ML20155B522
| ML20155B522 | |
| Person / Time | |
|---|---|
| Site: | Quad Cities  |
| Issue date: | 09/29/1998 |
| From: | Dan Collins COMMONWEALTH EDISON CO. |
| To: | |
| Shared Package | |
| ML20138L449 | List: |
| References | |
| QDC-1000-M-0535, QDC-1000-M-0535-R01, QDC-1000-M-535, QDC-1000-M-535-R1, NUDOCS 9810300166 | |
| Download: ML20155B522 (65) | |
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1 l
l ATTACHMENT B SVP-98-335 Comed Calculation No, QDC-1000-M-0535, Rev.1,"Long-Term RilR/ Core Spray Pump NPSil Analysis-Design Basis LOCA" l
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9910300166 981026 !.'"
PDR ADOCK 05000254.
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Exhibit C NEP-12-02 Revision 5 Page1 of2 PREPARATION, REVIEW AND APPROVAL OF CALCULATIONS CALCULATION TITLE PAGE Calculation No: ODC-1000-M 0535 DESCRIPTION CODE: M10 DISCIPLINE CODE:
M STATION Ouad Cities Units 1 and 2 TITLE: Long Term RHR/ Core Sorav Pumo NPSH Analysis - Design Basis LOCA X
Safety Related Augmented Quality Non-Safety Related REFERENCE NUMBERS Type Number g Type Number CMC ODCl000 'f 02"2 CALC ODC-1000-M-0419 A complete list of References can be found in Section 5 of this calculation.
COMPONENT EPN:
DOCUMENT NUMBERS:
EPN Compt Type Doc Type / Subtype Document Number 1(21-1002 A/B Pumos 1(21-1002C/D Pumos 1(2)-1401 A/B Pumos REM ARKS: This calculation supersedes Calc. No. QDC-1000-M-0292 in its entirety.
REV.
REVISING APPROVED DATE
~
ORGANIZATION PRINT / SIGN O
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( rg e e now w / [$7];f_ izjuk 12/s/q7 asu~al 1.AW I
coa o e ren wwu
Exhibit C NEP-12-02 Revision 6 Page 2 of 2 COMMONWEALTH EDISON COMPANY l
CALCULATION REVISION PAGE CALCULATION NO. QDC 1000-M 0535 PAGE NO.: 2 REVISION SUMMARIES REV: 1 REVISION
SUMMARY
Initial Issue Electronic Calculation Data Files:
(Program Name, Version. File name ext / size /date/ hour /: min)
SEE REV. D.
Prepared by: Douglas F. Collins / SIGNATURE ON FILE 12/23/97 Print / Sign Date Reviewed by: Rocer H. Hevn / SIGNATURE ON FILE 12/23/97 Print / Sign Date Type of Review
[X] Detailed
[' ] Altemate
[ ] Test Supplemental Review Required
( ] Yes (NEP-12-05 documentation attached) (X)No Supervisor N/A
/
)
DO ANY ASSUMPIlONS IN THIS CALCULATION REQUIRE LATER VERIFICATION [ ] YES [X] NO Tracked by:
REV: 1 REVISION
SUMMARY
This revision incorporates the results of the 1998 containment analysis, and provides time-dependent curves of the required containment pressure. Rev. I supersedes Rev. O in its entirety.
1 Electronic Calculation Data Files:
}
(Program Name. Version. File name exusize/date/ hour /: min)
PIPE FLO. Ver. 4.11. CASE 1.PLU / 36 KB / 09-25 98 / OI.26PM CK E 2 PLU / 36 KB / 09-25-98 / Ol:26PM CASE-3 PLU / 36 KB / 09 25 98 / 01.27PM CA
-l PLU / 36 KB / 09-25-98 / Ol:33PM CASE-5 PLU / 36 KB / 09-25-98 / Ol.33PM CA5i 6 PLU / 36 KB / 09-25-98 / 0134PM CASE 7 PLU / 36 KB / 09 25 98 / OI:41PM LO% NEW.PLL /135 KB / 09 25-98 /10.25AM LONG NEW.PLU / 36 KB / 09-25-98 / Ol:45PM Prepared by: OcwiM F~ CcJliew I)d
'5A 09!2B[98 Print / Sign '
' Date Reviewed bv: kwatsr-N Ne#.
/
11 1M L 36 fib
~
Mint /Sicn ' /
/
' Date Type of Review
()() Detailed
[ ] Alternate
[ ] Test Supplemental Review Required
[ ] Yes (NEP 12-05 documentation attached)
P([No Supervisor Jerr
/ V24Brt DO ANY ASSUMFilONS IN THIS CALCULATION REQUIRE LATER VERIFICAllON [ ] YES % NO Tracked by:
Exhibit D NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION TABLE OF CONTENTS CALCULATION NO. ODC-1000 M-0535 REV. NO. I PAGE NO. 3 SECTION PAGE NO.
SUB-PAGE NO.
TITLE PAGE I
REVISION
SUMMARY
2 TABLE OF CONTENTS 3
4 PURPOSE / OBJECTIVE 4
METHODOLOGY AND ACCEPTANCE CRITERIA 4-5 ASSUMPTIONS 5
DESIGN INPUT 6
REFERENCES 6-7 CALCULATIONS 7-9
SUMMARY
AND CONCLUSIONS 9
ATTACHMENTS A. Results of COP Analysis (8 pages)
A1 - A8 B. Results of Hydraulic Model(40 pages)
Bl - B40 C. GE Letters on Drawdown (5 pages)
C1-C5 D. New Strainer Design Basis (2 pages)
D1 - D2
t l
Exhibit E NEP-12-02 Revision 6 l
COMMONWEALTH EDISON COMPANY CALCULATION NO. QDC-1000-M-0535 PAGE NO. 4
- 1. PURPOSE / OBJECTIVE i
l The purpose of this calculation is to determine if sufficient net positive suction head (NPSH) is available for the i
Residual Heat Removal (RHR) and Core Spray (CS) pumps following a Design Basis LOCA. This calculation examines NPSH conditions under long term (>600 seconds) conditions following the accident. The results of this l
calculation will be used to support a Quad Cities License Amendment request. Upon approval of this request.
l this calculation will represent a Design Basis Document.
l
- 2. METHODOLOGY AND ACCEPTANCE CRITERIA l
l This calculation will utilize a FLO-Series model of the RHR and CS piping generated by Calculation No. QDC-l 1000-M-0419, Rev 1 (Ref. 5.1). This calculation will determine the minimum suppression chamber pressure l
required to ensure that the NPSH available (NPSHA) at the suction intakes of the RHR and CS pumps are greater than the NPSH required (NPSHR) for the pumps. NPSHR curves for the LPCl/CS pumps are provided on the original vendor pump curves (attached to Ref. 5.1).
l Per Refs. 5.2 and 5.3, the most limiting Dow case with respect to long term suppression pool temperature is the operation of one RHR pump at 5000 gpm and one CS pump at 4500 gpm. This pump combination is the long term design basis now case and is based on a single failure of one diesel generator (or battery failure),
This calculation will explore additional now cases, but additional RHR pumps running would increase the heat removal rate and decrease the maximum pool temperature. Operations personnel have also been trained in recognizing cavitation conditions (Ref. 5.16). If additional pumps were running, existing operating procedures would allow the operators to throttle or turn off pumps in order to maintain sufficient NPSHA. Quad Cities Procedure QCAP 0200-10 " Emergency Operating Procedure (QGA) Execution Standards"(Ref 5.9) provides NPSH limit curves which will be used by the operators to control pump Dow rates following an accident. These curves are based on the same now model as this calculation.
Per Equation 5.2 on page 66 of Ref 5.8, the equation for NPSHA is as follows:
N PS H A = h,,, + Z - h, - h.,.
(Eq.1)
Where:
h,,,
= Suppression chamber pressure, feet absolute.
Z-
= Static head above pump, feet.
h,
= Suction friction losses, feet.
h,,,
= Vapor pressure, feet absolute.
1 This equation can be rewritten in terms of the suppression chamber pressure, and the minimum suppression chamber pressure required is that which will yield a value of NPSHA which is equal to the NPSHR. Thus:
(
h,,, = N PS H R - Z + h, + h.,.
(Eq.2)
Or this equation can be written to solve for the suppression chamber pressure in units of psia:
REVISION NO. 0 l REVISION NO.1 l
l l
Exhibit E NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION NO. QDC-1000 M-0535 PAGE NO. 5 l
P., = (NPSHR - 2 + hr + h,,,y(144V)
(Eq.3)
Where:
i P.,,
= Minimum Required Suppression Chamber Pressure, psia.
V
= Specific volume, ft'/lb.
The value of P.,,, for each flow case will be plotted as a function of time and compared to the Available and Credited Pressure in the Suppression Chamber (bec Assumption 3.3).
Acceptance Criteria:
2.1 Available Pressure 2 Required Pressure at all times for each flow case (Adequate NPSH).
2.2 Total RHR flow 2 5000 gpm for each flow case (Adequate Containment Cooling).
2.3 Total CS flow 2 4500 gpm for each flow case (Adequate Core Cooling).
- 3. ASSUMPTIONS / ENGINEERING JUDGEMENTS 3.1 It is assumed that at 10 minutes into the accident, operator action will be taken to throttle the RHR/CS pumps as necessary. Therefore, the RHR/CS pumps will be at their rated flows (5000 and 4500 gpm, respectively) for the design basis flow case (Refs. 5.2 and 5.3).
3.2 To account for strainer plugging, one of the four suction strainers inside the torus is assumed 100 percent blocked, while the remaining three strainers are assumed clean (Ref. 5.4). For each flow case, the strainer nearest the pump with the lowest differential between NPSHA and NPSHR will be chosen.
3.3 The long term suppression chamber pressure response from the containment analysis (Ref 5.2) is contained in Attachment A along with the assumed pressure response which is modeled as a time-dependent step function, consistent with the NRC-approved methodology from Dresden station. The assumed (credited) pressure response was determined in Design input 4.1 such that it is conservatively bounded by the available pressure response from Ref. 5.2. The containment analysis incorporates assumptions to minimize containment overpressure that are consistent with NRC Information Notice 96-
- 55. This data will predict the minimum available overpressure and will, therefore, be conservative.
3A This calculation assumes the maximum temperature response of the suppression pool from the bounding containment analysis. This assumption is conservative because it minimizes the NPSHA at the pumps.
3.5 The value of the long term suppression pool drawdown comes from GE letters regarding Dresden station (Refs. 5.5 and 5.6). Based on a review of the letters, this information is applicable to Quad Cities station as well.
3.6 The initial suppression pool temperature of 95 F (Ref. 5.10) is used to determine the physical properties of water in the hydraulic model. Following a DBA-LOCA, the suppression pool temperature will increase from this initial condition. The use of the minimum temperature will conservatively maximize the friction losses through the suction piping. Other conservative assumptions from the hydraulic model are listed in Ref. 5.1.
REVISION NO. O REVISION NO.1 l
Exhibit E I
l NEP-12-02 Revision 6 i
COMMONWEALTH EDISON COMPANY l
CALCULATION NO. QDC-1000-M-0535 PAGE NO. 6
- 4. DESIGN INPUT 4.1 Per the results of the containment analyses contained in Refs. 5.2, the available pressure response in the long term conservatively bounds the following values (See Attachment A):
Time (sec)
Credited Pressure (psig) 600 - 10000 3.0 10000 - End 3.5 4.2 This calculation uses an approved FLO-Series model of the ECCS piping generated by Calculation No.
QDC-1000-M-0419, Rev. 0 (Ref. 5.1).
i 4.3 The long-term suppression pool temperature and pressure response was generated in Ref. 5.2 based on a containment model developed by GE. The intent of this model was to determine the maximum pool temperature expected post-LOCA and the minimum corresponding containment pressure response. A tabular representation of the suppression pool temperature / pressure response is provided in Ref 5.2 and is summarized in Attachment A.
4..t The maximum drawdown of the suppression chamber water level at the time of peak suppression pool temperature is I foot (Ref 5.5 and 5.6). Applying this drawdown to the minimum water level allowed by Technical Specifications used in Ref. 5.1 yields a water elevation of 569.6 ft.
4.5 The values for the vapor pressures and specific volumes of water at various temperatures are taken from Ref. 5,11 and are included in Attachment A.
4.6 NPSHR values at various RHR/CS pump flow rates are taken from the NPSHR curves provided on the manufacturer's pump curves attached to Ref. 5.1. These values are summarized in the following table:
Pump Flow NPSHR (gpm)
(feet) 3000 25.0 4500 27.0 5000 30.0
- 5. REFERENCES 5.1 Calculation No. QDC-1000-M-0419, Rev.1, " Flow Model of Emergency Core Cooling System (ECCS)
Suction Piping with Core Spray and Residual Heat Removal (RHR) Discharge Piping."
5.2 GE Report GE-NE-T2300750 00-02 RI," Quad Cities Nuclear Power Station Units 1 and 2 Containment Analysis for Long-Term NPSH Evaluation with ANS 5.1 - 1979 + 2 Sigma Decay Heat, September 1998."
5.3 Quad Cities UFSAR, Rev. 4, Section 6.2.1.3.3, " Containment Long Term Response to a Design Basis Accident."
5.4 Quad Cities UFSAR, Rev. 4, Section 6.3, " Emergency Core Cooling System."
5.5 GE Letter - S. Mintz to S. Eldridge, dated September 24,1992 (Attachment E).
5.6 GE Letter - S. Mintz to T. Chapman, dated January 25,1993 (Attachment E).
REVISION NO. O REVISION NO.1 l
Exhibit E NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION NO QDC-1000-M-0535 PAGE NO 7 5.7 Crane Technical Paper 410. " Flow of Fluids Through Valves, Fittings and Pipe" - 1991.
5.8 Durco Pump Engineering Manual-4th Edition.
5.9 Quad Cities Procedure QCAP 0200-10, Rev.17 " Emergency Operating Procedure (QG A) Execution Standards" 5.10 Quad Cities Technical Specifications DPR-29/DPR-30, Amendments 180 and 178, Section 3.7.K.
5.11 Keenan and Keyes. Steam Tables (English Units). Wiley and Sons, New York: 1969.
5.12 NDIT No. 9800039,"ECCS Flow to Meet 10CFR50.46 Core Cooling Requirements of a DBA LOCA for Short Term and Long Term."
5.13 "LOCA Break Spectrum for Quad Cities Unit I and 2," Siemens document EMF-96-184(P), dated December 1996.
5.14
" Quad Cities Nuclear Power Station Units 1 & 2, SAFER /GESTR - LOCA Loss-Of Cool' ant Accident Analysis," General Electric document NEDC-31345P, Revision 2, dated July 1989.
5.15 "Long Term Cooling of the Reactor Cores of the Dresden and Quad Cities Nuclear Plants Following Postulated Design Basis Accidents (DBA)," GE letter DRF:T23-685, to K. Ramsden (Comed) from R, Muralidharan (GE), dated February 12,1993.
5.16 Licensee Event Report No.96-025.
5.17 Duke Engineering and Services Report No. TR-VQl500-02, Rev. O.
5.18 Calculation No. QDC-0010-M 0396, Rev. O," Quad Cities Unit 2 - ECCS Strainer Head Loss Estimate."
5.19 Calculation No. QDC-1600-M 0545, Rev. 0," Quad Cities Unit 1 - ECCS Strainer Head Loss Estimate."
- 6. CALCULATIONS This calculation will analyze ten flow cases considering different possible pump combinations for the long term operation of RHR and CS pumps following the DBA LOCA. The flow cases analyzed in the calculation are as follows:
Flow Case Pump Combination i
1/1 Nominal Case 1 RHR at 5000 gpm and 1 CS at 4500 gpm 2
2/2 Nominal Case 2 RHR at 5000 gpm and 2 CS at 4500 gpm 3
2/2 Throttled Case 2 RHR at 3000 gpm and 2 CS at 4000 gpm 4
3/2 Nominal Case 3 RHR at 5000 gpm and 2 CS at 4500 gpm 5
3/2 Throttled Case 3 RHR at 3000 gpm and 2 CS at 4000 gpm 6
4/2 Nominal Case 4 RHR at 5000 gpm and 2 CS at 4500 gpm 7
4/2 Throttled Case 4 RHR at 3000 gpm and 2 CS at 4000 gpm REVISION NO. O REVISION NO.1 l
Exhibit E NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION NO QDC-1000-M-0535 PAGE NO,8 These now cases utilized a FLO-Series hydraulic model of the RHR and CS piping from Ref. 5.1 (Attachments B and C). The results of these cases are summarized in Attachment A. These results demonstrate that there is sufficient containment pressure available at all times following a DBA LOCA. Note also that in every Dow case, there is a minimum of 4500 gpm of CS flow and 5000 gpm of RHR flow. Per Ref. 5.12, the minimum flow rate to maintain the core flooded is 2200 gpm.
6.1 Example Calculation of Reauired Containment Pressure The required containment pressure for each flow case is determined in the tables of Attachment A. This example demonstrates how the numbers in the table were determined, speciucally for the RHR pump in Flow Case I at Time = 24372 sec.
Per Table A.1, at this time, the suppression pool temperature is 182.0 F, and thus per Ref. 5.l l:
V = 0.016521 ft'/lb.
h,,, = 18.68 feet.
The RHR pump is operating at 5000 gpm and, thus, per Design input 4.6:
NPSHR = 30.0 feet The value of Z-he is determined in the FLO-Series model:
Z - h, = 3.715 psia (for 95 F water, W = 0.016114 ft'/lb) 2 2
Z - hr = (144 in /ft )(0.016114 ft'/lb)(3.715 lblin ) = 8.62 feet.
This number is adjusted by I foot to account for the I foot drawdown assumed in the long term ( Assumption 3.4 and Design input 4.4) and thus:
Z - hr = 7.62 feet Per Eq. 3:
P,,,,,, = (NPSHR Z + hr + h,)/(144V)
= (30.00 - 7.62 + 18.68)/(144(0.016521))
= 17.3 psia = 2.6 psig This example represents one time for one Dow case. The results of the analysis for all seven Cow cases over time can be found in both tabular and graphical form in Attachment A.
REVISION NO. O REVISION NO.1 l l
Exhibit E NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY j
CALCULATION NO. QDC-1000-M-0535 PAGE NO. 9 / Final New Strainer Desien Basis The current Quad Cities design basis for strainer blockage is one strainer blocked and 3 strainers clean
( Assumption 3.2, Ref. S.4). In response to NRC Bulletin 96 03, Quad Cities plans to revise this design basis to four partially clogged strainers, with the head loss associated with the new strainers (Ref. 5.17) and the debris loading as modeled in Ref. 5.18 - 5.19. (This model is attached as file LONG,NEW.PLL) This possible, future l
design basis would slightly decrease the NPSH margin in the long term, as demonstrated in Attachment D.
However, there would still be adequate containment pressure available to satisfy the pump NPSH requirements.
Currently, one strainer completely blocked and three strainers clean is the Quad Cities straiaer debris loading design basis.
- 7.
SUMMARY
AND CONCLUSIONS This NPSH analysis was performed for the CS and RHR pumps under long term post-accident conditions as outlined in Ref. 5.2. Selecting inputs to minimize NPSH margin,it was determined that adequate NPSH exists to meet RHR and CS pump requirements for all pump combinations. However, the potential exists for the pumps to cavitate in several of the scenarios. For these cases, throttling of the pumps may be required to ensure NPSH 1
requirements are met. Operating procedures provide NPSH limit curves to the operators and direct the operators to throttle the pumps to maintain adequate NPSH to the pumps. Under all post LOCA pump combinations.
positive NPSH margin could be obtained by throttling the available pumps.
REVISION NO. O REVISION NO.1 l
Calc. No. QDC-1000-M-0535, R;v.1.
Attachm:nt A Pzg3 A1 RHR/CS Pump Pressure Requirements - Design Basis Case RHR CS P
T (deg.
P, V
h,,,
Z-he NPSHR P.m Z-h, NPSHR P.m Sec (psig)
F)
(psia)
(ft'ilb)
(feet)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig) 643 65 150.8 3.796 0 016347 8 94 7.62 30.0
-1.40 11.56 27.0
-4.34 l
1627 34 157.6 4.480 0 016382 10 57 7.62 30.0
-0.73 11.56 27.0
-3.67 3434 34 164.8 5.439 0.016421 12.86 7.62 30.0 0.20 11.56 27.0
-2.73 5412 34 170.1 6.010 0.016451 14.24 7.62 30.0 0.76 11.56 27.0
-2.17 8756 3.7 175.1 6.735 0 016480 15.98 7.62 30.0 1.47 11.56 27.0
-1 46 12290 4.1 178 8 7.318 0 016502 17.39 7.62 30.0 2.04 11.56 27.0
-088 16434 4.2 180 9 7.666 0 016514 18 23 7.62 30.0 2.38 11.56 27.0
-0.54 20372 4.3 181.8 7.820 0 016520 18.60 7.62 30 0 2.53 11.56 27.0
-039 24372 4.3 182.0 7.854 0 016521 18 68 7.62 30 0 2.56 11.56 27.0
-0 36 30424 4.3 181.6 7.786 0 016519 18.52 7.62 30.0 2.49 11.56 27.0
-0.42 40266 4.1 179.6 7.449 0.016507 17.71 7.62 30 0 2.16 11.56 27.0
-0.76 RHR Pump Pressure Requirements - Nominal Flows 4 RHRl 2 CS 3 RHR 12 CS 2 RHR 12 CS 1 RHR 11 CS Z-he NPSHR P.m Z-h, NPSHR P.m Z-h, NPSHR Pm Z-h, NPSHR P.m Sec (feet)
(feet)
(psig)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig) 643
-0.86 30.0 2.21 1 58 30.0 1.17 3 49 30 0 0 36 7 62 30.0
-1.40 1627
-0.86 30.0 2.86 1.58 30 0 1.83 349 30 0 1.02 7.62 30 0
-073 3434
-086 30 0 3.79 1.58 30 0 2.76 3 49 30 0 1.95 7.62 30 0 0.20 5412
-086 30.0 4.34 1.58 30.0 3 31 3.49 30.0 2.50 7.62 30.0 0 76 8756
-086 30.0 5 04 1.58 30.0 4.01 3 49 30 0 3 21 7.62 30.0 1.47 12290
-0.86 30 0 5.60 1.58 30.0 4.58 3.49 30.0 3.77 7.62 30.0 2 04 16434
-086 30 0 5 94 1.58 30 0 4.92 3 49 30 0 4 11 7 62 30 0 2.38 20372
-0.86 30.0 6 09 1.58 30 0 5.07 3 49 30 0 4 26 7.62 30.0 2 53 24372
-0.86 30.0 6.13 1.58 30 0 5.10 3 49 30 0 4.30 7.62 30.0 2.56 30424
-0.86 30 0 6.06 1.58 30 0 5.03 349 30 0 4 23 7.62 30 0 2.49 40266
-086 30 0 5.73 1.58 30.0 4.71 3.49 30 0 3 90 7 62 30 0 2.16
Calc. No. QDC-1000-M-0535, R:v.1.
Attachm:nt A Pcg3 A2 RHR Pump Pressure Requirements -Throttled Flows 4 RHR / 2 CS 3 RHR 12 CS 2 RHR / 2 CS 1 RHR 11 CS Z-h, NPSHR P.m Z-h, NPSHR P.m Z-h, NPSHR P.m Z-h, NPSHR P.
Sec (feet)
(feet)
(psig)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig) 643 7.85 25.0
-3 62 8 85 25 0
-4.04 9.67 25 0
-4.39 7 62 30 0
-1.40 1627 7.85 25 0
-2.95 8 85 25.0
-3.37 9 67 25 0
-3.72 7.62 30 0
-0.73 3434 7.85 25.0
-2.01 8.85 25.0
-2.43 9 67 25.0
-2.78 7.62 30.0 0.20 1
5412 7.85 25.0
-1 45 8.85 25.0
-1.87 9.67 25.0
-2.22 7.62 30 0 0.76 8756 7.85 25.0
-0.74 8.85 25 0
-1.16 9.67 25.0
-1.51 7.62 30 0 1.47 12290 7.85 25.0
-0.16 8.85 25.0
-0.59 9.67 25.0
-0.93 7.62 30.0 2.04 16434 7.85 25.0 0.18 8.85 25.0
-024 9 67 25.0
-0.59 7.62 30 0 2.38 20372 7.85 25.0 0.33 8.85 25.0
-009 9.67 25 0
-044 7.62 30.0 2.53 24372 7.85 25.0 0.36 8.85 25.0
-0.06 9 67 25.0
-0.40 7.62 30 0 2.56 30424 7.85 25.0 0.30 8.85 25.0
-0.12 9 67 25 0
-047 7.62 30 0 2.49 40266 7.85 25.0
-0.04 8.85 25.0
-0.46 9.67 25.0
-080 7.62 30.0 2.16 CS Pump Pressure Requirements - Nominal Flows 4 RHR / 2 CS 3 RHR 12 CS 2 RHR 12 CS 1 RHR /1 CS Z-h, NPSHR Pm Z-h, NPSHR Pm Z-h, NPSHR Pm Z-h, NPSHR Pm Sec (feet)
(feet)
(psig)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig) 643 5.43 27.0
-1.74 7.56 27.0
-2.65 9 29 27 0
-3 38 11.56 27.0
-4 34 1627 5.43 27.0
-1.08 7.56 27.0
-1.98 9.29 27.0
-2.71 11.56 27.0
-3 67 3434 5 43 27.0
-0.14 7.56 27.0
-1.04 9.29 27.0
-1.77 11.56 27.0
-2.73 5412 5.43 27.0 0.42 7.56 27.0
-048 9 29 27.0
-1.21 11.56 27.0
-2.17 8756 5 43 27.0 1.12 7.56 27.0 0.23 9.29 27.0
-050 11.56 27.0
-1.46 12290 5.43 27.0 1.70 7.56 27.0 0.80 9.29 27.0 0 07 11.56 27.0
-088 16434 5.43 27.0 2.04 7.56 27.0 1.14 9.29 27.0 0 41 11.56 27.0
-0 54 20372 5.43 27.0 2.19 7.56 27 0 1.29 9.29 27.0 0.56 11.56 27.0
-039 24372 5.43 27.0 2.22 7.56 27.0 1.33 9.29 27.0 0 60 11.56 27.0
-0.36 30424 5.43 27.0 2.15 7.56 27.0 1.26 9 29 27.0 0.53 11.56 27.0
-042 40266 5.43 27.0 1.82 7.56 27.0 0.93 9.29 27.0 0 20 11.56 27.0
-076
1 Calc. No. QDC-1000-M-0535, Rav.1.
Attachm';nt A Pags A3 i
4 j
CS Pump Pressure Requirements - Throttled Flows i
4 RHR 12 CS 3 RHR 12 CS 2 RHR 12 CS 1 RHR f 1 CS Z-h, NPSHR Pm Z-h, NPSHR Pm Z-h, NPSHR P..
Z-h, NPSHR Pm Sec (feet)
(feet)
(psig)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig)
(feet)
(feet)
(psig) 643 9.36 25.0
-4.26 10.26 25.0
-4.64 11.01 25.0
-4 96 11.56 27.0
-4.34 1627 9.36 25.0
-3.59 10.26 25.0
-3 97 11.01 25.0
-4 29 11.56 27.0
-3.67 3434 9.36 25.0
-2.65 10.26 25.0
-3.03 11.01 25.0
-3.34 11.5,6 27.0
-2.73 5412 9.36 25 0
-2.09 10.26 25.0
-2.47 11.01 25 0
-2.78 11.56 27.0
-2.17 8756 9.36 25.0
-1.37 10.26 25.0
-1.75 11.01 25.0
-2.07 11.56 27.0
-1.46 12290 9.36 25.0
-0.80 10.26 25.0
-1.18 11.01 25.0
-1.49 11.56 27.0
-0.88 16434 9.36 25.0
-0.46 10.26 25.0
-0.84 11.01 25 0
-1.15 11.56 27.0
-0 54 20372 9.36 25.0
-0.31 10.26 25.0
-0.68 11.01 25.0
-1.00 11.56 27.0
-039 24372 9.36 25.0
-0.27 10.26 25.0
-0.65 11.01 25.0
-0.97 11.56 27.0
-0.36 30424 9.36 25.0
-0.34 10.26 25.0
-0.72 11.01 25 0
-1.03 11.56 27.0
-0.42 40266 9.36 25.0
-0.67 10.26 25.0
-1.05 11.01 25 0
-1.37 11.56 27.0
-0.76 i
Cdc. No. QDC-1000-M-0535, R;,v.1.
Attachm:nt A P ga A4 Long Term Post-LOCA RHRICS Pump Pressure Requirement - DBA Case 80 I
I h
.{
7.0
_._ g
\\s 6.0 5.0
- \\
5 4.0 f
h --
.........j 3.0
- - - - - ---j------
r-j ; paj 2
l.
A_
f2.0 II'I,
~
li l
ji 1
l}
l i
r li!
1.0 7 ll f
j',
y Y
E 0.0
/
i e
i 3
- . p j
lll
~
3.i.0 ZZ1.i~ 1 Z A
u-
/,;
j i
2.0 g#
j COP
-3.0 8
- - - - - - COP (Credited)
A RHR 4.0
--m-- C S y
100 1000 10000 100000 Time (sec)
Calc. No. QDC-1000-M-0535, R:,v.1.
Attachm:nt A Paga A5 Long-Term Post-LOCA RHR Pump Pressure Requirements - Nominal Flows 8.0
.. J.
4 I
.____..i.__ _.. _.
6.0
" A7
-~--
\\
.. __. 9 _..._
. y
/_
g Z
_.._p t.
j g
4.0 li g
. _. g g,......
}
l
.l g
.I..
t c
Vl
/_..
/
i i
,e 2.0
/__g/y
- e -
i E
t i
1 i
i i i !
{
4
'I COP o
o r
}
~__..
- - - - - - COP (Credited) i 0.0
[
3 RHR/2 CS
^
2 RHR/2 CS
--o-1 RHR/1 CS g.-
I
-2.0 100 1000 10000 100000 Time (sec)
Ccic. No. QDC-1000-M-0535, R:v.1.
Attachm:nt A Pig 2 A6 Long-Term Post-LOCA RHR Pump Pressure Requirements -Throttled Flows 80 l
_. } __
i
_..'T
'~
6.0
\\g
\\
_t_
4.0
-y
~'-
.!!P l
g P
j-2.0 g
/g.
g
,, } l, j o.o n T N j
i c
_ [_.
_.I N
]
.r u
- ~
g
/
-2.0 gy#/
W COP
///
/8
- - - - - - COP (Credited) p A 4 RHR/2 CS 4.0 9
3 RHR/2 CS
- ~
0 2 RHR/2 CS
. _~
~
-e-1 RHR/1 CS
~
~~
l !!
i i
l 'ii
-6.0 100 1000 10000 100000 Time (sec)
Calc. No. QDC-1000-M-0535, R,v.1.
Attachm:nt A Prg3 A7 Long-Term Post-LOCA CS Pump Pressure Requirements - Nominal Flows 80 I
j_
___j-f.
l
__..___.}
1 j._
6.0
\\-
t K
- N 4.. _... _........p'- - - -
Mi -- -
4.0
...q.l
.,y}
l f~
2
- ' - - ~
' - ~
~
,'. e.
}
}
g 2.0 g
g j J'
_g
-. g[
g
_ %}
l 1
y
. g[l l
l P
l 3
j j
0.0 I- - ---
y t
7 j j
d e
l g
y._
l
/
o I
o 3
2.0
"~
~'
8
- - - - - - COP (Credited)
.$.[$.T i_.. _ ~ _ '
e-_
/
A 4 RHR/2 CS
-4.0 3 RHR/2 CS e-,-
2 RHR/2 CS
-e--1 RHR/1 CS I
' 'i
-6.0 100 1000 10000 100000 Time (sec) i
Calc. No. QDC-1000-M-0535, Rxv.1.
Attachm~nt A Pzg2 A8 (Fin:1)
Long-Term Post-LOCA CS Pump Pressure Requirements -Throttled Flows 80 6.0 N
-4 N
5 f T..... -.. [7..... p...-- -- f * - - -
4'0
.. r!
i 8.
..............d~. _..
i 1
i y
A
- g 2.0 t
l g
7 ;-
g I 1 l
g f.
l 0.d t'
h
.E.
I f I
~
8 t !
I o
-2.0 l
a p
- - - - - - COP (Credited)
- p 4
A 4 RHR/2 CS
-4.0 3 RHR/2 CS
- - - ~ ~
~~
2 RHR/2 CS y
-6.0 100 1000 10000 100000 Time (sec)
Comptny: Comed CASE-1 Project:
09/25/98 by: Doug Collins LINEUP REPORT rev: 09/25/98 LINELIST: ECCS DEVIATION: 0.000198 %
dated: 09/24/98 after: 7 iterations Design Basis Flow Case: 1 RHR pump @ 5000 gpm and 1 CS pump g 4500 gpm volumetric flow rates require constant fluid properties in all pipelines.
Fluid properties in the first specification were used.
NODE DEMAND NODE DEMAND 9Pm gpm Suc10C 5000 Suc14B 4500 FLOWS IN: 0 gpm FLOWS OUT: 9500 gpm NET FLOWS OUT: 9500 gpm PIPELINE FLOW PRESSURE SET gpm SOURCE psia 4
LA-1 3106 X-204A 0
LB-1 3111
<<< X-204B 0
LD-1 3283
<<< X-204D 0
FLOWS IN: 9500 gpm FLOWS OUT: 0 gpm NET FLOWS IN: 9500 gpm 2
I PIPE-FLO rev 4.11 Calc. No. ODC-1000-M-0535, Revi 1.
Attachment B Page Bl
LINEUP NODES CASE-1 09/25/98
)
NODE ELEVATION DEMAND PRESSURE H GRADE ft
-gpm psi a ft
]
l A
559.5 4.475 569.9 B
559.5 4.475 569.9 C
559.5 4.474 569.9 D
559.5 4.474 569.9 E
559.5 4.473 569.9 F
559.5 4.456 569.8 G-559.5 4.449 569.8 H
559.5 4.438 569.8 I
559.5 4.42 569.8 J
559.5 4.423 569.8 K
559.5 4.423 569.8 L
559.5 4.425 569.8 M
559.5 4.433 569.8 N
559.5 4.436 569.8 Q
559,5 4.439 569.8 P
559.5 4.439 569.8 Q
559.5 4.439 569.8 R
559.5 4.434 569.8 Red 10A 562.25 3.271 569.8 Red 10B 562.25 2.858 568.9 Red 14A 555.63 6.132 569.9 Red 14B 555.63 5.415 568.2 S
559.5 4.446 569.8 Suc10A 555.58 6.144 569.8 Suc10B 555.58 6.144 569.8 Suc10C 555.58
> 5000 3.715 564.2 Suc10D 555.58 5.868 569.2 Suc14A 555.63 6.132 569.9 Suc14B 555.63
> 4500 5.411 568.2 T
559.5 4.457 569.8 Tee 10A-1 562.25 3.271 569.8 l
Tee 10A-2 557.08 5.498 569.8 Tee 10B-1 562.25 2.994 569.2
-Tee 10B-2 556.75 5.64 569.8 Tee 10C-2 556.79 4.084 566.3 Tee 10D-2 556.92 5.291 569.2 Teel 4A 555.63 6.132 569.9 Teel 4B 555.63 5.441 568.3 j
U 359.5 4.465 569.9 1
PIPE-FLO rev 4.11 Calc. No. QDC 4000-M-0535, Revi 1.
Atuchment B Page BL
.. -. _... =.. - - ~. - - -. - =.
l LINEUP NODES CASE-1 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft i
l l
V 559.5 4.474 569.9 X-204A 570.6 p
0 570.6 X-204B 570.6 p
0 570.6 X-204C 570.6
- -0.359 569.8 X-204D 570.6 p
0 570.6 X-223A-559.5 4.456 569.8 X-223B 559.5 4.42 569.8 X-224A 559.5 4.465 569.9
.X-224B 559.5 4.434 569.8 X-225 559.5 4.443 569.8 X-226 559.5 4.433 569.8 ZA 560.5 4.109 570 ZB 560.5 4.108 570 ZC 560.5 3.992 569.8 ZD 560.5 4.081 570 l
i l
l.
f-1 i
t g
-PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1.
Attachment B Page B3
. ~..
. -. ~..
l-LINEUP PIPELINES
-CASE-1 09,'25/98 PIPEL2NE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1015A-1 X-223A Tee 10A-1 0 0
0 0
2-1015A-2 Tee 10A-1 Red 10A 0
0 0
0 2-1015B-1 X-223B Tee 10B-1 5000 3.781 1.425 0.558 2-1015B-2 Tee 10B-1 Red 10B 5000 3.781 0.137 0.318 2-1016A-1 Red 10A Tee 10A-2 0 0
0 0
2-1016A-2 Tee 10A-2 Suc10A 0
0 0
0 2-1016B-1 Tee 10A-1 Tee 10B-2 0 0
0 0
2-1016B-2 Tee 10B-2 Suc10B 0
0 0
0 l
2-1016C-1 Red 10B Tee 10C-2 5000 11.64 (1.226
)
2.614 2-1016C-2 Tee 10C-2 Suc10C 5000 11.64 0.368 2.065 2-1016D-1 Tee 10B-1 Tee 10D-2 0 0
0 0
2-1016D-2 Tee 10D-2 Suc10D 0
0 0
0 2-1025-1 A
B 399.9 0.319 0
0 2-1025-10 I
<-> X-223B 1489 1.189 0-0 2-1025-11 J
<-> I 1469 1.126 0.003 0.008 2-1025-12 K
<->J 1489 1.189 0
0 2-1025-13 L
<-> K 1489 1.189 0.002 0.005 2-1025-14 M
<-> L 1489 1.126 0.008 0.018 2-1025-15 X-226
<->M 1489 1.189 0
0 2-1025-16 N
<-> X-226 1489 1.189 0.002 0.005 2-1025-17 O
<->N 1489 1.126 0.003 0.007 2-1025-18 P
<-> 0 1489 1.189 0
0 2-1025-19 P
Q 1794 1.433 0
0 2-1025-2 B
C 399.9 0.302 0
0.002 2-1025-20 Q
R 1794 1.357 0.004 0.010 2-1025-21 R
X-224B 1794 1.433 0
0 2-1025-22 X-225
<-> X,224B 2706 2.161 0.009 0.021 2-1025-23 S
<-> X-225 2706 2.161 0.003 0.007 2-1025-24 T
<-> S 2706 2.046 0.011 0.025 2-1025-25 X-224A
<-> T 2706 2.161 0.008 0.018 2-1025-26 U
<-> X-224A 2706 2.161 0
0 2-1025-27 V
<-> U 2706 2.046 0.009 0.021 2-1025-28 A
<-> V 2706 2.161 0
0.001 2-1025-3 C
D 399.9 0.319 0
0 2-1025-4 D
E 3511 2.805 0
0.002 2-1025-5 E
F
.3511 2.656 0.017 0.039 2-1025-6 F
X-223A 3511 2.805 0
0.002 2-1025-7 X-223A G
3511 2.805 0.006 0.014 2-1025-8 G
H 3511 2.656 0.011 0.027 2-1025-9 H
X-223B 3511 2.805 0.018 0.0.42 I
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1.
Attachment B Page Bi
LINEUP PIPELINES 4ASE-1 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1318-1 X-226 Red 13 closed 0
0 0
2-1401-1.
X-224A Tee 14A 0
0 0
0 2-1401-2 Teel 4A Red 14A 0
0 0
0 2-1401-3 Red 14A Suc14A 0
0 0
0 2-1402-1 X-224B Teel 4B 4500 6.183 (1.007
)
1.533 2-1402-2 Teel 4B Red 14B 4500 6.183 0.026 0.061 2-1402-3 Red 14B Suc14B 4500 7.911 0.004 0.009 2-2302-1 X-225 Red 23-1 closed 0
0 0
LA-1 X-204A ZA 3106 3.76 (4.109
)
0.562
--- strainer --- dP:
0.241
--- El:
0.559 LA-2 ZA A
3106 3.426 (0.366
)
0.151' LB-1 X-204B ZB 3111 3.767 (4.108
)
0.564
--- strainer --- dP:
0.242
--- Hl:
0.562 LB-2 ZB D
3111 3.433 (0.366
)
0.151 LC-1 X-204C ZC 0
0 0
0
--- strainer --- dP:
--- Hl:
LC-2 ZC K
0 0
0 0
LD-1 X-204D ZD 3283 3.975 (4.081
)
0.628
--- strainer --- dP:
0.269
--- Hl:
0.625 LD-2 ZD P
3283 3.622 (0.358
)
0.168 Pmp10A Suc10A Dis 10A closed 0
0 0
a
--- RHR Pump --- dP:
--- Hl:
Pmp10B Suc10B Dis 10B closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10C Suc10C Dis 10C closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10D Suc10D Dis 10D closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp14A Suc14A Dis 14A closed 0
0 0
--- CS Pump --- dP:
--- Hl:
Pmp14B Suc14B Dis 14B closed 0
0 O
--- CS Pump --- dP:
--- Hl:
I PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1 Atachment B Page B5'
Compr_ny: Comed CASE-2 Projsct:
09/25/98 by: Doug Collins LINEUP REPORT rev: 09/25/98 LINELIST: ECCS DEVIATION: 9.27e-005 %
dated: 09/24/98 after: 7 iterations 2/2 Unthrottled Case: 2 RHR pump @ 5000 gpm and 2 CS pump 6 4500 gpm volumetric flow rates require constant fluid properties in all pipelines.
Fluid properties in the first specification were used.
NODE DEMAND NODE DEMAND 9Pm gpm Suc10C 5000 Suc10D 5000 Suc14A
>>> 4500 Suc14B 4500 FLOWS IN: 0 gpm FLOWS OUT: 19000 gpm NET FLOWS OUT: 19000 gpm i
PIPELINE FLOW PRESSURE SET J
gpm SOURCE psia LA-1 6288
<<< X-204A 0
LB-1 6288 X-204B 0
I LD-1 6424 X-204D 0
FLOWS IN: 19000 gpm FLOWS OUT: 0 gpm NET FLOWS IN: 19000 gpm l
i i
l l
l fI PIPE-FLO rev 4.11 Calc. No. QDC-10CO-M-0535, Rev:
1.
Attachment B Page B(,
i.
i
-.~
... _ _ _.. ~
LINEUP NODES CASE-2 09/25/98 EODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft i
A, 559.5 3.524 567.7 B
559.5 3.524 567.7 I
C 559.5 3.524 567.7 i
D 559.5 3.524 567.7 E
559.5 3.521 567.7 F
559.5 3.47 567.6 G
559.5 3.449 567.5 H
559.5 3.414 567.4 I
559.5 3.357 567.3 J
559.5 3.375 567.3 K
559.5 3.376 567.3 L
559.5 3.391 567.4 l
M 559.5 3.436 567.5 N
559.5 3.451 567.5 0
559.5 3.468 567.5 i
P 559.5 3.469 567.6 Q
559.5 3.468 567.6 R
559.5 3.459 567.5 Red 10A 562.25 2.283 567.5 Red 10B 562.25 1.079 564.8 Red 14A 555.63 4.448 566 Red 14B 555.63 4.439 565.9 i
S 559.5 3.464 567.5 Suc10A 555.58 5.157 567.5 Suc10B 555.58 5.157 567.5 Suc10C 555.58
> 5000 1.937 560.1 Suc10D 555.58
> 5000 2.876 562.3 Suc14A 555.63
> 4500 4.446 565.9 Suc14B 555.63
> 4500 4.435 565.9 T
559.5 3.469 567.6 Tee 10A-1 562.25 2.283 567.5 Tee 10A-2 557.08 4.511 567.5 Tee 10B-1 562.25 1.216 565.1 Tee 10B-2 556.75 4.653 567.5 Tee 10C-2 556.79 2.305 562.1 l
Tee 10D-2 556.92 3.194 564.3 Teel 4A 555.63 4.475 566 Teel 4B 555.63 4.465 566 U
559.5 3.474 567.6 I
l PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1.
Anaciunent B Page B7
LINEUP NODES CASE-2 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft V
559.5 3.521 567.7 X-204A 570.6 p
0 570.6 X-204B 570.6 p
0 570.6 X-204C 570.6
- -1.406 567.3 X-204D 570.6 p 0 570.6 X-223A 559.5 3.468 567.5 X-223B 559.5 3.356 567.3 X-224A 559.5 3.472 567.6 X-224B 559.5 3.459 567.5 X-225 559.5 3.463 567.5 X-226 559.5 3.436 567.5 ZA 560.5 3.359 568.3 ZB 560.5 3.359 568.3 ZC 560.5 2.946 567.3 ZD 560.5 3.315 568.2 1
t PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1.
Atachment B Page B8
- - - ~.
- -,.. -. ~
~_ - -..
t LINEUP PIPELINES CASE-2 l
l 09/25/98 i
PIPELINE FROM To FLOW VEL' dP H1 i
gpm ft/see psi e ft 2-1015A-1 X-223A Tee 10A-1 0 0
0 0
2-1015A-2 Tee 10A-1 Red 10A 0
0 0
0 2-1015B-1 X-223B Tee 10B-1 10000 7.563 2.14 2.217 2-1015B-2 Tee 10B-1 Red 10B 5000 3.781 0.137 0.318 2-1016A-1 Red 10A Tee 10A-2 0 0
0 0
2-1016A-2 Tee 10A-2 Suc10A 0
0 0
0 l
2-1016B-1 Tee 10A-1 Tee 10B-2 0 0
0 0
2-1016B-2 Tee 10B-2 Suc10B 0
0 0
0 2-1016C-1 Red 10B Tee 10C-2 5000 11.64 (1.226
)
2.614 2-1016C-2 Tee 10C-2 Suc10C 5000 11.64 0.368 2.065 2-1016D-1 Tee 10B-1 Tee 10D-2 5000 11.64 (1.978
)
0.738 4
2-1016D-2 Tee 10D-2 Suc10D 5000 11.64 0.318 2.0.77 j
2-1025-1 B
<->A 13.01 0.010 0
0 2-1025-10 I
<-> X-223B 3725 2.975 0
0.002 1
2-1025-11 J
<-> I 3725 2.817 0.019 0.044 l
2-1025-12 K
<-> J 3725 2.975 0
0.002 2-1025-13 L
<-> K 3725 2.975 0.014 0.034 2-1025-14 M
<-> L 3725 2.817 0.045 0.104 2-1025-15 X-226
<-> M 3725 2.975 0
0.002 2-1025-16 N
<-> X-226 3725 2.975 0.014 0.033 2-1025-17 0
<-> N 3725 2.817 0.017 0.039 2-1025-18 P
<-> 0 3725 2.975 0
0.002 2-1025-19 P
Q 2699 2.156 0
0.001 2-1025-2 C
<-> B 13.01 0.010 0
0 2-1025-20 Q
R 2699 2.041 0.009 0.021 2-1025-21 R
X-224B 2699 2.156 0
0 2-1025-22 X-225
<-> X-224B 1801 1.438 0.004 0.009 2-1025-23 S
<-> X-225 1801 1.438 0.001 0.003 2-1025-24 T
<-> S 1801 1.362 0.005 0.012 2-1025-25 X-224A
<-> T 1801 1.438 0.003 0.008 2-1025-26 U
<-> X-224A 6301 5.033 0.002 0.005 2-1025-27 V
<-> U 6301 4.765 0.047 0.109 2-1025-28 A
<-> V 6301 5.033 0.002 0.005 2-1025-3 D
<-> C 13.01 0.010 0
0 2-1025-4 D
E 6275 5.012 0.002 0.005 2-1025-5 E
F
.6275 4.746 0.051 0.119 2-1025-6 F
X-223A 6275 5.012 0.002 0.005 1
2-1025-7 X-223A G
6275 5.012 0.019 0.045 l'
2-1025-8 G
H 6275 4.746 0.035 0.080 l
2-1025-9 H
X-223B 6275 5.012 0.058 0.135, I
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1.
Anaciunent B Page B9
LINEUP PIPELINES
- CAS E - 2 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1318-1 X-226 Red 13 closed 0
0 0
2-1401-1 X-224A Teel 4A 4500 6.183 (1.003
)
1.542 2-1401-2 Teel 4A Red 14A 4500 6.183 0.027 0.063 2-1401-3 Red 14A Suc14A 4500 7.911 0.003 0.006 2-1402-1 X-224B Teel 4B 4500 6.183 (1.007
)
1.533 2-1402-2 Teel 4B Red 14B 4500 6.183 0.026 0.061 2-1402-3 Red 14B Suc14B 4500 7.911 0.004 0.009 2-2302-1 X-225 Red 23-1 closed 0
0 0
LA-1 X-204A ZA 6288 7.613 (3.359
)
2.303
--- strainer --- dP:
0.988
--- Hl:
2.293 LA-2 ZA A
6288 6.937 (0.165
)
0.617 l
LB-1 X-204B ZB 6288 7.613 (3.359
)
2.303
--- strainer --- dP:
0.988
--- Hl:
2.293 LB-2 ZB D
6288 6.937 (0.165
)
0.617 LC-1 X-204C ZC 0
0 0
0
--- strainer --- dP:
--- Hl:
LC-2 ZC K
0 0
0 0
LD-1 X-204D ZD 6424 7.778 (3.315
)
2.404
--- strainer --- dP:
1.031
--- Hl:
2.394 LD-2 ZD P
6424 7.087 (0.153
)
0.644 Pmp10A Suc10A Dis 10A closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10B Suc10B Dis 10B closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10C Suc10C Dis 10C closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
1 Pmp10D Suc10D Dis 10D closed 0
0 0
l
--- RHR Pump --- dP:
--- Hl:
Pmp14A Suc14A Dis 14A closed 0
0 0
--- CS Pump --- dP:
--- Hl:
Pmp14B Suc14B Dis 14B closed 0
0 0'
--- CS Pump --- dP:
--- Hl:
l 4
I I
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev:
1.
Atu chment B Page Bl0
.-. = ~ -.
l Comptny: Comed CASE-3 l
Projact:
09/25/98 l
by: Doug Collina I
LINEUP REPORT rev: 09/25/98 LINELIST: ECCS DEVIATION: 0.000255 %
dated: 09/24/98 after: 7 iterations 2/2 Throttled Case: 2 RHR pump @ 3000 gpm and 2 CS pump 6 4000 epm volumetric flow rates require constant fluid properties in all pipelines.
Fluid properties in the first specification were used.
NODE DEMAND NODE DEMAND gpm gpm
)
Suc10C 3000 Suc10D
>>> 3000 Suc14A 4000 Suc14B
>>> 4000 FLOWS IN: 0 gpm L
FLOWS OUT: 14000 gpm NET FLOWS OUT: 14000 gpm PIPELINE FLOW PRESSURE SET gpm SOURCE psia l
LA-1 4633 X-204A 0
LB-1 4624 X-204B 0
LD-1 4743 X-204D 0
FLOWS IN: 14000 gpm FLOWS OUT: 0 gpm NET FLOWS IN: 14000 gpm l
1 t
t PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev:
1.
Atuchment B Page Bil
CASE-3 LINEUP NODES
+
09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE
)
ft gpm psi a ft A
559.5 4.099 569 B
559.5 4.099 569 C
559.5 4.101 569 j
D 559.5 4.101 569 E
559.5 4.1 569 F
559.5 4.079 569 G
559.5 4.07 568.9 H
559.5 4.055 568.9 I
559.5 4.032 568.9 J
559.5 4.038 568.9 K
559.5 4.038 568.9 L
559.5 4.042 568.9 M
559.5 4.056 568.9 N
559.5 4.06 568.9 O
559.5 4.066 568.9 P
559.5 4.066 568.9
)
Q 559.5 4.065 568.9 R
559.5 4.056 568.9 j
Red 10A 562.25 2.893 569 Red 10B 562.25 2.452 567.9 Red 14A 555.63 5.183 567.7 l
Red 14B 555.63 5.18 567.7 i
S 559.5 4.058 568.9 Suc10A 555.58 5.767 569 Suc10B 555.58 5.767 569 Suc10C 555.58
> 3000 4.598 566.3 Suc10D 555.58
> 3000 4.936 567 Suc14A 555.63
> 4000 5.181 567.7 Suc14B 555.63
> 4000 5.176 567.6 T
559.5 4.061 568.9 Tee 10A-1 562.25 2.893 569 Tee 10A-2 557.08 5.121 569 Tee 10B-1 562.25 2.502 568.1 Tee 10B-2 556.75 5.263 569 Tee 10C-2 556.79 4.399 567 Tee 10D-2 556.92 4.683 567.8 Tee 14A 555.63 5.204 567.7 Tee 14B 555.63 5.2 567.7 U
559.5 4.064 568.9 f
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1 Atuchment B Page Bil
...~..~.-..
. ~.. ~
LINEUP NODES CASE-3 09/25/98 l
l NODE ELEVATION DEMAND PRESSURE H GRADE
'l ft gpm psi a ft 1
V.
559.5-4.097 569 LX-204A.
570.6 p
0 570.6
.X-204B 570.6 p
0 570.6 X-204C 570.6
- -0.744 568.9 X-204D 570.6 p
0 570.6 X-223A 559.5 4.078 569 X-223B 559.5 4.032 568.9 X-224A 559.5 4.063 568.9 X-224B 559.5 4.056 568.9-X-225.
559.5.'
4.058 568.9 X-226 559.5 4.056 568.9 ZA 560.5 3.812 569.3 ZB 560.5 3.814 569.4 i
ZC 560.5 3.607 568.9 ZD 560.5 3.787 569.3 i
i l
l l
l i
l 1
1 l
l l
l l
l l
I
~
l-i i
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1.
Attachment B Page BIS
. -. ~. - - - - - - - -..-.-
LINEUP PIPELINES CASE-3 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/sec psi a ft 2-1015A-1 X-223A Tee 10A-1 0 0
0 0
2-1015A-2 Tee 10A-1 Red 10A 0
0 0
0
'2-1015B-1 X-223B Tee 10B-1 6000 4.538 1.53 0.802 2-1015B-2 Tee 10B-1 Red 10B 3000 2.269 0.049 0.115 2-1016A-1 Red 10A Tee 10A-2 0 0
0 0
2-1016A-2 Tee 10A-2 Suc10A 0
0 0
0 2-1016B-1 Tee 10A-1 Tee 10B-2 0 0
0 0
2-1016B-2 Tee 10B-2 Suc10B 0
0 0
0 2-1016C-1 Red 10B Tee 10C-2 3000 6.986 (1.946
)
0.942 l
2-1016C Tee 10C-2 Suc10C 3000 6.986 (0.199
)
0.747 2-1016D-1 Tee 10B-1 Tee 10D-2 3000 6.986 (2.181
)
0.268 2-1016D-2 Tee 10D-2 Suc10D 3000 6.986 (0.253
)
0.752 2-1025-1 B
<-> A 629.6 0.503 0
0 2-1025-10 I
<-> X-223B 2006 1.602 0
0 2-1025-11 J
<-> I 2006 1.517 0.006 0.013 2-1025 K
<-> J 2006 1.602 0
0 l2-1025-13 L
<-> K 2006 1.602 0.004 0.010 2-1025-14 M
<-> L 2006 1.517 0.014 0.032 1025-15 X-226
<->M 2006 1.602 0
0 2-1025-16 N
<-> X-226 2006 1.602 0.004 0.010 1025-17 0
<-> N 2006 1.517 0.005 0.012 2-1025-18 P
<-> 0 2006 1.602 0
0 j
2-1025-19 P
Q 2737 2.186 0
0.001 1
. ~. - 10 2 5 - 2 C
<-> B 629.6 0.476 0.002 0.005 2-1025-20 Q
R 2737 2,07 0.009 0.022 2-1025-21 R
X-224B 2737 2.186 0
0 i
2-1025-22 X-225
<-> X-224B 1263 1.008 0.002
'O.005 2-1025-23 S
<-> X-225 1263 1.008 0
0.002 2-1025-24 T
<-> S 1263 0.955 0.003 0.006 2-1025-25 X-224A
<-> T 1263 1.008 0.002 0.004 2-1025-26 U
<-> X-224A 5263 4.203 0.001 0.003 2-1025-27 V
<-> U 5263 3.98 0.033 0.077 2-1025-28 A
<-> V 5263 4.203 0.002 0.004 2-1025-3 D
<-> C 629.6 0.503 0
0 2-1025-4 D
E 3994 3.191 0
0.002 2-1025-5 E
F
. 3994 3.021 0.021 0.050 2-1025-6 F
X-223A 3994 3.191 0
0.002 2-1025-7 X-223A G
3994 3.191 0.008 0.019 2-1025-8 G
H 3994 3.021 0.015 0.034 1025-9 H
X-223B 3994 3.191 0.024 0.055 h
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi 1.
Attachment B Page BH
~ _ - - _. ~
LINEUP PIPELINES CASE-3 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 l
epm ft/sec psi a ft l
2-1318-1 X-226 Red 13 closed 0
0 0
2-1401-1 X-224A Teel 4A 4000 5.496 (1.142
)
1.219 2-1401-2 Teel 4A Red 14A 4000 5.496 0.021 0.050 2-1401-3 Red 14A Suc14A 4000 7.032 0.002 0.005 2-1402-1 X-224B Teel 4B 4000 5.496 (1.145
)
1.213 l
2-1402-2 Teel 4B Red 14B 4000 5.496 0.021 0.048 2-1402-3 Red 14B Suc14B 4000 7.032 0.003 0.007 2-2302-1 X-225 Red 23-1 closed 0
0 0
LA-1 X-204A ZA 4633 5.609 (3.812
)
1.251
--- strainer --- dP:
0.536
--- Hl:
1.245 LA-2 ZA A
4633 5.111 (0.286
)
0.335 LB-1 X-204B ZB 4624 5.598 (3.814
)
1.246
--- strainer --- dP:
0.534
--- Hl:
1.24 LB-2 ZB D
4624 5.102 (0.287
)
0.334 LC-1 X-204C ZC 0
0 0
0
--- strainer --- dP:
--- El:
LC-2 ZC K
0 0
0 0
LD-1 X-204D ZD 4743 5.742 (3.787
)
1.311 strainer --- dP:
0.562
--- Hl:
1.305 LD-2 ZD P
4743 5.233 (0.279
)
0.351 j
Pmp10A Suc10A Dis 10A closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10B Suc10B Dis 10B closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10C Suc10C Dis 10C closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10D Suc10D Dis 10D closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp14A Suc14A Dis 14A closed 0
0 0
--- CS Pump --- dP:
--- Hl:
Pmp14B Suc14B Dis 14B closed 0
0 0
--- CS Pump --- dP:
--- Hl:
l l
l
~
i l
t t
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi,1. Anaciunent B Page Bt5'
(
~.
~-..
l Comp ny: Comed CA&E-4 j
Projset:
09/25/98 by: Doug Collins il' LINEUP REPORT rev: 09/25/98 LINELIST: ECCS DEVIATION: 0.000169 %
dated: 09/24/98 after: 6 iterations 3/2 Unthrottled Case: 3 RHR pump @ 5000 gpm and 2 CS pump 6 4500 9Pm volumetric flow rates require constant fluid properties in all pipelines.
Fluid properties in the first specification were used.
NODE DEMAND NODE DEMAND l
epm gpm i
l Suc10B 5000 Suc10C 5000 Suc10D 5000 Suc14A
>>> 4500 Suc14B 4500 FLOWS IN: 0 gpm FLOWS OUT: 24000 gpm NET FLOWS OUT: 24000 gpm l
PIPELINE FLOW PRESSURE SET gpm SOURCE psia LA-1 7957 X-204A 0
LB-1 8005 X-204B 0
LD-1 B038 X-204D 0
FLOWS IN: 24000 gpm FLOWS OUT: 0 gpm NET FLOWS IN: 24000 gpm I
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev-1.
Attachment B Page BW
_.... _..... _ = - _.
LINEUP NODES CASE-4 09/25/98 NODE-ELEFATION DEMAND PRESSURE H GRADE ft gpm psi a ft l
f l
A 559.5 2.767 565.9
)
B 559.5 2.767 565.9 C
559.5 2.747 565.9
]
D.
559.5.
2.743 565.9 E
559.5 2.737 565.9 F
559.5 2.609 565.6 G
559.5 2.591 565.5 H
559.5 2.568 565.5
)
I 559.5 2.532 565.4 J
559.5 2.564 565.5 K-559.5 2.566 565.5 L
559.5 2.591 565.5 M
559.5 2.669 565.7 N
559.5 2.695 565.8 O
559.5 2.725 565.8 P
559.5 2.726 565.P Q
559.5 2.726 565.8 R
559.5 2.714 565.8 Red 10A 562.25 1.18 565 Red 10B 562.25 0.254 562.8 Red 14A 555.63 3.698 564.2 JRed14B 555.63 3.694 564.2 S
559.5 2.717 565.8 Suc10A 555.58 4.054 565 Suc10B 555.58
> 5000 2.001 560.2 Suc10C 555.58
> 5000 1.111 558.2 Suc10D 555.58
> 5000 2.051 560.3 Suc14A 555.63
> 4500 3.695 564.2 Suc14B 555.63
> 4500 3.69 564.2 T
559.5 2.72 565.8
- iee10A-1 562.25 1.18 565 Tee 10A-2 557.08 3.407 565 Tee 10B-1 562.25 0.390 563.2 Tee 10B-2 556.75 2.421 562.4 Tee 10C-2 556.79 1,48 560.2 l
Tee 10D-2 556.92 2.369 562.4 Teel 4A 555.63 3.725 564.3 Teel 4B 555.63 3.72 564.3
.U 559.5 2.724 565.8 i
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Revi.1. Attachment B Page Br1
._-._m.
m.
LINEUP NODES CASE-4 09/25/98 1
NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft l
i 1
V 559.5_
2.765 565.9 X-204A 570.6 p 0 570.6 X-204B.
570.6 p 0 570.6 1
X-204C 570.6
- -2.216 565.5 X-204D 570.6 p'
O 570.6 X-223A 559.5 2.604 565.5 X-223B 559.5 2.53 565.4 I
-X-224A.
559.5 2.722 565.9 X-224B 559.5 2.713 565.8 X-225 559.5 2.716 565.8 X-226 559.5 2.67 565.7
-ZA 560.5 2.762 566.9 2.743 566.9 ZB 560.5 ZC 560.5 2.135 565.5 ZD 560.5 2.73 566.8 4
i t
1 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Atuchment B Page BlB
l LINEUP PIPELINES CASE-4 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/sec psi a ft 2-1015A-1 X-223A Tee 10A-1 5000 3.781 1.424 0.554 2-1015A-2 Tee 10A-1 Red 10A 0
0 0
0 2-1015B-1 X-223B Tee 10B-1 10000 7.563 2.14 2.217 l
2-1015B-2 Tee 10B-1 Red 10B 5000 3.781 0.137 0.318 2-1016A-1 Red 10A Tee 10A-2 0 0
0 0
2-1016A-2 Tee 10A-2 Suc10A 0
0 0
0 l
2-1016B-1 Tee 10A-1 Tee 10B-2 5000 11.64 (1.24
)
2.621 l
2-1016B-2 Tee 10B-2 Suc10B 5000 11.64 0.419 2.143 2-1016C-1 Red 10B Tee 10C-2 5000 11.64 (1.226
)
2.614 l
2-1016C-2 Tee 10C-2 Suc10C 5000 11.64 0.368 2.065 2-1016D-1 Tee 10B-1 Tee 10D-2 5000 11.64 (1.978
)
0.738 2-1016D-2 Tee 10D-2 Suc10D 5000 11.64 0.318 2.077 2-1025-1 A
B 2045 1.633 0
0 2-1025-10 I
<-> X-223B 4950 3.954 0.001 0.003 2-1025-11 J
<->I 4950 3.744 0.032 0.075 j
2-1025-12 K
<->J 4950 3.954 0.001 0.003 2-1025-13 L
<-> K 4950 3.954 0.025 0.059 2-1025-14 M
<-> L 4950 3.744 0.078 0.180 l
2-1025-15 X-226
<-> M 4950 3.954 0.001 0.003 2-1025-16 N
<-> X-226 4950 3.954 0.025 0.059 2-1025-17 O
<->N 4950 3.744 0.029 0.068 l
2-1025-18 P
<-> O 4950 3.954 0.001 0.003 2-1025-19 P
Q 3087 2.466 0
0.001 2-1025-2 B
C 2045 1.546 0.020 0.046 2-1025-20 0
R 3087 2.335 0.012 0.028 2-1025-21 R
X-224B 3087 2.466 0
0.001 2-1025-22 X-225
<-> X-224B 1413 1.128 0.002 0.006 2-1025-23 S
<-> X-225 1413 1.128 0
0.002 2-1025-24 T
<-> S 1413 1.068 0.003 0.007 2-1025-25 X-224A
<-> T 1413 1.128 0.002 0.005 2-1025-26 U
<-> X-224A 5913 4.723 0.002 0.004 2-1025-27 V
<-> U 5913 4.472 0.041 0.096 2-1025-28 A
<-> V 5913 4.723 0.002 0.005 2-1025-3 C
D 2045 1.633 0.004 0.010 l
2-1025-4 D
E 10050 8.027 0.006 0.013
(
2-1025-5 E
F
_ 10050 7.601 0.128 0.298 2-1025-6 F
X-223A 10050 8.027 0.005 0.012 i
2-1025-7 X-223A G
5050 4.033 0.013 0.029 I
2-1025-8 G
H 5050 3.819 0.023 0.053 2-1025-9 H
X-223B 5050 4.033 0.038 0.087 1
PIPE-FLO rev 4.11 Calc..No. QDC-1000-M-0535, Rev; 1-
.Anachment B Page B R
LINEUP PIPELINES CASE-4 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/sec psi a ft 2-1318-1 X-226 Red 13 closed 0
0 0
2-1401-1 X-224A Tee 14A 4500 6.183 (1.003
)
1.542 2-1401-2 Teel 4A Red 14A 4500 6.183 0.027 0.063 2-1401-3 Red 14A Suc14A 4500 7.911 0.003 0.006 2-1402-1 X-224B Tee 14B 4500 6.183 (1.007
)
1.533 2-1402-2 Teel 4B Red 14B 4500 6.183 0.026 0.061 2-1402-3 Red 14B Suc14B 4500 7.911 0.004 0.009 2-2302-1 X-225 Red 23-1 closed 0
0 0
LA-1 X-204A ZA 7957 9.634 (2.762
)
3.688
--- strainer --- dP:
1.582
--- Hl:
3.672 LA-2 ZA A
7957 8.779 (0.005
)
0.988 LB-1 X-204B ZB 8005 9.692 (2.743
)
3.733
--- strainer --- dP:
1.601
--- Hl:
3.717 LB-2 ZB D
8005 8.832 0
1 LC-1 X-204C ZC 0
0
.0 0
--- strainer --- dP:
--- Hl:
LC-2 ZC K
0 0
0 0
LD-1 X-204D ZD 8038 9.731 (2.73
)
3.763 i
--- strainer --- dP:
1.614
--- Hl:
3.747 LD-2 ZD P
8038 8.868 0.004 1.009 Pmp10A Suc10A Dis 10A closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10B Suc10B Dis 10B closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10C Suc10C Dis 10C closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10D Suc10D Dis 10D closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp14A Suc14A Dis 14A closed 0
0 0
--- CS Pump --- dP:
--- Hl:
Pmp14B Suc14B Dis 14B closed 0
0 0
--- CS Pump --- dP:
--- Hl:
h PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Atuchment B Page BLO
Company: Comed CASE-5 Proj6ct:
09/25/98 by: Doug. Collins LINEUP REPORT rev: 09/25/98 LINELIST: ECCS DEVIATION: 5.55e-005 %
dated: 09/24/98 after: 7 iterations 3/2 Throttled Case: 3 RHR pump @ 3000 gpm and 2 CS pump @ 4000 gpm Volumetric flow rates require constant fluid properties in all pipelines.
Fluid properties in the first specification were used.
NODE DEMAND NODE DEMAND gpm gpm Suc10B
>>> 3000 Suc10C 3000 Suc10D
>>> 3000 Suc14A
>>> 4000 Suc143
>>> 4000 FLOWS IN: 0 gpm j
FLOWS OUT: 17000 gpm NET FLOWS OUT: 17000 gpm l
PIPELINE FLOW PRESSURE SET gpm SOURCE psia j
LA-1 5640 X-204A 0
LB-1 5647 X-204B 0
LD-1 5712 X-204D 0
FLOWS IN: 16999 gpm FLOWS OUT: 0 gpm NET FLOWS IN: 16999 gpm J
I PIPE-FLO'rev 4.11 Calc.. No. QDC-1000-M-0535, Rev 1.
Attachment B Page B2.l
~ -
LINEUP NODES
- CASE - 5 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft A
559.5 3.769 568.2 B
559.5 3.769 568.2 C
559.5 3.767 568.2 D
559.5 3.767 568.2 E
559.5 3.765 568.2 F
559.5 3.714 568.1 G
559.5 3.706 568.1 H
559.5 3.697 568.1 I
559.5 3.681 568 J
559.5 3.692 568.1 K
559.5 3.692 568.1 L
559.5 3.7 568.1 M
559.5 3.725 568.1 N
559.5 3.733 568.2 0
559.5 3.743 568.2 P
559.5 3.743 568.2 Q
559.5 3.743 568.2 R
559.5 3.732 568.2 Red 10A 562.25 2.44 567.9 Red 10B 562.25 2.101 567.1 l
Red 14A 555.63 4.857 566.9 Red 14B 555.63 4.855 566.9 S
559.5 3.733 568.2 Suc10A
$55.58 5.314 567.9 Suc10B 555.58
> 3000 4.573 566.2 Suc10C 555.58
> 3000 4.247 565.4 Suc10D 555.38
> 3000 4.585
,566.2 Suc14A 555.63
> 4000 4.854 566.9 Suc14B 555.63
> 4000 4.852 566.9 T
559.5 3.735 568.2 Tee 10A-1 562.25 2.44 567.9 Tee 10A-2 557.08 4.668 567.9 Tee 10B-1 562.25 2.151 567.2 Tee 10B-2 556.75 4.403 567 Tee 10C-2 556.79 4.048 566.2 Tee 10D-2 556.92 4.332 567 Teel 4A 555.63 4.878 567 Teel 4B 555.63 4.876 966.9 U
559.5 3.738 568.2 h
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Attachment B Page B2.2.
. -. ~ - - _ _ -..
..~... - -.. -...
. -.. ~.
LINEUP NODES
-CAS E - 5 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft j
V 559.5 3.768 568.2 X-204A 570.6 p
0 570.6 X-204B 570.6 p
0 570.6 X-204C 570.6
- -1.09 568.1 X-204D 570.6 p
0 570.6 X-223A 559.5 3.712 568.1
'X-223B 559.5 3.681 568 X-224A 559.5 3.736 568.2 X-224B 559.5 3.731 568.2 X-225 559.5 3.733 568.2 X-226 559.5 3.726 568.1 ZA 560.5 3.553 568.7 ZB 560.5 3.551 568.7 ZC 560.5 3.261 568.1 ZD 56df5 3.532 568.7 i
i a
1 4
f PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Attachment B Page BD
_m.
LINEUP PIPELINES
- CASE-5 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1015A-1 X-223A Tee 10A-1 3000 2.269 1.271 0.201 2-1015A-2 Tee 10A-1 Red 10A 0
0 0
0 2-1015B-1 X-223B Tee 10B-1 6000 4.538 1.53 0.802 l
2-1015B-2 Tee 10B-1 Red 10B 3000 2.269 0.049 0.115 2-1016A-1 Red 10A Tee 10A-2 0 0
0 0
2-1016A-2 Tee 10A-2 Suc10A 0
0 0
0 2-1016B-1 Tee 10A-1 Tee 10B-2 3000 6.986 (1.963
)
0.944 I
2-1016B-2 Tee 10B-2 Suc10B 3000 6.986 (0.170
)
0.777 2-1016C-1 Red 10B Tee 10C-2 3000 6.986 (1.946
)
0.942 j
~
2-1016C-2 Tee 10C-2 Suc10C 3000 6.986 (0.199
)
0.747 2-1016D-1 Tee 10B-1 Tee 10D-2 3000 6.986 (2.181
)
0.268 2-1016D-2 Tee 10D-2 Suc10D 3000 6.986 (0.253
)
0.752 n
2-1025-1 A
B 603.3 0.482 0
0 2-1025-10 I
> X-223B 2749 2.196 0
0.001 2-1025-11' J
-> I 2749 2.079 0.011 0.024 2-1025-12 K
<-> J 2749 2.196 0
0.001 2-1025-13 L
<-> K 2749 2.196 0.008 0.018 2-1025-14 M
> L 2749 2.079 0.025 0.058 2-1025-15 X-226
<-> M 2749 2.196 0
0.001 2-1025-16 N
> X-226 2749 2.196.
0.008 0.018
'^
2-1025-17 O
<-> N 2749 2.079 0.010 0.022 1025-18 P
<-> 0 2749 2.196 0
0.001 2-1025-19 P
Q 2963 2.367 0
0.001 2-1025-2 B
C 603.3 0.456 0.002 0.005 2-1025-20 Q
R 2963 2.241 0.011 0.025 2-1025-21 R
X-224B 2963 2.367 0
0.001 2-1025-22 X-225
<-> X-224B 1037 0.828 0.001 0.003 2-1025-23 S
<-> X-225 1037 0.828 0
0.001 2-1025-24 T
<-> S 1037 0.784 0.002 0.004 i
2-1025-25 X-224A
> T 1037 0.828 0.001 0.003 2-1025-26 U
<-> X-224A 5037 4.023 0.001 0.003 2-1025-27 V
> U 5037 3.81 0.030 0.071 3
2-1025-28 A
<- > V 5037 4.023 0.002 0.004 2-1025-3 C
D 603.3 0.482 0
0 2-1025-4 D
E 6251 4.992 0.002 0.005 2-1025-5 E
F 6251 4.727 0.051 0.118 2-1025-6 F
X-223A 6251 4.992 0.002 0.005 2-1025-7 X-223A G
3251 2.596 0.005 0.012 j
2-1025-8 G
H 3251 2.458 0.010 0.023 2-1025-9 H
X-223B 3251 2.596 0.016
~0.036 i
PIPE-FLO.rev 4.11 Calc. No. QDC-1000-M-0535, Rev$
1.
Attachment B Page B14 a-M" T'
t
~*
$ u s
u-
LINEUP PIPELINES CASE-5 09/25/98 PIPELINE FROM TO FLOW VEL dP H1
-m ft/see psi a ft 2-1318-1 X-226 Red 13 0
0 0
2-1401-1 X-224A Teel 4A 4G00 5.496 (1.142
)
1.219 2-1401-2 Tee 14A Red 14A 4000 5.496 0.021 0.050 2-1401-3 Red 14A Suc14A 4000 7.032 0.002 0.005 2-1402-1 X-224B Tee 14B 4000 5.496 (1.145
)
1.213 2-1402-2 Teel 4B Red 14B 4000 5.496 0.021 0.048 2-1402-3 Red 14B Suc14B 4000 7.032 0.003 0.007 2-2302-1 X-225 Red 23-1 closed 0
0 0
LA-1 X-204A ZA 5640 6.829 (3.553
)
1.853
--- strainer --- dP:
0.795
--- Hl:
1.845 LA-2 ZA A
5640 6.223 (0.217
)
0.497 LB-1 X-204B ZB 5647 6.837 (3.551
)
1.d58 i
--- strainer --- dP:
0.797
--- Hl:
1.85 LB-2 ZB D
5647 6.23 (0.216
)
0.498 LC-1 X-204C ZC 0
0 0
0
--- strainer --- dP:
--- Hl:
LC-2 ZC K
0 0
0 0
LD-1 X-204D ZD 5712 6.916 (3.532
)
1.901 strainer --- dP:
0.815
--- Hl:
1.893 LD-2 ZD P
5712 6.302 (0.211
)
0.510 Pmp10A Suc10A Dis 10A closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10B Suc10B Dis 10B closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10C Suc10C Dis 10C closed 0
0
--- RHR Pump --- dP:
--- Hl:
Pmp10D Suc10D Dis 10D closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp14A Suc14A Dis 14A closed 0
0 0
--- CS Pump --- dP:
--- Hl:
Pmp14B Suc14B Dis 14B closed 0
0 0
--- CS Pump --- dP:
--- Hl:
i PIPE-FLO rev 4.11 Calc.'No. QDC-1000.M-0535, Rev.
1.
Attachment B Page B15'
~
~
Comp:ny: Comed CASE-6 Projsct:
09/25/98 by: Doug CollinD l
LINEUP REPORT rev: 09/25/98 l
LINELIST: ECCS DEVIATION: 0.000114 %
dated: 09/24/98 after: 6 iterations j
4/2 Nominal Case: 4 RHR pump @ 5000 gpm and 2 CS pump @ 4500 gpm Volumetric flow rates require constant fluid properties in all pipelines.
l Fluid properties in the first specification were used.
1 j
NODE DEMAND NODE DEMAND l
9Pm gpm l
Suc10A 5000 Suc10B 5000 Suc10C 5000 Suc10D 5000 Suc14A
>>> 4500 S,tc14B 4500 l
FLOWS IN: 0 gpm TLOWS OUT: 29000 gpm NET FLOWS OUT: 29000 gpm 1
PIPELINE FLOW PRESSURE SET gpm SOURCE psia LA-1 9603 X-204A 0
LB-1 9734
<<< X-204B 0
LD-1 9663 X-204D 0
FLOWS IN: 29000 gpm FLOWS OUT: 0 gpm l
NET FLOWS IN: 29000 gpm l
1 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Attachment B Page B2f.
1 I
LINEUP NODES CASE-6 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft A
559.5 1.848 563.8 B
559.5 1.847 563.8 C
559.5 1.782 563.6 D
559.5 1.767 563.6 E
559.5 1.757 563.6 F
559.5 1.527 563 l
G 559.5 1.512 563 1
H 559.5 1.5 563 I
559.5 1.484 562.9 J
559.5 1.538 563.1 1
K 559.5 1.541 563.1 I
L 559.5 1.584 563.2 M
559.5 1.714 563.5 N
559.5 1.759 563.6 0
559.5 1.808 563.7 P
559.5 1.811 563.7 Q
559.5 1.81 563.7 R
559.5 1.798 563.7 Red 10A 562.25
- -0.751 560.5 Red 10B 562.25
- -0.795 560.4 Red 14A 555.63 2.78 562.1 Red 14B 555.63 2.777 562.1 S
559.5 1.8 563.7 Suc10A 555.58
> 5000 0.773 557.4 Suc10B 555.58
> 5000 0.205
'556.1 Suc10C 555.58
> 5000 0.062 555.7 Suc10D 555.58
> 5000 1.002 557.9 Suc14A 555.63
> 4500 2.778 562.1 Suc14B 555.63
> 4500 2.773 562.1 T
559.5 1.802 563.7 Tee 10A-1 562.25
- -0.658 560.7 Tee 10B-2 556.75 0.624 558.2 Tee 10C-2 556.79 0.431 557.8 Tee 10D-2 556.92 1.32 560 Teel 4A 555.63 2.807 562.1 Tee 14B 555.63 2.804 562.1 U
559.5 1.806 563.7 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev. 1 Attachment B Page B2.1
LINEUP NODES.
-CASE-6 09/25/98' NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft V
559.5 1.846 563.8 X-204A 570.6 p
0 570.6 X-204B 570.6 p
0 570.6 X-204C 570.6
- -3.241 563.1 X-204D 570.6 p 0 570.6 X-223A 559.5
- - 1.518 563 X-223B 559.5 1.482 562.9 X-224A 559.5 1.804 563.7
. 559.5 1.797 563.7 X-224B X-225 559.5 1.799 563.7 i
1 X-226 559.5 1.716 563.5 ZA 560.5 2.037 565.2 ZB 560.5 1.973 565.1 ZC 560.5 1.11 563.1 ZD 560.5 2.008 565.2 v
9 I
9 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Attachment B Page B28
LINEUP PIFELINES CASE-6 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a f:
2-101SA-1 X-223A Tee 10A-1 10000 7.563 2.134 2.204 2-1015A-2 Tee 10A-1 Red 10A 5000 3.781 0.135 0.313 2-1015B-1 X-223B Tee 10B-1 10000 7.563 2.14 2.217 2-1015B-2 Tee 10B-1 Red 10B 5000 3.781 0.137 0.318 2-1016A-1 Red 10A Tee 10A-2 5000 11.64 (1.839
)
0.901 2-1016A-2 Tee 10A-2 Suc10A 5000 11.64 0.315 2.232 2-1016B-1 Tee 10A-1 Tee 10B-2 5000 11.64 (1.24
)
2.621 2-1016B-2 Tee 10B-2 Suc10B 5000 11.64 0.419 2.143 2-1016C-1 Red 10B Tee 10C-2 5000 11.64 (1.226
)
2.614 2-1016C-2 Tee 10C-2 Suc10C 5000 11.64 0.368 2.065 2-1016D-1 Tee 10B-1 Tee 10D-2 5000 11.64 (1.978
)
0.738 2-1016D-2 Tee 10D-2 Suc10D 5000 11.64 0.318 2.077 2-1025-1 A
B 3804 3.038 0
0.002 2-1025-10 I
<-> X-223B 6462 5.162 0.002 0.005 2-1025-11 J
<-> I 6462 4.887 0.054 0.126 2-1025-12 K
<-> J 6462 5.162 0.002 0.006 2-1025-13 L
<-> K 6462 5.162 0.043 0.101 I
2-1025-14 M
<-> L 6462 4.887 0.130 0.302 2-1025-15 X-226
<-> M 6462 5.162 0.002 0.005 2-1025-16 N
<-> X-226 6462 5.162 0.043 0.100 2-1025-17 0
<->N 6462 4.887 0.049 0.114 2-1025-18 P
<-> 0 6462 5.162 0.002 0.006 2-1025-19 P
Q 3201 2.557 0
0.001 2-1025-2 B
C 3804 2.877 0.065 0.151 2-1025-20 Q
R 3201 2.421 0.013 0.029 2-1025-21 R
X-224B 3201 2.557 0
O.001 2-1025-22 X-225
<-> X-224B 1299 1.038 0.002 0.005 2-1025-23 S
<-> X-225 1299 1.038 0
0.002 2-1025-24 T
<-> S 1299 0.983 0.003 0.006 2-1025-25 X-224A
<-> T 1299 1.038 0.002 0.004 i
2-1025-26 U
<-> X-224A 5799 4.632 0.002 0.004 2-1025-27 V
<-> U 5799 4.386 0.040 0.093 2-1025-28 A
<-> V 5799 4.632 0.002 0.005 2-1025-3 C
D 3804 3.038 0.015 0.035 2-1025-4 D
E 13538 10.81 0.010 0.024 2-1025-5 E
F 13538 10.24 0.230 0.533 2-1025-6 F
X-223A 13538 10.81 0.009 0.021 2-1025-7 X-223A G
3538 2.826 0.006 0.015 2-1025-B G
H 3538 2.676 0.012 0.027 2-1025-9 H
X-223B 3538 2.826 0.019 0.043 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Attachment B Page B2.'f
LINEUP PIPELINES CASE-6 09/25/98 I
PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft i
2-1318-1 X-226 Red 13 closed 0
0 0
2-1401-1 X-224A Teel 4A 4500 6.183 (1.003
)
1,542 2-1401-2 Tee 14A Red 14A 4500 6.183 0.027 0.063 l
2-1401-3 Red 14A Suc14A 4500 7.911 0.003 0.006 2-1402-1 X-224B Tee 14B 4500 6.183 (1.007
)
1.533 2-1402-2 Teel 4B Red 14B 4500 6.183 0.026 0.061 j
2-1402-3 Red 14B Suc14B 4500 7.911 0.004 0.009 2-2302-1 X-225 Red 23-1 closed 0
0 0
l LA-1 X-204A ZA 9603 11.63 (2.037
)
5.371 l
--- strainer --- dP:
2.304
--- Hl - 5.349 LA-2 ZA A
9603 10.59 0.189 1.439 l
l LB-1 X-204B ZB 9734 11.79 (1.973
)
5.519 l
--- strainer --- dP:
2.368
--- Hl:
5.496 LB-2 ZB D
9734 10.74 0.206 1.479 LC-1 X-204C ZC 0
0 0
0
--- strainer --- dP:
' --- Hl:
LC-2 ZC K
0 0
0 0
LD-1 X-204D ZD 9663 11.7 (2.008
)
5.439
--- strainer --- dP:
2.333
--- Hl:
5.416 LD-2 ZD P
9663 10.66 0.197 1.457 Pmp10A Suc10A Dis 10A closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
.j Pmp10B Suc10B Dis 10B closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10C Suc10C Dis 10C closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10D
.Suc10D Dis 10D closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp14A Suc14A Dis 14A closed 0
0 0
--- CS Pump --- dP:
--- Hl:
Pmp14B Suc14B Dis 14B closed 0
0 0
--- CS Pump --- dP:
--- Hl:
i l
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Anacknent B Page B30
= - -
Company: Comed CASE-7 Project:
09/25/98 by: Doug Collina LINEUP REPORT rev: 09/25/98 LINELIST: ECCS DEVIATION: 2.01c-005 %
dated: 09/24/98 after: 7 iterations l
4/2 Throttled Case: 4 RHR pump @ 3000 gpm and 2 CS pump 6 4000 epm volumetric flow rates require constant fluid properties in all pipelines.
Fluid properties in the first specification were used.
NODE DEMAND NODE DEMAND 9Pm gpm Suc10A 3000 Suc10B 3000 Suc10C 3000 Suc10D 3000 Suc14A 4000 Suc14B 4000 FLOWS IN: 0 gpm FLOWS OUT: 20000 gpm NET FLOWS OUT: 20000 gpm PIPELINE FLOW PRESSURE SET gpm SOURCE psia LA-1 6635 X-204A 0
LB-1 6675 X-204B 0
LD-1 6f90 X-204D 0
FLOWS IN: 20000 gpm FLOWS OUT: 0 gpm NET FLOWS IN: 20000 gpm
.i PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Armchmen: B Page BSI
4 LINEUP NODES CASE-7 l
09/25/98 i
NODE ELEVATION DEMAND PRESSURE H GRADE l
ft gpm psi a ft 4
i A
559.5 3.381 567.3 l
B' 559.5 3.381 567.3 l
1 C
559.5 3.367 567.3 D
559.5 3.364 567.3 1
E 559.5 3.36 567.3 i
F 559.5 3.27 567.1 G
559.5 3.264 567.1 l
H 559.5 3.258 567.1 1
I 559.5 3.251 567 J
559.5 3.269 567.1 K
559.5 3.27 567.1 L
559.5 3.283 567.1 M
559.5 3.326 567.2 N
559.5 3.341 567.3 0
559.5 3.357 567.3 I
P 559.5 3.358 567.3 Q
559.5 3.357 567.3 R
559.S 3.345 567.3 Red 10A 562.25 1.69 566.2 Red 10B 562.25 1.671 566.1 Red 14A 555.63 4.469 566 Red 14B 555.63 4.469 566 S
559.5 3.346 567.3 Suc10A 555.58
> 3000 4.074 565
-Suc10B 555.58
> 3000 3.871 564.6 Suc10C 555.58
> 3000-3.816 564.4 Suc10D 555.58
> 3000 4.154 565.2
]
Suc14A 555.63
> 4000 4.467 566 Suc14B 555.63
> 4000 4.466 566 T
559.5 3.348 567.3 Tee 10A-1 562.25 1.739 566.3 Tee 10A-2 557.08 3.776 565.8 l
Tee 10B-1 562.25 1.72 566.2 Tee 10B-2 556.75 3.701 565.3 Tee 10C-2 556.79 3.617 565.2
{
Tee 10D-2 556.92
~
3.901 566 i
Teel 4A 555.63 4.491 566.1 Teel 4B 555.63 4.49 566.1 4
U 559.5 3.35 567.3 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Attachment B Page B32.
1 LINEUP NODES CASE-7 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft V
559.5 3.38 567.3 X-204A 570.6 p 0 570.6 X-204B 570.6 p 0 570.6 X-204C 570.6
- -1.512 567.1 X-204D 570.6 p 0 570.6
'X-223A 559.5 3.267 567.1 J
X-223B 559.5 3.25 567
-X-224A 559.5 3.349 567.3 1
X-224B 559.5 3.345 567.3
)
X-225 559.5 3.346 567.3 X-226 559.5 3.327 567.2 ZA
-560.5 3.246 568 ZB 560.5 3.233 568 ZC 560.5 2.839 567.1 ZD 560.5 3.228 568 1
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Attachment B Page BB
LINEUP PIPELINES
- CAS E - 7 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1015A-1 X-223A Tee 10A-1 6000 4.538 1.528 0.797 2-1015A-2 Tee 10A-1 Red 10A 3000 2.269 0.049 0.113 2-1015B-1 X-223B Tee 10B-1 6000 4.538 1.53 0.802 2-1015B-2 Tee 10B-1 Red 10B 3000 2.269 0.049 0.115 2-1016A-1 Red 10A Tee 10A-2 3000 6.986 (2.086
)
0.328 2-1016A-2 Tee 10A-2 Suc10A 3000 6.986 (0.298
)
0.808 l
2-1016B-1 Tee 10A-1 Tee 10B-2 3000 6.986 (1.963
)
0.944 2-1016B-2 Tee 10B-2 Suc10B 3000 6.986 (0.170
)
0.777 2-1016C-1 Red 10B Tee 10C-2 3000 6.986 (1.946
)
0.942 I
2-1016C-2 Tee 10C-2 Suc10C 3000 6.986 (0.199
)
0.747 2-1016D-1 Tee 10B-1 Tee 10D-2 3000 6.986 (2.181
)
0.268 2-1016D-2 Tee 10D-2 Suc10D 3000 6.986 (0.253
)
0.752 2-1025-1 A
B 1689 1.349 0
0 2-1025-10 I
<-> X-223B 3636 2.904 0
0.002 2-1025-11 J
<->I 3636 2.75 0.018 0.042 2-1025-12 K
<->J 3636 2.904 0
0.002 2-1025-13 L
<-> K 3636 2.904 0.014 0.032 2-1025-14 M
<-> L 3636 2.75 0.043 0.099 2-1025-15 X-226
<->M 3636 2.904 0
0.002 2-1025-16 N
<-> X-226 3636 2.904 0.014 0.032 2-1025-17 O
<->N 3636 2.75 0.016 0.038 2-1025-18 P
<-> 0 3636 2.904 0
0.002 2-1025-19 P
Q 3054 2.439 0
0.001 2-1025-2 B
C 1689 1.277 0.014 0.032 2-1025-20 Q
R 3054 2.31 0.012 0.027 2-1025-21 R
X-224B 3054 2.439 0
0.001 2-1025-22 X-225
<-> X-224B 946.1 0.756 0.001 0.003 2-1025-23 S
<-> X-225 946.1 0.756 0
0 2-1025-24 T
<->S 946.1 0.716 0.002 0.003 2 *025-25 X-224A
<-> T 946.1 0.756 0
0.002 2-1025-26 U
<-> X-224A 4946 3.951 0.001 0.003 2-1025-27 V
<-> U 4946 3.741 0.029 0.068 2-1025-28 A
<-> V 4946 3.951 0.001 0.003 2-1025-3 C
D 1689 1.349 0.003 0.007 2-1025-4 D
E 8364 6.68 0.004 0.009 2-1025-5 E
F
.8364 6.326 0.090 0.208 2-1025-6 F
X-223A 8364 6.68 0.004 0.008 2-1025-7 X-223A G
2364 1.888 0.003 0.007 2-1025-8 G
H 2364 1.788 0.005 0.013 l
2-1025-9 H
X-223B 2364 1.888 0.008 0.0.19 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev. 1 Attachment B Page BH
LINEUP PIPELINES CASE-7 09/25/98 i
PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1318-1 X-226 Red 13 closed 0
0 0
2-1401-1 X-224A Tee 14A 4000 5.496 (1.142
)
1.219 2-1401-2 Teel 4A Red 14A 4000 5.496 0.021 0.050 2-1401-3 Red 14A Suc14A 4000 7.032 0.002 0.005 2-1402-1 X-224B Tee 14B 4000 5.496 (1.145
)
1.213 2-1402-2 Teel 4B Rud14B 4000 5.496 0.021 0.048 2-1402-3 Red 14B Suc14B 4000 7.032 0.003 0.007 2-2302-1 X-225 Red 23-1 closed 0
0 0
LA-1 X-204A ZA 6635 8.033 (3.246
)
2.564
--- strainer --- dP:
1.1
--- Hl:
2.553 i
LA-2 ZA A
6635 7.32 (0.135
)
0.687 LB-1 X-204B ZB 6675 8.081 (3.233
)
2.596
--- strainer --- dP:
1.113
--- Hl:
2.584 LB-2 ZB D
6675 7.364 (0.131
)
0.696 LC-1 X-204C ZC 0
0 0
0 strainer --- dP:
--- Hl:
LC-2 ZC K
0 0
0 0
LD-1 X-204D ZD 6690 8.1 (3.228
)
2.607
--- strainer --- dP:
1.118
--- Hl:
2.596 LD-2 ZD P
6690 7.381 (0.130
)
0.699 Pmp10A Suc10A Dis 10A closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10B Suc10B Dis 10B closed 0
0 0
RHR Pump --- dP:
--- Hl:
Pmp10C Suc10C Dis 10C closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10D Suc10D Dis 10D closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp14A Suc14A Dis 14A closed 0
0 0
--- CS Pump --- dP:
--- Hl:
Pmp14B Suc14B Dis 14B closed 0
0 O
--- CS Pump --- dP:
--- Hl:
1 i
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev. 1 Atachment B Page B3r l
_m
____.m Company: Comed LONG-NEW Project:
09/25/98 by: Doug Collins LINEUP REPORT rev: 09/25/98 l
l LINELIST: LONG-NEW DEVIATION: 6.32e-005 %
l dated: 09/25/98 after: 9 iteraticas Design Basis Flow Case: 1 RHR pump @ 5000 gpm and 1 CS pump 6 4500 gpm volumetric flow rates require constant fluid properties in all pipe'.ines.
Fluid properties in the first specification were used.
l NODE DEMAND NODE DEMAND 9Pm gpm l
Suc10C 5000 Suc14B
>>> 4500 FLOWS IN: 0 gpm FLOWS OUT: 9500 gpm NET FLOWS OUT: 9500 gpm PIPELINE FLOW PRESSURE SET gpm SOURCE psia LA-1 2274 X-204A 0
LB-1 2277 X-204B 0
LC-1 2475 X-204C 0
LD-1 2474 X-204D 0
FLOWS IN: 9500 gpm FLOWS OUT: 0 gpm NET FLOWS IN: 9500 gpm l
l:
l 4
4 I
l PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Attachment B Page B%
LINEUP NODES LONG-NEW 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft A
559.5 3.813 568.4 l
l B
559.5 3.813 568.4 C
559.5 3.813 568.4 D
559.5 3.813 568.4 l
E 559.5 3.813 568.3 F
559.5 3.804 568.3 G
559.5 3.801 568.3 H
559.5 3.795 568.3 I
559.5 3.786 568.3 J
559.5 3.796 568.3 K
559.5 3.796 568.3 L
559.5 3.796 568.3 M
559.5 3.796 568.3 N
559.5 3.796 568.3 O
559.5 3.796 568.3 P
559.5 3.796 568.3 Q
559.5 3.796 568.3 R
559.5 3.788 568.3
-Red 10A 562.25 2.619 568.3 Red 10B 562.25 2.224 567.4 Red 14A 555.63 S.474 568.3 Red 14B 555.63 4.769 566.7 S
559.5 3.795 568.3 Suc10A 555.58 5.493 568.3 Suc10B 555.58 5.493 568.3 Suc10C 555.58
> 5000 3.082 562.7-Suc10D 555.58 5.234 567.7 Suc14A 555.63 5.474 568.3 Suc14B 555.63
> 4500 4.765 566.7
.T 559.5 3.802 568.3 Tee 10A-1 562.25 2.619 568.3 Tee 10A-2 557.08 4.846 568.3 Tee 10B 562.25 2.361 567.7 Tee 10B-2 556.75 4.989 568.3 Tee 10C-2 556.79 3.45 564.8 Tee 10D-2 556.92 4.657 567.7 Teel 4A 555.63 5.474 568.3 l
Teel 4B 555.63 4.795 566.8 L
U 559.5 3.807 568.3 PIPE-FLO rev 4.11 Calc. No QDC-1000-M-0535, Rev.
1.
Atachment B Page B37
LINEUP NODES LONG-NEW 09/25/98 NODE ELEVATION DEMAMD PRESSURE H GRADE ft gpm psi a ft i
V 559.5 3.813 568.4 1
X-204A' 568.6 p
0 568.6 X-204B 568.6 p
0 568.6 X-204C 568.6 p
0 568.6 X-204D 568.6 p
0-568.6 X-223A 559.5 3.804 568.3 l
X-223B 559.5 3.786 568.3 X-224A 559.5 3.807 568.3 X-224B 559.5 3.788 568.3 X-225 559.5 3.794 568.3 l
X-226 559.5 3.796 568.3 j
3.417 568.4 ZA 560.5 ZB 560.5 3.417 568.4 ZC 560.5 3.406 568.4 ZD 560.5 3.407 568.4 i
L PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Atuchment B Page B'38 l
I,
~.
_ -. _ _ =. - - - - - --
i LINEUP PIPELINES LONG-NEW 09/25/98 P2PELINE FROM TO FLOW VEL dP H1 9Pm ft/sec psi a f:
]
l l
2-1015A-1 X-223A Tee 10A-1 0 0
0 0
2-1015A-2 Tee 10A-1 Red 10A 0
0 0
0 l
l 2-1015B-1 X-223B Tee 10B-1 5000 3.781 1.425 0.558 2-1015B-2 Tee 10B-1 Red 10B 5000 3.781 0.137 0.318 2-10'5A-1 Red 10A Tee 10A-2 0 0
0 0
2-1016A-2 Tee 10A-2 Suc10A 0
0 0
0 2-1016B-1 Tee 10A-1 Tee 10B-2 0 0
0 0
l l
2-1016B-2 Tee 10B-2 Suc10B 0
0 0
0 l
l 2-1016C-1 Red 10B Tee 10C-2 5000 11.64 (1.226
)
2.614 2-1016C-2 Tee 10C-2 Suc10C 5000 11.64 0.368 2.065 2-1016D-1 Tee 10B-1 Tee 10D-2 0 0
0 0
2-1016D-2 Tee 10D-2 Suc10D 0
0 0
0 2-1025-1 A
B 166.1 0.133 0
0 2-1025-10 I
<-> X-223B 2557 2.042 0
0 2-1025-11 J
<-> I 2557 1.934 0.009 0.021 2-1025-12 K
<-> J 2557 2.042 0
0 2-1025 L
<-> K 82.17 0.066 0
0 2-1025-14 M
<-> L 82.17 0.062 0
0 2-1025-15 X-226
<-> M 82.17 0.066 0
0 2-1025-16 N
<-> X-226 82.17 0.066 0
0 2-1025-17 0
<-> N 82.17 0.062 0
0 2-1025-18 P
<-> 0 82.17 0.066 0
0 2-1025-19 P
Q 2392 1.91 0
0 2-1025-2 B
C 166.1 0.126 0
0 1
2-1025-20 Q
R 2392 1.809 0.007 0.017 2-1025-21 R
X-224B 2392 1.91 0
O 2-1025-22 X-225
<-> X-224B 2108 1.684 0.005 0.013 2-1025-23 S
<-> X-225 2108 1.684 0.002 "0.005 2-1025-24 T
<-> S 2108 1.594 0.007 0.016 2-1025-25 X-224A
<-> T 2108 1.684 0.005 0.011 2-1025-26 U
<-> X-224A 2108 1.684 0
0 2-1025-27 V
<-> U 2108 1.594 0.006 0.013 2-1025-28 A
<-> V 2108 1.684 0
0 2-1025-3 C
D 166.1 0.133 0
0 2-1025-4 D
E 2443 1.951 0
0 2-1025-5 E
F 2443 1.848 0.008 0.019 2-1025-6 F
X-223A 2443 1.951 0
0 2-1025-7 X-223A G
2443 1.951 0.003 0.007 1
2-1025-8 G
H 2443 1.848 0.006 0.013 l
2-1025-9 H
X-223B 2443 1.951 0.009 0 021 l
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0535, Rev. 1 Atmchment B Page B38
,1
LINEUP PIPELINES
-LONG-NEW l
09/25/98 PIPELINE FROM TO FLOW VEL dP H1 l
gpm ft/see psi a ft 2-1318-1 X-226 Red 13 closed 0
0 0
2-1401-1 X-224A Teel 4A 0
0 0
0 2-1401-2 Teel 4A Red 14A 0
0 0
0 2-1401-3 Red 14A Suc14A 0
0 0
0 1
2-1402-1 X-224B Tee 14B 4500 6.183 (1.207
)
1.533 2-1402-2 Teel 4B Red 14B 4500 6.183 0.026 0.061 2-1402-3 Red 14B Suc14B 4500 7.911 0.004 0.009 2-2302-1 X-225 Red 23-1 closed 0
0 0
LA-1 X-204A ZA 2274 2.753 (3.417
)
0.168 strainer --- dP:
0.072
--- Hl:
0.166 LA-2 ZA -
A 2274 2.509 (0.396
)
0.081 LB-1 X-204B ZB 2277 2.757 (3.417
)
0.168
--- strainer --- dP:
0.072
--- Hl:
0.167 LB-2 ZB D
2217 2.512 (0.396
)
0.081 l
LC-1 X-204C ZC 2475 2.996 (3.406
)
0.193
--- strainer --- dP:
0.082
--- Hl:
0.191 LC-2 ZC K
2475 2.73 (0.390
)
0.096 LD-1 X-204D ZD 2474 2.995 (3.407
)
0.193 strainer --- dP:
0.082
--- Hl:
0.191 LD-2 ZD P
2474 2.729 (0.390
)
0.096 Pmp10A Suc10A Dis 10A closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10B Suc10B Dis 10B closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10C Suc10C Dis 10C closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp10D Suc10D Dis 10D closed 0
0 0
--- RHR Pump --- dP:
--- Hl:
Pmp14A Suc14A Dis 14A closed 0
0 0
--- CS Pump --- dP:
--- Hl:
Pmp14B Suc14B Dis 14B closed 0
0 0
+
--- CS Pump --- dP:
--- Hl:
l l
PIPE-FLO'rev 4.11 Calc. No. QDC-1000-M-0535, Rev.
1.
Atmchment B Page Bio (i~inal
coxa g uanoon rugo..
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.Q_dc. Ao..G W L m A..95s. U w=I A S & " +~ C September 24, 1992 Ms.-Sharon Eldridge Commonwealth Edison Company Rural Route f 1 Dresden Nuclear Power Station Morris, IL 60450
Subject:
Dresden Units 2 & 3 - Post LOCA Pool Drawdown
References:
1)
Telecopy, J.C. Elliott to S. Mintz, 'Small Job Authorization," September 21, 1992. (Small Job Task Number DR127)
Dear Ms. Eldridge:
In response to your request and per Reference 1, this letter provides an estimate of the maximum reduction in the Dresden suppression pool level following a less of-coolant accident (LOCA). The maximum suppression pool level decrease during a LOCA for Dresden is estimated to be 2.1 feet. This pool level decrease is the same as the value estimated for Quad Cities previously. A comparison of the key parameters between Quad Cities and Dresden confirmed that these plants are essentially identical and therefore allows application of the Quad Cities pool level decrease estimate to Dresden. This pool level decrease can be used together with the lower Technical Specification limit on pool level to determine the minimum post-LOCA pool level.
This estimate of 2.1 feet pool level reduction post-LOCA is based on a conservative analysis of another BWR with a 251 inch 10 reactor pressure vessel and a Mark I containment. This analysis considered the water which may be transferred to the reactor pressure vessel, drywell and drywell-to-wetwell vent system from the suppression pool.during a LOCA. A more detailed calculation could be performed with the Dresden specific geometry, but it is not expected that the results would change significantly.
Documentation and evidence of verification of this letter is included in the GE design record file, DRF-T23 00692.
Sincerely, ll.Aff S. Mintz ~
cc:,GL J. E. Torbeck C. T. Young J. E.,Nash
%y C\\
,-.n.-
..., _ - - _. ~. ---- - - - ~ - -
- + - - - -
- - - - - - - - - - ^ ^ ~ - - ' ' " ' ' "1 FknMs COM ED DG FOUR FLOOR FOX NO.8 1639663F199 06-03*9P 93t92P r,g:
(a \\c.. Alo, GDC-1000 - Wi- 0535~ Re e. 4
/ gaffs,ent c' r
se marmt nintdy sw asse, Ca PLAVT PEWontAuct ANALYSIS N0JECTS January 25, 1993 To:
T. L. Chapman From: S. Mintz subject: Dresden LPC1/Centainment Coeling System Attachment I provides the responses to CICO questions requesP.ed by sharon Odridge (CECOT in connection to the Dresden LPCI/Cantainment coolies systes evaluaties. Please provide these responses to sbaren Ddridge of CECO.
Documentation and evidence of verificatten is contained in ORF-T23-685.
5.
cc J. F. Terbeck J. E. %sh C. T. Yo DRF-T23 g ass 4
4
~ _.
FDOMs COM ED DG FOUR FLOOR FAM NO.8 163000SP199 86-03-97+ el:92P P.02
]
Ccdc. No SDt.-/000-M-0535 Sv. /
ATTACMENT 1 gHkdmt C RESPONSE TO CECO QUEST 1cm i
j DRE5 DEN LpCI/CONTA! MENT COOLING SYSTEM EVALUATION Questien 1:
mat is the impact en the peak suppmssion peel temperature calcolated for case 4a of scE-no-as-loss of assuming initiation at 1800 Centainment Coeling Service Water (CCSW) f the ties of 600 J
seconds for containment cooling instead o i
seconds used for the GDE T19-26-1992 analysis?
Response te Question 1 kt is estimated that the peak suppression peel temperature for Case 4e of SSE -MS-t$-1093 will' tecrease by no more than 2'F to ne more then 18B'F. This temperature increase was estimated-i by detemistag the renewed by the LpC1/Costainment Caeltag system heat hetmean 400 end 1800 seconds for l
Case 4a. This energy was added to the suppression peel at the time of the peak ten peel temperature to detemine
.the lacrease in ths suppressien pool temperature.
l
)
It sheeld he noted that this tasperature increase is j
conservative since it is more representative of the increase in the peel temperature at 1000 seconds (1.e., at the new initiattee time for CCSU) them the lacrease to the peak pool l
temperature. Once CCSW is initiated this increase la the suppressten peel temperatum will.he reduced dos to the increased effectiveness of the heat eschanger with a higher 1
j suppression pool temperature.
l, Questian 1:
hat is the tapact of initiatten of CCEN at 1000 seceed (with
!l estimated increase in the suppressies peel temperature to 188'F) l en the containment pressere at the time of the peak suppressies j
pool temperature relative to the value given in Appendix 5 of Reference 1 for Case 4a7 i,
l
(
4 P
e C3 g
FROMt COM ED 08 FC 37199 86-83-97 S i t 5'2 P P.03 4
C ale.. No GDc - ! ** ?
535 "' I Ak % +C Response to $westien 2 2
At the time of the peak suppressies peel temperature the suppression chamber airspace temperature is very close to the water temperature of the containment sprays. A change in the peak suppression pool temperature of 2*F will produce a change 2
in tennerature of the spr4y water temperature of approximately 3
i l'F.
Themfers the suppression chamber airspace temperature will aise increase by this amount. The change la the suppressten chamber veper pressure for this ch in airspace temperature is apprezimately 0.1 psi. This is refore the estimated increase in the suppression chamber airspace pressure due to an increase is the suppressten Peel temperature of 2*F to i
188'F.
i
.It should be noted that this estimate conservatively neglects (with respect to minimizing the containment pressors the effects eF the increase is the drywell temperature an)d drywell vapor pressure with an increase la the suppressten pool tageraters. An increase in the drywell pressure would result in an addittenal lacrease in the suppmssion cheder. airspace pressung due to the flew th the suppressies chamber-to-drywell vacsua bre question 3:
What is the maximum drawdown expected for a LOCA for Dresden?
Response to Qeesties 3:
Referemen I reported a maximum draudeus of 2.1 feet for Dresden.
This was based en a cesservative application of peel drawdeun analyses raadneted for a range of break sizes for another plant with a 251 ind 10 reacter pressere vessel and a Mark I contalement. Housiver this anximus draudoun for breaks smaller than the DEA-LOCA would o(dich occurs only the LOCA (< 1000 seconds) when suppre)ssima peel temperatures are nly occur early in significantly cooler than the maximum pool temperature. During the times of peak suppression pool temperatures when NPSH is of greatest concern a maximum draudous of 1 feet is expected.
Questten 4:
What is the impact of using May-Witt er Alts 5.1 + 2a en the peak suppression pool temperature detensined for Case 4a of GDIE-770-26-19207 1
Pqa
. - - - -.. - ~,. - - - - -
06-03-97 et852P P.04 c alc. Na, Q DG-1000 -M -0535 /av. /
AOodvemt C m '9,~
Respessetolivestian4:
The 1spect of using May-Witt en the peak suppression peel temperature is est'asted based on a comparison of the decay heat near the time of the peak suppressten pool temperature. The basis for usleg this comparisen is that at the time of the peak suppression peel temperature the heat rejection rate to the supprussion peel fpen the reacter pressure vessel (RPV) is equal to the rate of contatement coelleg uhtch is itself established by the suppressten pool temperature. The peak suppression peel temperature for Case 4e escurs et approximately 30000 seconds.
The value of the Nay-Witt decay heat is approxiastaly 155 higher
'than the AN5 5.1 value at this time This would produce en tecrease of apgreximately 14*F la the peak suppressten wel temperature. Ina decay heat for AIIS 5.1 + at is less tian the May-Witt decay beat therefers the.iacrease with Alls 5.1 + at will he hounded by the 14*F tactueos estimated for the Nay-Witt 1
decay heat.
Referseces:
1)
'GE Report 8 DIE-770-26-1992, *0resdes IInclear peuer statten Units 2 and 3, LPC1/Containmaat Cooling System Evaluaties." llovember 1982.
1)
Letter, 5. Nintz to 3. Eldridte "Dresden Units t & 3. - post LOCA Draudeun.' September 24, 1992.
9 0
e e
W e
7qe. C!i M
Calc. No. QDC-1000-M-0535, Rsv.1.
Attachm:nt D Pcg2 D1 1
1 RHRICS Pump Pressure Requirements - Design Basis Case Old Design Basis New Design Basis Sec P
T Pv V
Hvap Hsuc NPSHR Req. OP Hsuc NPSHR Req. OP i
643 6.5 150.8 3.796 0.016347 8.94 7.62 30.0
-1.40 7.15 30.0
-1.20 1627 3.4 157.6 4.480 0.016382 10.57 7.62 30.0
-0.73 7.15 30.0
-0.53 3434 3.4 164.8 5.439 0.016421 12.86 7.62 30.0 0 20 7.15 30.0 0.40 5412 3.4 170.1 6.010 0.016451 14.24 7.62 30.0 0.76 7.15 30.0 0.96 8756 3.7 175.1 6.735 0.016480 15.98 7.62 30.0 1.47 7.15 30 0 1.66 12290 4.1 178.8 7.318 0.016502 17.39 7.62 30.0 2.04 7.15 30.0 2.23 16434 4.2 180.9 7.666 0.016514 18.23 7.62 30.0 2.38 7.15 30.0 2.57 20372 4.3 181.8 7.820 0.016520 18.60 7.62 30.0 2.53 7.15 30 0 2.73 24372 4.3 182.0 7.854 0.016521 18.68 7.62 30 0 2.56 7.15 30 0 2.76 30424 4.3 181.6 7.786 0.016519 18.52 7.62 30.0 2.49 7.15 30.0 2 69 40266 4.1 179.6 7.449 0.016507 17.71 7.62 30 0 2.16 7.15 30 0 2.36
1 Calc. No. QDC-1000-M-0535, Rev.1.
Attachm:nt D
]
Prge D2 (Fin:1) 1 1
Old Strainer Design Basis vs. New Design Basis (NRC Bulletin 96-03) l 7.0 I
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l llf I
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6 1
1 1
l l
f l
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if I
6.0 COP ji j
- - - COP (Credited) il i
O RHR Req Press. (Old DB) ll 5.0 RHR Req. Press. (New DB) l i
! l l ll l'l
} 40 g
t j
j r
4 i
t 1
i l
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= 30 i
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l l
l i
5 IL i
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2.0 l [
l ll' i
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1 i
i I
i E
1.0 I
l i
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i 1
oo i
j ii I
l t
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-1.0 o
i i
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l t,
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-2.0 I
l 100 1000 10000 100000 Time (seconds) i i