1-Swing Check Vertical 1-Gate Wedge Disc 1-Reducer Enlargement 10 X 14 l

RH007A 16 Steel 17.6094 2-Elbow Short - r/d 1 @ 90' l 10 in / 40 1-Elbow Long - r/d 1.5 @ 90' l 1

1-Gate Wedge Disc 1-Tee Flow Thru Run 1-Reducer Enlargement 10 X 12 1-Swing Check Angled RH007B 16 Steet 19.2625 2-Elbow Short - r/d 1 @ 90*

10 in / 40 1-Swing Check Vertical 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Reducer Enlargement 10 X 14 RH007C 16 Steel 19.7656 3-Elbow Short r/d 1 @ 90' 10 in / 40 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Swing Check Angled RH0070 21 Steet 4.025 1-Tee Flow Thru Run 14 in / 30 RH008A 21 Steel 11.7875 1-Elbow Short - r/d 1 @ 90' 14 in / 30 1-Tee Flow Thru Run Calc / No. V76100.NSP97.00601 ATTACHMENT @ Page % of li.T.

PIPE-FLO ver 5.01 pg 6

PIPE MATERIALS LIST 06/12/97 ' 17 sm PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft

~

RH008B 21 Steel 2.875 1 Tee Flow Thru Run 14 in / 30 RHRHXA 21 Steel 28.4145 3-Elbow Short - t/d 1 @ 90*

14 in / 30 2-Gate Wedge Disc 1-Tee Flow Thru Run 1-Fixed K RHR HX RHRHXB 21 Steel 54.8343 3-Elbow Short - r/d 1 @ 90' 14 in / 30 2-Elbow Short - r/d 1 @ 45' 2-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Fixed K RHR HX RHXBYPSA 21 Steel 29.4849 1-Tee Flow Thru Branch 14 in / 30 3-Elbow Short - r/d 1 @ 90' 1-Globe Valve RHXBYPSB 21 Steet 15.4172 1-Elbow Short - r/d i @ 90*

14 in / 30 1-Tee Flow Thru Branch 1-Globe Valve RX01A 21 Steel 6.3849 1 Tee Flow Thru Branch 14 in / 30 RX01B 21 Steel 20.748 1 Elbow Short- r/d 1 @ 90' 14 in / 30 1-Tee Flow Thru Run 1 Tee Flow Thru Branch RX01C 21 Steel 83.5906 1-Tee Flow Thru Run 14 in / 30 3-Elbow Short - r/d 1 @ 90*

1-Tee Flow Thru Branch 1-Reducer Enlargement 14 X 16 1-Fixed K Flow Element RX01D 21 Steel 73.7917 1-Tee Flow Thru Run 14 in / 30 3-Elbow Short - r/d 1 @ 90' 1-Tee Flow Thru Branch 1-Reducer Enlargement 14 X 16 1-Fixed K Flow Element RX02A 21 Steet 12.3625 1-Globe Valve 16 in / 30 1-Tee Flow Thru Run RX02B 21 Steet 12.3625 1-Globe Valve 16 in / 30 RXO2C 35 Steel 102.769 7-Elbow Short - r/d 1 @ 90*

16 in / 80 2-Gate Double Disc 1-Swing Check Angled 1 Reducer Enlargement 16 X 18 Calc / No. V75100.NSP97.00501 ATTACHMENT b Page D of /6'l PIPE-FLO ver 5.01 pg 7

- .= _. . . . . . . _ .. . . _ . _ . - . .

PIPE MATERIALS LIST 06/12/97 8:17 sm PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft RX02D 35 Steet 97.9537 6-Elbow Short - r/d 1 @ 90* .

. 16 in / 80 2-Gate Double Disc l 1-Swing Check Angled )

1-Elbow Short - r/d 1 @ 45' '

1-Reducer Enlargement 16 X 18 RXO1A 16 Steel 6.3849 1-Tee Flow Thru Branch 14 in / 40 I'

i 1

4 d

6 l i

J Calc / No. V75100.NSP97.00501 ATTACHMENT b Page iff of /59 PIPE-FLO ver 5.01 pg 8

PIPE

SUMMARY

06/12/97 8:17 am PIPE MATERIAL SCHEDULE SIZE LENGTH j Steel 20 20 in 555.352 ft Steel 30 14 in 516.659 ft 16 in 24.725 ft Steel 40 2.5 in 190.464 ft 6 in 79.3144 ft 10 in 475.139 ft 12 in 130.603 ft l 14 in 6.3849 ft Steel 60 20 in 51.2265 ft Steel 80 2 in 10.4696 ft 8 in 112.445 ft 16 in 200.723 ft VALVE & FITTING

SUMMARY

SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS 16 LB30 Steel 40 Size: 2.5 in 7-Elbow Short - r/d 1 @ 45' 2-Tee Flow Thru Branch 3-Reducer Contraction 2.5 X 2 18-Elbow Short - r/d 1 @ 90' 2-Fixed K Orifice Min.

Size: 6 in 1-Elbow Long - r/d 1.5 @ 67.5*

1-Elbow Long - r/d 1.5 @ 45*

1-Elbow Long - r/d 1.5 @ 90*

2-Gate Wedge Disc 1 Swing Check Angled 2-Tee Flow Thru Branch 1-Elbow Short - r/d 1 @ 90*

1-Fixed K vel coretn Size: 10 in 28-Elbow Short - r/d 1 @ 90' 5-Tee Flow Thru Run 4-Swing Check Vertical 11-Elbow Short - r/d 1 @ 45' 2-Fixed K Flow Element 2-Fixed K Res. Orifice 2-Reducer Contraction 10 X 8 4-Gate Wedge Dise Calc / No. V75100.NSP97.00501 ATTACHMENT 6 PageN'lof lF7 PIPE-FLO ver 5.01 pg 9

VALVE & FITTING

SUMMARY

06/12/97 8:17 cm SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS Size: 10 in 2-Reducer Enlargement 10 X 14 1-Elbow Long - r/d 1.5 @ 90*

1-Reducer Enlargement 10 X 12 I

2-Swing Check Angled 2-Tee Flow Thru Branch j l

Size: 12 in 11-Elbow Short - r/d 1 @ 90' 2-Gate Wedge Disc 2-Gate Double Disc 2-Tee Flow Thru Run 2 Tee Flow Thru Branch 5-Elbow Short - r/d 1 @ 45' 2-Fixed K vel coretn 4-Reducer Contraction 12 X 10 Size: 14 in 1-Tee Flow Thru Branch 21 LB31 Steel 30 Size: 14 in 30-Elbow Short - r/d 1 @ 90' 9-Tee Flow Thru Run 1-Reducer Contraction 16 X 14 3-Reducer Enlargement 14 X 16 13-Gate Wedge Disc 1-Elbow Long - r/d 1.5 @ 22.5*

1-Swing Check Angled 3-Elbow Long - r/d 1.5 @ 90' 10-Tee Flow Thru Branch 5-Fixed K vel coretn 4-Reducer Contraction 20 X 14 2-Fixed K RHR HX 2-Elbow Short - r/d 1 @ 45' 2-Globe Valve i 2-Fixed K Flow Element Size: 16 in 2-Globe Valve l 1-Tee Flow Thru Run 26 LB32 Steel 20 Size: 20 in 16-Fixed K 22.5 mitre 3-Elbow Short - r/d 1 @ 90' 2-Gate Wedge Disc j 7-Tee Flow Thru Branch 2-Elbow Short - r/d 1 @ 45' I 1-Elbow Long - r/d 1.5 8 90' Calc / No. V75100.NSPS7.00501 ATTACHMENT b Page 60 of M PlPE-FLO ver 5.01 pg 10

._ =

. _- _ . _. . _ . . .. _ _ . . _ . ._ _ _ - . . . _ . . . .. _ > _ . ~ .

VALVE & FITTING

SUMMARY

06/12/97 8:17 tm i

SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS l Size:20 in 1-Tee Flow Thai Run 31 LB34 Steel 60 l

Size: 20 in 2-Fixed K strainer 5-Tee Flow Thru Branch 2-Fixed K STRAINER j 10-Fixed K contraction 8-Tee Flow Thru Run 10-Fixed K enlargement 35 LB34a Steel 80 Size: 2 in 1-Elbow Short - r/d 1 @ 90*

3-Reducer Enlargement 2 X 2.5 2-Globe Valve Size: 8 in 6-Gate Wedge Disc 2-Swing Check Angled 12-Elbow Short - r/d 1 @ 90*

1-Fixed K Spargers 1-Fixed K Sparger Size: 16 in 13-Elbow Short - r/d 1 @ 90* l 1

4-Gate Double Disc 2-Swing Check Angled 2-Reducer Enlargement 16 X 18 1-Elbow Short r/d 1 @ 45*

l l

4 Calc / No. V75100.NSP97.00601 ATTACHMENT G Page.f.L of./.18 PIPE-FLO ver 5.01 pg 11

Comprny: Duks Enginuring & Srrvicss 06/12/97 8:34 am Pr:Jict: Lintup: CASE 1 by: JosIph D. Sparacin) rsv: 06/12/97 8:34 cm System: OVRPRES1 Deviation: 1.86e-005 %

rev: 06/12/97 8:16 am after: 9 iterations short term, all pumps runout, O cont. press., A strainer plugged, sp wtr M 908*-9.3" Volumetric flow rates require constant fluid properties in all pipelines. Fluid properties in the first specification were used in this j calculation. l LINEUP SUMMARIES PlPELINE FLOW PRESSURE SET LEVEL gpm SOURCE psi g ft l

CSD3A >>> 4070 ACSD3 0 0 l l

CSD8A >>> 213.4 ACSD8 0 0 CSD3B >>> 3990 BCSD3 0 0 CSD6B >>> 208.8 BCSD6 0 0 RXO2D >>> 17268 RECIRC2 0 0 B <<< 9586 TB 0 4.459 C <<< 6313 TC 0 4.459 D <<< 9852 TD 0 4.459 Flows IN: 25751 gpm Flows OUT: 25750 gpm j NET FLOWS IN: 1 gpm j I

Calc / No. V75100.NSP97.00501 ATTACHMENT IS Paged of /67 PIPE-FLO ver 5.01 pg 1

LINEUP NODES 06/12/97 8:34 Em 1

NODE ELEVATION DEMAND PRESSURE H GRADE l h gpm pW g n 1 902.25 1.112 904.9 l 16 90225 2.348 907.7 11 902.25 2.329 907.7 12 902.25 2.313 907.7 13 902.25 2.223 907.5 4 14 902.25 2.06 907.1 15 902.25 1.762 906.4 16 90225 1.717 906.3 17 90225 1.692 906.2 18 902.25 1.629 906.1 l 19 902.25 1.265 905 2 2 902.25 1.061 904.7 20 902.25 1.21 905.1 3 90225 1.096 904.8 l 4 902.25 1.142 904.9 5 902.25 1.178 905 6 902.25 1.238 905.1 7 902.25 1.513 905.8 8 902.25 1.701 906.2 l 9 902.25 1.875 906.6 A.CS.IN 902.25 1.745 906.3 A.CS.SUCT 897.833 -1.153 "* 895.1 A.CS.T 899.916 -0.116 '" 899.6 A. DIS 897.833 112.9 1162 A.lN 897.583 1.341 900.7 A.RH.lN 902.25 1.214 905.1 A.RH.T 897.583 1.627 901.4 A.SUC 897.833 -0.109 *" 897.6 ACSD2 931.917 136.7 1252 ACSD3 981.188 0 (source) 981.2 ACSD4 900.156 261.3 *" 1512 ACSDS 900.74 237.1 '" 1456 ACSD6 925.875 14.64 960.2 ACSD7 928 8.636 948.2 ACSD8 927 0 (source) 927 ACSD9 971.25 114.9 1240 ACSDSCG 899.635 264.1 "* 1518 ADISTEE 901.083 105.8 1149 B.CS.IN 902.25 1.219 905.1 B.CS.SUCT 897.833 -1,38 *" 894.6 B.CS.T evs.665 U.v,0 s00 Calc / No. V75100.NSP97.00501 ATTACHMENT _,j3 Page T.3 of NT PIPE-FLO ver 5.01 pg 2

LINEUP NODES 06/12/97 8:34 sm l NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi g ft l B. DIS 899.5 107.6 1151 B.IN 897.583 1.054 900.1 .

1 B.RH.lN 902.25 1.056 904.7 j B.RH.T 897.583 1.52 901.1 B.SUC 897.833 -0.941 "* 895.6 BCSD2 927.833 134.9 1244 BCSD3 980.38 0 (source) 980.4 BCSD4 899.896 250.6 "* 1487 BCSD5 901.688 226.2 *" 1432 BCSD6 930.333 0 (source) 930.3 BCSD7 978.5 106.9 1229 BCSDSCG 899.583 253.5 "* 1493 BDISTEE 908 98.57 1139 C. DIS 897.833 114.2 1165 i C.lN 897.583 1.453 901 C.SUC 897.833 -0.543 "* 896.6 D. DIS. 899.5 106.8 1150 D.DISA 908 98.78 1139 D.IN 897.583 0.939 899.8 D.SUC 897.833 -0.555 "* 896.5 l HP.lN 902.25 1.682 906.2 HP.T 901.615 1.953 906.2 M02013 940.91 37.94 1030 MO2012 940.917 69.64 1104 RC.lN 902.25 2.206 907.4 RC.T 902.25 2.206 907.4 RECIRC2 951.75 0 (source) 951.8 RECIRCA 930.168 74.23 1104 RECIRCB 930.167 68.95 1092 RHRHXDA 916.333 93.62 1136 RHRHXDB 915.49 90.42 1127 RHRHXDC 916.336 91.39 1130 RHRHXDD 921.33 83.83 1118 RHRHXS1 909.406 100.6 1145 RHRHXS2 908 97.79 1137 SA 902.25 1.1 904.8 SB 902.25 2.36 907.8 SC 902.25 2.324 907.7 SD 902.25 1.662 906.1 TB 904.316 1.904 (source) 908.8 TC wu4. sic 1.vu+ (source) vue.c

Calc / No. V75100.NSP97.00501 ATNCHMENT 8 Page 8'l of !f3 PIPE-FLO ver 5.01 pg 3

. _ _ _. .-.- . . - - . _ . - . . -- .. .. . - . . - _. --_. . . - = - . .

t;NEUP NODES 06/12/97 8:34 cm

?

l NODE ELEVATION DEMAND PRESSURE H GRADE l ft gpm psi g ft TD 904.316 1.904 (source) 908.8 l

l l

l l l l

i l

l l

1 t

l I

l l

l i

I 1

L 1 l

l l

l Calc / No. V75100.NSP97.00501 ATTACHMENT b Page 88 0f 8 PIPE-FLO ver 5.01 pg 4

. . - - -. . . . . - . - . . - - . . - - . . - ~ . - . - . . - ~ . . . . . . _ . - . . . . -

LINEUP PIPELINES 06/12/97 8:34 sm PIPELINE FROM TO FLOW VEL dP HL gpm ft/see psi g ft !

l l A TA SA closed 0 0 0 l B TB SB 9586 11.61 (0.457) 0.997 i C TC SC 6313 7.644 (0.420) 1.082 i CDS1B B.CS.SUCT BCSDSCG 4199 *17.1 (254.9) (598.8)

- BCS - dP:(256.3) HL:(600.3)

CDS7A ACSD6 ACSD7 213.4

23.2 6.001 11.93 CROSSTIE RECIRCA <-> RECIRCB 8603

20.03 5.277 12.36 CS001A A.CS.IN A.CS.T 4284 *12.29 1.861 6.693 CS001B B.CS.lN B.CS.T 4199

12.05 1.179 5.126 CS003A A.CS.T A.CS.SUCT 4284

12.29 1.037 4.511 )

CS003B B.CS.T B.CS.SUCT 4199

12.05 1.42 5.378 CSD1A A.CS.SUCT ACSDSCG 4284

17.44 (265.2) (623) !

- A.CS - dP:(266.7) HL:(624.6)

CSD2A ACSDSCG ACSD2 4070

16.57 127.3 265.9 CSD2B BCSDSCG BCSD2 3990

16.25 118.7 249.6 CSD3A ACSD9 ACSD3 4070

28.62 114.9 259.1 CSD3B BCSD7 BCSD3 3990

28.06 106.9 248.5 CSD4A ACSDSCG ACSD4 213.4

14.31 2.758 5.939 ;

CSD4B BCSDSCG BCSD4 208.8

14 2.971 6.644 l CSD5A ACSD4 ACSDS 213.4

23.2 24.27 56.25 )

CSD5B BCSD4 BCSDS 208.8

22.71 24.35 55.24 l

CSD6A ACSD5 ACSD6 213.4

14.31 222.4 495.8 CSD6B BCSDS BCSD6 208.8 *14 226.2 501.2 CSD78 BCSD2 BCSD7 3990

16.25 27.97 14.84 CSD8A ACSD7 ACSD8 213.4

14.31 8.636 21.22 CSD9A ACSD2 ACSD9 4070

16.57 21.89 11.92 D TD SD 9852 11.93 0.242 2.633 H1 20 <-> 1 4624 5.102 0.098 0.229 H11 1 <-> B.RH.IN 4624 5.599 0.056 0.131 H12 A.RH.IN <> 20 4624 5.599 0.004 0.010 l H2 3 2 4041 4.459 0.036 0.083 H21 SA 3 4041 4.893 0.003 0.007 H22 2 B.RH.lN 4041 4.893 0.005 0.012 l

H3 5 4 4041 4.459 0.036 0.084 H31 B.CS.lN 5 4041 4.893 0.040 0.095 H32 4 SA 4041 4.893 0.043 0.100 H4a 9 8 8240 9.091 0.174 0.408 H4a1 SB 9 8240 9.977 0.485 1.136 H4a2 8 HP.lN 8240 9.977 0.019 0.045 H4b 7 6 8240 9.091 0.275 0.644 H4bi HP.lN 7 8240 9.977 0.169 0.396 H4b2 6 B.CS.IN 8240 9.977 0 0.045 Calc / No. V75100.NSP97.00601 ATTACHMENT @> Paged o.019f/W PIPE-FLO ver 5.01 pg 5

-. . . - . - - . _ - -._..._. - ,_ .-.~ _ . - - - . - . - . -. _ . . . . .. .

LINEUP PlPELINES 06/12/97 8:34 cm PIPEUNE FROM TO FLOW VEL dP HL 1 gpm ft/sec psi g ft

. )

l H5 10 11 1346 1.484 0.019 0.044 H51 11 SC 1346 1.629 0.005 0.011 H52 SB 10 1346 1.629 0.013 0.030 H6a 12 '13 7659 8.45 0.090 0.212 H6a1 13 RC.IN 7659 9.273 0.017 0.039 4 H6:2 SC 12 7659 9.273 0.011 0.026 H6b 14 15 7659 8.45 0.298 0.698 H6b1- 15 A.CS.lN 7659 9.273 0.017 0.039 H6b2 RC.lN 14 7659 9.273 0.146 0.342 H7 16 17 3375 3.724 0.025 0.059 )

H71 17 SD 3375 4.086 0.030 0.070 ,

1 H72 A.CS.lN 16 3375 4.086 0.028 0.067 H8 18 19 13227

11.59 0.364 0.852 ;

H81 19 A.RH.IN 13227

16.01 0.052 0.121 l H82 SD 18 13227

16.01 0.033 0.076 HP001 HP.lN HP.T 0 0 (0.271) 0 j HP002 HP.T HP.SUCT closed 0 0 0 j RC001 RC.lN RC.T 0 0 0 0 ]

RC002 RC.T RC.SUCT closed 0 0 0 RH001A A.RH.lN A.RH.T 8603 9.491 (0.414) 3.699 RH001B B.RH.lN B.RH.T 8666 9.561 (0.464) 3.58 RH002A C.IN A.IN 4276 4.717 0.112 0.261 RH002B B.lN D.lN 4343 4.791 0.115 0.268 RH003A A.RH.T C.lN 8603 9.491 0.174 0.408 i RH003B B.RH.T B.lN 8666 9.561 0.466 1.092 RH004A C.IN C.SUC 4327 10.08 1.996 4.425 RH004B B.IN B.SUC 4323 10.07 1.994 4.421 RH005A A.IN A.SUC 4276 9.956 1.451 3.147 RH005B D.lN D.SUC 4343 10.11 1.495 3.25 RH006A A.SUC A. DIS 4276

12.27 (113) (264.7)

- ARHR - dP:(113.3) HL:(265.4)

RH006B B.SUC B. DIS 4323 *12.4 (108.5) (255.8)

- BRHR - dP:(109.8) HL:(257.2) !

RH006C C.SUC C. DIS 4327

12.41 (114.7) (268.7) l

- CRHR - dP:(115.1) HL:(269.5) l RH006D D.SUC D. DIS 4343

12.46 (107.3) (253)

- DRHR - dP:(108.6) HL:(254.5) l l

RH006DA D. DIS D.DISA 4343

17.68 7.989 10.21 RH007A A. DIS ADISTEE 4276

17.41 7.065 13.3 RH007B B. DIS BDISTEE 4323

17.6 9.006 12.59 RH007C C. DIS ADISTEE 4327

17.62 8.368 16.35 RH007D n ntc:A RDISTFm d'ta't in 11 n OnA 0.481 Calc / No. V76100.NSP97.00601 ATTACHMENT 6 Page N of./.,8 PIPE-FLO ver 5.01 pg 6

. . . .. - . . - . - . . . - - . - . _ ~ ~ . _ . . . - . - - - .. . . - . -- _

LINEUP PIPELINES 06/12/97 8:34 cm i

PIPELINE FROM TO FLOW VEL dP HL gpm ft/sec psi g ft RH008A ADISTEE RHRHXS1 8603

20.03 5.278 4.04 RH008B BDISTEE RHRHXS2 8666

20.18 0.778 . 6 72 RHRHXA- RHRHXS1 RHRHXDA 4378 10.19 6.938 9.322 j RHRHXS RHRHXS2 RHRHXDB 4080 9.5 7.374 9.781 RHXBYPSA RHRHXS1 RHRHXDA 4225 9.838 6.938 9.322 l l

RHXBYPSB RHRHXS2 RHRHXDB 4586 10.68 7.374 9.781 l RX01A RHRHXDA RHRHXDC 8603

20.03 2.231 5.222 l RX01B RHRHXDB RHRHXDD 8666

20.18 6.589 9.593 RX01C RHRHXDC RECIRCA 8603

20.03 17.16 26.35 I RX01D RHRHXDD RECIRCB 8666

20.18 14.88 26.01 RX02A RECIRCA MO2012 0 0 4.59 0 RX02B RECIRCB M02013 17268

30.36 31.02 61.9 RX02C MO2012 RECIRC1 closed 0 0 0 RX02D M02013 RECIRC2 17268

34.47 37.94 78 l

l l

i I

Calc / No. V75100.NSP97.00501 ATTACHMENT b Pag.58 or.LS PIPE-FLO ver 5.01 pg 7

l l DE&S !

Naperville, Illinois

\

l i

PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 )

l '

OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 -

CLIENT i Monticello Nuclear Station REFERENCE dTTACHMENT C FLO-SERIES MODEL PIPING AND NETWORK INPUT AND OUTPUT :

FOR CASE #2, e

6 REVISION O PAGE 59 PREPARED BY/DATE /,2 6/[dp OF /$

CHECKED BY/DATE

-w

O TB g q, TA TD q, TC Q B A D Bp H4a gtg4g H5 ,g H5p g6ag H6a q , 13 H4a4 9 SB 10 11 SC 12 RCtN '

HP W :

N ~

TtM1 B.CS IN B.RH ttA RH IN A.CS.:N H4by4gQggggggpl?1 N7 M% : H6b j H6b2 O 7 5 4 SA 3 2 120 1915017 16 , df001A _ 1$.CS.T g B.CS.T qpSg18 '

gy HP001 T RC001 RHOO1!!

CSCO3B . ,fSOO3A HP.SUCT .3 S UCT A.CS.Sb O HP.T q p 4 m HPOO2 RH001A A.RH.T RCOO2 B RH.T p ' '

r e

> / RH003)> C.IN A.tN D IN B.IN RC.SUCT hp g r 0 ""* *'l

/ < ano7"w I /

RHOO4B RHOO4A ,

i p

2 B.SUC C.SUC i RHOO58 _. ._ RHOO5A CDS1B D.SUC A.SUC CSD1A "U

5 BRHR /

CRHR DRHR ARHR D A.CS q BCS .

RHOO68 N RH006D RHOO6C RHOO5A

. ~ ~ .

BCSDSCo Com Duke Engggring & gges 06MWM 5:04 pm f, D. dis Pr : Linelist: OVRPRES2 RHM6DA by: J8eepPrD. g$araCirmM7^ CSO2A Lineup:

^ flO W rate: gpm g _g,SA hRHOO7D _

COmfqgggg RHOO88 ,

ACSE2 Pressure: pSie

+- / SD2B IDtSTgersion: PIPE .FLO vePHPEP level & grade: ft

/ _ _ _ _ _ _ . _ _ . _ _ . _ _ _ _ _ _ . _ _ _ _ _ _ _

- . ~ .

RH006D RHOO68 RHOO6C RH00iA ACSDSCG CSD4A CSD4B j i 4>BDS hp C. DIS hpADS th =

u qp D. DIS ADISTEE N / D.DtSA [p RH007Dqg ,RH0078 i

,y i

, yg RH0088 BDtSTEE

o. 1H00BA , ,

O RHRHXS2h p_. RHRHXS1 ' e

g qp ACSO4 g , RHRHXE F HXBYPSB RHRHX), 1HXBYPSA e4 3CSD4 q(BCSD2

SD5A 8 CSD9A g

RHRHXDB 4 RHRHXDAep RXO18 IX01A CSD7B

> RHRHXDD qp RHRHXDC qp qp ACSD5 y RX01D 1X01C Z ACSc9qp

< SD50 CROSSTIE g RECtRCS p .

p RECIRCA CSD6A m

Z RXO2A

--t jpBCSD7 1XO2B p M02013qp q, MO2012 ,

i CSD3A 4> ACSD6

SD3B RXO2D RXO2C CDS7A y ,

4> dI BCSDS Dyy 4> RECIRC2 RECtRC1 jp BCSD3 ACSD3 S.

s j,ACSD7 D

CSD6B Company: Duke Engineering & Services 06/11/97 5:04 pntSDBA Project: Linelist: OVRPRES2 by: Joseph D. Sparacino Lineup:

Comments: flow rate: gpm

. . . pressure: . psig

, ,j Q , ,

' Version: ',' PING-FLO irer 5.01 ; [' [' .' '

' level & grade: ft

Crmp ny: Duks Engine 1 ring & SIrviers 06/12/97 8:19 am Pr$ct: Systim: OVRPRES2 by: Joseph D. Sp:r cino rsv: 06/12/97 8:19 cm SYSTEM REPORT Created: 11/04/9611:56 am Pipes: 93 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6

! NSP RHR and CS piping model, SP Temp.152.7'F. and 0 psig cont press. Containment overpressure cales.

SYSTEM NODES NODE ELEVATION PIPELINES IN PIPELINES OUT 1 902.25 H11 H1 i 10 902.25 H52 HS 2

11 902.25 H5 H51 -

J 12 902.25 H6a2 H6a W

13 902.25 H6a H6a1 14 902 3 H6b2 H6b 15 902.25 H6b H6bt i 16 902.25 H72 H7

} 17 902.25 H7 H71 1

18 902.25 H82 H8 19 902.25 H8 H81 i

2 902.25 H2 H22 20 902.25 H1 H12 j 3 902.25 H21 H2 4 902.25 H3 H32 5 902.25 H31 H3 6 902.25 H4b H4b2 7 902.25 H4b1 H4b 8 902.25 H4a H4a2 9 902.25 H4a1 H4a A.CS.IN 902.25 H6bi CS001A H72 A.CS.SUCT 897.833 CS003A CSD1A A.CS.T 899.916 CS001A CS003A A. DIS 897.833 RH006A RH007A PIPE-FLO ver gp/ No. V75100.NSP97.00501 ATTACHMENT C PagebM of _Lff pg j

._ . . .- - ~ _ . . . . _ . .-.

SYSTEM NODES 06/120' 8:19 tm I NODE ELEVATION PIPELINES IN PIPELINES OUT ft l A.IN 897.583 RH002A RH005A l

l A.RH.lN 902.25 H12 RH001A H81 l

l l A.RH.T 897.583 RH001A RH003A .

l

[ A.SUC 897.833 RH005A RH006A l ACSD2 931.917 CSD2A CSD9A ACSD3 981,188 CSD3A l

ACSD4 900.156 CSD4A CSD5A

. l ACSD5 900.74 CSDSA CSD6A I ACSD6 925.875 CSD6A CDS7A ACSD7 928 CDS7A CSD8A -

ACSD8 927 CSD8A ACSD9 971.25 CSD9A CSD3A ACSDSCG 899.635 CSD1A CSD2A CSD4A e l ADISTEE 901.083 RH007A RH008A l RH007C B.CS.IN 902.25 H4b2 CS001B

l H31 B.CS.SUCT 897.833 CS003B CDS1B B.CS.T 899.885 CS001B CS0038 B. DIS 899.5 RH006B RH007B B.IN 897.583 RH003B RH002B RH004B B R H.IN 902.25 H22 H11 RH001B B.RH.T 897.583 RH001B RH0033 B.SUC 897.833 RH004B RH006B BCSD2 927.833 CSD2B CSD78 BCSD3 980.38 CSD3B BCSD4 899.896 CSD4B CSDSB BCSD5 901.688 CSDSB CSD6B BCSD6 930.333 CSD6B -

PIPE-FLO ver 9.$ No. V75100.NSP97.00501 ATTACHMENT C PageM of f.ff pg 2

l SYSTEM NODES 06/12/97 8:19 cm l

NODE ELEVATION PIPELINES IN PIPELINES OUT ft BCSD7 978.5 CSD7B CSD3B BCSDSCG 899.583 CDS1B CSD2B CSD4B BDISTEE 908 RH007B RH008B RH007D C. DIS 897.833 RH006C RH007C 1

C.IN 897.583 RH003A RH002A RH004A ,

I C.SUC 897.833 RH004A RH006C D. DIS 899.5 RH006D RH006DA D.DISA 908 RH006DA RH007D D.lN 897.583 RH002B RH005B l

D.SUC 897.833 RH005B RH006D HP.lN 902.25 H4a2 H4bi HP001 HP.SUCT 901.615 HP002 HP.T 901.615 HP001 HP002 M02013 940.91 RXO2B RX02D MO2012 940.917 RX02A RXO2C RC.lN 902.25 H6a1 H6b2 RC001 RC.SUCT 899.042 RC002 RC.T 902.25 RC001 RC002 RECIRC1 951.75 RXO2C RECIRC2 951.75 RX02D RECIRCA 930.168 CROSSTIE RXO2A RX01C RECIRCB 930.167 RX01D CROSSTIE RXO2B RHRHXDA 916.333 RHRHXA RX01A RHXBYPSA RHRHXDB 915.49 RHRHXB RX01B RHXBYPSB RHRHXDC 916.336 RX01A RX01C

's PIPE-FLO verggp/ No. V75100.NSP97.00601 ATTACHMENT l PageM of /69 pg 3

i SYSTEM NODES 06/12/97 8:19 Em

. -NODE ELEVATION PIPELINES IN PIPELINES OUT l ft RHRHXDD 921.33 RX018 RX01D RHRHXS1 909.406 RH008A RHRHXA RHXBYPSA RHRHXS2 908 RH008B RHRHXB RHXBYPSB SA 902.25 A H21

H32 1

SB 902.25 B H4a1 l H52 SC 902.25 C H6a2 HS1 SD 902.25 D H82 l H71 TA 904.316 A i

, TB 904.316 B TC 904.316 C f

TD 904.316 D l 3

l 1

l PIPE-FLO vergp/ No. V75100.NSP97.00501 ATTACHMENT C- Paged of15.i' pg 4

SYSTEM PIPES 06/12/97 8:19 sa PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP A 31 TA SA B 31 TB SB 4 C 31 TC SC 4 CDS15 16 B.CS.SUCT BCSDSCG BCS '

CDS7A 35 ACSD6 ACSD7

=

CROSSTIE 21 RECIRCB RECIRCA CS001A 16 A.CS.IN A.CS.T CS0018 16 B.CS.lN B.CS.T CS00A 16 A.CS.T A.CS.SUCT CS003B 16 B.CS.T B.CS.SUCT

, CSD1A 16 A.CS.SUC T ACSDSCG A.CS I CSD2A 16 ACSCSCG ACSl?2 CSD2B 16 BCGDSCG BCSD2 l CSD3A 35 ACSD9 ACSD3 CSD3B 35 BCSD7 BCSD3 CSD4A 16 ACSDSCG ACSD4 CSD4B 16 BCSDSCG BCSD4 CSD5A 35 ACSD4 ACSDS CSD5B 35 BCSD4 BCSD5 CSD6A 16 ACSD5 ACSD6 j CSD6B 16 BCSDS BCSD6 CSD7B 16 BCSD2 BCSD7 CSD8A 16 ACSD7 ACSD8 CSD9A 16 ACSD2 ACSD9 D 31 TD SD l H1 26 1 20 H11 31 B.RH.IN 1 H12 31 20 A.RH.lN H2 2S 3 2 j H21 31 SA 3 H22 31 2 B.RH.IN H3 26 5 4 H31 31 B.CS.IN 5 H32 31 4 SA >

H4a 26 9 8

H4a1 21 SB 9 H4a2 31 8 HP.IN H4b 26 Y 6 H4bi 31 HP.lN 7 H4b2 31 6 B.CS.lN H5 26 10 11 H51 31 11 SC Calc / No. V75100.NSP97,00501 ATTACHMENT L Page bbof M PIPE-FLO ver 5.01' Pg 5

SYSTEM PIPES 06/12/97 8:19 Em i PIPELINE SPEC FROM_ NODE TO_, NODE PUMP / COMP H52 31 SB 10 H6a 26 12 13 H6a1 31 13 RC.lN ,

H6a2 31 SC 12 H6b 26 14 15 H6b1 31 15 A.CS.lN i

H6b2 31 RC.IN 14 H7 26 16 17 H71 31 17 SD H72 31 A.CS.lN 16 H8 26 18 19 H81 31 19 A.RH.lN H82 31 SD 18 I HP001 21 HP.IN HP.T HP002 21 HP.T HP.SUCT RC001 16 RC.IN RC.T l RC002 16 RC.T RC.SUCT RH001A 26 A.RH.IN A.RH.T RH001B 26 B.RH.lN B.RH.T

( RH002A 26 C.IN A.IN i RH002B 26 B.lN D.IN RH003A 26 A.RH.T C.IN RH003B 26 B.RH.T B.lN RH004A 21 C.IN C.SUC RH004B 21 B.IN B.SUC RH005A 21 A.lN A.SUC RH005B 21 D.lN D.SUC RH006A 16 A.SUC A. DIS ARHR RH006B 16 B.SUC B. DIS BRHR RH006C 16 C.SUC C. DIS CRHR RH006D 16 D.SUC D. DIS DRHR RH006DA 16 D. DIS D.DISA RH007A 16 A. DIS ADISTEE RH007B 16 B. DIS BDISTEE RH007C 16 C. DIS ADISTEE RH007D 21 D.DISA BDISTEE RH008A 21 ADISTEE RHRHXS1 RH008B 21 BDISTEE RHRHXS2 RHRHXA 21 RHRHXS1 RHRHXDA RHRHXB 21 RHRHXS2 RHRHXDB RHXBYPSA 21 RHRHXS1 RHRHXDA RHXBYPSB 21 RHRHXS2 RHRHXDB Cale/ No. V75100.NSP97.00501 ATTACHMENT C Page [O7 of./5_f PIPE-FLO ver 5.01 pg 6

SYSTEM PIPES 06/12/97 8: 19 Em PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP

. RX01A 21 RHRHXDA RHRHXDC RX01B 21 RHRHXDB RHRHXDD

]

RX01C 21 RHRHXDC RECIRCA 3

RX01D 21 RHRHXDD RECIRCB RX02A 21 RECIRCA MO2012 RX02B 21 RECIRCB M02013 RX02C 35 MO2012 RECIRC1 4

RX02D 35 M02013 RECIRC2 RXO1A 16 . .

4 i

~

Calc / No. V75100.NSP97.00601 ATTACHMENT C- PageMof /6 '7 PIPE-FLO ver 5.01 pg 7

SYSTEM COMPONENTS 06/12/97 8:19 Em l PUMP / COMP PERFORMANCE DATA A.CS gpm: 0 2179 3990 5040 5755

~

ft: 850.3 795.5 664 536.2 411.7 egn: 850.3 - 4.49715e-006 Q ^ 2.12033 ARHR gpm; O 3365- 4000 4250 4540 ft: 810.3 498.9 350 280 171.8 egn: 810.3 - 1.3787e-006 Q ^ 2.36763 BCS gpm: 0 1948 3080 4875 5600 I i

ft: 844 770.1 719.4 535.2 418.1 egn: 844 - 0.000218414 Q ^ 1.66917 l l

BRHR gpm; 0 36SS 4000 4250 4408 ft: 813.8 436 350 280 230 egn: 813.8 - 2.04305e-006 Q ^ 2.32005 CRHR gpm: 0 3540 4000 4250 4440 l ft: 763.9 461.1 360 290 235.4 egn: 763.9 - 5.58043e-007 Q ^ 2.46066 DRHR gpm: 0 3542 4000 4250 4425 ft: 810.1 463 350 285 227 egn: 810.1 - 2.16007e-006 Q ^ 2.31196 l

i Calc / No. V75100.NSP97.00501 ATTACHMENT C Page bT of /f9 PIPE-FLO ver 5.01 pg 8

C:mpIny: Duk2 Enginsinng & Szrvicts 06/12/97 8:20 am Prrjtet: Systrm: OVRPRES2 by: Josrph D. Spiricino rav: 06/12/97 8:19 Em PIPELIST REPORT Created: 11/04/9611:56 am Pipes: 93 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.152.7'F. and 0 psig cont. press. Containment overpressure cales.

SPECIFICATIONS SPECIFICATION PIPE MATERIAL FLUID VALVE TABLE DESIGN LIMITS Sch / Roughness Temp / Pres Vel / Pres 16 LB30 Steel Water Standard 0 - 12 ft/sec rev: 06/12/97 8:18 am Sch 40 152.7 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 21 LB31 Steel Water Standard 0 - 12 ft/see rey: 06/12/97 8:18 am Sch 30 152.7 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 26 LB32 Steel Water Standard 0 - 12 ft/sec rev: 06/12/97 8:19 am Sch 20 152.7 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 31 LB34 Steel Water Standard 0 - 12 ft/sec l

rev: 06/12/97 8:19 am Sch 60 152.7 'F 0 - 200 psi g 0.0018 in 0 psig Size for: 8 ft/sec 35 LB34a Steel Water Standard 0 - 12 ft/sec rey: 06/12/97 8:19 am Sch 80 152.7 'F 0 - 200 psi g 0.0018 in 0 psig Size for: 8 ft/sec ;

l 1

l Calc / No. V75100.NSP97.00501 ATTACHMENT E Page 90 of /69 PIPE-FLO ver 5.01 pg i

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PIPELIST 06/12/97 8:20 am l

PlPELINE SPEC MATERIAL LENGTH FLUlO VALVES l Size / Sch ft Temp / Pres Total-K A 31 Steel 3.6777 Water 1.163 20 in / 60 152.7 'F / 0 psi g

! B 31 Steel 3.6777 Water 0.4469 l 20 in / 60 152.7 *F / 0 psi g C 31 Steel 3.6777 Water 1.163 20in / 60 152.7 'F / 0 psi g CDS1B 16 Steel 3.45 Water 0.2689 10 in / 40 152.7 'F / 0 psi g CDS7A 35 Steel 7.73835 Water 0.478 2 in / 80 152.7 'F / 0 psi g CROSSTIE 21 Steet 49.0188 Water 1.403 14 in / 30 152.7 'F / 0 psi g CS001A 16 Stee! 41.8129 Water 2.285 12 in / 40 152.7 'F / 0 psi g CS001B 16 Steel 42.5259 Water 1.695 12 in / 40 152.7 'F / 0 psi g CS003A 16 Steel 10.7215 Water 1.779 12 in / 40 152.7 'F / 0 psi g l CS003B 16 Steel 27.109 Water 2.018 12 in / 40 152.7 'F / 0 psi g l

CSD1A 16 Steel 3.7973 Water 0.2689 10 in / 40 152.7 *F / 0 psi g l

CSD2A 16 Steel 108.553 Water 60.59 10 in / 40 152.7 'F / 0 psi g CSD2B 16 Steel 108.723 Water 59.14 10 in / 40 152.7 *F / 0 psi g CSD3A 35 Steel 57.0055 Water 19.08 8 in / 80 152.7 'F / 0 psi g CSD3B 35 Steel 55.4392 Water 19.08 8 in / 80 152.7 'F / 0 psi g CSD4A 16 Steel 2.22525 Water 1.664 2.5 in / 40 152.7 'F / 0 psi g CSD4B 16 Steel 2.7485 Water 1.93 2.5 in / 40 152.7 'F / 0 psi g CSD5A 35 Steel 0.67045 Water 6.654 2 in / 80 152.7 'F / 0 psi g CSDSB 35 Steel 2.0608 Water 6.654 2 in / 80 152.7 'F / 0 psi g

~ CSDSA 16 Steel 38.6803 Water 152.5 2.5 in / 40 152.7 'F / 0 psi g CSD6B 16 Steel 101.051 Water 155.4 2.5 in / 40 152.7 'F / 0 psi g CSD7B 16 Steel 97.3901 Water 1.995 10 in / 40 152.7 'F / 0 pal g CSD8A 16 Steel 45.7585 Water 2.453 2.5 in / 40 152.7 'F / 0 psi g CSD9A 16 Steel 75.8885 Water 1.53 10 in / 40 152.7 'F / 0 psi g Calc / No. V75100.NSP97.00501 ATTACHMENT O- Page Il o'i /57 PIPE-FLO ver 5.01 pg 2

PIPELIST 06/12/97 8:20 trn PIPELINE SPEC MATERIAL LENGTH FLUID VALVES Size / Sch ft Temp / Pres Total-K D 31 Steel 3.6777 Water 1.163 20 in / 60 152.7 'F / 0 psi g H1 26 Steet 52 2054 Water 0.144 20 in / 20 152.7 'F / 0 psi g H11 31 Steel 1.9171 Water 02536 20 in / 60 152.7 'F / 0 psi g H12 31 Steet 1.9171 Water 0.00366 20 in / 60 152.7 'F / 0 psi g H2 26 Steel 24.1869 Water 0.072 20 in / 20 152.7 'F / 0 psi g H21 31 Steel 1.9171 Water 0.00366 20 in / 60 152.7 *F / 0 psi g H22 31 Steel 1.9171 Water 0.01484 20 in / 60 152.7 *F / 0 psi g H3 26 Steel 24.3777 Water 0.072 20 in / 20 152.7 'F / 0 psi g H31 31 Steel 1.4375 Water 0.2425 20 in / 60 152.7 'F / 0 psi g H32 31 Steel 1.9171 Water 0.2536 20 in / 60 152.7 'F / 0 psi g H4a 26 Steel 31.4S75 Water 0.072 20 in / 20 152.7 'F / 0 psi g H4a1 31 Steel 1.9171 Water 0.7201 20 in / 60 152.7 'F / 0 psi g H4a2 31 Steel 1.725 Water 0.01484 20 in / 60 152.7 'F / 0 psi g H4b 26 Steel 45.6907 Water 0.144 20 in / 20 152.7 'F / 0 psi g H4bi 31 Steel 1.725 Water 0.2425 20 in / 60 152.7 *F / 0 psi g H4b2 31 Steel 1.725 Water 0.01484 20 in / 60 152.7 'F / 0 psi g HS 26 Steet 108.244 Water 0.288 20 in / 20 152.7 *F / 0 psi g H51 31 Steel 1.9171 Water 0.2536 20 in / 60 152.7 'F / 0 psi g H52 31 Steel 1.9171 Water 07201 20 in / 60 152.7 'F / 0 psi g H6a 26 Steel 15.1777 Water 0.072 20 in / 20 152.7 'F / 0 psi g H6a1 31 Steel 1.725 Water 0.01484 20 in / 60 152.7 'F / 0 psi g H6a2 31 Steel 1.9171 Water 0.00366 20 in / 60 152.7 'F / 0 psi g H6b 26 Steel - 61.7884 Water 0.144 20 in / 20 152.7 'F / 0 psi g H6b1 31 Steel 1.725 Water 0.01484 20 in / 60 152.7 'F / 0 psi g Calc / No. V75100.NSP97.00501 ATTACHMENT C- Page W of _/ff PIPE-FLO ver 5.01 pg 3

PIPELIST 06/12/97 8:20 am PIPELINE SPEC MATERIAL LENGTH FLU O VALVES Size / Sch ft Tema / Pres Total-K H6b2 31 Steet 1.725 Water 0.2425 20 in / 60 152.7 *F / 0 psi g H7 26 Steel 24.3777 Water 0.072 20 in / 20 152.7 'F / 0 psi g H71 31 Steel 1.9171 Water 0.2536 20 in / 60 152.7 'F / 0 psi g H72 31 Steel 1.725 Water 0.2425 20 in / 60 152.7 'F / 0 psi g H8 26 Steel 24.1868 Water 0.072 20 in / 20 152.7 'F / 0 psi g H81 31 Steel 1.0171 Water 0.01484 l 20 in / 60 152.7 'F / 0 psi g H82 31 Steel 1.9171 Water 0.00366 20 in / 60 152.7 'F / 0 psi g HP001 '21 Steet 67.5027 W ater 3.127 14 in / 30 152.7 'F / 0 psi g HP002 21 Steel 9.3679 Water 1.356 14 in / 30 152.7 'F / 0 psi g RC001 16 Steel 22.7965 Water 4.054 6 in / 40 152.7 'F / 0 psi g RC002 16 Steel 56.5179 Water 1.298 6 in / 40 152.7 'F / 0 psi g RH001A 26 Steel 62.1357 Water 2.161 20 in / 20 152.7 'F / 0 psi g RH001B 26 Steel 55.6198 Water 2.09 20 in / 20 152.7 'F / 0 psi g RH002A 26 Steet 5.75 W ater 0.7101 20 in / 20 152.7 'F / 0 psi g RH002B 26 Steel 5.3671 Water 0.7101 20 in / 20 152.7 'F / 0 psi g RH003A 26 Steel 7.1093 Water 0.2367 20 in / 20 152.7 'F / 0 psi g RH003B 26 Steel 7.6671 W ater 0.7101 20 in / 20 152.7 'F / 0 psi g RH004A 21 Steel 14.758 Water 2.63 14 in / 30 152.7 'F / 0 psi g RH004B 21 Steet 14.95 Water 2.63 14 in / 30 152.7 'F / 0 psi g RH005A 21 Steel 14.758 Water 1.867 14 in / 30 152.7 'F / 0 psi g RH005B 21 Steet 14.95 Water 1.867 14 in / 30 152.7 'F / 0 psi g RHOGM 16 Steel 1.15 W ater 0.2977 12 in / 40 152.7 'F / 0 psi g RH006B 16 Steel 3.0671 Water 0.5573 12 in / 40 152.7 *F / 0 psi g RH006C 16 Steel 1.15 Water 0.2977 12 in / 40 152.7 'F / 0 psi g Calc / No V75100.NSP97.00501 ATTACHMENT C- Page Dof /O PlPE-FLO ver 5.01 pg 4

PIPELIST 06/12/97 8:20 Em PIPELINE SPEC MATERIAL LENGTH FLUID VALVES Size / Sch ft Temp / Pres Total-K RH006D 16 Steel 3.06671 Water 0.5573 12 in / 40 152.7 'F / 0 psi g RH006DA 16 Steel 20.7 Water 1.76 10 in / 40 152.7 'F / 0 psi g RH007A 16 Steel 17.6094 Water 2.534 10 in / 40 152.7 'F / 0 psi g RH007B 16 Steet 19.2625 Water 2298 10 in / 40 152.7 'F / 0 psi g RH007C 16 Steel 19.7656 Water 3.065 10 in / 40 152.7 'F / 0 psi g RH007D 21 Steet 4.025 Water 0.2543 14 in / 30 152.7 'F / 0 psi g RH008A 21 Steel 11.7875 Water 0.5086 14 in / 30 152.7 'F / 0 psi g RH0080 21 Steel 2.875 Water 0.2543 14 in / 30 152.7 'F / 0 psi g RHRHXA 21 Steel 28.4145 Water 5.436 14 in / 30 152.7 'F / 0 psi g RHRHXB 21 Steel 54.8343 Water 6.316 14 in / 30 152.7 'F / 0 psi g RHXBYPSA 21 Steel 29.4849 Water 5.85 14 in / 30 152.7 'F / 0 psi g RHXBYPSB 21 Steel 15.4172 W ater 5.341 14 in / 30 152.7 'F / 0 psi g RX01A 21 Steel 6,3849 Water 0.763 14 in / 30 152.7 *F / 0 psi g RX01B 21 Steel 20.748 Water 1.272 14 in / 30 152.7 'F / 0 psi g RX01C 21 Steel 83.5906 Water 3.24 14 in / 30 152.7 'F / 0 psi g RXO10 21 Steet 73.7917 W ater 3.24 14 in / 30 152.7 'F / 0 psi g RXO2A 21 Steel 12.3625 Water 4.454 16 in / 30 152.7 'F / 0 psi g RX028 21 Steel 12.3625 Water 4.207

?6 in / 30 152.7 'F i 0 psi g RXO2C 35 Snel 102.769 Water 3.252 ,

16:n / 80 152.7 'F / 0 psi g !

RX02D 35 StetI 97.9537 W ater 3.184 !

1G in / 80 152.7 'F / 0 psi g RXO1A 16 Steel 6.3849 Water 0.7645 14 in / 40 152.7 'F / 0 psi g i

Calc / No. V75100.NSP97.00501 ATTACHMENT C- Page Wof /5'T PIPE-FLO ver 5.01 pg 5

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Comp ny: Duka Enginnring & Sirvicts 06/12/97 8.20 sm Projict: Systim: OVRPRES2 by: Josiph D. Spir:cino rsv: 06/12/97 8:19 am Created: 11/04/9611:56 am Pipes: 93 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.152.7'F. and 0 psig cont. press. Containment overpressure cales.

PIPE MATERIALS LIST PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft A 31 Steel 3.6777 1-Fixed K strainer 20 in / 60 1-Tee Flow Thru Branch l

l B 31 Steel 3.6777 1-Fixed K STRAINER 20 in / 60 C 31 Steel 3.6777 1-Fixed K STRAINER 20 in / 60 1-Tee Flow Thru Branch CDS1B 16 Steel 3.45 1-Elbow Short - r/d 1 @ 90*

10 in / 40 CDS7A 35 Steet 7.73835 1-Elbow Short - r/d 1 @ 90*

2 in / 80 1-Reducer Enlargement 2 X 2.5 CROSSTIE 21 Steel 49.0188 3-Elbow Short - r/d 1 @ 90' 14 in / 30 1-Tee Flow Thru Run 1-Reducer Contraction 16 X 14 1-Reducer Enlargement 14 X 16 2-Gate Wedge Disc CS001A 16 Steel 41.8129 4-Elbow Short - r/d 1 @ 90*

12 in / 40 1-Gate Wedge Disc 1-Gate Double Disc 1-Tee Flow Thru Run 1-Tee Flow Thru Branch CS0018 16 Steet 42.5259 1-Elbow Short - r/d 1 @ 90*

12 in / 40 1-Elbow Short - r/d 1 @ 45' 1-Tee Flow Thru Run 1-Gate Wedge Disc 1-Gate Double Disc 1-Tee Flow Thru Branch CS003A 16 Steel 10.7215 3-Elbow Short - r/d 1 @ 90' 12 in / 40 1-Fixed K vel coretn CS003B 16 Steel 27.109 1-Elbow Short - r/d 1 @ 90*

12 in / 40 4-Elbow Short - r/d 1 @ 45' 1 Fixed K vel coretn CSD1A 16 Steel 3.7973 1-Elbow Short - r/d 1 @ 90' 10 in / 40 Calc / No. V75100.NSP97.00501 ATTACHMENT C- Page 7Iof /,ff PIPE-FLO ver 5.01 pg 1

PIPE MATERIALS LIST 06/12/97 8:20 Em PIPELINE SPEC MATERIAL LENGTH VALVES 2. FITTINGS i Size / Sch ft !

l CSD2A 16 Steet 108.553 1-Tee Flow Thru Run 1 10 in / 40 1-Swing Check Vertical 5-Elbow Short - r/d 1 @ 90' l 8-Elbow Short - r/d 1 @ 45' !

1-Fixed K Flow Element 1 Fixed K Res. Orifice CSD2B 16 Steel 108.723 4-Elbow Short - r/d 1 @ 90' 10 in / 40 1-Swing Check Vertical 2-Elbow Short - r/d 1 @ 45' 1-Tee Flow Thru Run 1-Fixed K Res. Orifice 1-Fixed K Flow Element CSD3A 35 Steel 57.0055 3-Gate Wedge Disc l 8 in / 80 1-Swing Check Angled i 6-Elbow Short - r/d 1 @ 90*

1-Fixed K Spargers i

CSD3B 35 Steel 55.4392 3-Gate Wedge Disc l 1 Swing Check Angled 8 in / 80 6-Elbow Short - r/d 1 @ 90* j 1-Fixed K Sparger i CSD4A 16 Steel 2.22525 1-Elbow Short - r/d 1 @ 45' ;

2.5 in / 40 1-Tee Flow Thru Branch 1-Reducer Contraction 2.5 X 2 CSD4B 16 Steel 2.7485 2-Elbow Short - r/d 1 @ 45*

2.5 in / 40 1-Tee Flow Thru Branch 1-Reducer Contraction 2.5 X 2 CSDSA 35 Steel 0.67045 1-Globe Valve 2 in / 80 1-Reducer Enlargement 2 X 2.5 CSD5B 35 Steel 2.0608 1-Globe Valve 2 in / 80 1-Reducer Enlargement 2 X 2.5 CSD6A 16 Steel 38.6803 1-Elbow Short - r/d i @ 45' 2.5 in / 40 2-Elbow Short - r/d 1 @ 90' 1-Reducer Contraction 2.5 X 2 1 Fixed K Orifice Min.

CSD6B 16 Steel 101.051 10-Elbow Short - t/d 1 @ 90' 2.5 in / 40 2-Elbow Short - r/d i @ 45' 1-Fixed K Orifice Min.

CSD7B 16 Steel 97.3901 1-Heducer Contraction 10 X 8 10 in / 40 4-tilbow Short - r/d 1 @ 90*

bElbow Short - r/d 1 @ 45' Calc / No. V75100.NSP97.00501 ATTACHMENT C. Page 7b of /12 PlPE-FLO ver 5.01 pg 2

P!PE MATERIALS LIST 06/12/97 8.20 Em PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft 1-Tee Flow Thru Run CSD8A 16 Steel 45.7585 6-Elbow Short - r/d 1 @ 90' I 2.5 in / 40 1-Elbow Short - r/d 1 @ 45' CSD9A 16 Steel 75.8885 1 Reducer Contraction 10 X 8 10 in / 40 1-Tee Flow Thru Run 3-Elbow Short - rid 1 @ 90' l

D 31 steel 3.6777 1-Fixed K strainer l 20 in / 60 1-Tee Flow Thru Branch 1 H1 26 Steel 52.2054 2-Fixed K 22.5 mitre 20 in / 20 )

H11 31 Steet 1.9171 1-Fixed K contraction j 20 in / 60 1-Tee Flow Thru Run H12 31 Steel 1.9171 1 Fixed K er.'argement 20 in / 60 1

H2 26 Steel 24.1868 1-Fixed K 22.5 nitre 20 in / 20 H21 31 Steci 1.9171 1-Fixed K enlar!jernent 20 in / 60 H22 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 H3 26 Steel 24.3777 1-Fixed K 22.5 mitre 20 in / 20 H31 31 Steet 1.4375 1-Fixed K enlarge.nent 20 in / 60 1-Tee Flow Thru Run H32 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 1-Tee Flow Thru Run H4a 26 Steel 31.4675 1-Fixed K 22.5 mitre 20 in / 20 H4a1 31 Steet 1.9171 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Branch H4a2 31 Steel 1.725 1-Fixed K contraction 20 in / 60 H4b 26 Steel 45.6907 2-Fixed K 22.5 mitre 20 in / 20 -

H4bt 31 Steet 1.725 1-Fixed K enlargement Calc / No. V75100.NSP97.00501 ATTACHMENT C- Page 77 of /57 PIPE-FLO ver 5.01 pg 3

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l PIPE MATERIALS LIST 06/12/97 8:20 am l 1

PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS l Size / Sch ft 20 in / 60 1-Tee Flow Thru Run H4b2 31 Steel 1.725 1-Fixed K contraction 20 in / 60 HS 26 Steet 108244 4-Fixed K 22.5 mitre 20 in / 20 H51 31 Steet 1.9171 1-Tee Flow Thru Run 20 in / 60 1 Fixed K contraction H52 31 Steet 1.9171 1-Tee Flow Thru Branch 20 in / 60 1-Fixed K enlargement H6a 26 Steel 15.1777 1 Fixed K 22.5 mitre 20 in / 20 .

l H6a1 31 Steel 1.725 1 -Fixed K contraction 20 in / 60 i

H6a2 31 Steel 1.9171 1-Fixed K enlargement l 20 in / 60 l

H6b 26 Steet 61.7884 2-Fixed K 22.5 mitre 20 in / 20 H6b1 31 Steel 1.725 1-Fixed K contraction 20 in / 60 H6b2 31 Steel 1.725 1-Fixed K enlargement 20 in / 60 1 Tee Flow Thru Run H7 26 Steel 24.3777 1-Fixed K 22.5 mitre 20 in / 20 H71 31 Steel 1.9171 1-Tee Flow Thru Run 20 in / 60 1-Fixed K contraction H72 31 Steel 1.725 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Run HB 26 Steel 24.1868 1-Fixed K 22.5 mitre 20 in / 20 H81 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 H82 31 Steet 1.9171 1-Fixed K enlargement 20 in / 60 HP001 21 Steet 67.5027 1-Elbow Long - r/d 1.5 @ 22.5*

14 in / 30 2-Gate Wedge Disc 1-Swing Check Angled 3-Elbow Long - r/d 1.5 @ 90' Calc / No. V75100.NSP97.00501 ATTACHMENT C, Page3 of f.f?

PIPE-FLO ver 5.01 P94

. PlPE MATERIALS LIST 06/12/97 8:20 om l

PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS .,

Size / Sch ft l 1-Tee Flow Thru Run 1-Tee Flow Thru Branch HP002 21 Steel 9.3679 1-Elbow Short - r/d 1 @ 90*

14 in / 30 1 Gate Wedge Disc 1-Fixed K vel coretn RC001 16 Steel 22.7965 1-Elbow Long - r/d 1.5 @ 67.5*

6 in / 40 1-Elbow Long - r/d 1.5 @ 45' i 1-Elbow Long - r/d 1.5 @ 90*

2-Gate Wedge Disc 1 Swing Check Angled 2-Tee Flow Thru Branch RC002 16 Steel 56.5179 1-Elbow Short - r/d 1 @ 90' l 6 in / 40 1-Fixed K vel coretn l

RH001A 26 - Steel 62.1357 2-Elbow Short'- t/d 1 @ 90' 20 in / 20 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1 Elbow Short - r/d 1 @ 45*

1-Tee Flow Thru Branch i

RH001B 26 Steel 55.6198 1-Elbow Long - r/d 1.5 @ 90*

20 in / 20 1 Eloow Short - t/d 1 @ 90*

1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Elbow Short - r/d 1 @ 45' 1-Tee Flov: Thru Branch RH002A 26 Steel 5.75 1 Tee Flow Thru Branch 20 in / 20 RH002B 26 Steel 5.3671 1-Tee Flow Thru Branch 20 in / 20 RH003A 26 Steet 7.1093 1-Tee Flow Thru Run 20 in / 20 RH003B 26 Steel 7.6671 1 Tee Flow Thru Branch 20 in / 20 RH004A 21 Steel 14.758 1-Tee Flow Thru Branch 14 in / 30 1-Reducer Contraction 20 X 14 1-Gate Wedge Disc 2-Elbow Short - t/d 1 @ 90' 1-Fixed K vel coretn RH004B 21 Steel 14.95 1-Reducer Contraction 20 X 14 14 in / 30 2-Elbow Short - r/d 1 @ 90*

1 Gate Wedge Disc 1-Tee Flow Thru Branch 1-Fixed K vel coretn Calc / No. V75100.NSP97.00501 ATTACHMENT C. Page N of.ff.f PIPE-FLO ver 5.01 pg 5

PIPE MATERIALS LIST 06/12/97 8:20 am 4

PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft RH005A 21 Steel 14.758 1-Reducer Contraction 20 X 14 14 in / 30 1-Gate Wedge Disc 2-Elbow Short - r/d 1 @ 90' 1-Fixed K vel coretn RH005B 21 Steel 14.95 1-Reducer Contraction 20 X 14 14 in / 30 2-Elbow Short - r/d 1 @ 90' 1-Gate Wedge Disc 1-Fixed K vel coretn RH006A 16 Steet 1.15 1-Reducer Contraction 12 X 10 12 in / 40 RH006B 16 Steel 3.0671 1-Elbow Short - r/d 1 @ 90' 12 in / 40 1-Reducer Contraction 12 X 10 RH006C 16 Steel 1.15 1-Reducer Contraction 12 X 10 12 in / 40 RH006D 16 Steel 3.06671 1-Elbow Short - r/d 1 @ 90' 12 in / 40 1-Reducer Contraction 12 X 10 RH006DA 16 Steel 20.7 3-Elbow Short - r/d 1 @ 90' 10 in / 40 1-Swing Check Vertical 1-Gate Wedge Disc 1-Reducer Er.largement 10 X 14 RH007A 16 Steel 17.6094 2-Elbow Short - r/d 1 @ 90' 10 in / 40 1-Elbow Long - r/d 1.5 @ 90' 1-Gate Wedge Disc 1-Tee Flow Thru Run 1-Reducer Enlargement 10 X 12 1-Swing Check Angled RH007B 16 Steel 19.2625 2-Elbow Short - r/d 1 @ 90' 10 in / 40 1-Swing Check Vertical 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Reducer Enlargement 10 X 14 RH007C 16 Steel 19.7656 3-Elbow Short - r/d 1 @ 90*

10 in / 40 1-Gate Wedge Disc 1 Tee Flow Thru Branch 1-Swing Check Angled RH007D 21 Steel 4.025 1-Tee Flow Thru Run 14 in / 30 RH008A 21 Steel 11.7875 1-Elbow Short - r/d 1 @ 90' 14 in / 30 1-Tee Flow Thru Run Calc / No. V75100.NSP97.00501 ATTACHMENT C Page_8.d.of Lff PIPE-FLO ver 5.01 pg 6

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PIPE MATERIALS LIST 06/12/97 d:20 am PIPELINE SPEC MATERIAL LENGTH VALVES & FITTING S Size / Sch ft RH008B 21 Steel 2.875 1-Tee Flow Thru Run 14 in / 30 RHRHXA 21 Steel 28.4145 3-Elbow Short - r/d 1 @ 90' 14 in / 30 2-Gate Wedge Disc 1-Tee Flow Thru Run 1-Fixed K RHR HX RHRHXB 21 Steet 54.8343 3-Elbow Short - r/d 1 @ 90' 14 in / 30 2-Elbow Short - r/d 1 @ 45' 2-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Fixed K RHR HX RHXBYPSA 21 Steel 29.4849 1-Tee Flow Thru Branch 14 in / 30 3-Elbow Short - r/d 1 @ 90' 1-Globe Valve RHXBYPSB 21 Steet 15.4172 1-Elbow Short- r/d 1 @ 90' 14 in / 30 1-Tee Flow Thru Branch 1-Globe Valve RX01A 21 Steel 6.3849 1-Tee Flow Thru Branch 14 in / 30 RX01B 21 Steel 20.748 1-Elbow Short - r/d 1 @ 00*

14 in / 30 1-Tee Flow Thru Run 1-Tee Flow Thru Branch RX01C 21 Steel 83.5906 1-Tee Flow Thru Run 14 in / 30 3-Elbow Short - r/d 1 @ 90' 1-Tee Flow Thru Branch 1-Reducer Enlargement 14 X 16 1-Fixed K Flow Element RX010 21 Steel 73.7917 1-Tee Flow Thru Run 14 in / 30 3-Elbow Short - r/d 1 @ 90' 1-Tee Flow Thru Branch 1 Reducer Enlargement 14 X 16 1 Fixed K Flow Element l

l RX02A 21 Steel 12.3625 1-Globe Valve 16 in / 30 1-Tee Flow Thru Run I

RX02B 21 Steet 12.3625 1-Globe Valve j 16 in / 30 l RX02C 35 Steet 102.769 7-Elbow Short - r/d 1 @ 90' 16 in / 80 2-Gate Double Disc 1-Swing Check Angled 1-Reducer Enlargement 16 X 18 Calc / No. V75100.NSP97.00601 ATTACHMENT C- Page 9/ of _/I?

PIPE-FLO ver 5.01 pg 7 j j

PIPE MATERIALS LIST 06/12/97 8:20 am l

PIPELINE SPEC MATERIAL LENGTH VALVES A FITTINGS Size / Sch ft I RXO2D - 35 Steet 97.9537 6-Elbow Short - r/d 1 @ 90*

l 16 in / 80 2-Gate Double Disc 1-Swing Check Angled l 1-Elbow Short - r/d 1 @ 45' 1-Reducer Enlargement 16 X 18 RXO1A 16 Steet 6.3849 1-Tee Flow Thru Branch 14 in / 40 Calc / No. V75100.NSP97.00501 ATTACHMENT C- Page$ of /S'/

PIPE-FLO ver 5.01 pg 8

PIPE

SUMMARY

06/1?/97 8:20 am PIPE MATERIAL SCHEDULE SIZE LENGTH Steel 20 20 in 555.352 ft Steel 30 14 in 516.659 ft 16 in 24.725 ft Steet 40 2.5 in 190.464 ft j 1

6 in 79.3144 ft 4

10 in 475.139 ft 12 in 130.603 ft 14 in 6.3849 ft l I

Steet 60 20 in 51.2285 ft i 4

Steet 80 2 in 10.4696 ft 8 in 112.445 ft 16 in 200.723 ft I 1

VALVE & FITTING

SUMMARY

SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS 16 LB30 Steet 40 Size: 2.5 in 7-Elbow Short - r/d 1 @ 45' 2-Tee Flow *ihru Branch 3-Reducer Contraction 2.5 X 2 18-Elbow Short - t/d 1 @ 90' 2-Fixed K Orifice Min.

Size: 6 in 1-Elbow Long - r/d 1.5 @ 67.5*

1-Elbow Long - r/d 1.5 @ 45' 1-Elbow Long - r/d 1.5 @ 90*

2-Gate Wedge Disc 1-Swing Check Angled 2-Tee Flow Thru Branch 1-Elbow Short - r/d 1 @ 90* l 1-Fixed K vel coretn Size: 10 in ;

28-Elbow Short - r/d 1 @ 90*

5-Tee Flow Thru Run l 4-Swing Check Vertical ;

11-Elbow Short- r/d 1 @ 45' 2-Fixed K Flow Element 2-Fixed K Res. Orifice 2-Reducer Contraction 10 X 8 4-Gate Wedae Disc Calc / No. V75100.NSP97,00601 ATTACHMENT C- PageM of /S9 PIPE-FLO ver 5.01 pg 9 j l

VALVE & FITTING

SUMMARY

06/12/97 8:20 cm SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS Size: 10 in 2-Reducer Enlargement 10 X 14 1-Elbow Long - r/d 1.5 @ 90*

1-Reducer Enlargement 10 X 12 2-Swing Check Angled 2-Tee Flow Thru Branch Size: 12 in 11-Elbow Short - r/d 1 @ 90' 2-Gate Wedge Disc 2-Gate Double Disc 2-Tee Flow Thru Run 2 Tee Flow Thru Branch 5-Elbow Short - rid 1 @ 45*

2-Fixed K vel coretn 4-Reducer Contraction 12 X 10 Size: 14 in 1-Tee Flow Thru Branch 21 LB31 Steel 30 Size: 14 in 30-Elbow Short - r/d 1 @ 90' !

9-Tee Flow Thru Run j 1-Reducer Contraction 16 X 14 3-Reducer Enlargement 14 X 16 13-Gate Wedge Disc 1-Elbow Long - t/d 1.5 @ 22.5*

1-Swing Check Angled 3-Elbow Long - r/d 1.5 @ 90' 10-Tee Flow Thru Branch 5-Fixed K vel coretn 4-Reducer Contraction 20 X 14 2-Fixed K RHR HX 2-Elbow Short - r/d 1 @ 45' 2-Globe Valve 2-Fixed K Flow Element Size: 16 in 2-Globe Valve 1-Tee Flow Thru Run 26 LB32 Steel 20 Size: 20 in 16-Fixed K 22.5 mitre 3-Elbow Short - r/d 1 @ 90*

2-Gate Wedge Disc 7 Tee Flow Thru Branch 2-Elbow Short - r/d 1 @ 45*

1-Elbow Lono - r/d 1.5 @ 90' Calc / No. V75100.NSP97.00501 ATTACHMENT C- Page D of /5~9 PIPE-FLO ver 5.01 pg 10

i i

VALVE & FITTING

SUMMARY

06/12/97 B:20 om i l

l SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS Size: 20 in 1-Tee Flow Thru Run ;

l l

31 LB34 Steel 60 Size:20 in 2-Fixed K strainer 5-Tee Flow Thru Branch 2-Fixed K STRAINER l

10-Fixed K contraction 8-Tee Flow Thru Run 10-Fixed K enlargement 1

35 LB34a Steel 80 l Size: 2 in 1-Elbow Short - r/d 1 @ 90* l 3-Reducer Enlargement 2 X 2.5 2-Globe Valve i

Size: 8 in 6-Gate Wedge Disc j 2-Swing Check Angled )

12-Eioow Short - r/d 1 @ 90*

1-Fixed K Spargers 1 Fixed K Sparger Size: 16 in 13-Elbow Short - r/d 1 @ 90*

4-Gate Double Disc 2-Swing Check Angled 2-Reducer Enlargement 16 X 18 1-Elbow Short - r/d 1 @ 45' PIPE-FLO ver 5.01 pg 11

C:mpany: Duka Engineiring & Sirvicts 06/17/97 8:25 pm Project Uneup: CASE 2 by: Josiph D. Spartcino rev: 06/17/97 8:22 pm System: OVRPRES2 Deviation: 0.00893 %

rev: 06/12/97 8:19 am after: 12 iterations long term, B RHR @4000 and B CS @ 2800gpm, O cont. pres., A strainer plugged, sp wtr M 908'-9.3".

Volumetric flow rates require constant fluid properties in all pipelines. Fluid properties in the first specification were used in this calculation.

LINEUP SUMMARIES PIPELINE FLOW PRESSURE SET LEVEL gpm SOURCE psi g ft CSD3B >>> 2800 BCSD3 0 0 CSD6B >>> 228.6 BCSD6 0 0 RX02C >>> 4000 RECIRC1 0 0 B <<< 2854 TB 0 4.459 C <<< 1736 TC 0 4.459 D <<< 2439 TD 0 4.459 Flows IN: 7029 gpm Flows OUT: 7029 gpm NET FLOWS: 0 gpm l

l l

l i

Calc / No. V75100.NSP97.00501 ATTACHMENT Pagedof 13 PIPE-FLO ver 5.01 p91

LINEUP NODES 06/12/97 8:33 Cm i

l NODE ELEVATION DEMAND PRESSURE H GRADE I ft gpm psi g ft l 1 90225 2.593 908.4 10 902.25 2.732 908.7 11 90225 2.734 908.7 12 00225 2.734 908.7 13 90225 2.731 908.7 14 90225 2.725 903.7 15 902.25 2.715 908.6 16 902.25 2.71 908.6 )

17 902.25 2.705 908.6 18 902.25 2.698 908.6 19 902.25 2.666 908.5 2 902.25 2.555 908.3 20 902.25 2.659 908.5 3 902.25 2.555 908.3 l 4 902.25 2.555 908.3 5 902.25 2.556 908.3 6 902.25 2.559 908.3 7 902.25 2.602 908.4 8 902.25 2.63 908.4 9 902.25 2.658 908.5 l A.CS.IN 902.25 2.714 908.6 l A.CS.SUCT 897.833 4.589 908.6 A.CS.T 899.916 3.705 908.6 A. DIS 897.833 4.536 908.5 A.IN 897.583 4.642 908.5 A.RH.IN 902.25 2.662 908.5 A.RH.T 897.583 4.642 908.5 A.SUC 897.833 4.536 908.5 ACSD2 931.917 -9.875 ' " 908.6 ACSD4 900.156 3.603 908.6 ACSDS 900.74 3.355 908.6 ACSD6 925.875 -7.311 '" 908.6 ACSD7 928 -8.213 *" 908.6 ACSD9 971.25 -26.57 "* 908.6 ACSDSCG 899.635 3.824 908.6 ADISTEE 901.083 24.84 959.6 B.CS.IN 902.25 2.556 908.3 B.CS.SUCT 897.833 2.108 902.8 B.CS.T 899.885 2.426 905.6 B. DIS 899.5 149.3 1251 B.IN 6s7.583 4.i i i 907.3 Calc / Na. V75100.NSP97.00501 ATTACHMENT C- Page 89 of /5'7 PIPE-FLO ver 5.01 pg 2

.. . . - . . . . . _ .. _. _ - _ _ - _.~-_ . _ _ . - _ _ . _ . _ . . _ _ _ _ _ _ . . _ _ _ _ _ _

LINEUP NODES 06/12/97 8:33 tm NODE ELEVATION DEMAND PRESSURE H GRADE R gpm pd g n B.RH.IN 902.25 2.555 908.3 B.RH.T 897.583 4.21 907.5 B.SUC 897.833 2.399 903.5

BCSO2 927.833 77.35 1110 BCSD3 980.38 0 (source) 980.4 BCSD4 899.896 295.7 "* 1597 BCSD5 901.688 266.9 *" 1531 BCSD6 930.333 0 (source) 930.3 BCSD7 978.5 52.74 1103 BCSDSCG 899.583 299.3 *" 1605 BDISTEE 908 27.33 , 972.4 C. DIS 897.833 4.53o 908.5 C.IN 897.583 4.642 908.5 C,SUC 897.833 4.536 908.5 D. DIS 899.5 3.298 907.3 D.DISA 908 27.33 972.4 D.IN 897.583 4.111 907.3 D.SUC 897.833 4.005 907.3 HP.lN 902.25 2.627 908.4 HP.T 901.615 2.897 908.4 M02013 940.91 9.077 962.3 MO2012 940.917 6.442 956.1 RC.IN 902.25 2.73 908.7 RC.T 902.25 2.73 908.7 RECIRC1 951.75 0 (source) 951.7 !

RECIRCA 930.168 12.49 959.6 RECIRCB 930.167 13.64 962.3 RHRHXDA 916.333 18.37 959.6 RHRHXDB 915.49 23.1 969.9 RHRHXDC 916.336 18.36 959.6 RHRHXDD 921.33 19.75 967.9 RHRHXS1 909.406 21.31 959.6 RHRHXS2 908 27.16 972 SA 902.25 2.555 908.3 SB 902.25 2.731 908.7 SC 902.25 2.734 908.7 SD 902.25 2.7 908.6 TB 904.316 1.892 (source) 908.8 TC 904.316 1.892 (source) 908.8

.TD 904.316 1.892 (source) 908.8-Calc / No. V75100.NSP97.00501 ATTACHMENT C. PageT8 of /6'f PIPE-FLO ver 5.01 P9 3

LINEUP PIPELINES 06/12/97 8:33 am I

PlPELINE FROM TO FLOW VEL dP HL l gpm ft/sec psi g ft A TA SA closed 0 0 0 B_ TB SB 2854 3.455 (0.839) 0.089 C TC SC 1736 2.102 (0.842) 0.082 CDS1B B.CS.SUCT BCSDSCG 3029

12.33 (297.1) (702)

- BCS - dP:(298.2) HL:(702.7)

CDS7A ACSD6 ACSD7 0 0 0.902 0 CROSSTIE REClRCB RECIRCA 4000 9.315 1.141 2.688 CS001A A.CS.lN A.CS.T 0 0 (0.990) 0 ;

CS001B B.CS.IN B.CS.T 3029 8.688 0.130 2.671 )

CS003A A.CS.T A.CS.SUCT 0 0 (0.884) 0 I CS003B B.CS.T B.CS.SUCT 3029 8.688 0.318 2.8 l CSDIA A.CS.SJCT ACSDSCG 0 0 0.765 0 l

- A.CS - dP: HL:

CSD2A ACSDSCG ACSD2 0 0 13.7 0 CSD2B BCSDSCG BCSD2 2800 11.4 64.16 122.9 l

- FCV@2800 - dP: 157.7 HL: 371.7 I CSD3A ACSD9 ACSD3 closed 0 0 0 CSD3B BCSD7 BCSD3 2800

19.69 52.74 122.4 CSD4A ACSDSCG ACSD4 0 0 0.221 0 CSD4B BCSDSCG BCSD4 228.6

15.33 3.508 7.955 )

CSDSA ACSD4 ACSDS 0 0 0.248 0 i CSDSB BCSD4 BCSDS 228.6

24.86 28.85 66.18 CSD6A ACSDS ACSD6 0 0 10.67 0 CSD6B BCSDS BCSOti 228.6

15.33 266.9 600.3 CSD78 BCSD2 BCSD7 2800 11.4 24.61 7.326 CSD8A ACSD7 ACSD8 closed 0 0 0 CSD9A ACSD2 ACSD9 0 0 16.69 0 D TD SD 2439 2.953 (0.808) 0.162 H1 20 <> 1 3811 4.205 0.066 0.156 H11 1 <> B.RH.lN 3811 4.615 0.038 0.089 H12 A.RH.lN <-> 20 3811 4.615 0.003 0.007 H2 3 2 188.5 0.208 0 0 H21 SA 3 188.5 0228 0 0 H22 2 B.RH.lN 188.5 0.228 0 0 H3 5 4 188.5 0.208 0 0 H31 B.CS.IN 5 188.5 0.228 0 0 H32 4 SA 188.5 0.228 0 0 H4a 9 8 3217 3.549 0.027 0.065 H4s1 SB 9 3217 3.895 0.074 0.173 H4:2 8 HP.lN 3217 3.895 0.003 0.007 H4b 7 6 3217 3.549 0.043 0.102 H4bi iiF.iN 7 32i7 3.695 0.026 0.061 Calc / No. V75103.NSPA7.00501 ATTACHMENT C PageN of /69 PIPE-FLO ver 5.01 pg 4

LINEUP PlPELINES 06/12/97 8:33 tm PIPELINE FROM TO FLOW VEL dP HL i

gpm ft/see psi g ft

- 1 H4b2 6 B.CS.IN 3217 3.895 0.003 0.007 l HS 11 <-> 10 363.5 0.401 0.002 0.004 H51 SC <-> 11 363.5 0.440 0 0 H52 10 <-> SB 363.5 0.440 0 0.002 i.

i H63 12 13 1372 1.514 0.003 0.007 H631 13 RC.lN 1372 1.662 0 0.001 H6.2 SC 12 1372 1.662 0 0 H6b 14 15 1372 1.514 0.010 0.025 H6b1 15 A.CS.lN 1372 1.662 0 0.001 H6b2 RC.IN 14 1372 1.662 0.005 0.011 H7 16 17 1372 1.514 0.004 0.010 H71 17 SD 1372 1.662 0.005 0.012 H72 A.CS.IN 16 1372 1.662 0.005 0.011 H8 18 19 3811 4.205 0.031 0.074 H81 19 A.RH.!N 3811 4.615 0.004 0.010 H82 SD 18 3811 4.615 0.003 0.007 HP001 HP.lN HP.T 0 0 (0.269) 0 HP002 HP.T HP.SUCT closed 0 0 0 i RC001 RC.lN RC.T 0 0 0 0 RC002 RC.T RC.SUCT closed 0 0 0 RH001A A.RH.lN A.RH.T 0 0 (1.981) 0 l RH001B B.RH.IN B.RH.T 4000 4.413 (1.655) 0.767 RH002A C.lN A.IN 0 0 0 0 l RH002B B.lN D.lN O O O O i

RH003A A.RH.T C.IN 0 0 0 0 j RH003B B.RH.T 8.lN 4000 4.413 0.099 0.233 RH004A C.IN C.SUC 0 0 0.106 0 RH004B B.IN B.SUC 4000 9.315 1.712 3.784 RH005A A.lN A.SUC 0 0 0.106 0 RH005B D.lN D.SUC 0 0 0.106 0 RH006A A.SUC A. DIS 0 0 0 0

- ARHR - dP: HL:

RH006B B.SUC B. DIS 4000 11.47 (146.9) (347.8)

- BRHR - dP:(14 3.1) HL:(349)

RH006C C .SUC C. DIS 0 0 0 0

- CRHR -- dP: HL:

RH006D D.SUC D. DIS 0 0 0.707 0

--DRHR- -dP; HL:

RH006DA D. DIS D.DISA closed 0 0 0

' RH007A A. DIS ADISTEE closed 0 0 0 RH007B B. DIS BDISTEE 4000 *16.29 8.18 10.78

- FCV@4000 - dP; 113.8 HL: 268.1 RH007C C. DIS ADISTEE closed 0 0 0 Calc / No. V76100.NSP97.00601 ATTACHMENT C- Page 90 of 67 PIPE-FLO ver 5.01 pg 5

LINEUP PIPELINES 06/12/97 8:33 am PIPELINE FROM TO FLOW VEL dP HL 9pm ft/sec psi 9 ft RH007D D.DISA BDISTEE O O O O RH008A ADISTEE RHRHXS1 0 0 3.532 0 l

RH008B BDISTEE RHRHXS2 4000 9.315 0.165 0.389 I RHRHXA RHRHXDA <-> RHRHXS1 0.839 0.002 (2.94) 0 i RHRHXB RHRHXS2 RHRHXDB 1882 4.383 4.065 2.088 RHXBYPSA RHRHXS1 RHRHXDA 0.839 0.002 2.94 0 RHXBYPSB RHRHXS2 RHRHXDB 2118 4.932 4.065 2.088 RX01A RHRHXDA RHRHXDC 0 0 0.001 0 RX01B RHRHXDB RHRHXDD 4000 9.315 3.349 2.051 RX01C RHRHXDC RECIRCA 0 0 5.87 0 RX01D RHRHXDD RECIRCB 4000 9.315 6.112 5.565 RX02A RECIRCA MO2012 4000 7.032 6.053 3.515 RX028 RECIRCB M02013 0 0 4.559 0 l RX02C MO2012 RECIRC1 4000 7.984 6.442 4.347 RX02D M02013 RECIRC2 closed 0 0 0 1

Calc / No. V75100.N3P97.00601 ATTACHMENT C- Page 9i of 8 PIPE-FLO ver 5.01 pg 6

DE&S Naperville, Illinois l PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc No: V75100.NSP97.00501 CLIENT Monticello Nuclear Station l l

l REFERENCE j ATTACHMENT D ,

. FLO SERIES MODEL PIPING AND NETWORK INPUT AND OUTPUT FOR CASE #3.

1 I l l

l l

4 REVISION O PAGE Q PREPARED BY/DATE [ 4 64 @ OF /p CHECKED BY/DATE &

18 q , q, TA TD q , q , TC 8 A O

~

_ . _ . _ _ 8,g H4 gla.i pV, _ !'s . ., !'95.; gogg _ Hg3 ,g g3 O

o ,_

"**2 H I g, , s BCSIN Se 30 8 RH DA RH IN

SC 32 A CS IN RC.m [*' H6b2 E i, "*?.S*tUlh,"3 B'42FB2F' F* ""*'8

& N' #!U9"b = "** in 5 4 SA 3 2 120 1915017 16 ,

djoogg _ , ,t k.CS.T

l

< HPOO1 ,

on RCOO1 '4 RHOO1 i . ,CSOO3A

f

$o CSOO3B __ .

/"

i B CS.SUCT A.CS.S +

"z HP.SUCT Tqp HP.T qp .g ,

so HPOO2 RH001A

." l A.RH.T RCOO2 8

a

- B RH T gg 9 _2 O

RH003J. C.IN A.tN ilHOO38 DW 8 IN

-- *4>RHOO2T RC.SUCT q p q 4H,O__02_4 g_p 3 f46t0048 ,,, ,_p RH004A I

h e.SUC C.SUC x

E RHOOSA ITI RHOO5B _. ._

z - -

-4 CDSIB SUC A.SUC CSDIA O . / N sRHR CRHR el en

k. A.CS W BCS

[ RHooeD RHOO68 RHOO6C RHOOBA e.

3 C-__,--,.

Duke Engineedng & Services ACsosCo 08/11/9 ;

sCSoSco Projestt LineNst[,, 05 pm PRES 3 -

C.o S A. DIS CSo48 fi, j, o.o S Lineup:

CongHtents:

by: gD. Speracino C RHOO7A flO W F888: gPm CSO2A i i ADISTEE t D.DtSA p RHOOFD_, RHOO7s Pressure: pSie ,

RH00se meStMersion: PIPE-FLO ver 5.01 ma== =

odR1el& 9tmie: It l So2s

/ , ,

PL m L. - m C0518 ,/ D SO: A SUC '- CSUIA BRHR, CRHR ARHit

)DRHR BCS o RHGOtis, RHOO68 RH006C RHOOlA AC8DSCO CSD4A BM q,CMq,AWD CSD4B

il RHOO6DA' D Dis RH007CADISTEE ltH007A Q D DISA $lHgog <

egoo7s -*4 W ACSD2 Z ,f'SD28 SDtSTEE ,

WOO 8A p F f RHRHxS2 gp .. RHRHxSI g r i

< 7 <> ACsoe ,

N. RHRHxt fHxBYPSB RHRHXj WX8YM % 9(,

-. q,eCSD4 g(sCSD2 o :Sosa

, CSDse RHRHMDBqW RHRHXDA q to RX01B tx01A g"O CSD78 RHRHMDD qp RHRHKDCyp (> ACSDS o RKOID 4x01C o ACSD9 q, CSD58 RECIRCS q) CROSSTIE q, RECIRCA CSD6A 1x028 RM02A y,BCSD7 M02013 qp j p MO2012 4,ACSD6 CSD3A d :SDas Rxo20 ax02C CDSFA eCSDs ' "

l o 8 RECIRC2 RECIRC1 I>

m ACSD3 z BCSD3

-4 yp ACSDF G CSD6B CSDeA T

=

c S

Q ,

. L qp BCSD6 qp ACSD8 S.

G Company: Duke Engineering & ServlCes 06/11/97 5:06 pm Project: Linetist: OVRPRES3 .

try: Joseph D. Sparecino L!7eup:

Comments: flow rate: gpm pressure: pSlo Version: PIPE-FLO ver 5.01 level & grade: ft

C mprny: Duks Enginunng & S:rvic:s 06/16/97 9:13 am Pr:jict: SystIm: OVRPRES3 by: Josiph D. Sprrr.cino rzv: 06/16/97 9:09 cm Created: 11/04/9611:56 am Pipes: 93 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.1502'F. and 0 psig cont, press. Containment overpressure cales.

SYSTEM NODES

-NODE ELEVATION PIPELINES IN PIPELINES OUT ft 1 902.25 H11 H1 10 902.25 H52 H5 11 90225 h5 H51 12 902.25 H6a2 H6a 13 902.25 H6a H6a1 14 90225 H6b2 H6b 15 90225 H6b H6bi 16 902.25 H72 H7 17 902.25 H7 H71 18 902.25 H82 H8 19 902.25 H8 H81 2 902.25 H2 H22 20 902.25 H1 H12 3 902.25 H21 H2 4 902.25 H3 H32 5 902.25 H31 H3 6 902.25 H4b H4b2 7 902.25 H4b1 H4b 8 902.25 H4a H4a2 9 90225 H4a1 H4a A.CS.IN 902.25 H6b1 CS001A H72 A.CS.SUCT 897.833 CS003A CSD1A A.CS.T 899.916 CS001A CS003A A. DIS 897.833 RH006A RH007A Calc / No. V75100.NSP97.00601 ATTACHMENT D Page 96of /67 PIPE FLO ver 5.01 pg 1

SYSTEM NODES 06/16/97 9:13 am I

NODE ELEVATION PIPELINES IN PIPELINES OUT ft A.IN 897.583 RH002A RH005A A.RH.lN 902.25 H12 RH001A H81 A.RH.T 897.583 RH001A RH003A A.SUC 897.833 RH005A RH006A l ACSD2 931.917 CSD2A CSD9A ACSD3 981.188 CSD3A ACSD4 900.156 CSD4A CSD5A l l

ACSDS 900,74 CSD5A CSD6A I ACSD6 925.875 CSD6A CDS7A ACSD7 928 CDS7A CSD8A I l

ACSD8 927 CSD8A ACSD9 971.25 CSD9A CSD3A .

1 ACSDSCG 899.635 CSD1A CSD2A CSD4A ADISTEE 901.083 RH007A RH008A l RH007C j 1

B.CS.lN 902.25 H4b2 CS001B H31 B.CS.SUCT 897.833 CS003B CDSIB B.CS.T 899.885 CS001B CS003B B. DIS 899.5 RH006B RH007B B.lN 897.583 RH003B RH002B RH004B B.RH.lN 902.25 H22 H11 RH001B B.RH.T 897.583 RH001B RH003B B.SUC 897.833 RH004B RH006B BCSD2 927.833 CSD2B CSD7B l l

BCSD3 980.38 CSD3B BCSD4 899.896 CSD4B CSDSB BCSDS 901.688 CSDSB CSD6B BCSD6 930.333 CSD6B l l

Calc / No. V78100.NSP97.00501 ATTACHMENT D Page1of /O PIPE-FLO ver 5.01 pg 2

SYSTEM NODES 06/16/97 9:13 sm NODE ELEVATION PlPEUNES IN PlPEUNES OUT h

BCSD7 978.5 CSD78 CSD3B )

BCSDSCG 899.583 CDS1B CSD2B l CSD4B BDISTEE 908 RH0078 RH0J8B l RH007D l C. DIS 897.833 RH006C RH007C C.lN 897.583 RH003A RH002A RH004A C.SUC 897.833 RH004A RH006C D. DIS 899.5 RH006D RH006DA D.DISA 908 RH006DA RH007D D.lN 897.583 RH002B RH005B D.SUC 697.833 RH005B -

RH006D HP.lN 902.25 H4a2 H4b1 )

HP001 l

HP.SUCT 901.615 HP002 HP.T 901.615 HP001 HP002 M02013 940.91 RXO2B RXO2D MO2012 940.917 RX02A RXO2C RC.IN 902.25 H6a1 H6b2 RC001 RC.SUCT 899.042 RC002 RC.T 902.25 RC001 RC002 RECIRC1 951.75 RXO2C RECIRC2 951.75 RXO2D RECIRCA 930.168 CROSSTIE RX02A RX01C RECIRCB 930.167 RX01D CROSSTIE RXO2B RHRHXDA 916.333 RHRHXA RX01A RHXBYPSA RHRHXDB 915.49 RHRHXB RX01B RHXBYPSB RHRHXDC 916.336 RX01A RX01C Calc / No. V75100.NSP97.00601 A71Acv. MENT D Page 97 of M PIPE-FLO ver 5.01 p9 3

, SYSTEM NODES 06/16/97 9:13 cm NODE ELEVATION PIPELINES IN PIPELINES OUT ft RHRHXDD 921.33 RX01B RX01D RHRHXS1 909.406 RH008A RHRHXA RHXBYPSA RHRHXS2 908 RH008B RHRHXB RHXBYPSB SA 902.25 A H21 H32 SB 902.25 B H4a1 H52 SC 902.25 C H6a2 H51 SD 902.25 D H82 H71 TA 904.316 A TB 904.316 B TC 904.316 C TD 904.316 D Cale/ No. V75100.NSP97.00601 ATTACHMENT D Page 96 of /527 PIPE-FLO ver 5.01 pg 4

j' SYSTEM PIPES 06/16/97 9:13 stm i PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP A 31 TA SA B 31 TB SB i C 31 TC SC CDS1B 16 B.CS.SUCT BCSDSCG BCS CDS7A 35 ACSD6 ACSD7 CROSSTIE 21 RECIRCB RECIRCA CS001A 16 A.CS.lN A.CS.T CS001B 16 B.CS.IN B.CS.T i CS003A 16 A.CS.T A.CS.SUCT CS003B 16 B.CS.T B.CS.SUCT ,

CSDIA 16 A.CS.SUCT ACSDSCG A.CS CSD2A 16 - ACSDSCG ACSD2 CSD2B 16 BCSDSCG BCSD2 CSD3A 35 ACSD9 ACSD3 CSD3B 35 BCSD7 BCSD3 CSD4A 16 ACSDSCG ACSD4 CSD4B 16 BCSDSCG BCSD4 CSDSA 35 ACSD4 ACSDS CSDSB 35 BCSD4 BCSDS CSD6A 16 ACSDS ACSD6 CSD6B 16 BCSD5 BCSD6 CSD7B 16 BCSD2 BCSD7 CSD8A 16 ACSD7 ACSD8 CSD9A 16 ACSD2 ACSD9 0 31 TD SD H1 26 1 20 H11 31 B.RH.IN 1 H12 31 20 A.RH.IN H2 26 3 2 H21 31 SA 3 H22 31 2 B.RH.IN H3 26 5 4 H31 31 B.CS.lN 5 H32 31 4 SA H4a 26 9 8 H4a1 31 SB 9 H4a2 31 8 HP.IN H4b 26 7 6 H4bi 31 HP.lN 7 H4b2 31 6 B.CS.IN HS 26 10 11 HS1 31 11 SC Calc / No. V75100.NSP97.00501 ATTACHMENT D Page@ of /f'l PIPE-FLO ver 5.01 pg 5

SYSTEM PIPES 06/16/97 9:13 tm l

l PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP l

l H52 31 SB 10 H6a 26 12 13 H6a1 31 13 RC.!N H6a2 31 SC 12 H6b 26 14 15 H6bi 31 15 A.CS !N H6b2 31 RC.lN 14 H7 26 16 17 H71 31 17 SD H72 31 A.CS.lN 16 H8 26 18 19 H81 31 19 A.RH.IN H82 31 SD 18 HP001 21 HP.lN HP.T HP002 21 HP.T HP.SUCT RC001 16 RC.IN RC.T RC002 16 RC.T RC.SUCT RH001A 26 A.RH.lN A.RH.T RH001B 26 B.RH.IN B.RH.T RH002A 26 C.IN A.IN RH002B 26 B.IN D.IN RH003A 26 A.RH.T C.IN RH003B 26 B.RH.T B.IN RH004A 21 C.lN C.SUC RH004B 21 B.lN B.SUC RH005A 21 A.lN A.SUC RH005B 21 D.IN D.SUC RH006A 16 A.SUC A.D!S ARHR RH006B 16 B.SUC B. DIS BRHR RH006C 16 C.SUC C. DIS CRHR RH006D 16 D.SUC D. DIS DRHR RH006DA 16 D. DIS D.DISA RH007A 16 A. DIS ADISTEE RH007B 16 B. DIS BDISTEE RH007C 16 C. DIS ADISTEE RH007D 21 D.DISA BDISTEE RH008A 21 ADISTEE RHRHXS1 RH008B 21 BDISTEE RHRHXS2 RHRHXA 21 RHRHXS1 RHRHXDA RHRHXB 21 RHRHXS2 RHRHXDB RHXBYPSA 21 RHRHXS1 RHRHXDA RHXBYPSB 21 RHRHXS2 RHRHXDB Calc / No. V75100.NSP97.00501 ATTACHMENT D PagelQhofM PIPE-FLO ve 5.01 pg 6

SYSTEM PIPES 06/16/97 9:13 sm PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP RX01A 21 RHRHXDA RHRHXDC RX018 21 .RHRHXDB RHRHXDD RX01F, 21 RHRHXDC RECIRCA RX01D 21 RHRHXDD RECIRCB

, RX02A 21 RECIRCA MO2012 RX02B 21 RECIRCB M02013 RX02C 35 MO2012 RECIRC1 ;

RX02D 35 M020i3 RECIRC2 RXO1A 16 . .

t i

I 1

i I

i 9

4 i

Calc / No. V75100.NSP97.00601 ATTACHMENT D Page J.12[ of _/f_T PIPE-FLO ver 5.01 pg 7

SYSTEM COMPONENTS 06/16/97 9:13 am PUMP / COMP PERFORMANCE DATA l A.CS gpm: 0 2179 3990 5040 5755 ft: 850.3 795.5 664 536.2 411.7 egn: 850.3 - 4.49715e-006 Q ^ 2.12033 ARHR gpm: 0 3365- 4000 4250 4540 ft: 810.3 498.9 350 280 171.8 egn: 810.3 1.3787e-006 Q ^ 2.36763 BCS gpm: 0 1948 3080 4875 5600 ft: 844 770.1 719.4 535.2 418.1 egn: 844 - 0.000218414 Q ^ 1.66917 BRHR gpm: 0 3656- 4000 4250 4408 ft: 813.8 436 350 280 230 egn: 813.8 - 2.04305e-006 Q ^ 2.32005 CRHR gpm: 0 3540 4000 4250 4440 ft: 763.9 461.1 360 290 235.4 egn: 763.9 - 5.58043e-007 Q ^ 2.46066 DRHR gpm: 0 3542 4000 4250 4425 ft: 810.1 463 350 285 227 egn: 810.1 - 2.16007e-006 Q ^ 2.31196 Calc / No. V75100.NSP97.00501 ATTACHMENT D Page ICQ of M PIPE-FLO ver 5.01 pg 8

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Ccmp:ny: Duka Enginunng & Strvices 06/16/97 9:13 am '

Projict: SystIm: OVRPRES3 by: Joseph D. Spiracino r: v: 06/16/97 9:09 am PIPEllST REPORT l Created: 11/04/9611:56 am Pipes: 93 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.150.2*F. and 0 psig cont. press. Containment overpressure cales.

SPECIFICATIONS SPECIFICATION PIPE MATERIAL FLUID VALVE TABLE DESIGN LIMITS Sch / Roughness Temp / Pres Vel / Pres 16 LB30 Steel Water Standard 0 - 12 ft/see rev: 06/16/97 9:08 am Sch 40 150.2 'F 0 - 200 psi g 0.0018 in 0psig Size for: 8 ft/see 21 LB31 Steel Water Standard 0 - 12 ft/sec rev: 06/16/97 9:08 am Sch 30 150.2 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 26 LB32 Steel Water Standard 0 - 12 ft/sec rev: 06/16/97 9:08 am Sch 20 150.2 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 31 LB34 Steel Water Standard 0 - 12 ft/sec rev: 06/16/97 9:08 am Sch 60 150.2 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 35 LB34a Steel W ater Standard 0 - 12 ft/sec rey:06/16/97 9:09 am Sch 80 150.2 'F 0 - 200 psi g 0.0018 in 0 psig Size for: 8 ft/sec Calc / No. V75100.NSP97.00501 ATTACHMENT d PageMof Li1 PIPE-FLO ver 5.01 pg 1

PIPELIST 06/16/97 9:13 cm i

l

! PIPELINE SPEC MATERIAL LENGTH FLUID VALVES l Size / Sch ft Temp / Pres Total-K i

A L1 Steel 3.6777 Water 1.163 l 20 in / 60 150.2 'F / 0 psi g B 31 Steel 3.6777 Water 0.4469 20 in / 60 150.2 'F / 0 psi g C 31 Steel 3.6777 Water 1.163 20 in / 60 150.2 'F / 0 psi g CDS1B 16 Steel 3.45 Water 0.2689 10 in / 40 150.2 *F / 0 psi g CDS7A 35 Steel 7.73835 Water 0.478 2 in / 80 150.2 *F / 0 psi g CROSSTIE 21 Steel 49.0188 Water 1.403 14 in / 30 150.2 'F / 0 psi g CS001A 16 Steel 41.8129 Water 2285 12 in / 40 150.2 'F / 0 psi g CS001B 16 Steel 42.5259 Water 1.695 12 in / 40 150.2 'F / 0 psi g CS003A 16 Steel 10.7215 Water 1.779 12 in / 40 1502 'F / 0 psi g CS0038 16 Steel 27.109 Water 2.018 12 in / 40 150.2 'F / 0 psi g CSD1A 16 Steel 3.7973 Water 0.2689 10 in / 40 150.2 'F / 0 psi g CSD2A 16 Steel 108.553 Water 60.59 10 in / 40 150.2 'F / 0 psi g CSD2B 16 Steel 108.723 Water 59.14 10 in / 40 150.2 'F / 0 psi g CSD3A 35 Steel 57.0055 Water 19.08 8 in / 80 150.2 'F / 0 psi g CSD3B 35 Steel 55.4392 Water 19.08 8 in / 80 150.2 'F / 0 psi g CSD4A 16 Steel 2.22525 Water 1.664 2.5 in / 40 150.2 'F / 0 psi g CSD4B 16 Steel 2.7485 Water 1.93 2.5 in / 40 1502 'F / 0 psi g CSDSA 35 Steel 0.67045 Water 6.654 2 in / 80 150.2 'F / 0 psi g CSDSB 35 Steel 2.0608 Water 6.654 2 in / 80 1502 'F / 0 psi g CSD6A 16 Steel 38.6803 Water 152.5 2.5 in / 40 1502 'F / 0 psi g CSD6B 16 Steel 101.051 Water 155.4 2.5 in / 40 1502 'F / 0 psi g CSD78 16 Steel 97.3901 Water 1.995 10 in / 40 150.2 'F / 0 psi g CSD8A 16 Steel 45.7585 Water 2.453 2.5 in / 40 150.2 'F / 0 psi g CSD9A 16 Steel 75.8885 Water 1.53 10 in / 40 150.2 'F / 0 psi g Calc / No. V75100.NSP97.00501 ATTACHMENT b Page /04 of /5V PIPE-FLO ver 5.01 pg 2

PIPELIST 06/16/97 9:13 sm PIPELINE SPEC MATERIAL LENGTH FLUID VALVES Size / Sch ft Temp / Pres Total-K D 31 Steel 3.6777 Water 1.163 20 in / 60 1502 *F / 0 psi g H1 26 Steel 52.2054 Water 0.144 20 in / 20 1502 *F / 0 psi g H11 31 Steel 1.9171 Water 02536 20 in / 60 1502 'F / 0 psi g H12 31 Steel 1.9 71 Water 0.00366 20 in / 60 1502 'F / 0 psi g H2 26 Steel 24.1868 Water 0.072 20 in / 20 1502 'F / 0 psi g H21 31 Steel 1.9171 Water 0.00366 20 in / 60 150.2 'F / 0 psi g H22 31 Steel 1.9171 Water 0.01484 20 in / 60 150.2 'F / 0 psi g H3 26 Steel 24.3777- Water 0.072 ,

i '

20 in / 20 150.2 'F / 0 psi g

, H31 31 Steel 1.4375 Water 0.2425 20 in / 60 150.2 'F / 0 psi g H32 31 Steel 1.9171 Water 0.2536 20 in / 60 150.2 'F / 0 psi g l H4a 26 Steel 31.4675 Water 0.072 20 in / 20 150.2 'F / 0 psi g H4a1 31 Steel 1.9171 Water 0.7201 20 in / 60 150.2 'F / 0 psi g i H4a2 31 Steel 1.725 Water 0.01484 l 20 in / 00 150.2 'F / 0 psi g H4b 26 Steel _ 45.6907 Water 0.144 l 20 in / 20 150.2 'F / 0 psi g H4b1 31 Steel 1.725 Water 02425 20 in / 60 150.2 'F / 0 psi g H4b2 31 Steel 1.725 Water 0.01484 20 in / 60 1502 'F / 0 psi g HS 26 Steel 108.244 Water 0.288

. 20 in / 20 150.2 *F / 0 psi g H51 31 Steel 1.9171 Water 0.2536 20 in / 60 150.2 'F / 0 psi g H52 31 Steel 1.9171 Water 0.7201 20 in / 60 150.2 'F / 0 psi g H6a 26 Steel 15.1777 Water 0.072 20 in / 20 1502 'F / 0 psi g H6a1 31 Steet 1.725 Water 0.014P4 20 in / 60 150.2 'F / 0 psi g H6a2 31 Steet 1.9171 Water 0.00366 20 in / 60 1502 'F / 0 psi g H6b 26 Stee! 61.7884 Water 0.144 20 in / 20 150.2 'F / 0 psi g H6b1 31 Steel 1.725 Water 0.01484 20 in / 60 150.2 'F / 0 psi g Calc / No. V75100.NSP97.00501 ATTACHMENT h Page /6of /6T PIPE-FLO ver 5.01 pg 3

PIPELIST 06/16/97 9:13 tm PIPELINE SPEC MATERIAL LENGTH FLUID VALVES Size / Sch ft Temp / Pres Total-K H6b2 31 Steel 1.725 Water 02425 20 in / 60 1502 'F / 0 psi g H7 26 Steel 24.3777 Water 0.072 20 in / 20 150.2 *F / 0 psi g H71 31 Steel 1.9171 Water 0.2536 20 in / 60 1502 *F / 0 psi g H72 31 Steet 1.725 Water 0.2425 20 in / 60 150.2 'F / 0 psi g H8 26 Steel 24.1868 Water 0.072 20 in / 20 150.2 'F / 0 psi g H81 31 Steel 1.9171 Water 0.01484 20 in / 60 1502 *F / 0 psi g H82 31 Steel 1.9171 Water 0.00366 20 in / 60 150.2 'F / 0 psi g HP001 21 Steel 67.5027 Water 3.127 14 in / 30 150.2 'F / 0 psi g HP002 21 Steel 0.3679 Water 1.356 14 in / 30 1502 'F / 0 psi g RC001 16 Steel 22.7965 Water 4.054 6 in / 40 150.2 'F / 0 psi g RC002 16 Steet 56.5179 Water 1298 6 in / 40 150.2 'F / 0 psi g RH001A 26 Steel 62.1357 Water 2.161 20 in / 20 150.2 'F / 0 psi g RH001B 26 Steel 55.6198 Water 2.09 20 in / 20 150.2 'F / 0 psi g RH002A 26 Steel 5.75 Water 0.7101 !

20 in / 20 150.2 'F / 0 psi g RH002B 26 Steel 5.3671 Water 0.7101 20 in / 20 150.2 'F / 0 psi g RH003A 26 Steel 7.1093 Water 0.2367 20 in / 20 150.2 'F / 0 psi g RH003B 26 Steet 7.6671 Water 0.7101 20 in / 20 150.2 'F / 0 psi g RH004A 21 Steel 14.758 Water 2.63 14 in / 30 1502 *F / 0 psi g RH004B 21 Steel 14.95 Water 2.63 14 in / 30 150.2 'F / 0 psi g RH005A 21 Steel 14.758 Water 1.867 14 in / 30 150.2 'F / 0 psi g ,

RH005B 21 Steel 14.95 - W ater 1.867 I 14 in / 30 150.2 'F / 0 psi g RH006A 16 Steet 1.15 Water 0.2977 12 in / 40 150.2 'F / 0 psi g RH006B 16 Steel 3.0671 Water 0.5573 12 in / 40 150.2 'F / 0 psi p. l RH006C 16 Steel 1.15 Water 0.2977 )

12 in / 40 1502 *F / 0 psi g Calc / No. V75100.NSP97.00501 ATTACHMENT N Page /d[>of /59 PIPE-FLO ver 5.01 pg 4

PIPELIST 06/16/97 9:13 Em i PIPELINE SPEC MATERIAL LENGTH FLUlO VALVES Size / Sch ft Temp / Pres Total-K RH006D 16 Steel 3.06671 Water 0.5573 12 in / 40 150.2 'F / 0 psi g RH006DA 16 Steel 20.7 Water 1.76 10 in / 40 150.2 'F / 0 psi g RH007A 16 Steet 17.6094 Water 2.534 10 in / 40 1502 'F / 0 psi g RH0078 16 Steel 19.2625 Water 2298 10 in / 40 150.2 'F / 0 psi g l

RH007C 16 Steel 19.7656 Water 3.065 10 in / 40 1502 'F / 0 psi g RH007D 21 Steel 4.025 Water 02543 14 in / 30 1502 'F / 0 psi g RH008A 21 Steel 11.7875 Water 0.5086 14 in / 30 1502 'F / 0 psi g RH008B 21 Steel 2.875 Water 0.2543 14 in / 30 150.2 'F / 0 psi g )

RHRHXA 21 Steel 28.4145 Water 5.436 l 14 in / 30 1502 *F / 0 psi g RHRHXB 21 Steel 54.8343 Water 6.316 14 in / 30 150.2 'F / 0 psi g KHXBYPSA 21 Steel 29.4849 Water 5.85 14 in / 30 150.2 'F / 0 psi g RHXBYPSB 21 Steel 15.4172 Water 5.341 14 in / 30 1502 'F / 0 psi g RX01A 21 Steel 6.3849 Water 0.763 14 in / 30 150.2 'F / 0 psi g RX01B 21 Steel 20.748 Water 1.272 14 in / 30 150.2 'F / 0 psi g RX01C 21 Steel 83.5906 Water 3.24 14 in / 30 150.2 'F / 0 psi g RX01D 21 Steel 73.7917 Water 3.24 ;

14 in / 30 150.2 'F / 0 psi g !

RXO2A 21 Steel 12.3625 Water 4.454 16 in / 30 1502 'F / 0 psi g RXO2B 21 Steel 12.3625 Water 4.207 16 in / 30 150.2 'F / 0 psi g RXO2C 35 Steet 102.769 Water 3.252 l 16 in / 80 150.2 'F / 0 psi g RX02D 35 Steel 97.9537 Water 3.184 16 in / 80 150.2 'F / 0 psi g RXOIA 16 Steel 6.3849 W ater 0.7645 14 in / 40 150.2 'F / 0 psi g Calc / No. V76100.NSP97.00501 ATTACHMENT d Page,lO2 of /5T PIPE-FLO ver 5.01 pg 5

M a & 9. en+ 3 i. 5 -4+=. %M _ _ A bw. ., . .alu #-. 4 + _-- mus ,4._ e . 4,.m..a Comp:ny: Duks Enginaring & SIrvicts 06/16/97 9:14 sm i Pr:JIct: Systim; OVRPRES3 by: Jos ph D. Spir:cino rsv: 06/16/97 9:09 mm MATERIALS REPORT l

. Created: 11/04/9611:56 am Pipes: 93 I l Design file: Nodes: 87 ;

Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.150.2*F. and 0 psig cont. press. Containment overpressure cales.

PIPE MATERIALS LIST PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft l

A 31 Steel 3.6777 1-Fixed K strainer 20 in / 60 1-Tee Flow Thru Branch B 31 Steel 3.6777 1-Fixed K STRAINER j 20 in / 60 C 31 Steel 3.6777 1-Fixed K STRAINER 20 in / 60 1 Tee Flow Thru Branch CDS1B 16 Steel 3.45 1-Elbow Short - r/d 1 @ 90*

10 in / 40 CDS7A 35 Steel 7.73835 1-Elbow Short - r/d 1 @ 90*

2 in / 80 1-Reducer Enlargement 2 X 2.5 CROSSTIE 21 Steel 49.0188 3-Elbow Short - r/d 1 @ 90*

14 in / 30 1-Tee Flow Thru Run 1-Reducer Contraction 16 X 14 1-Reducer Enlargement 14 X 16 2-Gate Wedge Disc CS001A 16 Steel 41.8129 4 Elbow Short - r/d 1 @ 90*

12 in / 40 1-Gate Wedge Disc 1 Gate Double Disc 1 Tee Flow Thru Run 1-Tee Flow Thru Branch CS001B 16 Stee! 42.5259 1-Elbow Short - r/d 1 @ 90*

12 in / 40 1-Elbow Short- r/d 5 @ 45*

1-Tee Flow Thru Run 1-Gate Wedge Disc 1-Gate Double Disc 1-Tee Flow Thru Branch CS003A 16 Steel 10.7215 3-Elbow Short - r/d 1 @ 90*

12 in ' 40 1-Fixed K vel coretn CS003B 16 Steel 27.109 1-Elbow Short - r/d 1 @ 90*

12 in / 40 4-Elbow Short - r/d 1 @ 45*

1-Fixed K vel coretn CSD1A 16 Steel 3.7973 1-Elbow Short - r/d 1 @ 90*

10 in / 40 Calc / No. V76100.NSP97.00601 ATTACHMENT D Page /06 of./.dj PIPE FLO ver 5.01 pg 1

PIPE MATERIALS LIST 06/16/97 9:14 am PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS l Size / Sch ft l

~ CSD2A 16 Steel 108.553 1 Tee Flow Thru Run 10 in / 40 1-Swing Check Vertical 5-Elbow Short - r/d 1 @ 90' I 8-Elbow Short - r/d 1 @ 45' l 1-Fixed K Flow Element i 1-Fixed K Res. Orifice CSD2B 16 Steet 108.723 4-Elbow Short - r/d 1 @ 90*

10 in / 40 1-Swing Check Vertical 2-Elbow Short - r/d 1 @ 45' 1-Tee Flow Thru Run 1-Fixed K Res. Orifice 1-Fixed K Flow Element CSD3A 35 Steel 57.0055 3-Gate Wedge Disc 8 in / 80 1-Swing Check Angled 6-Elbow Short - r/d 1 @ 90' 1-Fixed K Spargers CSD3B 35 Steel 55.4392 3-Gate Wedge Disc 8 in / 80 1-Swing Check Angled 6-Elbow Short - r/d 1 @ 90' 1-Fixed K Sparger CSD4A 16 Steel 2.22525 1-Elbow Short - r/d i @ 45*

2.5 in / 40 1-Tee Flow Thru Branch 1 Reducer Contraction 2.5 X 2 CSD4B 16 Steel 2.7485 2-Elbow Short - r/d 1 @ 45' 2.5 in / 40 1-Tee Flow Thru Branch 1 Reducer Contraction 2.5 X 2 CSD5A 35 Steel 0.67045 1-Globe Valve 2 in / 80 1-Reducer Enlargement 2 X 2.5 CSDSB 35 Steel 2.0608 1-Globe Valve l 2 in / 80 1-Reducer Enlargement 2 X 2.5 l CSD6A 16 Steel 38.6803 1-Elbow Short - r/d 1 @ 45*

2.5 in / 40 2-Elbow Short - r/d 1 @ 90*

1-Reducer Contraction 2.5 X 2 1-Fixed K Orifice Min. I CSD6B 16 Steel 101.051 10-Elbow Short - r/d 1 @ 90' 2.5 in / 40 2-Elbow Short - r/d 1 @ 45' 1-Fixed K Orifice Min.

CSD78 16 Steel 97.3901 1-Reducer Contraction 10 X 8 10 in / 40 4-Elbow Short - r/d 1 @ 90' 1-Elbow Short - r/d 1 @ 45' Calc / No. V75100.NSP97.00501 ATTACHMENT D Page 104 of M PIPE-FLO ver 5.01 pg 2

PIPE MATERIALS LIST 06/16/97 9:14 sm PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft 1-Tee Flow Thru Run CSD8A 16 Steel 45.7585 6-Elbow Short - r/d 1 @ 90' 2.5 in / 40 1-Elbow Short r/d 1 @ 45' CSD9A 16 Steel 75.8885 1-Reducer Contraction 10 X 8 10 in / 40 1-Tee Flow Thru Run i 3-Elbow Short - r/d 1 @ 90' 1

D 31 Steel 3.6777 1-Fixed K strainer 20 in / 60 1-Tee Flow Thru Branch H1 26 Steel 52.2054 2-Fixed K 22.5 mitre 20 in / 20 H11 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 1-Tee Flow Thru Run H12 31 Steel 1.9171 1-Fixed K enlargement 20 in / 60 H2 26 Steel 24.1868 1-Fixed K 22.5 mitre 20 in / 20 H21 31 Steel 1.9171 1-Fixed K enlargement 20 in / 60 H22 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 H3 26 Steel 24.3777 1-Fixed K 22.5 mitre 20 in / 20 j H31 31 Steel 1.4375 1-Fixed K enlargement l 20 in / 60 1-Tee Flow Thru Run H32 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 1-Tee Flow Thru Run H4a 26 Steel 31.4675 1-Fixed K 22.5 mitre 20 in / 20 H4a1 31 Steel 1.9171 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Branch H4a2 31 Steel 1.725 1-Fixed K contraction 20 in / 60 H4b 26 Steel 45.6907 2-Fixed K 22.5 mitre 20 in / 20 H4b1 31 Steet 1.725 1-Fixed K enlargement Calc / No. V75100.NSP97.00501 ATTACHMENT D Page$ of /5'[

PIPE-FLO ver 5.01 pg 3

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[- PIPE MATERIALS LIST 06/16/97 9.14 tm PIPELINE - SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft

! 20 in / 60 1-Tee Flow Thru Run l-H4b2' 31 Steel 1.725 1-Fixed K contraction

20 in / 60 l

H5 26 - Steel 108244 4-Fixed K 22.5 mitre 20 in / 20 H51 31 Steel 1.9171 1-Tee Flow Thru Run 20 in / 60 1-Fixed K contraction H52 31 Steel 1.9171 1-Tee Flow Thru Branch 20 in / 60 1 Fixed K enlargement H6a 26 Stee) 15.1777 1-Fixed K 22.5 mitre 20 in / 20 H6a1 31 Steel 1.725 1-Fixed K contraction 20 in / 60 H6a2 31 Steel 1.9171 1-Fixed K enlargement 20 in / 60

.H6b 26 Steel 61.7884 2-Fixed K 22.5 mitre 20 in / 20 H6b1 31 Steet 1.725 1-Fixed K contraction 20 in / 60 Htib2 31 Steel 1.725 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Run H7 26 Steel 24,3777 1-Fixed K 22.5 mitre I 20 in / 20 l H71 31 Steel 1.9171 1 Tee Flow Thru Run 20 in / 60 1-Fixed K contraction H72 31 Steel 1.725 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Run H6 26 Steel 24.1868 1-Fixed K 22.5 mitre 20 in / 20 H81 31- Steel 1.9171 1-Fixed K contraction 20 in / 60 H82 31 Steet 1.9171 1-Fixed K enlargement 20 in / 60 HP001 21 Steel 67.5027 1-Elbow Long - r/d 1.5 @ 22.5*

14 in / 30 2-Gate Wedge Disc l 1-Swing Check Angled 3-Elbow Long - r/d 1.5 @ 90' Calc / No. V76100.NSP97.00601 ATTACHMENT _.D_ Page lIi of di PIPE-FLO ver 5.01 P94

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PIPE MATERLALS LIST 06/16/97 9:14 am PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Jiize / Sch ft 1-Tee Flow Thru Run '

1-Tee Flow Thru Branch HP002 21 Steel 9.3679 1-Ebow Short r/d 1 @ 90' 14 in / 30 ' 1-Gate Wedge Disc 1-Fixed K velcorctn RC001 16 Steel 22.7965 1-Ebow Long - r/d 1.5 @ 67.5*

6 in / 40 1-Ebow Long - r/d 1.5 @ 45' l 1-Ebow Long - r/d 1.5 @ 90' 2-Gate Wedge Disc l

1 Swing Check Angled 2-Tee Flow Thru Branch '

' RC002 16 Stee! 56.5179 1-Ebow Short- r/d 1 @ 90' 6 in / 40 1-Fixed K vel coretn RH001A 26 Steel 62.1357 2-Ebow Short-r/d 1 @ 90' 20 in / 20 ' 1-Gate Wedge Disc -

1-Tee Flow Thru Branch 1-Ebow Short - r/d 1 @ 45' 1-Tee Flow Thru Branch RH001B 26 Steel 55.6198 1 Elbow Long - r/d 1.5 @ 90' 20 in / 20 1-Elbow Short - r/d 1 @ 90' 1-Gate Wedge Disc 1-Tee F!cw Thru Branch 1-Ebow Short - t/d 1 @ 45' 1-Te s Flow Thru Branch j l

RH002A 26 Steel 5.75 1-Tee Flow Thru Branch 20 in / 20 RH002B 26 Steel 5.3671 1-Tee Flow Thru Branch 20 in / 20 RH003A 26 Steet 7.1093 1-Tee Flow Thru Run 20 in / 20 RH003B 26 Steel 7.6671 1-Tee Flow Thru Branch 20 in / 20 RH004A 21 Steet 14.758 1-Tee Flow Thru Branch 14 in / 30 1-Reducer Contraction 20 X 14 1-Gate Wedge Disc 2-Elbow Short - r/d 1 @ 90* 1 1-Fixed K vei corctn RH004B 21 Steet 14.95 1 Reducer Contraction 20 X 14 l 14 in / 30 2-Ebow Short - r/d 1 @ 90*

1-Gate Wedge Disc 1 Tee Flow Thru Branch l 1-Fixed K vel coretn Calc / No V75100.NSP97.00501 ATTACHMENT D Page_l.l.2.of /.E1 i PIPE-FLO ver 5.01 pg 5

-.7 -, Ty- r' nhp - y.m --- -

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l PlPE MATERIALS LIST 06/16/97 9:14 atm PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft RH005A 21 Steel 14,758 1-Reducer Contraction 20 X 14 14 in / 30 1-Gate Wedge Disc 2-Elbow Short - r/d 1 @ 90*

1-Fixed K vel coretn RH005B 21 Steet 14.95 1 Reducer Contraction 20 X 14 14 in / 30 2-Ebow Short - r/d 1 @ 90*

1-Gate Wedge Disc 1-Fixed K vel coretn RH006A 16 Steel 1.15 1-Reducer Contraction 12 X 10 12 in / 40 RH0068 16 Steel 3.0671 1-Elbow Short - r/d 1 @ 90*

12 in / 40 1-Reducer Contraction 12 X 10 RH006C 16 Steel 1.15 1-Reducer Contraction 12 X 10 12 in / 40 RH006D 16 Steel 3.06671 1-Elbow Short - r/d 1 @ 90*

12 in / 40 1-Reducer Contraction 12 X 10 l

l RH006DA 16 Steel 20.7 3-Elbow Short - r/d 1 @ 90* 1 10 in / 40 1 Swing CheckVertical l 1-Gate Wedge Disc l

1-Reducer Enlargement 10 X 14 i RH007A 16 Steel 17.6094 2-Elbow Short - r/d i @ 90*

10 in / 40 1-Elbow Long - r/d 1.5 @ 90*

1-Gate Wedge Disc 1-Tee Flow Thru Run 1-Reducer Enlargement to X 12 1-Swing Check Angled RH007B 16 Steel . 19.2625 2-Elbow Short- r/d 1 @ 90*

10 in / 40 1-Swing Check Vertical ,

1-Gate Wedge Disc {

1-Tee Flow Thru Branch '

1-Reducer Enlargement 10 X 14 RH007C 16 Steel 19.7656 3-Elbow Short - r/d 1 @ 90*

10 in / 40 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Swing Check Angled RH0070 21 Steel 4.025 1-Tee Flow Thru Run 14 in / 30 RH008A 21 Steel 11.7875 1-Elbow Short - r/d 1 @ 90*

14 in / 30 1-Tee Flow Thru Run Calc / No. V76100.NSP97.00601 ATTACHMENT d Pagejl3.of /6T PIPE-FLO ver 5.01 pg 6

4 PIPE MATERIALS LIST 06/16/97 9:14 sm PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS l Size / Sch ft l RH008B T Steel 2.875 1-Tee Flow Thru Run i 14 in / 30 i RHRHXA 21 Steel 28.4145 3-Elbow Short - r/d 1 @ 90*

14 in / 30 2-Gate Wedge Disc 1-Tee Flow Tnru Run 1-Fixed K RHR HX l

l RHRHXB 21 Steel 54.8343 3-Elbow Short - r/d 1 @ 90*

14 in / 30 2-Elbow Short - r/d 1 @ 45' ,

2-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Fixed K RHR HX ,

. I RHXBYPSA 21 Steel 29.4849 1-Tee Flow Thru Branch ,

14 in / 30 3-Elbow Short - r/d i @ 90' l 1-Globe Valve RHXBYPSB 21 Steet 15.4172 1-Elbow Short - r/d 1 @ 90*

l 14 in / 30 1-Tee Flow Thru Branch 1-Globe Valve RX01A 21 Steel 6.3849 1-Tee Flow Thru Branch 14 in / 30 RX018 21 Steel 20.748 1-Elbow Short - r/d 1 @ 90' 14 in / 30 1-Tee Flow Thru Run 1-Tee Flow Thru Branch RXO1C 21 Steel 83.5906 1-Tee Flow Thru Run 14 in / 30 3-Elbow Short - r/d 1 @ 90' 1 Tee Flow Thru Branch 1-Reducer Enlargement 14 X 16 l 1-Fixed K Flow Element l I

RX01D 21 Steel 73.7917 1-Tee Flow Thru Run 14 in / 30 3-Elbow Short - r/d 1 @ 90*

1-Tee Flow Thru Branch 1-Reducer Enlargement 14 X 16 1-Fixed K Flow Element RX02A 21 Steet 12.3625 1-Globe Valve 16 in / 30 1-Tee Flow Thru Run RXO2B 21 Steet 12.3625 1-Globe Valve 16 in / 30 RXO2C 35 Steel 102.769 7-Elbow Short - r/d 1 @ 90' 16 in / 80 2-Gate Double Disc 1-Swing Check Angled 1-Reducer Enlargement 16 X 18 Calc / No. V75100.NSP97.00501 ATTACHMENT D Page lI4 of /$_'T PIPE-FLO ver 5.01 pg 7

PIPE MATERIALS LIST 06/16/97 9:14 tm PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft RX02D 35 Steel 97.9537 6-Elbow Short - r/d 1 @ 90' l

16 in / 80 2-Gate Double Disc 1-Swing Check Angled 1-Elbow Short - r/d 1 @ 45' 1-Reducer Enlargement 16 X 18 RXO1A 16 Steet 6.3649 1-Tee Flow Thru Branch l

14 in / 40 l

i Calc / No. V75100.NSP97.00501 ATTACHMENT N PageIof /59 PIPE-FLO ver 5.01 pg 8

. _ _ _ . . _ m.. , _ . _ . . _ _ _ _ _ . - _ . . . . _ . _ . _ _ . _ _ _ _ _ _. .

PIPE

SUMMARY

06/16/97 9:14 am i

PIPE MATERIAL. SCHEDULE SIZE LENGTH Steel 20 20 in 555.352 ft Steel 30 14 in 516.659 ft 16 in 24.725 ft Steet 40 2.5 in 190.464 ft l

6 in 79.3144 ft 10 in 475.139 ft 12 in 130.603 ft 14 in 6.3849 ft Steet 60 20 in 51.2285 ft -

Steel 80 2 'n 10.4696 ft 8 in 112.445 ft 16 in 200.723 ft VALVE & FITTING

SUMMARY

SPECIFICATION MATERIAL SOHEDULE VALVES & FITTINGS 16 LB30 Steel 40 Size: 2.5 in 7-Elbow Short - r/d i @ 45' 2-Tee Flow Thru Branch 3-Reducer Contraction 2.5 X 2 18-Elbow Short - t/d 1 @ 90' 2-Fixed K Orifice Min.

Size: 6 in 1-Elbow Long - r/d 1.5 @ 67.5*

1-Elbow Long - r/d 1.5 @ 45' 1-Elbow Long - r/d 1.5 @ 90*

2-Gate Wedge Disc 1-Swing Check Angled 2-Tee Flow Thru Branch 1-Elbow Short - r/d 1 @ 90' 1-Fixed K vel coretn Size: 10 in 28-Elbow Short - r/d 1 @ 90' 5-Tee Flow Thru Run 4-Swing Check Vertical 11-Elbow Short r/d 1 @ 45' 2-Fixed K Flow Element 2-Fixed K Res. Orifice 2-Reducer Contraction 10 X 8 4-Gate Wedge Disc Calc / No. V75100.NSP97.00501 ATTACHMENT D Page llb of /ST PIPE-FLO ver 5.01 pg 9

VALVE & FITTING

SUMMARY

06/16/97 9:14 cm SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS

, Size: 10 in 2-Reducer Enlargement 10 X 14 1-Elbow Long - r/d 1.5 @ 90*

1 Reducer Enlargement to X 12 2-Swing Check Angled 2 Tee Flow Thru Branch Size: 12 in 11-Elbow Short - r/d 1 @ 90*

2-Gate Wedge Disc

.1-Gate Double Disc 2-Tee Flow Thru Run 2-Tee Flow Thru Branch 5-Elbow Short - r/d 1 @ 45' 2-Fixed K vel coretn 4-Reducer Contraction 12 X 10 Size: 14 in 1-Tee Flow Thru Branch 21 LB31 Steel 30 Size: 14 in 30-Elbow Short - r/d 1 @ 90' 9-Tee Flow Thru Run 1-Reducer Contraction 16 X 14 3-Reducer Enlargement 14 X 16 13-Gate Wedge Disc 1-Elbow Long - r/d 1.5 @ 22.5*

1-Swing Check Angled 3-Elbow Long - r/d 1.5 @ 90' 10-Tee Flow Thru Branch 5-Fixed K vel coretn 4-Reducer Contraction 20 X 14 2-Fixed K RHR HX 2-Elbow Short - r/d 1 @ 45' 2-Globe Valve 2-Fixed K Flow Element Size: 16 in 2-Globe Valve 1-Tee Flow Thru Run 26 LB32 Steel 20 Size: 20 in 16-Fixed K 22.5 mitre 3-Elbow Short - r/d 1 @ 90*

2-Gate Wedge Disc 7-Tee Flow Thru Branch 2-Elbow Short - r/d 1 @ 45' 1-Elbow Long - r/d 1.5 @ 90' Calc / No. W6100.NSP97.00601 ATTACHMENT U Page l Nof /f'l PIPE-FLO ver 5.01 pg 10

.,U - p J .,_,-,Ap A. -i.. -4 __wA.t 2_+4 4 m h__&... *w. - .*

VALVE & FITTING

SUMMARY

06/16/97 9:14 atm SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS Size: 20 in 1-Tee Flow Thru Run 31 LB34 Steel 60 Size: 20 in 2-Fixed K strainer 5-Tee Flow Thru Branch 2-Fixed K STRAINER 10-Fixed K contraction 8-Tee Flow Thru Run 10-Fixed K enlargement !

35 LB34a Steel 80 l Size: 2 in 1-Elbow Short - r/d 1 @ 90* l 3-Reducer Enlargement 2 X 2.5 l 2-Globe Valve Size: 8 in 6-Gate Wedge Disc 2-Swing Check Angled 12-Elbow Short - r/d 1 @ 90*

1-Fixed K Spargers 1-Fixed K Sparger l

Size: 16 in 13-Elbow Short - r/d 1 @ 90*

4-Gate Double Disc l 2-Swing Check Angled 2-Reducer Enlargement 16 X 18 1-Elbow Short - r/d 1 @ 45*

l l

Calc / No. V75100.NSP97.00501 ATTACHMENT h PageMof 67 PIPE-FLO ver 5.01 pg 11

Ccmptny; Duke Enginssring & Szrvices 06/16/97 9:17 am ProjIct: Lintup: CASE 3 by: Josrph D. Spirecino rev: 06/16/97 9:17 am System: OVRPRES3 Deviation: 0.000203 % i rev: 06/16/97 9:09 am after: 9 iterations j long term, B &C RHR 4000 ea & A&B CS 2800gpm A strainer plugged, O cont. press., sp wtr M 908'-9.3" )

Volumetric flow rates require constant fluid properties in all pipelines. Fluid properties in the first specification were used in this l calculation.

LINEUP SUMMARIES ,

I PIPELINE FLOW PRESSURE SET LEVEL gpm SOURCE psi g ft CSD3A >>> 2800 ACSD3 0 0 CSD8A >>> 234.9 ACSD8 0 0 l CSD3B >>> 2800 BCSD3 0 0 .

l CSD6B >>> 228.5 BCSD6 0 0 RX02D >>> 8000 RECIRC2 0 0 B <<< 5250 TB 0 4.459 i l

C <<< 3473 TC 0 4.459 D <<< 5341 TD 0 4.459 )

Flows IN: 14064 gpm i Flows OUT: 14063 gpm NET FLOWS IN: 1 gpm l

1 Calc / No. V75100.NSP97.00601 ATTACHMENT D Page I$ of /f/

PIPE-FLO ver 5.01 pg i

LINEUP NODES 06/16/97 9:17 em NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi g ft 1 902.25 2.3 907.7 10 902.25 2.64 908.5 11 902.25 2.634 908.5 12 902.25 2.629 908.4 13 902.25 2.601 908.4 14 902.25 2.551 908.3 15 902.25 2.458 908 16 902.25 2.45 908 17 902.25 2.446 908 18 902.25 2.434 908 I 1

19 902.25 2.344 907.8 l

'2 902.25 2.284 907.6 20 902.25 2.33 907.7 i 3 902.25 2.289 907.6 4 902.25 2.295 907.7 5 902.25 2.3 907.7 6 902.25 2.311 907.7 7 902.25 2.393 907.9 8 902.25 2.449 908 902.25 2.501 908.1 ;

9 1

A.CS.IN 902.25 2.453 908 A.CS.SUCT 897.833 1.938 902.4 A.C S.T 899.916 2.015 904.7 A. DIS 897.833 3.828 906.8 A.IN 897.583 3.934 906.8 A.RH.IN 902.25 2.332 907.7 A.RH.T 897.583 3.972 906.9 A.SUC 897.833 3.828 906.8 ACSD2 931.917 75.41 1109 ACSD3 981.188 0 (source) 981.2 ACSD4 900.156 312.5 *" 1636 ACSDS 900.74 283.3 *" 1568 ACSD6 925.875 17.47 967 ACSD7 928 10.45 952.6 ACSD8 927 0 (source) 927 ACSD9 971.25 56.3 1104 ACSDSCG 899.635 315.8 *" 1643 ADISTEE 901.083 39.58 994.3 B.CS.lN 902.25 2.305 907.7 B.CS.SUCT 897.833 1.857 902.2 B.CS.T 000.305 2.175 005 Calc / No. V76100.NSP97.00601 ATTACHMENT D Page,$QofR PIPE-FLO ver 5.01 pg 2

l LINEUP NODES 06/16/97 9:17 am NODE ELEVATION DEMAND PRESSURE H GRADE l M pm Ng n i

l. l B. DIS 899.5 149.1 1251 B.lN 897.583 3.84 906.6 l B.RH.IN 902.25 2.283 907.6 i B.RH.T 897.583 3.939 906.9 B.SUC 897.833 2.127 902.8 I BCSD2 927.833 77.42 1110 )

BCSD3 980.38 0 (source) 980.4 BCSD4 899.896 295.7 "' 1596 !

BCSD5 901.688 266.9 "* 1530 BCSD6 930.333 0 (source) 930.3 BCSD7 978.5 52.78 1103 ;

BCSDSCG 899.583 299.2 "* 1604 BDISTEE 908 35.65 991.9 C. DIS 897.833 153.3 1259 C.lN 897.583 3.934 906.8 C.SUC 897.833 2.222 903.1 D. DIS 899.5 3.026 906.6 D.DISA 908 35.65 991.9 )

D.lN 897.583 3.84 906.6 D.SUC 897.833 3.734 906.6 HP.lN 902.25 2.443 908 HP.T 901.615 2.713 908 M02013 940.91 11.74 968.6 MO2012 940.917 18.52 984.5 RC.lN 902.25 2.595 908.4 RC.T 902.25 2.595 908.4 RECIRC2 951.75 0 (source) 951.7 RECIRCA 930.168 23.09 984.5 l

RECIRCB 930.167 21.95 981'.8 RHRHXDA 916.333 31.88 991.4 RHRHXDB 915.49 31.41 989.5 RHRHXDC 916.336 31.39 990.3 RHRHXDD 921.33 28.06 987.4 RHRHXS1 909.406 35.68 993.4 RHRHXS2 908 35.48 991.5 SA 902.25 2.289 907.6 SB 902.25 2.644 908.5 SC 902.25 2.632 908.4 SD 902.25 2.442 908 TB 904.316 1.894 (source) 908.8 TC G04.31G 1.004 (evvie) 300.0 Calc / No. V75100.NSP97.00601 ATTACHMENT D Page Rl of jf_'T PIPE-FLO ver 5.01 pg 3

NODE ELEVATION DEMAND PRESSURE H GRADE M gpm psig n i TD 904.316 1.894 (source) 908.8 4 1 Calc / No. V75100.NSP97.00501 ATTACHMENT U PageMofRt PIPE-FLO ver 5.01 pg 4 a t

LINEUP PlPELINES 06/16/97 9:17 cm l

PlPELINF FROM TO FLOW VEL dP HL 7

gpm ft/sec psi g ft A TA SA closed 0 0 0

, B TB SB 5250 6.356 (0.750) 0.299 C TC SC 3473 4.205 (0.738) 0.328 CDS1B B.CS.SUCT BCSDSCG 3028

12.33 (297.4) (702)

- BCS - dP: (298.5) HL:(702.7)

CDS7A ACSD6 ACSD7 234.9

25.54 7.021 14.41 CROSSTIE RECIRCA <-> RECIRCB 4000 9.315 1.142 2.689 CS001A A.CS.!N A.CS.T 3035 8.706 0.438 3.365 CS0018 B.CS.IN B.CS.T 3028 8.688 0.130 2.671 CS003A A.CS.T A.CS.SUCT 3035 8.706 0.078 2.266 CS0038 B.CS.T B.CS.SUCT 3028 8.688 0.318 2.801 CSD1A A.CS.SUCT ACSDSCG 3035

12.36 (313.9) (740.8)

- A.CS - dP: (315) HL: (741.6)

CSD2A ACSDSCG ACSD2 2800 11.4 67.17 125.9

- FCV@2800 - dP: 173.2 HL: 407.9 CSD2B BCSDSCG BCSD2 2800 11.4 64.21 123

- FCV@2800 - dP: 157.6 HL: 371.1 CSD3A ACSD9 ACSD3 2800

19.69 56.3 122.6 CSD3B BCSD7 BCSD3 2800

19.69 52.78 122.4 CSD4A ACSDSCG ACSD4 234.9

15.75 3.276 7.192 CSD4B BCSDSCG BCSD4 228.5

15.32 3.508 7.948 CSDSA ACSD4 ACSDS 234.9

25.54 29.2 68.18 l CSDSB BCSD4 BCSDS 228.5

24.84 28.84 66.12 l CSD6A ACSDS ACSD6 234.9

15.75 265.8 600.8 CSD6B BCSDS BCSD6 228.5

15.32 266.9 599.8 CSD7B BCSD2 BCSD7 2800 11.4 24.63 7.329 CSD8A ACSD7 ACSD8 234.9

15.75 10.45 25.6 CSD9A ACSD2 ACSD9 2800 11.4 19.11 5.661 D TD SD 5341 6.466 (0.549) 0.774 H1 20 <> 1 2544 2.807 0.030 0.071 H11 1 <-> B.RH.IN 2544 3.08 0.017 0.040 H12 A.RH.IN <-> 20 2544 3.08 0.001 0.003 H2 3 2 1456 1.606 0.005 0.011 H21 SA 3 1456 1.763 0 0.001 H22 2 B.RH.IN 1456 1.763 0 0.002 H3 5 4 1456 1.606 0.005 0.012 H31 B.CS.IN 5 1456 1.763 0.005 0.012 H32 4 SA 1456 1.763 0.006 0.013 H4a 9 8 4485 4 948 0.052 0.123 H4a1 SB 9 4485 5.429 0.143 0.337 H4:2 8 HP.IN 4485 5.429 0.006 0.013 H4b 7 6 4485 4.948 0.082 0.194 Calc / No. V75100.NSP97.00501 ATTACHMENT D Page$ of M PIPE-FLO b f 5.01 pg 5

i LINEUP PIPELINES 06/16/97 9.17 am PIPELINE FROM TO FLOW VEL dP .HL gpm ft/sec psi g ft 1

H4b1 HP.lN 7 4485 5.429 0.050 - 0.118 l

H4b2 6 B.CS.IN 4485 5.429 0.006 0.013 H5 10 11 765.5 0.845 0.006 0.015 H51 '11 SC 765.5 0.927 0.002 0.004 H52 SB 10 765.5 0.927 0.004 0.010 l l

H63 12 13 4238 4.676 0.028 0.066 H631 13 RC.IN 4238 5.131 0.005 0.012 H6:2. SC 12 -4238 5.131 0.003 0.008 H6b 14 15 4238 4.676 0.093 0.218 H6bt 15 A.CS.IN 4238 5.131 0.005 0.012 i H6b2 RC.IN 14 4238 5.131 0.045 0.105 H7 16 17 1203 1.328 0.003 0.008 l H71 17 SD 1203 1.457 0.004 0.009 )

H72 A.CS.lN 16 1203 1.457 0.004 0.009 H6 18 19 6544 7.22 0.090 0.212 i H81 19 A.RH.IN 6544 7.923 0.013 0.030 l H82 SD 18 6544 7.923 0.008 0.019 l

HP001 HP.lN HP.T 0 0 (0.270) 0 HP002 HP.T HP.SUCT closed 0 0 0 RC001 RC.IN RC.T 0 0 0 0 RC002 RC.T RC.SUCT closed 0 0 0 RH001A A.RH.IN A.RH.T 4000 4.413 (1.64) 0.805 I RH001B B.RH.lN B.RH.T 4000 4.413 (1.656) 0.768 l RH002A C.IN A.IN 0 0 0 0 RH0028 B.lN D.lN O O 0 0 RH003A A.RH.T C.lN 4000 4.413 ' 0.038 0.089 RH003B B.RH.T B.IN 4000 4.413 0.099 0.233 RH004A C.IN C.SUC 4000 9.315 1.712 3.781 RH004B B.lN B.SUC 4000 9.315 1.713 3.784 RH005A A.IN A.SUC 0 0 0.106 0 RH005B D.lN D.SUC 0 0 0.106 0 RH006A A.SUC A. DIS 0 0 0 0

- ARHR - dP: HL: i R H0.)6B B.SUC B. DIS 4000 11.47 (147) (347.8)

- BRHR - dP: (148.2) HL:(349)

RH006C C.SUC C. DIS 4000 11.47 (151.1) (355.8)

- CRHR - dP: (151.4) HL:(356.4)

RH006D D.SUC D. DIS 0 0 0.708 0 l

- DRHR - dP: HL:

RH006DA D. DIS D.DISA closed 0 0 0 RH007A A. DIS ADISTEE closed 0 0 0 RH007B B. DIS BDISTEE 4000

16.29 8.187 10.78

- FCV@4000 -U'P: 105.3 HL: 247.9 Calc / No. V7510's.NSP97.00601 ATTACHMENT D Page 124 of /5T PlPE-FLO ver 5.01 pg 6

J LINEUP PIPELINES 06/16/97 9:17 Em j PIPELINE FROM TO FLOW VEL dP HL gpm ft/see psi g ft RH007C C. DIS ADISTEE 4000 *1629 7.312 13.97 I

- FCV@4000 - dP: 106.4 HL: 250.6 l RH007D 2.bsA BDISTEE 0 0 0 0 l RH008A ADISTEE RHRHXS1 4000 9.315 3.907 0.877 l RH008B BDISTEE RHRHXS2 4000 9.315 0.165 0.389

. RHRHXA RHRHXS1 RHRHXDA 2036 4.74 3.8 2.02 RHRHXB RHRHXS2 RHRHXDB 1882 4.382 4.068 2.089 RHXBYPSA RHRHXS1 RHRHXDA 1964 4.574 3.8 2.02 RHXBYPSB RHRHXS2 RHRHXDB 2118 4.932 4.068 2.089

RX01A RHRHXDA RHRHXDC 4000 9.315 0.482 1.131 RX01B RHRHXDB RHRHXDD 4000 9.315 3.351 2.051 ,

RX01C RHRHXDC RECIRCA 4000 9.315 8.306 5.726 RX01D RHRHXDD RECIRCB 4000 9.315 6.117 5.566 RX02A RECIRCA MO2012 0 0 4.565 0 RX02B RECIRCB M02013 8000

14.06 10.21 13.29 RXO2C MO2012 RECIRC1 closed 0 0 0 RX02D M02013 RECIRC2 8000

15.97 11.74 16.8 Calc / No. V75100.NSP97.00501 ATTACHMENT O Page_.}.dof M PIPE-FLO ver 5.01 pg 7

E DE&S Naperville, Illinois PROJECT Monticello Nuclear Station File No: V75100.NSP97.00501 OWNER Northern States Power Co. Calc No: v75100.NSP97.00501 CLIENT Monticello Nuclear Station l

I REFERENCE

ATTACHMENT E FLO-SERIES MODEL PIPING AND NETWORK INPUT AND OUTPUT FOR CASE #4.

l REVISION O PAGE lM PREPARED BY/DATE pQ 6/iQ OF /$

CHECKED BY/DATE /

- _ - . - . _. - - ~.

1B q, 4, TA TD q , q, TC

~

8 A D g e a g !'*

glL* * *d%, tts ,,HS( l6pg H6gg, g3

4 9 $8 10 11 up s SC 12 RC.IN -

4's H$$I e CS IN 8 RH IR RH IN A.CS IN N in"**-#'M W lfO9'%'II"M 4"# M11*b "** [

.U 4 SA 3 2 120 1915017 16 i. CIE0t A -- 34.CS.T 8 CSb q CS061B p 5 HPOO1 On RCOO1 l RHOOl

$ CSOO38_ ,

B

.QSOO3A x

pS g

o HP.SUCT S CS.SUCT A.CS.SUC I*

g C' 4>

(pg HP.T a ,

T HP002 RHOO1A A M.T g B RH T qp 1 lp RCOO2 "o

RH003J. C.M AW

$ 8 IN g D IN 1.

M > RC.SUCT hp 1 h ---- >+

RH004A i 4

_RHOO484 _

BSUC C.SUC

@ Ruoose_ , g ,,, RHoosA___

CDS10 [D.SU( A SUC CSO1A si ./

BRHR CRHR N N BCS T RH006D RH0068 RH006C RHOO1A 9s IO e

D !

i 4 i O ACSDSCO

^

BCSDSCG C_SD4A qp A. DIS >

N CSO4B 4> E US 1> C. DIS

',4> q, D DIS

, RHOO6DA munase --.

C y: Duke EPigM6erngTBerwice4"^ 06/11/97 5:07 pm D Disa 4,"!'09'Ri s fact: Linellet: OVRPRES4 '

RH0000 gI GTEE ACSD2 CSD2B { .

RHRHXS2 4g ggggggggg; RMMXS1 ' '

flO W rate: gpm psummere: pSie ; ;

RHRHxi RHMersion: PifWpRe ver 5.01RHX8YPSA level & grade; ft ! [

4 SD4 BCSD2 s a a e .

,% e m.__m._- - . _ . . _ _ _ . . _ _ . _ _ _ _ . _ _ _ _ _ _ _ _ . _ _ _ _ _ . _ _ . _ _ m __ _ _ _ _ _ _ _ _ _ _ . _ _ _ _ _ _ _ _ _ . _ . . _ _ _ _ _ _ _ . . _ . . _ __ .m._ _ _ _ _

e s 8RHR CRHR SCS RHOO60 RHOO68 RHOO6C RHOOLA O

t.1 Q BCSDSCG ACSDSCO CSD4A Z CSD40 hp 8 DtS qp C DIS qp A.DtS 4>

p . 4> 4, D DtS

' A CSD2 AD g

$ , D DfSA hpRHOO70, _ <6 78 k _ISTEE i

h , tsp 23 RHOO98 BDtSTEE u,oogg /,

gi ,/ RHRHxS2 o = RHRHxSi o_ =

] / q,ACSD4 U / RHRHXI fHXBYPS8 RHRHX>. UtX8YPSA

@ lpBCSD4 q(BCSD2 a CSO9A

SD5A RHRHXD3 1W RHRHXDAe'-

RXO18 gxotA H CSD78 ,

=4 RHRHXDDqp RHRHXDCqp qp ACSDS O RXO10 4XO1C CS'58 0 ACSDS qp RECIRC8 qp CROSSTIE _- :, RECIRCA ITI CSD6A Z

ax02s RXO2A q,eCSD7 MO2013h p q, MO2012 CSD3A 4> ACSD6

S038 RXO21i RXO2C T

COS7A

$. i> d>

qpBCSD5 i d> RECIRC2 RECIRCf qp q

BCSD3 ACSD3 ap ACSDF Company: Duke Engineering & Services 06/11/97 5.08 pm csDeu Project: Linellst: OVRPRES4 by: Joseph D. Speracino Lineup:

Comments: flow rate: MM^ r Pressure: pele ,

Verslom 7;PE-FLO ver 5.01 level & grade: ft a

.d . [ ; .s ' -

5 .* 'd*, ?-

~ - .T . 'y , N.

8

1 C:mp ny: Duks Enginstring & SIrvicts 06/16/97 9:26 am Pr jIct: 4tsm: OVRPRES4 by: JosIph D. Spiracino rsv: 06/16/97 9:24 cm SYSTEM REPORT Created: 11/04/9611:56 am Pipes: 93 4 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 d

NSP RHR and CS piping model, SP Temp.150.5'F. and 0 psig cont. press. Containment overpressure cales.

SYSTEM NODES NODE ELEVATION PIPELINES IN PIPELINES OUT ft 1 902.25 H11 H1 10 902.25 H52 HS 11 902.25 H5 H51 l 12 902.25 H6a2 H6a 13 902.25 H6a H6a1 14 902.25 H6b2 H6b 15 902.25 H6b H6b1

, 16 902.25 H72 H7 l 17 902.25 H7 H71 18 902.25 H82 H8 19 902.25 H8 H81 2 902.25 H2 H22 20 902.25 Hi H12 3 902.25 H21 H2 4 902.25 H3 H32 5 902.25 H31 H3 6 902.25 H4b H4b2 7 902.25 H4b1 H4b 8 902.25 H4a H4a2 9 902.25 H4a1 H4a A.CS.lN 902.25 H6b1 CS001A H72 A.CS.SUCT 897.833 CS003A CSD1A A.CS.T 899.916 CS001A CS003A A. DIS 897.833 RH006A RH007A Calc / No. V75100.NSP97.00501 ATTACHMENT E Page ic27 of d PlPE-FLO ver 5.01 pg i

. - . ~. .. - - . . - _ . _ _ - =- _..

SYSTEM NODES 06/16/97 9:26 atm NODE ELEVATION PIPELINES IN PIPELINES OUT

. A.IN 897.583 RH002A RH005A A.RH.IN 902.25 H12 RH001A H81 l

A.RH.T 897.583 RH001A RH003A

! A.SUC 897.833 RH005A RH006A ACSD2 931.917 CSD2A CSD9A I l

ACSD3 981.188 CSD3A I l

ACSD4 900.156 CSD4A CSD5A ACSD5 900.74 CSD5A CSD6A ACSD6 925.875 CSD6A CDS7A ACSD7 928 CDS7A CSD8A ACSD8 927 CSD8A ACSD9 971.25 CSD9A CSD3A ACSDSCG 899.635 CSD1A CSD2A CSD4A ADISTEE 901.083 RH007A RH008A RH007C l B.CS.IN 902.25 H4b2 CS001B H31 B.CS.SUCT 897.833 CS003B CDSIB B.CS.T 899.885 CS001B CS003B B. DIS 899.5 RH006B RH007B B.IN 897.583 RH003B RH002B RH004B B.RH.lN 902.25 H22 H11 RH0018 B.RH.T 897.583 RH0018 RH003B B.SUC 897.833 RH004B RH006B BCSD2 927.833 CSD2B CSD78 BCSD3 980.38 CSD3B BCSD4 899.896 CSD4B CSDSB BCSDS 901.688 CSD5B CSD6B BCSD6 930.333 CSD6B Calc / No. V75100.NSP97.00501 ATTACHMENT 6 PageM of M PIPE-FLO ver 5.01 pg 2

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SYSTEM NODES 06/16/97 9:26 am NODE ELEVATION PIPELINES IN PIPELINES OUT A

i BCSD7 978.5 CSD7B CSD3B BCSDSCG 899.583 CDS1B CSD2B CSD4B l

! BDISTEE 908 RH007B RH008B >

RH007D l C. DIS 897.833 RH006C RH007C C.lN 897.583 RH003A RH002A RH004A 1

, C.SUC 897.833 RH004A RH006C I L

D. DIS 899.5 RH006D RH006DA D.DISA 908 RH006DA RH007D D.lN 897.583 RH002B RH005B D.SUC 897.833 RH0058 -

RH006D HP.lN 902.25 H4a2 H4bi HP001 HP.SUCT 901.615 HP002 HP.T 901.615 HP001 HP002 I

M02013 940.91 RX02B RX02D MO2012 940.917 RX02A RX02C RC.lN 902.25 H6a1 H6b2 RC001 RC.SUCT 899.042 RC002 RC.T 902.25 RC001 RC002 RECIRC1 951.75 RX02C RECIRC2 951.75 RX02D RECIRCA 930.168 CROSSTIE RX02A RX01C RECIRCB 930.167 RX01D CROSSTIE RX02B RHRHXDA 916.333 RHRHXA RX01A RHXBYPSA RHRHXDB 915.49 RHRHXB RX01B RHXBYPSB RHRHXDC 916.336 RX01A RX01C i

Calc / No. V75100.NSP97.00501 ATTACHMENT 1 PageM of /5V PIPE-FLO ver 5.0i P9 3

, SYSTEM NODES 06/16/97 9:26 tm

! NODE ELEVATION PIPELINES IN PIPELINES OUT ft i RHRHXDD 921.33 RX01B RX01D 1

i RHRHXS1 909.406 RH008A RHRHXA RHXBYPSA RHRHXS2 908 RH008B RHRHXB RHXBYPSB SA 90225 A H21 H32 SB 902.25 B H4a1

! H52 SC 902.25 C H6a2 H51 SD 902.25 D H82 H71 TA 904.316 A TB 904.316 B TC 904.316 C TD 904.316 D Calc / No. V75100.NSP97.00501 ATTACHMENT _ f Page i3Rof /54 PIPE-FLO ver 5.01 p94

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I SYSTEM PIPES 06/16/97 9:26 am PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP A 31 TA SA B 31 TB SB C 31 TC SC CDSIB 16 B.CS.SUCT BCSDSCG BCS CDS7A . 35 ACSD6 ACSD7 i CROSSTIE 21 RECIRCB RECIRCA CS001A 16 A.CS.IN A.CS.T l CS001B 16 B.CS.lN B.CS.T CS003A 16 A.CS.T A.CS.SUCT CS0038 - 16 B.CS.T B.CS.SUCT l CSD1A 16 A.CS.SUCT ACSDSCG A.CS CSD2A 16 ACSDSCG ACSD2 1 CSD2B 16 BCSDSCG BCSD2 CSD3A 35 ACSO9 ACSD3 CSD3B 35 BCSD7 BCSD3 CSD4A 16 ACSDSCG ACSD4 CSD4B 16 BCSDSCG BCSD4 CSD5A 35 ACSD4 ACSDS I CSD5B 35 BCSD4 BCSDS CSD6A 16 ACSDS ACSD6 l

CSD6B 16 BCSDS BCSD6 CSD7B 16 BCSD2 BCSD7 CSD8A 16 ACSD7 ACSD8 CSD9A 16 ACSD2 ACSD9 D 31 TD SD H1 26 1 20 H11 31 B.RH.IN 1 H12 31 20 A.RH.lN H2 26 3 2 H21 31 SA 3 H22 31 2 B.RH.IN H3 26 5 4 H31 31 B.CS.lN 5 H32 31 4 SA 3 H4a 26 9 8 H4a1 31 SB 9 H4a2 31 8 HP.lN H4b 26 7 6 H4b1 31 HP.IN 7 H4b2 31 6 B.CS.lN HS 26 10 11 H51 31 11 SC Calc / No. V75100.NSP97.00601 ATTACHMENT 6 Page L13of /84 PIPE-FLO ver 5.01 pg 5

SYSTEM PIPES 06/16/97 9:26 am PIPEUNE SPEC FROM_ NODE TO_ NODE PUMP / COMP H52 31 SB 10 H6a 26 12 13 H6a1 31 13 RC.IN H6a2 31 SC 12 H6b 26 14 15 H6bi 31 15 A.CS.IN H6b2 31 RC.lN 14 H7 26 16 17 l

H71 31 17 SD H72 31 A.CS.IN 16 i H8 26 18 19 H81 31 19 A.RH.IN H82 31 SD 18 l HP001 21 HP.lN HP.T HP002 21 HP.T HP.SUCT RC001 16 RC.lN RC.T RC002 16 RC.T RC.SUCT RH001A 26 A.RH.IN A.RH.T l

RH001B 26 B.RH.lN B.RH.T '

RH002A 26 C.IN A.IN RH002B 26 B.IN D.IN RH003A 26 A.RH.T C.lN RH003B 26 B.RH.T B.IN RH004A 21 C.IN C.SUC RH0048 21 B.lN B.SUC RH005A 21 A.lN A.SUC i RH005B 21 D.lN D.SUC RH006A 16 A.SUC A. DIS ARHR RH006B 16 B.SUC B. DIS BRHR RH006C 16 C.SUC C. DIS CRHR RH006D 16 D.SUC D. DIS DRHR RH006DA 16 D. DIS D.DISA RH007A 16 A. DIS ADISTEE RH0078 16 B. DIS BDISTEE RH007C 16 C. DIS ADISTEE RH007D 21 D.DISA BDISTEE RH008A 21 ADISTEE RHRHXS1 RH008B 21 BDISTEE RH81HXS2 RHRHXA 21 RHRHXS1 RHRHXDA RHRHXB 21 RHRHXS2 RHRHXDB RHXBYPSA 21 RHRHXS1 RHRHXDA RHXBYPSB 21 RHRHXS2 RHRHXDB Calc / No. V75100.NSP97.00501 ATTACHMENT $ Page 134of /64 PIPE-FLO ver 5.01 Pg 6

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i SYSTEM PIPES 06/16/97 9:26 am )

PIPELINE SPEC FROM_ NODE TO_ NODE PUMP / COMP RX01A 21 RHRHXDA RHRHXDC I RX01B 21 RHRHXDB RHRHXDD I RX01C 21 RHRHXDC RECIRCA f RX010 21 RHRHXDD RECIRCB j RX02A 21 RECIRCA MO2012

. RX02B 21 RECIRCB M02013 RX02C 35 MO2012 RECIRC1 RXO2D 35 M02013 RECIRC2 RXO1A 16 . .

l l

Calc / No. V75100.NSP97.00601 ATTACHMENT _f_, Page 136of R PIPE-FLO ver 5.01 Pg 7

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SYSTEM COMPONENTS 06/16/97 9:26 tm PUMP / COMP PERFORMANCE DATA A.CS gpm: 0 2179 3990 5040 5755 ft: 850.3 795.5 664 536.2 411.7 egn: 850.3 - 4.49715e-006 Q ^ 2.12033 ARHR gpm: 0 3365 4000 4250 4540 ft 810.3 498.9 350 280 171.8 egn: 810.3 - 1.3787e-006 Q ^ 2.36763 BCS gpm: 0 1948 3080 4875 5600 ft: 844 770.1 719.4 535.2 418.1 egn: 844 - 0.000218414 Q ^ 1.66917 BRHR gpm: 0 3656 4000 4250 4408 ft 813.8 436 350 280 230 egn: 813.8 - 2.04305e-006 Q ^ 2.32005 CRHR gpm: 0 3540 4000 4250 4440 ft: 763.9 461.1 360 290 235.4 egn: 763.9 - 5.58043e-007 Q ^ 2.46066 DRHR gpm: 0 3542 4000 4250 4425 ft: 810.1 463 350 285 227 egn: 810.1 - 2.16007e-006 Q ^ 2.31196 Calc / No. V75100.NSP97.00501 ATTACHMENT E Page 136 of f PlPE-FLO ver 5.01 pg 8

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' Comp:ny: Duke Enginssring & Strvicts 06/16/97 9:26 am ProjIct: Systim: OVRPRES4 I by: Jos1ph D. Spir:cino tsv: 06/16'97 9:24 sm I l

PIPELIST REPORT Created: 11/04/9611:56 am Pipes: 93

( Design file: Nodes: 87 l

Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.150.5'F. and 0 psig cont. press. Containment overpressure cales.

SPECIFICATIONS SPECIFICATION PIPE MATERIAL FLUID VALVE TABLE DESIGN LIMITS Sch / Roughness Temp / Pres Vel / Pres 16 LB30 Steel Water Standard 0 - 12 ft/sec rev: 06/16/97 9:23 am Sch 40 150.5 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec 21 LB31 Steel Water Standard 0 - 12 ft/sec rev: 06/16/97 9:23 am Sch 30 150.5 'F 0 - 200 psi g 0.0018 in 0 psig l Size for: 8 ft/sec 26 LB32 Steel Water Standard 0 - 12 ft/see rev: 06/16/97 9:24 am Sch 20 150.5 'F 0 - 200 psi g 0.0018 in 0 psig Size for: 8 ft/sec 31 LB34 Steel Water Standard 0 - 12 ft/sec rev: 06/16/97 9:24 am Sch 60 150.5 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec l 35 LB34 Steel Water Standard 0 - 12 ft/sec rev: M,16/97 9:24 am Sch 80 150.5 'F 0 - 200 psi g 0.0018 in 0 psi g Size for: 8 ft/sec Calc / No. V75100.NSP97.00501 ATTACHMENT l Page 63.2ofIT PIPE-FLO ver 5.01 pg 1

)

PIPELIST 06/16/97 9:26 am PlPELINE SPEC MATERIAL LENGTH FLUID VALVES Size / Sch ft Temp / Pres Total-K A 31 Steel 3.6777 Water 1.163 20 in / 60 150.5 'F / 0 psi g B 31 Steel 3.6777 Water 0.4469

- 20 in / 60 150.5 'F / 0 psi g C 31 Steel 3.6777 Water 1.163 20 in / 60 150.5 'F / 0 psi g CDS1B 16 Steel 3.45 Water 0.2689 10 in / 40 150.5 'F / 0 psi g CDS7A 35 Steel 7.73835 Water 0.478 2 in / 80 150.5 'F / 0 psi g CROSSTIE 21 Steel 49.0188 Water 1.403 14 in / 30 150.5 'F / 0 psi g CS001A 16 Steel 41.8129 Water 2.285 12 in / 40 150.5 'F / 0 psi g CS001B 16 Steel 42.5259 Water 1.695 12 in / 40 150.5 'F / 0 psi g CS003A 16 Steel 10.7215 Water 1.779 ,

12 in / 40 150.5 'F / 0 psi g l CS0038 16 Steel 27.109 Water 2.018 12 in / 40 150.5 'F / 0 psi g l CSD1A 16 Steel 3.7973 Water 0.2689 !

10 in / 40 150.5 'F / 0 psi g l

CSD2A 16 Steel 108.553 Water 60.59 j 10 in / 40 150.5 *F / 0 psi g !

CSO2B 16 Steel 108.723 Water 59.14 10 in / 40 150.5 *F / 0 psi g CSD3A 35 Steel 57.0055 Water 19.08 -)

8 in / 80 150.5 'F / 0 psi g l CSD3B 35 Steel 55.4392 Water 19.08 8 in / 80 150.5 'F / 0 psi g CSD4A 16 Steel 2.22525 Water 1.664 2.5 in / 40 150.5 'F / 0 psi g CSD4B 16 Steel 2.7485 Water 1.93 2.5 in / 40 150.5 'F / 0 psi g CSD5A 35 Steel 0.67045 Water 6.654 2 in / 80 150.5 *F / 0 psi g CSDSB 35 Steel 2.0608 Water 6.654 2 in / 80 150.5 'F / 0 psi g ;

CSD6A 16 Steel 38.6803 Water 152.5 l 2.5 in / 40 150.5 'F / 0 psi g CSD6B 16 Steet 101.051 Water 155.4 2.5 in / 40 150.5 'F / 0 psi g CSD7B 16 Steel 97.3901 Water 1.995 10 in / 40 150.5 'F / 0 psi g CSD8A 16 Steel 45.7585 Water 2.453 2.5 in / 40 150.5 'F / 0 psi g CSD9A 16 Steel 75.8885 Water 1.53 10 in / 40 150.5 'F / 0 psi g Calc / No. V75100.NSP97.00501 ATTACHMENT E Page 138 of _/ff PIPE-FLO ver 5.01 pg 2

l PIPELIST 06/16/97 9:26 sm PIPELINE SPEC MATERIAL LENGTH FLUlO VALVES Size / Sch ft ' Temp / Pres Total-K D 31 Steel 3.6777 Water 1.163 20 in / 60 150.5 'F / 0 psi g Hi 26 Steel 52.2054 Water 0.144 20 in / 20 150.5 'F / 0 psi g H11 31 Steel 1.9171 Water 0.2536 20 in / 60 150.5 'F / 0 psi g H12 31 Steel 1.9171 Water 0.00366 20 in / 60 150.5 'F / 0 psi g H2 26 Steel 24.1868 Water 0.072 20 in / 20 150.5 'F / 0 psi g H21- 31 Steet 1.9171 Water 0.00366 l 20 in / 60 150.5 'F / 0 psi g j H22 31 Steet 1.9171 Water 0.01484 l 20 in / 60 150.5 'F / 0 psi g l H3 26 Steel 24.3777 Water 0.072 20 in / 20 150.5 'F / 0 psi g l H31 31 Steet 1.4375 Water 0.2425 l 20 in / 60 150.5 'F / 0 psi g i H32 31 Steel 1.9171 Water 0.2536 20 in / 60 150.5 'F / 0 psi g H4a 26 Steel 31.4675 Water 0.072 20 in / 20 150.5 'F / 0 poi g l H4a1 31 Steel 1.9171 Water 0.7201 20 in / 60 150.5 'F / 0 psi g i l

H4a2 31 Steel 1.725 Water 0.01484 20 in / 60 150.5 'F / 0 psi g H4b- 26 Steet 45.6907 Water 0.144 20 in / 20 150.5 'F / 0 psi g H4bi 31 Steet 1.725 Water 0.2425 20 in / 60 150.5 'F / 0 psi g H4b2 31 Steel 1.725 Water 0.01484 20 in / 60 150.5 'F / 0 psi g H5 26 Steel 108.244 Water 0.288 20 in / 20 150.5 'F / 0 psi g H51 31 Steel 1.9171 Water 0.2536 20 in / 60 150.5 'F / 0 psi g H52 31 Steel 1.9171 Water 0.7201 20 in / 60 150.5 'F / 0 psi g H6a 26 Steel 15.1777 Water 0.072 20 in / 20 150.5 'F / 0 psi g H6a1 31 Steet 1.725 Water 0.01484 20 in / 60 150.5 'F / 0 psi g H6a2 31 Steet 1.9171 Water 0.00366 20 in / 60 150.5 'F / 0 psi g H6b 26 Steel 61.7884 Water 0.144 20 in / 20 150.5 *F / 0 psi g H6bi 31 Steel 1.725 Water 0.01484 20 in / 60 150.5 'F / 0 psi g Calc / No. V76100.NSP97.00501 ATTACHMENT _ f_,, Page.].33.of /57 PIPE-FLO ver 5.01 pg 3

PIPELIST 06/16/97 9:26 om PIPELINE SPEC MATERIAL LENGTH FLUID VALVES Size / Sch ft Temp / Pres Total-K ,

H6b2 31 Steet 1.725 Water 0.2425 20 in / 60 150.5 'F / 0 psi g H7 26 Steel 24.3777 Water 0.072

20 in / 20 150.5 'F / 0 psi g H71 31 Steel 1.9171 Water 02536 i 20 in / 60 150.5 'F / 0,.ssi g H72 31 Steel 1.725 Water 02425 i 20 in / 60 150.5 'F / 0 psi g i H6 26 Steel 24.1868 W ater 0.072 20 in / 20 150.5 'F / 0 psi g H81 31 Steel 1.9171 W ater 0.01484 l 20 in / 60 150.5 'F / 0 psi g H82 31 Steet 1.9171 W ater 0.00366 ,

20 in / 60 150.5 'F / 0 psi g l

, HP001 21 Steel 67.5027 W ater 3.127 14 in / 30 150.5 'F / 0 psi g l HP002 21 Steel 9.3679 Ws.ter 1.356 14 in / 30 150.5 'F / 0 psi g RC001 16 Steel 22.7965 Water 4.054 l 6 in / 40 150.5 'F / 0 psi g l RC002 16 Steel 56.5179 Water 1.298 6 in / 40 150.5 'F / 0 psi g RH001A 26 Steel 62.1357 Water 2.161 20 in / 20 150.5 'F / 0 psi g RH001B 26 Steel 55.6198 Water 2.09 l 20 in / 20 150.5 'F / 0 psi g RH002A 26 Steel 5.75 Water 0.7101 20 in / 20 150.5 'F / 0 psi g j RH002B 26 Steel 5.3671 W ater 0.7101 l 20 in / 20 150.5 'F / 0 psi g l I

RH003A 26 Steel 7.1093 W ater 0.2367 20 in / 20 150.5 'F / 0 psi g RH003B 26 Steel 7.6671 W ater 0.7101 l 20 in / 20 150.5 'F / 0 psi g l RH004A 21 Steel 14.758 W ater 2.63 14 in / 30 150.5 'F / 0 psi g j RH0048 21 Steel 14.95 W ater 2.63 14 in / 30 150.5 'F / 0 psi g RH005A 21 Steel 14.758 W ater 1.867 14 in / 30 150.5 'F / 0 psi g RH005B 21 Steel 14.95 Water 1.867 14 in / 30 150.5 'F / 0 psi g '

RH006A 16 Steel 1.15 Water 0.2977 12 in / 40 150.5 'F / 0 psi g RH006B 16 Steel 3.0671 Water 0.5573 12 in / 40 150.5 'F / 0 psi g RH006C 16 Steel 1.15 W ater 0.2977 ;

12 in / 40 150.5 'F / 0 psi g Calc / No. V76100.NSP97.00601 ATTACHMENT 6 Page No of /69 P!PE-FLO ver 5.01 pg 4

PIPELIST 06/16/97 9:26 trn i

I PIPELINE SPEC MATERIAL LENGTH FLUID VALVES i

Size / Sch ft Temp / Pres Total-K RH006D 16 Steel 3.06671 Water 0.5573 12 in / 40 150.5 'F / 0 psi g i RH006DA 16 Steel 20.7 Water 1.76 1

10 in / 40 150.5 'F / 0 psi g l

RH007A 16 Steel 17.6094 Water 2.534 i 4

10 in / 40 150.5 'F / 0 psi g 'l RH007B 16 Steel 19.2625 Water 2.298

! 10 in / 40 150.5 'F / 0 psi g RH007C 16 Steel 19.7656 Water 3.065 10 in / 40 150.5 'F / 0 psi g RH007D 21 Steel 4.025 Water 0.2543 14 in / 30 150.5 'F / 0 psi g RH008A 21 Steel 11.7875 Water 0.5086 14 in / 30 150.5 'F / 0 psi g RH008B 21 Steel 2.875 Water 0.2543 14 in / 30 150.5 'F / 0 psi g RHRHXA 21 Steel 28.4145 Water 5.436 14 in / 30 150.5 'F / 0 psi g RHRHXB 21 Steel 54.8343 Water 6.316 14 in / 30 150.5 'F / 0 psi g RHXBYPSA 21 Steel 29.4849 Water 5.85 14 in / 30 150.5 'F / 0 psi g RHXBYPSB 21 Steet 15.4172 Water 5.341 14 in / 30 150.5 'F / 0 psi g RX01A 21 Steel 6.3849 Water 0.763 14 in / 30 150.5 'F / 0 psi g RX01B 21 Steel 20.748 Water 1.272 14 in / 30 150.5 'F / 0 psi g l

RX01C 21 Steel 83.5906 Water 3.24 14 in / 30 150.5 'F / 0 psi g i

RX01D 21 Steel 73.7917 Water 3.24 14 in / 30 150.5 'F / 0 psi g RX02A 21 Steel 12.3625 Water 4.454 16 in / 30 150.5 *F / 0 psi g RX028 21 Steel 12.3625 Water 4.207 16 in / 30 150.5 'F / 0 psi g RXO2C 35 Steel 102.769 Water 3.252 16 in / 80 150.5 'F / 0 psi g RXO2D 35 Steel 97.9537 Water 3.184 16 in / 80 150.5 'F / 0 psi g RXO1A 16 Steet 6.3849 Water 0.7645 14 in / 40 150.5 'F / 0 psi g J

Calc / No. V76100.NSP97.00601 ATTACHMENT /E Page 14l of M PlPE-FLO ver 5.01 pg 5

Ccmprny: Duks Enginnring & Strvicts 06/16/97 9:26 tm PrrjIct: SystIm: OVRPRES4 by:Jos:ph D. Spar:cina riv: 06/16/97 9:24 sm MATERIALS REPORT Created: 11/04/9611:56 am Pipes: 93 Design file: Nodes: 87 Pipe Specs: 5 Pumps / Comps: 6 NSP RHR and CS piping model, SP Temp.150.5'F. and 0 psig cont. press. Containment overpressure cales.

PIPE MATERIALS LIST PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft A 31 Steel 3.6777 1-Fixed K strainer 20 in / 60 1-Tee Flow Thru Branch 9 B 31 Steel 3.6777 1-Fixed K STRAINER 20 in / 60 C 31 Steel 3.6777 1-Fixed K STRAINER 20 in / 60 1-Tee Flow Thru Branch CDS1D 16 Steel 3.45 1-Elbow Short - r/d 1 @ 90' 10 in / 40 CDS7A 35 Steel 7.73835 1-Elbow Short - r/d 1 @ 90' 2 in / 80 1-Reducer Enlargement 2 X 2.5 CROSSTIE 21 Steel 49.0188 3-Elbow Short - r/d 1 @ 90' 14 in / 30 1 Tee Flow Thru Run 1-Reducer Contraction 16 X 14 1-Reducer Enlargement 14 X 16 2-Gate Wedge Disc CS001A 16 Steel 41.8129 4-Elbow Short - r/d 1 @ 90' 12 in / 40 1-Gate Wedge Disc 1-Gate Double Disc 1-Tee Flow Thru Run 1-Tee Flow Thru Branch CS001B 16 Steel 42.5259 1-Elbow Short - t/d 1 @ 90' 12 in / 40 1-Elbow Short - r/d 1 @ 45' 1 Tee Flow Thru Run 1-Gate Wedge Disc 1-Gate Double Disc 1-Tee Flow Thru Branch

)

1 CS003A 16 Steel 10.7215 3-Elbow Short - r/d 1 @ 90' l 12 in / 40 1-Fixed K vel coretn CS0038 16 Steel 27.109 1-Elbow Short - r/d 1 @ 90' 12 in / 40 4-Elbow Short - r/d 1 @ 45' 1 Fixed K vel coretn CSD1A 16 Steel 3.7973 1-Elbow Short - r/d 1 @ 90* I 10 in / 40 l l

Calc / No. V75100.NSP97.00501 ATTACHMENT E~ PageR of /M PIPE-FLO ver 5.01 p91

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PIPE MATERIALS LIST 06/16/97 9:26 am PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft CSD2A 16 Steet 108.553 1-Tee Flow Thru Run 10 in / 40 1 Swing Check Vertical 5-Ebow Short- r/d 1 @ 90' 8-Elbow Short - r/d 1 @ 45' 1-Fixed K Flow Element 1-Fixed K Res. Orifice CSD2B 16 Steel 108.723 4-Ebow Short- r/d 1 @ 90*

10in / 40 1-Swing Check Vertical 2-Elbow Short - r/d 1 @ 45' 1-Tee Flow Thru Run 1-Fixed K Res. Orifice 1 Fixed K Flow Element CSD3A 35 Steel 57.0055 3-Gate Wedge Disc 8 in / 80 1 Swing Check Angled 6-Elbow Short - r/d 1 @ 90' 1-Fixed K Spargers CSD3B 35 Steel 55.4392 3-Gate Wedge Disc 8 in / 80 1-Swing Check Angled 6-Elbow Short - r/d i @ 90' 1-Fixed K Sparger CSD4A 16 Steel 2.22525 1-Elbow Short - r/d 1 @ 45' 2.5 in / 40 1 Tee Flow Thru Branch 1-Reducer Contraction 2.5 X 2 CSD4B 16 Steel 2.7485 2-Elbow Short - r/d 1 @ 45' 2.5 in / 40 1 Tee Flow Thru Branch 1-Reducer Contraction 2.5 X 2 CSDSA 35 Steel 0.67045 1 Globe Valve 2 in / 80 1-Reducer Enlargement 2 X 2.5 CSDSB 35 Steel 2.0608 1-Globe Valve 2 in / 80 1-Reducer Enlargement 2 X 2.5 CSD6A 16 Steel 38.6803 1-Elbow Short - r/d 1 @ 45' 2.5 in / 40 2-Elbow Short - r/d 1 @ 90' 1-Reducer Contraction 2.5 X 2 1-Fixed K Orifice Min.

CSD6B 16 Steel 101.051 10-Elbow Short - r/d 1 @ 90' 2.5 in / 40 2-Elbow Short - r/d 1 @ 45' 1-Fixed K Orifice Min.

CSD78 16 Steel 97.3901 1-Reducer Contraction 10 X '8 10 in / 40 4-Elbow Short - r/d 1 @ 90' 1-Elbow Short - r/d 1 @ 45' Calc / No. V75100.NSP97.00601 ATTACHMENT 6 Page_/,,13 of /67 PIPE-FLO ver 5.01 pg 2

PIPE MATERIALS LIST 06/16/97 9:26 am PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft 1-Tee Flow Thru Run CSD8A 16 Steel 45.7585 6-Elbow Short - r/d 1 @ 90*

2.5 in / 40 1 Elbow Short- r/d 1 @ 45' CSD9A 16 Steel 75.8885 1-Reducer Contraction 10 X 8 10 in / 40 1-Tee Flow Thru Run 1 3-Elbow Short - r/d 1 @ 90' l l

D 31 Steel 3.6777 1-Fixed K strainer 20 in / 60 1 Tee Flow Thru Branch H1 26 Steel 52.2054 2-Fixed K 22.5 mitre 20 in / 20 H11 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 1-Tee Flow Thru Run 5

H12 31 Steel 1.9171 1-Fixed K enlargement i

20 h / 60 H2 26 Steel 24.1868 1-Fixed K 22.5 mitre 20 in / 20

H21 31 Steet 1.9171 1-Fixed K enlargement 20 in / 60 H22 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 H3 26 Steel 24.3777 1-Fixed K 22.5 mitre 20 in / 20 H31 31 Steel 1.4375 1-Fixed K enlargement 1 20 in / 60 1-Tee Flow Thru Run H32 31 Steel 1.9171 1-Fixed K contraction 20 in / 60 1-Tee Flow Thru Run H4a 26 Steel 31.4675 1-Fixed K 22.5 mitre 20 in / 20 H4a1 31 Steet 1.9171 1 Fixed K enlargement 20 in / 60 1-Tee Flow Thru Branch H4a2 31 Steet 1.725 1 Fixed K contraction 20 in / 60 H4b 26 Steel 45.6907 2-Fixed K 22.5 mitre 20 in / 20 H4bt 31 Steel 1.725 1 Fixed K enlargement Calc / No. V75100.NSP97.00501 ATTACHMENT d Page if/ of /.5.~T.

PIPE-FLO ver 5.01 pg 3

PIPE MATERIALS LIST 06/16/97 9:26 Em PAPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft 20 in / 60 1 Tee Flow Thru Run i

H4b2 31 Steel 1.725 1-Fixed K contraction 20 in / 60 H5 26 Steet 108.244 4-Fixed K 22.5 mitre 20 in / 20 HS1 31 Steel 1.9171 1 Tee Flow Thru Run 20 in / 60 1-Fixed K contraction H52 31 Steel 1.9171 1-Tee Flow Thru Branch 20 in / 60 1-Fixed K enlargement i

H6a 26 Steel 15.1777 1-Fixed K 22.5 mitre 20 in / 20 i

H6a1 31 Steel 1.725 1-Fixed K contraction 20 in / 60 l H6a2 31 Steel 1.9171 1-Fixed K enlargement 20 in / 60 l

H6b 26 Steel 61.7884 2-Fixed K 22.5 mitre l 20 in / 20 l

H6b1 31 Steel 1.725 1-Fixed K contraction j 20 in / 60 H6b2 31 Steel 1.725 1-Fixed K enlargement 20 in / 60 1 Tee Flow Thru Run H7 26 Steel 24.3777 1-Fixed K 22.5 mitre 20 in / 20 t

H71 31 Steet 1.9171 1-Tee Flow Thru Run !

20 in / 60 1-Fixed K contraction H72 31 Steel 1.725 1-Fixed K enlargement 20 in / 60 1-Tee Flow Thru Run H8 26 Steel 24.1868 1-Fixed K 22.5 mitre .

20 in / 20 !

H81 31 Steel 1.9171 1-Fixed K contraction i' 20 in / 60 H82 31 Steel 1.9171 1-Fixed K enlargement .

20 in / 60 '

i HP001 21 Steel 67.5027 1-Elbow Long - r/d 1.5 @ 22.5' 14 in / 30 2-Gate Wedge Disc 1-Swing Check Angled ,

3-Elbow Long - r/d 1.5 @ 90' l l

Calc / No. V75100.NSP97.00501 ATTACHMENT 1 Pagedof /@

PlPE-FLO ver 5.01 pg 4 I

- . . . . - - . . . . - . . ~ . _--..-. ---- ~._-.. . . - - - - ~ ~ - . . . - . - . . . .

PIPE MATERIALS LIST 06/16/97 9:26 cm PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS

, Size / Sch ft 1

1-Tee Flow Thru Run 1-Tee Flow Thru Branch

! 'HP002 21 Steel 9.3679 1-Ebow Short - r/d 1 @ 90' 14 in / 30 1 Gate Wedge Disc 1-Fixed K vel coretn t RC001 16 Steel 22.7965 1-Ebow Long - r/d 1.5 @ 67.5*

l' 6 in / 40 1-Ebow Long - r/d 1.5 @ 45' 1-Ebow Long - r/d 1.5 @ 90' 2-Gate Wedge Disc 1-Swing Check Angled j 2 Tee Flow Thru Branch

RC002 16 Steel 56.5179 1 Ebow Short- r/d 1 @ 90'

{ 6 in / 40 1-Fixed K vel coretn i

) RH001A 26 Steel 62.1357 2-Ebow Short - r/d 1 @ 90*

! 20 in / 20 1-Gate Wedge Disc j 1-Tee Flow Thru Branch 1-Elbow Short - r/d 1 @ 45' 1-Tee Flow Thru Branch RH001B 26 Steel 55.6198 1-Ebow Long - r/d 1.5 @ 90' l 20in / 20 1-Ebow Short- r/d 1 @ 90' l

, 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Ebow Short - r/d 1 @ 45' 1-Tee Flow Thru Branch 1

RH002A 26 Steel 5.75 1 Tee Flow Thru Branch 20 in120 RH002B 26 Steel 5.3671 1-Tee Flow Thru Branch 20 in / 20 l

i RH003A 26 Steel 7.1093 1-Tee Flow Thru Run 1 20 in / 20 RH003B 26 Steel 7.6671 1-Tee Flow Thru Branch 20 in / 20 I

+

i RH004A 21 Steet 14.758 1-Tee Flow Thru Branch 14 in / 30 1-Reducer Contraction 20 X 14 1-Gate Wedge Disc 2-Ebow Short - r/d i @ 90'

1-Fixed K vel coretn -j RH004B 21 Steel 14.95 1-Reducer Contraction 20 X 14

,. 14 in / 30 2-Ebow Short - r/d 1 @ 90' i' 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Fixed K vel coretn Calc / No. V75100.NSP97.00501 ATTACHMENT 1 Page./.jk>of df.7 PIPE-FLO ver 5.01 pg 5

I PIPE MATERIALS LIST 06/16/97 9:26 Em PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft i

RH005A 21 Steel 14.758 1-Reducer Contraction 20 X 14 14 in / 30 1-Gate Wedge Disc Elbow Short - r/d 1 @ 90*

1-Fixed K vel coretn RH005B 21 Steel 14.95 1-Reducer Contraction 20 X 14 j 14 in / 30 2-Elbow Short - r/d 1 @ 90*

1-Gate Wedge Disc 4 1-Fixed K vel coretn RH006A 16 Steel 1.15 1-Reducer Contraction 12 X 10 12 in / 40

RH0068 16 Steel 3.0671 1 Elbow Short - r/d 1 @ 90*

1 12 in /40 1-Reducer Contraction 12 X 10 RH006C 16 Steel 1.15 1-Reducer Contraction 12 X 10 j 12 in / 40 RH006D 16 Steel 3.06671 1-Elbow Short - r/d 1 @ 90*

12 in / 40 1-Reducer Contraction 12 X 10 RH006DA 16 Steel 20.7 3-Elbow Short - r/d 1 @ 90*

10 in / 40 1-Swing Check Vertical 1-Gate Wedge Disc 1-Reducer Enlargement 10 X 14 t

RH007A 16 Steel 17.6094 2-Elbow Short - r/d 1 @ 90*

10 in / 40 1-Elbow Long - r/d 1.5 @ 90*

1-Gate Wedge Disc 1-Tee Flow Thru Run i

1-Reducer Enlargement 10 X 12 1-Swing Check Angled RH007B 16 Steet 19.2625 2-Elbow Short - r/d 1 @ 90*

10 in / 40 1-Swing Check Vertical

' 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1-Reducer Enlargement 10 X 14 RH007C 16 Steel 19.7656 3-Elbow Short - r/d 1 @ 90*

10 in / 40 1-Gate Wedge Disc 1-Tee Flow Thru Branch 1 Swing Check Angled RH007D 21 Steel 4.025 1-Tee Flow Thru Run 2

14 in / 30 RH008A 21 Steet 11.7875 1-Elbow Short - r/d 1 @ 90*

14 in / 30 1-Tee Flow Thru Run Calc / No. V76100.NSP97.00601 ATTACHMENT _f_ Page 147of /6T PIPE-FLO ver 5.01 pg 6

PIPE MATERIALS LIST 06/16/97 9:26 am l

PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS Size / Sch ft l RH008B 21 Steel 2.875 1 Tee Flow Thru Run 14 in / 30 RHRHXA 21 Steel 28.4145 3-Elbow Short - r/d 1 @ 90*

14 in / 30 2-Gate Wedge Disc I 1-Tee Flow Thru Run 1-Fixed K RHR HX 4

~

RHRHXB 21 Steel 54.8343 3-Elbow Short - r/d 1 @ 90*

14 in / 30 2-Elbow Short - r/d 1 @ 45' 2-Gate Wedge Disc 1-Tee Flow Thru Branch i

1-Fixed K RHR HX RHXBYPSA 21 Steel 29.4849 1-Tee Flow Thru Branch 14 in / 30 3-Elbow Short - r/d 1 @ 90* l 1-Globe Valve t

(

RHXBYPSB 21 Steel 15.4172 1-Elbow Short

r/d 1 @ 90*

14 in / 30 1-Tee Flow Thru Branch 1-Globe Valve RX01A 21 Steel 6.3849 1 Tee Flow Thru Branch 14 in / 30 s

RX01B 21 - Steel 20.748 1 Elbow Short - r/d 1 @ 90* I 14 in / 30 1-Tee Flow Thru Run l

1-Tee FlowThru Branch I RX01C 21 Steel 83.5906 1-Tee Flow Thru Run 14 in / 30 3-Elbow Short - r/d 1 @ 90*

1-Tee Flow Thru Branch 1-Reducer Enlargement 14 X 16 1-Fixed K Flow Element RX01D 21 Steel 73.7917 1 Tee Flow Thru Run 14 in / 30 3-Elbow Short - r/d 1 @ 90*

1-Tee Flow Thru Branch 1-Reducer Enlargement 14 X 16 1-Fixed K Flow Element RXO2A 21 Steel 12.3625 1-Globe Valve 16 in / 30 1 Tee Flow Thru Run RXO2B 21 ' Steel 12.3625 1-Globe Valve 16 in / 30 RX02C 35 Steel 102.769 7-Elbow Short - r/d 1 @ 90*

16 in / 80 2-Gate Double Disc 1 Swing Check Angled 1-Reducer Enlargement 16 X 18 Calc / No. V75100.NSP97.00501 ATTACHMENT E Paged of M PIPE-FLO ver 5.01 Pg 7

l i

PIPE MATERIALS LIST 06/16/97 9:26 tm i

i PIPELINE SPEC MATERIAL LENGTH VALVES & FITTINGS

Size / Sch ft I

l RXO2D 35 Steel 97.9537 6-Elbow Short - r/d 1 @ 90*

I 16 in / 80 2-Gate Double Disc 1-Swing Check Angled 1-Elbow Short - r/d 1 @ 45' 1-Reducer Enlargement 16 X 18 RXO1A 16 Steel 6.3849 1-Tee Flow Thru Branch ,

14 in / 40 l

I 1

1 i

l 1

i I

l l

i I

1 Calc / No. V75100.NSP97.00501 ATTACHMENT E page.H9 of E PIPE-FLO ver 5.01 pg 8

PIPE

SUMMARY

06/16/97 9.26 gm o PIPE MATERIAL SCHEDULE SIZE LENGTH Steel 20 20 in 555.352 ft Steel 30 14 in 516.659 ft 16 in 24.725 ft Steel 40 2.5 in 190.464 ft 6 in 79.3144 ft 10 in 475.139 ft 12 in 130.603 ft 14 in 6.3849 ft Steel 60 20 in 51.2285 ft Steel 80 2 in 10.4696 ft 8 in 112.445 ft 16 in 200.723 ft VALVE & FITTING

SUMMARY

SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS 16 LB30 Steel 40 Size: 2.5 in 7-Elbow Short - t/d 1 @ 45' 2-Tee Flow Thru Branch 3-Reducer Contraction 2.5 X 2 18-Elbow Short - r/d 1 @ 90' 2-Fixed K Orifice Min.

Size: 6 in 1-Elbow Long - r/d 1.5 @ 67.5' 1-Elbow Long - r/d 1.5 @ 45' 1-Elbow Lwg - r/d 1.5 @ 90' 2-Gate Wed.1e Disc 1-Swing Check Angbd 2-Tee Fiowitw 3 ranch 1-Elbow Short >!d 1 @ 90*

1-Fixed K vel:oretn Size: 10 in 28-Elbow Short - r/d 1 @ 90' 5-Tee Flow Thru Run 4-Swing Check Vertical 11-Elbow Short - t/d 1 @ 45' 2-Fixed K Flow Element 2-Fixed K Res. Orifice 2-Reducer Contraction 10 X 8 4-Gate Wedge Dise Calc / No. V75100.NSP97.00501 ATTACHMENT E Page lfre of d'f PIPE-FLO ver 5.01 -

pg 9

VALVE & FITTING

SUMMARY

06/16/97 9:26 am

SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS I

Size: 10 in 2-Reducer Enlargemerit 10 X 14 1-Elbow Long - r/d 1.5 @ 90' 1 Reducer Enlargement 10 X 12 l 2-Swing Check Angled 2-Tee Flow Thru Branch Size: 12 in 11-Elbow Short - r/d 1 @ 90' 2-Gate Wedge Disc 2-Gate Double Disc 2-Tee Flow Thru Run 2-Tee Flow Thru Branch 5-Elbow Short - r/d 1 @ 45' 2-Fixed K vel corr'.n 4-Reducer Cont action 12 X 10 Size: 14 in 1-Tee Flow Thru Branch

,?1 LB31 Steel 30 Size: 14 in 30-Elbow Short - r/d 1 @ 90*

9-Tee Flow Thru Run 1-Reducer Contraction 16 X 14 3 Reducer Enlargement 14 X 16 13-Gate Wedge Disc 1-Elbow Long - r/d 1.5 @ 22.5*

1-Swing Check Angled 3-Elbow Long - r/d 1.5 @ 90' 10-Tee Flow Thru Branch 5-Fixed K vel coretn 4-Redacer Contraction 20 X 14 2-Fixed K RHR HX 2-Elbow Short - r/d 1 @ 45' 2-Globe Valve 2-Fixed K Flow Element We: 16 in 2-Globe Valve 1-Tee Flow Thru Run 26 LB32 Steel 20 Size: 20 in 16-Fixed K 22.5 mitre 3-Elbow Short - r/d 1 @ 90' 2-Gate Wedge Disc 7-Tee Flow Thru Branch 2-Elbow Short - r/d 1 @ 45' 1-Elbow Lono - r/d 1.5 @ 90' Calc / No. V75100.NSP97.00501 ATTACHMENT E Page.]$]. of M PIPE-FLO ver 5.01 pg 10

! ~ VALVE & FITTING

SUMMARY

06/16/97 9:26 am SPECIFICATION MATERIAL SCHEDULE VALVES & FITTINGS Size: 20 in 1-Tee Flow Thru Run j 31 LB34 Stee! 60 Size: 20 in 2-Fixed K strainer 5-Tee Flow Thru Branch 2-Fixed K STRAINER 10-Fixed K contraction 8-Tee Flow Thru Run 10-Fixed K enlargement 35 LB34a Steel 80 Size: 2 in 1-Elbow Short - r/d 1 @ 90*

3-Reducer Enlargement 2 X 2.5 2-Globe Valve Size: 8 in 6-Gate Wedge Disc 2-Swing Check Angled 12-Elbow Short - r/d 1 @ 90' 1-Fixed K Spargers 1-Fixed K Sparger Size: 16 in 13-Elbow Short - r/d 1 @ 90' 4-Gate Double Disc 2-Swing Check Angled 2-Reducer Enlargement 16 X 18 1-Elbow Short - r/d 1 @ 45' Calc / No. V75100.NSP97.00501 ATTACHMENT f Page,.[fd of g PIPE-FLO ver 5.01 pg 11

. = _ . _ . - . . - . . . . . . -- --- ._ . - - .- -. _.. . _ . . .-.

Comptny: Duka Enginatring & Stryicss 06/16/97 9.34 am

, Projtet: Lintup: CASE 4 1

by: Jos::ph D. Spiracino rsv 06/16/97 9:34 cm i

System: OVRPRES4 Deviation: 7.98e-005 %

rey: 06/16/97 9:24 am after: 9 iterations long term,4 RHR 8000gpm per division, A&B CS 2800gpm, O cont press., A strnr plugged, sp wtr M 908'-9.3 Volumetric flow rates require constant fluid properties in all pipelines. Fluid properties in the first specification were used in this calculation.

LINEUP SUMMARIES ,

PIPELINE FLOW PRESSURE SET LEVEL gpm SOURCE psig ft

{

CSD3A >>> 2800 ACSD3 0 0 CSD8A >>> 234.7 ACSD8 0 0 CSD3B >>> 2800 BCSD3 0 0

CSD6B >>> 228.2 BCSD6 0 0 RXO2D >>> 16000 RECIRC2 0 0 B <<< 8172 TB 0 4.459 C <<< 5397 TC 0 4.469 l D <<< 8494 TD 0 4.459

Flows IN: 22063 gpm Flows OUT: 22063 gpm

. NET FLOWS: 0 gpm l Calc / No. V75100.NSP97.00501 ATTACHMENT E Paged of M PlPE-FLO ver 5.01 pg 1

- . . . - . -. .- - - .. - -- . .~ .- . _. .. _

LINEUP NODES 06/16/97 9:34 am NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi g ft 1 90225 1.503 905.8 l 10 90225 2.455 908 11 902.25 2.443 908 a 12 902.25 2.431 908 13 902.25 2.367 907.8 j 14 902.25 2.251 907.6 15 902.25 2.038 907 16 902.25 1.997 907 17 902.25 1.971 906.9 )

$ 18 90225 1.913 906.8

. 19 90225 1.619 906.1 2 902.25 1.467 905.7

. 20 902.25 1.574 906 3 902.25 1.503 , 905.8 4 4 902.25 1.549 905.9

5 902.25 1.584 906 4

6 902.25

636

. 906.1 7 902.25 1.84 906.6 8 902.25 1.979 906.9 9 902.25 2.107 9072 A.CS.lN 902.25 2.026 907 A.CS.SUQT 897.833 1.511 901.4 A.CS.T 899.916 1.589 903.7 A. DIS 897.833 148.7 1248 A.!N 897.583 1.955 902.2 A.RH.IN 902.25 1.577 906 A.RH.T 897.583 2.201 902.8 A.SUC 897.833 0.688 899.5 ACSD2 931.917 75.4 1109 ACSD3 981.188 0(source) 981.2 ACSD4 900.156 312.1 "* 1635 ACSD5 900.74 282.9 '" 1567 ACSD6 925.875 17.44 966.9 ACSD7 928 10.43 952.6 ACSD8 927 0 (source) 927 ACSD9 971.25 56.29 1104 ACSDSCG 899.635 315.3 *" 1642 ADISTEE 901.083 142.4 1236 B.CS.lN 902.25 1.624 906.1 B.CS.SUCT 897.833 1.177 900.6 B.CS.T 090.000 1.490 9034 Calc / No. V75100.NSP97.00501 ATTACHMENT 6 Pagedof /f9 PIPE-FLO ver 5.01 pg 2

.- . , .. . . ~ _ . - . . . - _ . ~ ~ . . - . . - . - . - - . - . - . - . . . . - - . ~ . . - . . . . . . ...~.

LINEUP NODES 06/16/97 9:34 am NODE. ELEVATION DEMAND PRESSURE. H GRADE R gpm pd g A B. DIS 899.5 147.9 1248 B.IN 897.583 1.754 901.7

' B.RH.lN 902.25 1.462 905.7 B.RH.T 897.583 2.149 902.6 B.SUC 897.833 0.047 897.9 BCSD2 927.833 77.41 1110 BCSD3 980.38 0 (source) 980.4

'BCSO4 899.896 295 "* 1595 BCSD5 901.688 266.3 "* 1529 BCSD6 930.333 0 (source) 930.3 BCSD7 978.5 52.78 1103 BCSDSCG 899.583 298.5 *" .-1603 BDISTEE 908 139.7 1237 C. DIS. 897.833 149.8' 1251 C.lN 897.583 2.051 902.4 C.SUC 897.833 0.327 898.6 D. DIS 899.5 147.2 1246 D.DISA 908 139.9 1237 D.IN 897.583 1.657 901.5 D.SUC 897.833 0.376 898.7.

HP.IN 902.25 1.965 906.9 HP.T 901.615 2.234 906.9 M02013 940.91 33.03 1019 MO2012 940.917 60.13 1083 RC.lN 902.25 2.355 907.8 RC.T 902.25 2.355 907.8 RECIRC2 951.75 0 (source) 951.8 PECIRCA 930.168 64.7 1083 (ECIRCB 930.167 60.16 1072

, RHRHXDA 916.333 82.16 1110 RHRHXDB 915.49 79.27 1102 RHRHXDC 916.336 80.24 1105 RHRHXDD 921.33 73.32 1094.

RHRHXS1 - 909.406 88.53 1118 RHRHXS2 908 85.99 1110 SA 902.25 1.506 905.8 l- SB 902.25 2.463 908.1 SC 902.25 2.439 908 SD 902.25 1.94 906.8

[ TB 904.316 1.894 (source) 908.8 TC $0.;.316 1.000 (ewee) 000.0

~ Calc / No. V76100.NSP97.00501 ATTACHMENT 1 Pagegof /j,9 l- PIPE-FLO ver 5.0i pg 3 l

l_,. _ . _ . _ . , _

,. . . = _ . . . . . _ . . . _ . -. ._ __ _ _ _ _ . _ . . . . _ . _ _ _ . _ . _ . . _ _ _ . . _ _ _

LINEUP NODES 06/16/97 9:34 Gm i NODE ELEVATION DEMAND PRESSURE H GRADE n gpm pd g n TD 904.316 1.894 (source) 908.8 1

l i l 1 l

l l

1 i

Calc / No. V75100.NSP97.00501 ATTACHMENT E Paged of M PIPE-FLO ver 5.01 pg 4

LINEUP PIPELINES 06/16/97 9:34 am l

l PIPELINE FROM TO FLOW VEL dP HL l gpm ft/sec psi g ft A TA SA closed 0 0 0 B TB SB 8172 9.894 (0.570) 0.724 l C TC SC 5397 6.534 (0.542) 0.791 CDS1B B.CS.SUCT ECSDSCG 3028

12.33 (297.4) (702)

- BCS - dP:(298.4) HL:(702.8)

CDS7A ACSD6 ACSD7 234.7

25.53 7.012 14.39 l

CROSSTIE RECIRCA <-> RECIRCB 8000

18.63 4.536 10.68 CS001A A.CS.lN A.CS.T 3035 8.706 0.438 3.364 CS001B B.CS.IN B.CS.T 3028 8.687 0.130 2.671 CS003A A.CS.T A.CS.SUCT 3035 8.706 0.077 2.265 CS003B B.CS.T B.CS.SUCT 3028 8.687 0.318 2.8 CSD1A A.CS.SUC7 ACSDSCG 3035

12.36 (313.8) (740.8)

- A.CS - dP: (314.9) HL: (741.6)

CSD2A ACSDSCG ACSD2 2800 11.4 67.16 125.9 -

- FCV@2800 - dP: 172.8 HL: 406.9 CSD2B BCSDSCG BCSD2 2800 11.4 64.21 123 I

- FCV@2800 - dP: 156.9 HL: 369.5 CSD3A ACSD9 ACSD3 2800

Ili.69 56.29 122.6 CSD3B BCSD7 BCSD3 2800

19.69 52.78 122.4 CSD4A ACSDSCG ACSD4 234.7

15.74 3.271 7.182 CSD4B BCSDSCG BCSD4 228.2 *15.3 3.5 7.929 CSDSA ACSD4 ACSD5 234.7

25.53 29.16 68.09 CSD5B BCSD4 BCSDS 228.2

24.81 28.78 65.97 CSD6A ACSDS ACSD6 234.7

15.74 265.5 600 CSD6B BCSDS BCSD6 228.2 *15.3 266.3 598.4 CSD78 BCSD2 BCSD7 2800 11.4 24.63 7.328 CSD6A ACSD7 ACSD8 234.7

15.74 10.43 25.56 CSD9A ACSD2 ACSD9 2800 11.4 19.11 5.661 D TD SD 8494 10.28 (0.046) 1.957 H1 20 <-> 1 3946 4.354 9.071 0.167 H11 1 <-> B.RH.IN 3946 4.776 0.041 0.096 H12 A.RH.tN <-> 20 3946 4.778 0.003 0.007 H2 3 2 4054 4.472 0.035 0.083 H21 SA 3 4054 4.908 0.003 0.007 H22 2 B.RH.1N 4054 4.908 0.005 0.012 H3 5 4 4054 4.472 0.035 0.084 H31 B.CS.IN 5 4054 4.908 0.040 0.095 H32 4 SA 4054 4.908 0.043 0.101 H4s 9 8 7082 7.813 0.128 0.302 H4s1 SB 9 7082 8.574 0.356 0.839 H412 8 HP.lN 7082 8.574 0.014 0.033 H4b 7 6 7082 7.813 0.202 0.475 Calc / No. V75100.NSP97.00501 ATTACHMENT 6 PageRofd PIPE-FLO ver 5.01 pg 5

1 LINEUP PIPELINES 06/16/97 9:34 cm PIPELINE FROM TO FLOW VEL dP HL ,

gpm ft/see psi g ft j H4bi HP.!N 7 7082 8.574 0.124 0.293 H4b2 6 B.CS.IN 7082 8.574 0.014 0.033 HS 10 11 1090 1.203 0.012 0.029 i

H51 11 SC 1090 1.32 0.003 0.007 .

1 H52 SB 10 1090 1.32 0.008 0.020 l H60 12 13 6487 7.157 0.065 0.152 H601 13 RC.IN 6487 7.854 0.012 0.028 H602 SC 12 6487 7.854 0.008 0.019 H6b 14 15 6487 7.157 0.213 0.501 H6bi 15 A.CS.lN 6487 7.854 0.012 0.028 H6b2 RC.lN 14 6487 7.854 0.104 0.246 H7 16 17 3452 3.809 0.026 0.061 H71 17 SD 3452 4.179 0.031 0.073 H72 A.CS.lN 16 3452 4.179 0.030 0.070 H6 18 19 11946

13.18 0.295 0.694 H81 19 A.RH.IN 11946

14.46 0.042 0.098 H82 SD 18 11946

14.46 0.026 0.062 HP001 HP.IN HP.T 0 0 (0.270) O HP002 HP.T HP.SUCT closed 0 0 0 l RC001 RC.lN RC.T 0 0 0 0 RC002 RC.T RC.SUCT closed 0 0 0 RH001A A.RH.lN A.RH.T 8000 8.826 (0.624) 3.196 RH001B B.RH.IN B.RH.T 8000 8.826 (0.687) 3.049 RH002A C.IN A.lN 3985 4.396 0.096 0.227 RH002B B.lN D.IN 4007 4.421 0.097 0.229 RH003A A.RH.T C.lN 8000 8.826 0.150 0.353 RH003B B.RH.T B.lN 8000 8.826 0.395 0.930 RH004A C.IN C.SUC 4015 9.351 1.724 3.81 RH004B B.IN B.SUC 3993 9.297 1.707 3.77 RH005A A.IN A.SUC 3985 9.279 1.267 2.733 RH005B D.IN D.SUC 4007 9.332 1.281 2.767 RH006A A.SUC A. DIS 3985 11.43 (148) (348.5)

- ARHR - dP: (148.3) HL: (349.2)

RH006B B.SUC B. DIS 3993 11.45 (147.8) (349.8)

- BRHR - dP: (149.1) HL: (3C1)

RH006C C.SUC C. DIS 4015 11.52 (149.4) (351.9)

- CRHR - dP: (149.7) HL:(352.5)

RH006D D.SUC D. DIS 4007 11.5 (146.8) (347.4)

- DRHR - dP: (148.1) HL: (348.6)

RH006DA D. DIS D.DISA 4007

16.32 7.301 8.692 RH007A A. DIS ADISTEE 3985

16.22 6.283 11.54 RH007B B. DIS BDISTEE 3993

16.26 8.169 10.74 Calc / No. V75100 NSP97.00501 ATTACHMENT 6 Page_f@of /$

PIPE-FLO ver 5.01 pg 6

. _ . . _ .. _ _ . . _ . . . . _ _ . _ _ _ . . . . . . _ . . . _ _ _ _ _ . _ __ _ _ . . . _ _ - _ . . _ - .m.._

l LINEUP PIPELINES 06/16/97 9:34 am l

PIPELINE FROM TO FLOW VEL dP HL gpm ft/sec psi g ft RH007C C. DIS ADISTEE 4015

16.35 7.357 14.08 RH0070 D.DISA BDISTEE 4007 9.332 0.174 0.410 RH008A ADISTEE RHRHXS1 8000

18.63 5.017 3.491

- FCV@8000 - dP: 48.86 HL: 115.1 RH0088 BDISTEE RHRHXS2 8000 *18.63 0.659 1.553

-FCV@8000-dP: 53.07 HL: 125 RHRHXA RHRHXS1 RHRHXDA 4071 9.481 6.365 8.06 RHRHXS RHRHXS2 RHRHXDB 3767 8.771 6.72 8.334 RHXBYPSA RHRHXS1 RHRHXDA 3929 9.149 6.365 8.06 RHXBYPSB RHRHXS2 RHRHXDB 4233 9.858 6.72 8.334 RX01A RHRHXDA RHRHXDC 8000 *18.63 1.919 4.515 RX01B RHRHXDB RHRHXDD 8000

18.63 5.951 8.173 RX01C RHRHXDC RECIRCA 8000

18.63 15.55 22.78 RX01D RHRHXDD RECIRCB 8000 *18.63 13.16 22.15 RX02A RECIRCA MO2012 0 0 4.565 0 RXO2B '1ECIRCB M02013 16000

28.13 27.13 53.14 RXO2C MO2012 RECIRC1 closed 0 0 0 RXO2D M02013 RECIRC2 16000

31.93 33.03 66.94 Calc / No. V75100.NSP97.00501 ATTACHMENT _,E_ Page.,,/12 of M PIPE-FLO ver 5.01 pg 7

iL ATTACHMENT - 2

CA-97-166 CORRECTED CONTAINMENT P_RESS_URE REO.UIRED for NPSH for.COR_E SPRAY.

PUMPS UNDER,RUN_O_UT CO_N.DITION. ,

Time (sec) Req'd Cont. _ Specific. . , Corrected -

fress. (psig), Weight (Ib/ft3) Press. (psig)

Po SW Pc 86.3 .

2.3539 61.5195 -0.2094 86.3 2.6234 61.5195 0.0601 148.8 -, 2.7457.-.- 61.4119 - 0.1869

~ ' ~ ~ ~

~~-. 215.2..-. . 3.5_5~28. -. . 6.i.5459 ' 7 ~ 57s5i.~.~..

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. 337.:2_ , 3.5572 61.283_9 _ _1.0037 399.7 ~ 3.3926 61.2482 i

~

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~

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~~462.2~ ~ ' 3.7583 61.2389 1.2067 524I7 3.551i' ~ ~ ' ~63.s239

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Page 1 of 1 ;

_s-

GS-10-97 15:35 ID= P 01 t

Tcinfax SULZER PUMP 5 DMston of Stizer Reteq Sulzer Bingham Pumpa Inc.

Field Engineering !

, Kenny Thomson Manager 2800 N.W. Front Avenue Portland, OR 97210-1502 Date: 18 June,1997 U.S.A.

To: Dave Pennington Tet (503)226-6243 NORTHERN STATES POWER Fax (503) 226-5383 Monticello Nuclear Power Plant Fax: 612-295-1017 Phone: 612-295 1354 l 1

Pages: T.(inc!uding this one)

Subject:

NPSH of Sutzer Bingham Pumps S/N 270417/418 Core Spray Pumps 10 x 12 x 14.5 CVDS i' G"- O - itA Lt.

Dear Dave:

'I We hope to send out report by June 23,1997. HowevelIn the Interim period, we confinn that the NPSH test on 270417 (Monticello: 10 x 12 x 14.5 CVDS) is identical to 270425 (Quad City 12 x 14 x 14.5 CVDS) between the 4000 to 5300 GPM flow range. Attached is SBPI curve #26895. .

Regards, ,

l h% % l Kenny Thomson J i

na ,

cc: D. Eddy - Hydraulles T. Pjchlield - Field Services I Psoe 1/1 kennyltartctavapen.15.04.97.14:52

i Exhibit F i

l Monticello Nuclear Generating Plant l

l Revision No. 2 to License Amendment Reauest Dated January 23.1997 l

" Torus Attached Pioina Evaluation." Monticello Nuclear Generatina Plant. Revised June.1997 Torus attached piping has been conservatively analyzed for 195*F by Duke Engineering and Services. The results of this analysis are summarized below.

Ac_gert3nce Criteria In accordance with Section 12.2.2.12.2 of the Updated Safety Analysis Report (USAR),

Torus attached piping is analyzed to withstand loss of coolant accident (LOCA) related loads and safety relief valve (SRV) discharge-related loads postulated to occur during a LOCA or a SRV discharge event defined by Nuclear Regulatory Commission (NRC)

Safety Evaluation Report NUREG-0661. NUREG-0661 requires compliance with the American Society of Mechanical Engineers (ASME) Code, Section Ill,1977 Edition, Summer 1977 Addenda, to evaluate the acceptability of torus attached piping designs.

Analvsis Assumotions Torus attached piping was previously analyzed for a peak suppression pool temperature of 184 'F in March,1995, following an update of the Monticello design basis accident containment pressure and temperature response analysis reported in NEDO-32418.

General Electric has reanalyzed the LOCA containment pressure and temperature response for Monticello in a more conservative manner at a reactor power level of 1880 Mwt. The results of this analysis are contained in Report GE-NE-T2300731-2,

'Monticello Nuclear Generating Plant LOCA Containment Analysis for Use in Evaluation of NPSH for the RHR and Core Spray Pumps," June,1997. Worst case suppression pool temperature increases in this analysis to 194.2 F with RHRSW temperature at the upper limit of 90 *F specified in Section 6.2.3.2.4.c of the USAR.

For conservatism, the piping was reanalyzed for a suppression pool temperature of 195

F.

Methodoloav The postulated Mark I containment hydrodynamic loads for operation at 1880 MWt do not change since there is no change in reactor operating pressure. There will be no increase in piping stresses, support loads, and stresses in the torus penetrations.

F-1

l The SRV discharge line dynamic loads are influenced by parameters such as SRV discharge line geometry, torus geometry, water leg length, and SRV flow rate which is linearly proportional to the SRV opening pressure.

The SRV opening setpoint pressures will not be changed since the reactor pressure !

remains unchanged. Therefore, the SRV discharge dynamic loads will remain within the original SRV load definition. There will be no increase in piping stresses, support loads and stresses in the torus penetrations due to the SRV discharge line dynamic loads '

Torus attached piping was designed for the suppression pool design pressure of 56 psig.

The suppression pool pressure under rerate conditions will still be bounded by the current suppression pool design pressure.

Based on the above, it is concluded that the impact of power rerate on torus attached piping will be limited to the impact of higher peak suppression pool temperature. The )

affected torus attached lines which require evaluation include large bore and small bore lines of the following systems, o SRV Discharge Lines o Residual Heat Removal o Reactor Core isolation Cooling offgas line (steam side) o Primary Containment & Atmospheric Control o Core Spray o High Pressure Coolant Injection (water side) o Reactor Core Isolation Cooling (water side) o Primary Containment Nitrogen Control o Miscellaneous torus attached piping (instrument lines, construction drains, and cantilevered lines)

Resula The torus attached piping has been evaluated for the peak suppression pool temperature of 195 *F and concurrent Mark I containment hydrodynamic loads.

Evaluations concluded that all pipe stresses, pipe supports, and torus penetrations are in compliance with the requirements of NUREG-0661 and the ASME Code.

This evaluation is conservative since Mark I containment hydrodynamic loads will terminate before the design peak suppression pool temperature of 195 *F is reached.

Termination of DBA Mark I containment hydrodynamic loads will occur at a suppression pool temperature of about 134 F for the design basis loss of coolant accident and 170 F for the small break loss of coolant accident ,

l 1

i l

F-2 i i

No physical changes to piping or associated supports is required to support this change in design temperature.

The detailed torus attached piping calculations are currently being transferred from the contractor to the site. They will be available on site for inspection.

F-3 l

4 Exhibit G Monticello Nuclear Generating Plant

! Revision No. 2 to License Amendment Reauest Dated January 23.1997 ,

l

" Evaluation of RHR Room Temperature Durina DBA LOCA." Monticello Nuclear .

Generatina Plant. Revised June.1997 Maximum RHR room temperature under long-term design basis acciou it loss of coolant accident (LOCA) conditions was determined in Calculations CA-96-113, CA-97-074, and CA-97-157. The results of these calculations are summarized below.

Acceotance Criteria Maximum long-term ambient temperature in the Residual Heat Removal (RHR) pump rooms is specified as 140 F in Section 6.2.2.2.1 of the Updated Safety Analysis Report (USAR).

Analvsis Assumotions Calculations were performed for three scenarios:

Case 1 - One RHR pump and one RHR service water (RHRSW) pump are running in suppression pool cooling mode. One Core Spray pump is running for reactor makeup. Suporession cool temperature is maximized at 194.2 F. This is the peak long-term suppression pool temperature at a conservative bounding reactor operating power level of 1880 MWt. RHRSW (Mississippi River) temperature was assumed to be at the maximum analyzed value of 90 'F for the entire period.

Case 2 - Two RHR pumps and two RHRSW pumps are running in suppression pool cooling mode. One Core Spray pump is running for reactor makeup. Heat added to the RHR room from motor losses is maximized. Peak suppression pool temperature is 178.9

'F for this combination of RHR and RHRSW pumps. RHRSW temperature was assumed to be at the maximum analyzed value of 90 *F for the entire period.

Case 3 - Same as Case #2 except RHRSW temperature was assumed to be 89 *F for the entire period.

Summer time steady state room temperatures were assumed before the LOCA.

G-1

- . - .. - _ - . .-=. - . - .- --- .- - .- . -.. .

T l

l At the time the LOCA is initiated, loss of all normal air conditioning and ventilation is assumed.

4 l Ground water temperature was determined to be 48 F for purposes of this analysis.

a

3. All sources of heat input to the room were modeled. Significant sources included:

i . Core Spray and RHR piping

. RHR Heat Exchanger

. . Electrical cables, lighting, and misc electrical loads I

. Core Spray and RHR pump motors Heat input to the room from the core spray and RHR pump motors was conservatively assumed to be based on rated pump brake horsepower of 800 HP for core spray and 600 HP for RHR. Actual motor loads would be expected to be substantially less than this.

Concrete and steel heat sinks were conservatively modeled. Heat removal by room coolers and heat transfer to the building structure and adjacent soil and ground water was conservatively modeled.

While both A and 8 pump rooms are similar, RHR pump room B was chosen for modeling. Because of the layout of the plant, RHR pump room B requires longer pipe runs for cooling water. Tests have shown that the A pump room receives approximately 30% more cooling water flow.

i Methodoloav I

A lumped parameter model was used to calculate the average bulk air temperature in the RHR pump room following initiation of the LOCA and loss of normal ventilation and air conditioning equipment. If possible, the computation was carried on long enough .

until room temperature peaks and begins trending down with time. Equations were i formulated on a Lotus 123 spreadsheet.

Maximum RHRSW temperature was assumed for piping temperature upstream of heat exchangers. Classic heat exchanger formulas were used for temperature of piping downstream of heat exchangers. ,

Convective surface to air and radiation surface to surface heat transfer was modeled for all significant heat transfer surfaces. For conservatism, all nominal convective heat transfer coefficients were reduced by 25% . The extra dampening capacity of steel and reinforcing bar buried in concrete walls was conservatively ignored.

G-2

Results

, The maximum RHR pump room temperatures during a design basis LOCA were determined to d

be:

Case: Assumptions Maximum RHR

, Pump Room

. Ternperature ( F) j 1 Suppression Pool 130.84 Temperature Maximized With RHRSW at 90 F 2 Heat Added to RHR Pump 140*

Room From Motor Losses Maximized With RHRSW at 90 F i 3 Heat Added to RHR Pump 139.86**

j Room From Motor Losses Maximized With RHRSW at 89 F RHR room temperature at 25.7 hours8.101852e-5 days <br />0.00194 hours <br />1.157407e-5 weeks <br />2.6635e-6 months <br /> after the beginning of the accident. Only

one RHR pump and one core spray pump would be running at this point in the accident since this is well after the time of the peak suppression pool temperature for this scenario.

- 8 RHR room temperature at 10 seconds (about 11.5 days) after the beginning of I the accident. Only one RHR pump would be running at this point in the accident.

j 1

Details of the RHR pump room heatup calculations are available on site for inspection.

4 i

G-3

f Exhibit H Monticello Nuclear Generating Plant l l

Evaluation of Environmental Oualification Boundina Conditions." Monticello Nuclear Generatina Plant. June.1997 Equipment required to be environmentally qualified per 10CFR50.49 are qualified to the worst case bounding conditions. The bounding accident temperature conditions in the drywell used for Environmental Qualification is based on the small break accident. The bounding accident pressure conditions in the drywell occur during the DBA LOCA. The humidity for accident scenarios is assumed to be 100% at the start of the accident. The Monticello Environmental Qualification central file references General Electric report AE-083-0983, " Extended Drywell Temperature Analysis", as containing the drywell accident enveloping temperatures. The central file references General Electric report NEDO-30485,"Monticello Design Basis Accident l Containment Pressure and Temperature Response for FSAR Update," as containing the '

bounding drywell accident pressure profile General Electric report NEDO-30477," Safety Analysis of the RHR Intertie Line Monticello Nuclear Generating Plant" analyzed for the peak short-term (30 second) containment response. This analysis reported a peak drywell pressure of 42.3 psig at 1.2 seconds. The environmentally qualified equipment inside containment was verified to be qualified to the peak drywell pressure of 42.3 psig. The postulated normal and post accident containment radiation doses will remain unchanged. Normal radiation dose assumes no accident and post accident radiation dose assumes core damage.

The bounding conditions used for environmental qualification,42.3 psig and 335 F, will not be changed by the reanalysis of long term suppression pool temperature.

RATED DBA-LOCA SHORT-TERM SBA-LOCA POWER LEVEL DRYWELL PEAK LOCA DRYWELL PEAK TEMP DW PRESS PEAK TEMP 1670 MW 282 F

42.3 PSIG 335 F

Evaluations completed at 102% of the rated power level.

Note 1- From NEDO - 30485, Table 1; Code HXSlZ with May-Witt decay heat.

Note 2 - From NEDO - 30477, Table 3-3 : S: -

ICPT with May-Witt dc ay heat.

Note 3 - From AE-083-0983, Table ', ' HEX with May-W' ay heat.

H-4

References

1) General Electric report AE-083-0983, " Extended Drywell Temperature Analysis", Dated:

October 1983.

2) General Electric report NEDO-30485, "Monticello Design Basis Accident Containment Pressure and Temperature Response for FSAR Update", Dated: December,1983.

3) General Electric report NEDO-30477, " Safety Analysis of the RHR Intertie Line Monticello Nuclear Generating Plant" Dated: June 1984.

i H-2

\

i J

l l

Exhibit I ;

1 Monticello Nuclear Generating Plant I Revision No. 2 to License Amendment Reauest Dated January 23.1997 l

Response to NRC Reauest for Additional Information (RAI) dated March 12.1997 I

1. Which Code is used in the decay heat analyses? Was this code used in the previous analyses? If not, then justify its use. !

2. List and justify the changes in input parameters used in the ANS 5.1 versus those used

- previously in the May Witt Analyses.

3. Provide and justify the values for the following ANS 5.1 input parameters:

1. O (total recoverable energy) = (MeV/ fission)

2. SO (net recoverable energy) = (MeV/ fission)

3. P (total power from fissioning of one nuclide) = (MeV/sec)

4. SP (new power from fissioning of nuclide) = (MeV/sec)

)

5. Fractional fission product power for: U235, U238, Pu239, and Pu241 )

6. R-factor (the actinide production multiplier) l

7. G-factor (a decay heat multiplier to account for the effect of neutron 1 capture in fission products)

8. Si (a multiplier applied to the G-factor equation i

4. Provide the value used for estimating the length of time of full power operation before I shutdown.

5. Justify that your use of the ANS 5.1 analyses is conservative by showing that at least two standard deviations of confidence in your analyses results is provided.

6. Were the contributions to the decay heat from U-239 and Np-239 calculated in accordance with Branch Technical Position ASB 9-2? If not, provide the equation used to calculate them.

Resoonse

1. The ANS 5.1-1979 decay heat model, with no adders, was used by General Electric in the containment pressure and temperature analysis originally submitted by NSP on January 23, 1997. Previous analyses used the May-Witt decay heat model.

A new analysis has been completed by Genera! Electric which includes the appropriate baseline and benchmark analyses for the new computer codes and decay heat model used.

The reanalysis is contained in General Electric Report GE-NE-T2300731-2, "Monticello Nuclear I1

I J

Generating Plant LOCA Containment Analysis for Use in Evaluation of NPSH for the RHR and l Core Spray Pumps," June,1997. This report is included as Exhibit D.

! Refer to Exhibit D. l 1

l 2 - 6. In response to NRC concerns related to the sensitivity of ANS 5.1-1979 to input j parameters and the confidence level of the results, the containment pressure and temperature analysis has been revised. The analysis was performed at a power level of 1880 Mwt to provide i assurance that the results are conservative with respect to selection of input parameters and confidence level. Refer to Exhibit D.

This approach was discussed with the NRC Staff during a telephone conference call on May 22, 1997. The analysis performed at 1880 Mwt bounds an analysis performed at the current license i power level of 1670 Mwt plus two sigma.

l i

I I I i

E i l

l l-2

(

Exhibit J Monticello Nuclear Generating Plant Revision No. 2 to License Amendment Reauest Dated Januarv 23.1997 Response to NRC Reauest for Additional Information dated May 13.1997 i

1. Please specify the amount of containment overpressure necessary to meet both short.

and long-term NPSH (not positive suction head) requirements for all four cases provided in the March 4,1997 submittal.

2. Provide the minimum containment pressure analyses that support the amount of .

containment overpressure assumed in the NPSH calculations. If new code is used for !

the containment pressure analyses, then the new code should be benchmarked against a code that has been approved by the staff. Results from such benchmarking studies shouM be provided for staff review.

3. Has the operation of containment sprays been factored into the assumption of containment overpressure?

4. How much of an impact will the higher than rated pump flow have on the brake horsepower requirements for the core spray and LPCI (low pressure core injection) pump motors?

Resoonse 1-3. Refer to the two new attached reports related to analysis of containment pressure and temperature response and ECCS pump NPSH requirements:

Exhibit D -

General Electric Report GE-NE-T2300731-2, "Monticello Nuclear Generating Plant LOCA Containment Analysis For Use in Evaluation of NPSH for the RHR and Core Spray Pumps," June,1997 Exhibit E -

Duke Engineering & Services Calculation Package V75100.NSP97.00501," Determination of Conta.1 ment Overpressure Required for Adequate NPSH of the Low Pressure ECCS Pumps," June 18,1997 J-1

l I

4. Per the pump curves for the ECCS pumps, it is evident that the higher than rated pump flows result in brake horsepower requirements which are equal to or slightly less than the rated horsepower of the motors. Furthermore, the electrical input power to the motors of these pumps when pumping the specified higher than rated pump flows is less I than the values analyzed for in Table 8.4-2 of the USAR for Standby Diesel-Generator System Emergency Loads for these pumps.

Data Summarv I

USAR 8.4-2 Limiting Electrical Electrical Input Pumo Flow Rate BHP Efficiency Inout Power (kw) Power (kw) 11 RHR 4292 gpm 575 hp 0.93 462 kw 497 kw 12 RHR 4289 gpm 575 hp 0.93 462 kw 497 kw 13 RHR 4344 gpm 600 hp 0.95 472 kw 497 kw 14 RHR 4308 gpm 575 hp 0.945 454 kw 497 kw 11 CS 4298 gpm 800 hp 0.95 629 kw 663 kw 12 CS 4218 gpm 800 hp 0.94 636 kw 663 kw inouts

1. Limiting flow rates in Calculation CA-97-163 were applied to the pump curves for the specific pumps to determine brake horsepower requirements under the high flow rate conditions. Limiting flow rates are the flow rates which require the highest brake horsepower. In some cases, lower flow rates which require more brake horsepower were used.

2. Brake horsepower requirements are from the pump curves for the subject pumps,

3. Efficiencies utilized are in agreement with those determined in Condition Report 96001901," Clarification of ECCS Motor operating horsepower."

4. Electrical Input Power (kw) = (BHP / efficiency) X 0.7459 kw/hp.

J-2 I

-J

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Conclusion:

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Latest revision as of 02:39, 22 July 2020

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Title:

8.0 REFERENCES

Subject:

SUMMARY

Conclusion:

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SUMMARY

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Dear Dave:

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