ML20155A674
| ML20155A674 | |
| Person / Time | |
|---|---|
| Site: | Quad Cities  |
| Issue date: | 09/29/1998 |
| From: | Dan Collins COMMONWEALTH EDISON CO. |
| To: | |
| Shared Package | |
| ML20138L443 | List: |
| References | |
| QDC-1000-M-0454, QDC-1000-M-0454-R01, QDC-1000-M-454, QDC-1000-M-454-R1, NUDOCS 9810290214 | |
| Download: ML20155A674 (73) | |
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Exhibit C NEP-12-02 Revision 5 Page 1 of 2 PREPARATION, REVIEW AND APPROVAL OF CALCULATIONS CALCULATION TITLE PAGE Calculation No: ODC-1000-M-0454 DESCRIPTION CODE: M10 DISCIPLINE CODE: M STATION Quad cities Units 1 and 2 TITLE: Short Term RHR/ Core Sorav Pumn NPSH Analysis - Design Basis LOCA X Safety Related Augmented Quality Non-Safety Related REFrT.' NCE NUMBERS
"'I$ m, , _ ,, .D i+ Type Nureber 3E* ,-
t.,. uu uvu i uvu vi-va i . , 'I/,3 CALC .ODC-1000-M-0419 .
-CALC d"I"'0012 '"lM l, 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(2)-1002 A/B Pumos 1(2)-1002C/D Pumos _ 1(2)-1401 A/B Pumos REMARKS: This calculation supersedes Calc. No. QDC-1000-M-0291 in its entirety. REY. REVISING APPROVED DATE ORGANIZATION PRINT / SIGN O (omga upog (,at,ug j' , fMA Jz/n)9) I conso < rse sw~e / trwxx 1ku'n 9810290214 981023 PDR ADOCK 05000254 P PDR
- Exhibit D , NEP-12-02 Revision 6 Page 2 0f 2 COMMONWEALTH EDISON COMPANY CALCULATION REVISION PAGE CALCULATION NO. QDC-1000-M 0454 PAGE NO.: 2 , REVISION SUMMARIES REV: 0 REVISION
SUMMARY
initial issue Electronic Calculation Data Files: (Program Name. Version. File name ext / size /date/ hour /: min) SEE REV. O. I Prepared by: Douclas F. Collins / SIGNATURE ON FILE 12/23/97
- Print / Sign Date l Reviewed by
- Rocer H. Hevn / SIGNATURE ON FILE 12/23/97 j Print / Sign Date l Type of Review
[X] Detailed [ ] Alternate [ ] Test t Supplemental Review Required [ ] Yes (NEP-12-05 documentation attached) [X]No Supervisor N/A / DO ANY ASSUMI' DONS IN WIS CALCULATION REQUIRE LATER VERIFICATION [X] YES []NO Tracked by: 2542519715701 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. Electronic Calculation Data Files: (Program Name. Version. File name exusize/date/ hour!: min) PIPE-FLO. Ver. 4.11, SilORT.PLL / 36 KB / 09-25 98 /10:03AM LSL FULL.PLU / 36 KB / 09-25 98 / OI:48PM LSL 3RHR.PLU/ 36 KB / 09-25-98 / Ol:49PM LSL-CAV.PLU / 36 KB / 09 25 98 / OI:49PM SF-DG PLU / 36 KB / 09 25-98 / Ol:50PM SilRT NEW.PLL /135 KB / 09 25-98 /10.07AM SHRT NEW.PLU / 36 KB / 09 25 98 / 01:51PM LSL-FEW.PLU 36 KB / 09-29 98 / 07.24AM Prepared by: AmlasE Collm51 4 Oi!28/78 Print / sign ' Date Reviewed by: Fou, #, dei /t / u #w- 9- 2 F -9E Type of Review d / Print /$ f'" ' I Date [y] Detailed [ ] Alternate [ ] Test Supplemental Review Required [ ] Yes (NEP-12-05 documentation attached) ()d No Supervisor f#rps. / fhrht , . DO ANY ASSUMFilONS IN NIS CALCULATION REQUIRE LATER VERIFICATION [ ] YES DQ NO Tracked by:
l Exhibit D j NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION TABLE OF CONTENTS l CALCULATION NO. ODC-1000-M-0454 REV. NO.1 PAGE NO. 3 SECTION PAGE NO. SUB-PAGE NO. TITLE PAGE I REVISION
SUMMARY
2 l TABLE OF CONTENTS 3 l PURPOSE / OBJECTIVE 4 METHODOLOGY AND ACCEPTANCE CRITERIA 4-6 ASSUMPTIONS 6-7 DESIGN INPUT 7-8 REFERENCES 8 CALCULATIONS 9 - 10 t
SUMMARY
AND CONCLUSIONS 10 TABLES AND FIGURES Table I A: SF-LSL (4 RHR/2 CS Injection) 1I Table 'U: SF-LSL (3 RHR/2 CS In.jection) 12 Table 2. SF-DG (2.RHR/l CS injection) 13 Figure 1: SF-LSL 14 Figure 2: SF-DG 15 ATTACHMENTS A. FLO-SERIES Flow Cases (50 pages) Al - A50 B. GE Letter on drawdown (1 page) Bl C. Curve Fit of NPSHR vs. Flow (2 pages) C1 - C2 D. New vs. Old Strainer Design Basis (2 pages) D1 - D2 E. Required Pressure for PCT (2 pages) El - E2 i I s
l l Exhibit E NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION NO. QDC-1000-M-0454 PAGE NO. 4
- 1. PURPOSE / OBJECTIVE !
The purpse of this calculation is to determine if sufficient net positive suction head (NPSH) is available to the Residual Heat Removal (RHR) pumps and the Core Spray (CS) pumps following a Design Basis Loss of Coolant Accident (DBA-LOCA). This ani be accomplished by developing a time-dependent set of curves comparing the available containment pressure to the pressure required to satisfy the RHR/CS pump NPSH requirements. This calculation is limited to the first 600 seconds of the accident, during which no credit is taken for operator action. The results of this calculation will be used to support a Quad Cities License Amendment request. Upon approval of this request, this calculation will represent a Design Basis Document.
- 2. METHODOLOGY AND ACCEPTANCE CRITERIA i
This calculation m utilize a FLO-SERIES hydraulic model of the RHR and CS suction and discharge piping (Ref. 5.1) to develop a time-delandent set of curves comparing the available containment pressure to the , pressure required to satisfy the RHR/CS pump NPSH requirements. NPSH required (NPSHR) curves for the LPC1/CS pumps are provided on the original vendor pump curves (attached to Ref. 5.1). These curves represent the point at which a 3% reduction in pump developed head has occurred due to insufficient NPSH available (NPSHA). Cavitation tests were performed on this pump model by the vendor at various Dow rates (Ref. 5.9). These tests demonstrate that the pumps can operate in cavitation for at least one hour without any damage to pump internals or any degradation of pump performance. These tests also demonstrate that the pump head remains stable for NPSHA vr. lues several feet below the NPSHR before the pump head collapses. For the purposes of this calculation, the pump head will conservatively be assumed to collapse when NPSHA is equal to NPSHR (Assumption 3.6). Per Ref. 5.12, the two most limiting single failures with respect to Peak Clad Temperature (PCT) are:
- 1) SF-LPCI: Failure of LPCI This case results in only two CS pumps injecting into the reactor vessel.
- 2) SF-DG: Failure of a Diesel Generator This case results in one CS pump and two RHR pumps injecting into the reactor vessel.
For the LPCI failure, this calculation will use a failure of the LPCI loop select logic (SF-LSL), which causes all 4 RHR pumps to inject into the broken Reactor Recirculation loop. This Oow case will yield the highest Dow rates through the ECCS suction piping, and thus the bounding NPSH case for the CS pumps. The SF-DG case leads to the highest RHR Dow rate per pump and, thus, is the bounding NPSH case for RHR. For the SF-LSL case, due to the higher Dow rates of the CS pumps in the short term, they will cavitate before the RHR pumps will. The flow through the CS pumps is also the main concern in the analysis of the SF LSL case. All RHR pumps are assumed to discharge to the drywell through the broken Reactor Recirculation line, and the only cooling water to reach the reactor vessel is assumed to come from the CS system. 4 REVISION NO. O REVISION NO. I
I - Exhibit E NEP-12-02 Revision 6 l COMMONWEALTH EDISON COMPANY ! CALCULATION NO. QDC-1000 M-0454 PAGE NO. 5 RHR/CS pump flow requirements are as follows: l l Failure 1: SF-LSL For the SF-LSL case, a two-pump CS flow of 211,300 gpm is required for approximately the first 180 seconds post LOCA to maintain the PCT within acceptable limits. For the purposes of this calculation, a two-pump CS flow requirement of 211,300 gpm for the first 210 seconds will conservatively be used. After PCT has been achieved, a two-pump CS flow of 29,000 gpm (nominal flow) is required for reflooding , purposes. Per Ref. 5.11, with 9,000 gpm of flow into tin core, the core is reflooded at 7.5 minutes Following l core reflood, a flow rate of 2,200 gpm is required into the core. For the purposes of this calculation. a two- ! pump flow rate of 29,000 gpm is required between 210 and 600 seconds. Failure 2: SF-DG e For the SF-DG case, a two-pump RHR flow of 29,000 gpm and a single CS pump flow of 25.650 gpm are required for approrunately the first 180 seconds post LOCA to maintain the PCT within acceptable limits. For the purposes of this calculation, a two-pump RHR flow requirement of 29,000 gpm and a single CS pump flow requirement of 25,650 gpm for the first 210 seconds will conservatively be used.
- After PCT has been achieved, the flow entering the core is needed only for reflood (lev !) purposes.
The refore, the SF-DG case has the same total ECL3 flow requirement as the SF-LSL case above, which is a contbined RHR/CS flow of 29,000 gpm between 210 and 600 seconds. This c alculation is conservative due to the use of the following inputs: Maximum suppression pool temperature response - Refs. 5.2 and 5.3 determine the maximum suppression p>ol temperatures post LOCA, thus maximizing the vapor pressure and minimizing NPSH margin. l Minimum suppression pool pressure response - the credited pool pressure response was developed based on a minimum pressure response generated by General Electric (GE)(Refs. 5.2 and 5.3). The GE pressure response utilizes inputs and assumptions that minimize suppression chamber pressures consistent with NRC information Notice 96-55, thus minimizing overpressure credit and minimizing NPSH margin.
- Technical Specifications minimum suppression pool level including maximum drawdown, minimizing elevation head and minimizing NPSH margin.
Maximum LPCI and CS pump flow conditions (unthrottled system, reactor /drywell differential pressure at 0 psid). maximizing suction piping friction losses and NPSH Required (NPSHR). e increased clean commercial steel suction pipe length by 20% to account for potential aging effects , (Assumption 3.1 in Ref. 5.1), thus maximizing suction losses. J Per Equation 5.2 on page 66 of Ref 5.8, the equation for NPSHA is as follows: - - REVISION NO. O REVISION NO.1 l
l l Exhibit E NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION NO. QDC-1000-M-0454 PAGE NO. 6 l NPSHA = h, + Z - hr- h, (Eq.1) Where: i h,,, = Suppression chamber pressure, feet absolute. Z = Static head above pump, feet. h, = Suction friction losses, feet. h, = Vapor pressure, feet r.bsolute. This equation can be rewritten in terms of the suppression chamber possure, and the minimum suppression chamber pressure required is that which will yield a value of NPSHA that is equal to the NPSHR. Thus: l h, = NPSHR - Z + hr + h, (Eq.2) Or this equation can be written to solve for the suppression chamber pressure in units of psia: P., = (NPSHR - Z + h, + h,)/(144V) (Eq.3) Where: P., = Minimum Required Suppression Chamber Pressure, psia. V = Specific volume, ft'/lb. The value of P., for each now case will be plotted as a function of time and compared to the Available and Credited Pressure in the Suppression Chamber (See Assumption 3.6).
- 3. ASSUMPTIONS / ENGINEERING JUDGEMENTS 3.1 PJiR/CS pump suction losses were developed using a FLO-SERIES model of the Quad Cities ECCS ring header and pump suction piping (Ref. 5.1). This piping model was then run at the various RHR/CS pump combinations and Hows required to support the cases evaluated in this calculation (Attachment A).
The model was developed using clean commercial steel pipe. In order to compensate for the increased loss due to the potential effects of aging, the piping lengths of the suction lines were increased by 20%. This 20% addition is consistent with guidance on the GE Process Flow Diagrams. An example can be found in Note 2 of Ref. 5.17. Other assumptions in the model can be found in Ref. 5.1. 3.2 To account for strainer plugging, one of the four suction strainers inside the torus is assumed 100% blocked, while the remaining three strainers are assumed clean (Refs. 5.5 and 5.6). For each Dow case, the strainer nearest the pump with the lowest differential between NPSHA and NPSHR will be considered blocked. 3.3 Per Ref. 5.1, the RHR/CS discharge piping is modeled such that the now rate through these lines is maximized. This assumption is conservative since this assumption will lead to the maximum Dow rates through the systems and will maximize NPSHR and minimize NPSHA. 3.4 The maximum allowable leakage from the CS nozzle safe end is 200 gpm (Ref. 5.16). This flow is modeled in the How model exiting the CS nozzle and bypassing the CS sparger. This assumption is conservative since it leads to the highest How rates through the CS pumps. REVISION NO. O REVISION NO.1
Exhibit E NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION NO. QDC-1000-M-0454 PAGE NO. 7 3.5 GE SIL 151 includes a case of all 4 RHR pumps injecting into both reactor recirculation loops simultaneously, with one loop broken. While it is expected that this case may result in slightly higher LPCI pump flow rates than the case being evaluated, a significant amount of water will be injected into the reactor through the intact loop. Therefore, any reduction in CS system flow due to cavitation below the minimum required flow will be made up by the LPCI flow injecting into the reactor. Therefore. it is expected that the PCT will not be challenged in this case and it will not be explored in this calculation. 3.6 The short term suppression chamber pressure responses from the containment analyses (Refs. 5.2 and j 5.3) are contair-d in Figures I and 2 along with the assumed pressure response which is modeled as a time-dependen* up function, consistent with the NRC-approved methodology from Dresden station. The assumed (credited) pressure response was determined in Design input 4.2 such that it is conservatively bounded by the available pressure response from Refs. 5.2 and 5.3. The containment analyses incorporate 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. 3.7 Based on a review of Ref. 5.1, there is less resistance in the RHR injection line to loop A of Reactor Recirculation. This calculation will assume RHR injection into the A loop to maximize the flows through the RHR system. Ref. 5.3 is based on a Recirculation suction line break. The model assumes a discharge line break which will also serves to maximize flow rates.
- 4. DESIGN INPUT 4.1 This calculation uses an approved FLO-SERIES model of the ECCS piping generated by Calculation No.
QDC-1000-M-0419 (Ref. 5.1) 4.2 Per the results of the containment analyses contained in Refs. 5.2 and 5.3, the available pressure response in the short term conservatively bounds the following values (see Figures I and 2): Time (sec) Credited Pressure (psig) 0 - 210 8.0 210 - 600 2.5 4.3 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) 4000 25.0 5000 30.0 l 6012 40.9 l REVISION NO. 0 l REVISION NO.1 l
- -. - - - . - . ~ . - - . - - - - - . . - . - - ---
I
. 1 Exhibit E NEP-12-02 !
Revision 6 ! COMMONWEALTH EDISON COMPANY CALCULATION NO. QDC-1000-M-0454 PAGE NO. 8 1 Quadratic interpolation of these three points yields a curve fit for the NPSHR versus flow rate (Q) of: NPSHR = (2.868x10-6)q2 -(0.02081)Q + 62.35 (Attachment C) l 4.4 ' The pressure / temperature responses of containment predicted by Refs. 5.2 and 5.3 are contained m Tables I A,1B and 2 and Figures 1 and 2 on pages 11 - 15. l 4.5 Saturation pressures and specific volumes at various temperatures are taken from Ref. 5.15 and are l included in Tables I A , IB and 2. 4.6 The maximum drawdown of the suppression chamber water level post LOCA is 2.1 ft (Ref 5.4). Applying this drawdown to the minimum water level allowed by Technical Specifications used in the model from Ref. 5.1 yields a water elevation of 568.5 ft. 4.7 The flow requirements for the RHR and CS pumps post-LOCA were determined from Refs. 5.11 - 5.14.
- 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 " 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," General Electric Nuclear Energy Report GE-NE-T2300750-00-02-R1, September 1998. 5.3 " Quad Cities Nuclear Power Station Units 1 and 2 Containment Analysi: for Short-Term NPSH l Evaluation with ANS 5.1-1979 + 2 Sigma Decay Heat," General Electic Nuclear Energy Report GE-NE-T2300750-00-03, September 1998. 5.4 GE Letter - S. Mintz to S. Eldridge dated September 24,1992 (Attachment B). 5.5 UFSAR, Rev. 4, Section 6.2.2.3, " Containment Heat Removal Systems - Design Evaluation." 5.6 UFSAR, Rev. 4, Section 6.3, " Emergency Core Cooling System." 5.7 Calculation No. QDC-0010-M-0396, Rev. O," Quad Cities Unit 2 ECCS Strainer Head Loss Estimate." 5.8 Calculation No. QDC-1600-M-0545, Rev. O," Quad Cities Unit 1 - ECCS Strainer Head Loss Estimate." 5.9 Cavitation Test Report - 12x14x14-l/2 CVDS Pump," Bingham Pump Co., May 22,1969. 5.10 Durco Pump Engineering Manual- 4th Edition. 5.11 Nuclear Fuels Services NDIT No. 9800039,"ECCS Flow to Meet 10 CFR 50.46 Core Cooling Requirements of a DBA LOCA for Short Term and Long Term." 5.12 "LOCA Break Spectrum Analysis for Quad Cities Units 1 and 2," Siemens Document EMF-96-184(P)- Siemens Power Corporation, dated December 1996. 5.13 - Principal LOCA Analysis Parameters for Quad Cities Units 1 and 2, EMF-95 165 - Siemens Power Corporation. 5.14 "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.
.'4uralidharan (GE), dated February 12,1993.
5,15 Ke-nan, et. al. Steam Tab 4slWiley: New York: 1969. 5.16 SESR Number 4-0496 - i' 5.17 Duke Engineering and Services Report No. TR-VQl500-02, Rev. O. ' 5.18 General Electric Process Flow Diagram No.161F312, Rev.1. 5.19 SESR Number 4-0496 - - i REVISION NO. O REVISION NO.1
Exhibit E NEP-12-02 Revision 6 COMMONWEALTH EDISON COMPANY CALCULATION NO. QDC-1000-M-0454 , PAGE NO. 9 6, CALCULATIONS The equation (Eq. 3) presented in Section 2.4 provides the minimum pool pressure required to meet pump NPSH requirements: P.,. = (NPSHR - Z + he + h.,,)/(144V) (Eq.3) Solving Eq. 3, the minimum suppression chamber pressure required to meet RHR and CS pump NPSH requirements for the SF-LSL case is calculated (Tables l A and IB). Similarly, the minimum chamber pressure required to meet RHR and CS pump NPSH requirements for the SF-DG case is calculated (Table 2). These results are plotted in Figures 1 and 2, along with the credited suppression chamber pressure. The GE available chamber pressure response for each case is also provided (Refs. 5.2 and 5.3). It can be seen that for both cases, no cavitation is expected for the first 210 seconds post LOCA. During this time, the RHR/CS pumps will deliver maximum Dow. Since PCT occurs at time < 210 seconds, adequate Dow will exist to ensure no impact on PCT. After 210 seconds, the RHR/CS pumps may cavitate, resulting in reduced . Hows. For the SF-LSL case, the maximum NPSH deficit of 11.29 feet occurs at the 600 second mark of the 4/2 case. In order to estimate the reduced now at which the CS pumps will operate under these conditions, a Dow estimate of 5400 gpm per CS pump is used in conjunction with Eq. 3: CS CS Required Credited Available CS Pump Pool Vapor Specific Pump Torus Torus Torus NPSH Flow Temp. Z-hr Pressure Volume NPSHR Pressure Pressure Pressure Margin (gpm) (*F) (feet) (feet) (ft3/lb) (feet) (psig) (psig) (psig) (feet) 6202 150.7 0.74 8.91 0.016347 43.60 7.29 2.50 3.40 -11.29 5400 150.7 2.34 8.91 0.016347 33.61 2.37 2.50 3.40 0.3 i Since the NPSH margin at 5400 gpm is approximately 0 feet, it is at this now that the NPSHA equals the vendor published NPSHR. Under this NPSH condition, the pump exn. bits incipient cavitation but is not yet in the full cavitation stage. As full cavitation and total head collapse have not yet been achieved, pump Dow will continue to increase, i.e. the pump is expected to operate above 5400 gpm. It is therefore conservative to use the Dow at which NPSHA equals NPSHR to bound the minimum now rate at which the CS pump will operate. Thus, under the most limiting scenario for NPSH, CS pump Dow will reduce from 25,650 gpm per pump at time s 210 seconds to a minimum flow of about 5400 gpm per pump at 600 seconds post LOCA. For the SF-DG case, the 2 RHR and i CS pumps must produce 9,000 gpm total, or 3,000 gpm per pump. Based on the NPSH deficiencies determined in Table 2, and the reduced now calculation above, it is obvious that this now requirement can easily be met > ' REVISION NO. O REVISION NO.1
Exhibit E l NEP-12-02 Revision 6 l \ COMMONWEALTH EDISON COMPANY l
\
CALCULATION NO. QDC-1000-M-0454 PAGE NO.10 New Strainer Desian Basis l The current Quad Cities design basis for strainer blockage is one strainer blocked and 3 strainers clean (Assumption 3.2, Ref. 5.6). In response to NRC Bulletin 96-03, Quad Cities plans to revise this design basis to I four partially clogged strainers, with the head loss associated with the new strainers (Ref. 5.17) and the debris ! loading as modeled in Ref. 5.7 - 5.8. (This model is attached as file SHRT_NEW.PLL) This possible, future design basis would increase the NPSH margin in the short term, as demonstrated in Attachment D. However. ' currently, one strainer completely blocked and three strainers clean is the Quad Cities strainer debris loading ,
- design basis. i l
( Containment Pressure Reauired to Assure PCT l Attachment E provides a curve of the containment pressure required to ensure CS flow of 5650 gpm per pump during the first 210 seconds for the limiting single failure (SF-LSL). The maximum required pressure of 3.1 psig is well less than the 8 psig credited for the first 210 seconds post LOCA.
- 7.
SUMMARY
AND CONCLUSIONS This NPSH analysis was performed for the CS/RHR pumps under short-term design basis post-accident conditions. Specifically, two limiting single failures for the accident were modeled. A failure of LPCI loop select logic causing all RHR pumps to inject into the broken Reactor Recirculation loop was analyzed as well as a failure of a diesel generator. The analysis concludes that the pumps will supply the required flows for the first 210 seconds without cavitating. From 210 seconds to 600 seconds into the accident, the pumps may begin to cavitate, but they will be able to supply the required flow to the reactor. The total time that any of the pumps may cavitate is possibly 6.5 minutes, which is significantly less than the one hour allowed in section 2.0. Therefore. there is sufficient NPSHA to ensure the ability of the RHR/CS pumps to perform their safety function under all accident scenarios. 1 i REVISION NO. O REVISION NO. I
Calc. No. QDC-1000-M-0454, Rnv.1. ' Pigs 11 Table 1 A SF-LSL: 4 RHR12 CS injection RHR CS Available Credited Pool Pool Pool Specific Required Required Time Pressure Pressure Temp Volume Py Flow NPSHR Z-hr Pressure Margin Flow NPSHR Z-h, Pressure Margin (sec) (psig) (psig) (deg. F) (ft'llb) (psia) (gpm) (feet) (feet) (psig) (feet) (gpm) (feet) (feet) (psig) (feet) 12 21.6 8.0 112.6 0.016175 1.376 38 23.4 8.0 132.7 0.016260 2.391 47 23.2 8.0 133.6 0.016263 2.448 5121 30.99 -3.60 2.52 12.84 6202 43.60 0.74 6.05 4.57 60 23.1 8.0 133.6 0.016263 2.448 5121 30.99 -3.60 2.52 12.84 6202 43.60 0.74 6.05 4.57 80 20.8 8.0 134.2 0.016266 2.487 5121 30.99 -3.60 2.55 12.75 6202 43.60 0.74 6.09 4.48 109 18.3 8.0 135.7 0.016274 2.587 5121 30.99 -3.60 2.65 12.54 6202 43.60 0.74 6.18 4.27 129 16.8 8.0 137.4 0.016281 2.704 5121 30.99 -3.S0 2.76 12.29 6202 43.60 0.74 6.29 4.02 146 15.3 8.0 138.6 0.016287 2.789 5121 30.99 -3.60 2.84 12.11 6202 43.60 0.74 6.36 3.84 166 13.5 8.0 140.3 0.016295 2.915 5121 30.99 -3.60 2.96 11.84 6202 43 60 0.74 6.48 3.57 188 11.3 8.0 141.8 0.016302 3.029 5121 30.99 -3.60 3.06 11.59 6202 43.60 0.74 6.59 3.32 209 9.2 8.0 142.8 0.016307 3.106 5121 30.99 -3.60 3.14 11.42 6202 43.60 0.74 6.66 3.15 239 6.9 2.5 143.9 0.016313 3.195 5121 30.39 -3.60 3.22 -1.69 6202 43.60 0.74 6.74 -9.96 276 5.2 2.5 145.1 0.016319 3.293 5121 30.99 -3.60 3.31 -1.91 6202 43 60 0.74 6.83 - -10.18 311 4.2 2.5 146.0 0.016323 3.368 5121 30.99 -3.60 3.38 -2.08 6202 43.60 0.74 6.90 -10.35 352 ^4 2.5 147.0 0.016328 3.454 5121 30.99 -3.60 3.47 -2.27 6202 43.60 0.74 6.98
-10.54 394 3.1 2.5 147.7 0.016332 3.515 5121 30.99 -3.60 3.52 -2.41 6202 43.60 0.74 7.04 -10.68 441 3.1 2.5 148.4 G.016335 3.577 5121 30.99 -3.60 3.58 -2.55 6202 43.60 0.74 '7.10 -10.82 491 3.2 2.5 149.2 0 016339 3.648 5121 30.99 -3.60 3.65 -2.70 6202 43.60 0.74 7.16 -10.97 516 3.3 2.5 149.5 0.016341 3.676 5121 30.99 -3.60 3.68 -2.77 6202 43.60 0.74 7.19 -11.04 566 3.3 2.5 150.2 0.016344 3.741 5121 30.99 -3.60 3.74 -2.91 6202 43.60 0.74 7.25 -11.18 600 ~ 3.4 2.5 150.7 0.016347 3.787 5121 30.99 -3.60 3.78 -3.02 6202 43.60 0.74 7.29 -11.29
l Calc. No. QDC-1000-M-0454, R:v.1. .
. Piga 12 Table 1B l
l SF-LSL: 3 RHR/2 CS injection RHR CS l Available Credited Pool Pool Poog Specific Required Required 5 Time Pressure Pressure Temp Volume Py Flow NPSH, Z-h, Pressure Margin Flow NPSHR Z-h, Pressure Margin (sec) (psig) (psig) (deg. F) (ft'llb) (psia) (gpm) (feet) (feet) (psig) (feet) (gpm) (feet) (feet) (psig) (feet) _ 12 21.6 8.0 112.6 0.016175 1.376 ! 38 -23.4 8.0 132.7 0.016260 2.391 l 47 23.2 8.0 133.6 0.016263 2.448 5508 34.74 -3.02 3.87 9.67 6212 43.75 2 62 5.31 6.30 l 60 23.1 8.0 133.6 0.016263 2.448 5508 34.74 -3.02 3.87 9.67 6212 43.75 2 62 5.31 6.30 80 20.8 8.0 134.2 0.016266 2.487 5508 34.74 -3.02 3.91 9.58 6212 43.75 2.62 5.35 6.21 ! 109 18.3 8.0 135.7 0.016274 2.587 5508 34.74 -3.02 4.00 9.37 6212 43.75 2.62 5.44 I 6.00 129 16 8 8.0 137.4 0.016281 2.704 5508 34.74 -3.02 4.11 9.12 6212 43.75 2.62 5.55 5.75 146 15.3 8.0 138.6 0.016287 2.789 5508 34.74 -3.02 4.19 8.94 6212 43.75 2.62 5.63 5.57 166 13.5 8.0 140.3 0.016295 2.915 5508 34.74 -3.02 4.31 8.67 6212 43.75 2.62 5.74 5.30 188 11.3 8.0 141.8 0.016302 3.029 5508 34.74 -3.02 4.41 8.42 6212 43.75 2.62 5.85 5.05 j 209 9.2 8.0 142.8 0.016307 3.106 5508 34.74 -3.02 4.49 8.25 6212 43.75 2.62 5.92 4.88 1 239 6.9 2.5 143.9 0.016313 3.195 5508 34.74 -3.02 4.57 -4.86 6212 43.75 2.62 6.00 -8.23
- 276 5.2 2.5 145.1 0.016319 3.293 5508 34.74 -3.02 4.66 -5.08 6212 43.75 2.62 6.10 '8.45 311 4.2 2.5 146.0 0.016323 3.368 5508 34.74 -3.02 4.73 -5.25 6212 43.75 2.62 6.17
- -8.62 352 3.4 2.5 147.0 0.016328 3.454 5508 34.74 -3.02 4.81 -5.44 6212 43.75 2.62 6.25 -8.81 394 3.1 2.5 147.7 0.016332 3.515 5508 34.74 -3.02 4.87 -5.58 6212 43.75 2.62 l
6.30 -8.95 441 3.1 2.5 148.4 0.016335 3.577 5508 34.74 -3.02 4.93 -5.72 6212 43.75 2.62 6.36 -9.09 j 491 3.2 2.5 149.2 0.016339 3.648 5508 34.74 -3.02 5.00 -5.87 6212 43.75 2.62 6.43 -9.24 i 516 3.3 2.5 149.5 0.016341 3.676 5508 34.74 -3.02 5.02 -5.94 6212 43.75 2.62 6.46 -9.31 566 3.3 2.5 150.2 0.016344 3.741 5508 34.74 -3.02 5.08 -6.08 6212 43.75 2.62 6.52 -9.45 600 ' 3.4 2.5 150.7 0.016347 3.787 5508 34.74 -3.02 5.13 -6.19 6212 43.75 2.62 6.56 -9.56 s
C:Ic. No. QDC-1000-M-0454, R:;v.1. - Piga 13 t Table 2 i SF-DG: 2 RHR/1 CS Injection RHR CS Credited , Pool Pool Specific Required Required Time Prossure Temp Volume Py Flow NPSHR Z-h, Pressure Margin Flow NPSHR Z-he Pressure Margin (sec) (psig) (dog. F) (ft*/lb) (psia) (gpm) (feet) (feet) (psig) (feet) (gpm) (feet) (feet) (psig) (feet) 12 8.0 112.6 0.016175 1.376 38 8.0 132.7 0.016260 2.391 47 8.0 133.6 0.016263 2.448 5745 37.45 0.84 3.38 10.82 6229 44.00 6.98 3.56 1G.41 4 60 8.0 133.6 0.016263 2.448 5745 37.45 0.84 3.38 10.82 6229 44.00 6.98 3.56 10.41 80 8.0 134.2 0.016266 2.487 5745 37.45 0.84 3.42 10.73 6229 44.00 6.98 3.59 10.32 j 109 8.0 135.7 0.016274 2.587 5745 37.45 0.84 3.51 10.52 6229 44.00 6.98 3.68 10.11 129 8.0 137.4 0.016281 2.704 5745 37.45 0.84 3.62 10.27 6229 44.00 6.98 3.79 9.86 146 8.0 138.6 0.016287 2.789 5745 37.45 0.84 3.70 10.09 6229 44.00 6.98 3.87 9.68 166 8.0 140.3 0.016295 2.915 5/45 37.45 0.84 3.82 9.82 6229 44.00 6.98 3.99 9.41 188 8.0 141.8 0.016302 3.029 5745 37.45 0.84 3.92 9.57 6229 44.00 6.98 4.10 9.16 209 8.0 142.8 0.016307 3.106 5745 37.45 0.84 4.00 9.40 6229 44.00 6.98 4.17 8.99 l 239 2.5 143.9 0.016313 3.195 5745 37.45 0.84 4.08 -3 71 6229 44.00 6.98 4.25 -4.12 276 2.5 145.1 0.016319 3.293 5745 37.45 0.84 4.17 -3.93 6229 '44.00 6.98 4.35 -4.34 311 2.5 146.0 0.016323 3.368 5745 37.45 0.84 4.24 -4.10 6229 44.00 6.98 4.42 -4.51 352 2.5 147.0 0.016328 3.454 5745 37.45 0.84 4.32 -4.29 6229 44.00 6.98 4.50 -4.70 < 394 2.5 147.7 0.016332 3.515 5745 37.45 0.84 4.38 -4.43 6229 44.00 6.98 4.56 -4.84 l 441 2.5 148.4 0.016335 3.577 5745 37.45 0.84 4.44 -4.57 6229 44.00 6.98 4.62 ' - -4.98 491 2.5 149.2 0.016339 3.648 5745 37.45 0.84 4.51 -4.72 6229 44.00 6.98 4.68 -5.13 l 516 2.5 149.5 0.016341 3.676 5745 37.45 0.84 4.53 -4.79 6229 44.00 6.98 4.71 -5.20 566 2.5 150.2 0.016344 3.741 5745 37.45 0.84 4.60 -4.93 6229 44.00 6.98 4.77 -5.34 600 2.5 150.7 0.016347 3.787 5745 37.45 0.84 4.64 -5.04 6229 44.00 6 98 4.81 -5.45 4 1 1
4 l Ccic. No. QDC-1000-M-0454, R:v.1. - Piga 14 1 ,'1 < 1 i i Figure 1 - SF-LSL 25 160 d 4, I a 20 Available Pool Pressure \ .- 150 _ - - Credited Pool Pressure \ ',,
*~
g y ^ RHR Required Pressure (4/2) ,,, ch 1 1 .
/ e ! - --M--CS Required Pressure (4/2) ,- V e , ~
l g 0 RHR Required Pressure (3/2) , e 15
--e--CS Required Pressure (3/2) '
140 - E -
- - PoolTemperature ,e g E '
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o 10 o ." 130 e 4 ,' 3 3 - - : :: TH r
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I s c 0 0 0 0 T . .
. _ ~
s I 0 I i 110 10 100 1000 Time (seconds) 4 i i
4 Ccic. No. QDC-1000-M-0454, R.v.1. Pegs 15 (Finil) 1 Figure 2 - SF-DG 25 160 N i l i 20 Available Pool Pressure - f 150 Credited Pool Pressure j
^
_ RHR Required Pressure .,. cm " e a -91E-CS Required Pressure ..~ ~
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- - PoolTemperature ' '
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1 1 0 110 10 100 1000 Time (seconds)
Company: Comed LSL-FULL Projoct: . 09/25/98 by: Doug Collins LINEUP REPORT rev: 09/25/98 LINELIST: SHORT DEVIATION: 0.00012 % dated: 09/25'/98 after: 12 iterations Volumetric flow rates require constant fluid properties in all pipelines. Fluid properties in the first specification were used. NODE DEMAND NODE DEMAND gpm gpm InletA >>> 200 InletB >>> 200 FLOWS IN: 0 gpm FLOWS OUT: 400 gpm NET FLOWS OUT: 400 gpm PIPELINE FLOW PRESSURE SET ypm SOURCE psia 4 Break-A >>> 20084 >>> Break-A 14.7 SpargerA >>> 6002 >>> CSOutA 14.7 SpargerB' >>> 5950 >>> CSOutB 14.7 2-1079-1 >>> 298 >>> Torus 2 14.7 LB-1 <<< 11022 <<< X-204B 14.7 LC-1 <<< 10863 <<< X-204C 14.7 LD-1 <<< 10849 <<< X-204D 14.7 FLOWS IN: 32734 gpm FLOWS OUT' 32334 gpm NET FLOWS IN: 400 gpm t PIPE-FLO rev .4.11, Calc . - No. QI/C-1000-M-04 54, Rev. 1. Attachment A Page M
. . . . . - ,. -. - - . _ - . - . . . - . ~ . . - . . ~ = _ . -
LINEUP NODES -LSL-FULL 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft A 559.5
- 14.67 593.6 B 559.5
- 14.67 593.6 Break-A 605.5 p 14.7 639.6 Break-B 605.5
- 135.2 919.2 C 559.5
- 14.7 593.6 CSoutA 647.5- p 14.7 681.6 CSoutB 647.5 p 14.7 681.6 D 559.5
- 14.71 593.6 Dis 10A 555.58
- 158.2 922.8 Dis 10B 555.58
- 158.2 922.8 Dis 10C 555.58
- 162.8 933.6 Dis 10D 555.58
- 162.9 933.6 Dis 14A- 555.63
- 185.7 986.7 Dis 14B 555.63
- 189.3 995.1 E 559.5
- 14.71' 593.6 F 559.5
- 14.62 593.4 G 559.5
- 14.62 593.4 H 559.5
- 14.62 593.4 HPCI2 556.08 16.17 593.6 I 559.5
- 14.63 593.5 InHXA 566.79
- 149.3 913.5 InHXB 566.79
- 154.1 924.5 InletA 647.5 > 200 *- 96.89 872.4 InletB 647.5 > 200
- 95.48 869.1 J 559.5 + 14.81 593.9 K 559.5
- 14.82 593.9 L 559.5
- 14.82 593.9 M '559.5
- 14.83 593.9 N- 559.5
- 14.83 593.9
, Noz2C 623.25
- 127.5 919.2 Noz2D 623.25
- 127.5 919.2 t Noz2E 623.25
- 127.5 919.2 No:2F 623.25
- 127.5 919.2 Noz2G 623.25
- 127.5 919.2 0 559.5 .
- 14.83 593.9 OutHXA 584.5
- 139.9 909.2 .
OutHXB 584.5
- 144.8 920.5 P 559.5
- 14.83 593.9 - '
Q 559.5
- 14.83 593.9 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A7.
l
. . . .- . . . . - .- - . ~ . . - - - - - . . - .. - - ..- --
( LINEUP NODES . LSL-FULL 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft R 559.5
- 14.72 593.7 !
l R1032C 563
- 27.56 627 Ram 2C 634.23
- 122.8 919.2 l Ram 2D 634.23
- 122.8 919.2 Ram 2E 634.23
- 122.8 919.2 Ram 2F- 634.23
- 122.8 919.2 Ram 2G 634.23
- 122.8 919.2 1
RCIC2 556.83 15.98 593.9 RecircA 605.5
- 24.73 662.9 RecircB 605.5
- 135.2 919.2 l -Red 1012A 581
- 119.6 858.6 l Red 1012B 580.67
- 145.9 919.2 Red 10A 562.25
- 12.29 590.8 Red 10B 562.25
- 12.32 590.8 Red 13 561.46 13.98 593.9 Red 14A 555.63 15.02 590.5 Red 14B 555.63 15.1 590.7 Red 23-1 562.25
- 13.51 -593.6 Red 23-2 556.08 16.17 593.6 RedCSA 636.5
- 115 903.5 RedCSB 642.25
- 112.5 903.5 l S 559.5
- 14.69 593.6 Suc10A 555.58 13.74 587.5 l Suc10B 555.58 13.15 586.1 l Suc10C 555.58 13.13 . 586.1
! Suc10D 555.58 14.09 588.3
'Suc14A 555.63 15.02 590.5 Suc14B 555.63 15.09 590.7 T 559.5
- 14.67 593.6 l T1006A 564
- 151 914.4
'T1006B ~564
- 151 914.4 T1006C- 564
- 155.7 925.3 l 'T1006D 564
- 155.7 925.3
-T1008A 584.5
- 139.8 909
' T1008B 584.5 .
- 144.7 920.3 T1010A 584.5
- 139.2 907.7 ,
T1010B 584 5
- 144.2 919.2 T1032A 555.58
- 158.2 922.7 - -
. T1032B 555.58
- 158.1 922.7
- PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Atachment A Page A3 f
i
, . ~ . _ _ _ _
. -. - . ._ . - ._~ . . - - .
LINEUP NODES - LSL-FULL 09/35/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft T1032C 555.58
- 162.6 933
-T1032D 555.58 -*
162.6 933 T1079-1 563 * -27.41 626.6 T1079-2 588 6.299 602.6 Tee 10A-1 562.25.
- 12.43 591.1 Tee 10A-2 557.08 14.11 589.8 Tee 10B-1 562.25
- 12.46 591.2 Tee 10B-2 556.75 13.62 588.4 Tee 10C-2 :556.79 13.52 588.2 Tee 10D-2 .556.92 14.43 590.4 Tee 13 557.33 15.76 593.9 Teel 4A 355.63 15.07 590.6 Teel 4B 555.63 15.15 590.8 Tee 23 562.67 13.33 593.6 Tee 2C 610
- 133.2 919.2 Tee 2D 610
- 133.2 919.2 Tee 2E 610
- 133.2 919.2 Tee 2F 610
- 133.2 919.2 Tee 2G 610
- 133.2 919.2 Torus 2 568.5 p .14.7 602.6 U 559.5
- 14 ~. 6 6 593.5 V 559.5 + 14.67 593.6 V24A 638.17
- 113.7 902.2 V28A 589.08
- 107.6 838.8 V28B 591.25
- 141.3 919.2 V29A 589.08
- 60.51 729.5 V29B 591.25
- 141.3 919.2
~X-204A 568.5 10.79 593.6 X-204B 568.5 p 14.7 602.6 X-204C 568.5 p 14.7 602.6 X-204D- 568.5 p 14.7 602.6 X-223A 559.5
- 14.61 593.4 X-223B 559.5
- 14.63 593.4 X-224A 559.5 14.66 593.5 X-224B 559.5 .
14.71 593.7 X-225. 559.5
- 14.7 593.6 -
X-226 559.5 14.83 593.9 ZA 560.5
- 14.24
- 593.6 -
ZB 560.5
- 15.1 595.5 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A%
. . .~ . . . .. . - . . . - . .-.-- -.. -. - . . - . . .. ... ~._.. . - - - - . _ . ~ , . - - . . _ - - . .
LINEUP NODES LSL-FULL 09/25/98 NODE ' ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft i l ZC 550.5
- 15.19 595.7
-ZD 560.5
- 15.19 595.8 t
t l i
- i 1
l l i l I l l: i i l P PIPE-FLO rev 4.11- Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page As-
, r wn -- w - - - ,,,4n .ww. -n r- -- -
..,,,w ,--v -- ,, , w -~ , -, - -
LINEUP PIPELINES LSL-FDLL 09/25/98 PIPELIME FROM TO FLOW VEL dP H1 gpm ft/sec psi a ft 2-0201A-1 RecircA Tee 2L closed 0 0 0 2-0201B-1 RecircB Tee 2F 0 0 0 0 2-0201B-2 Tee 2F Tee 2G 0 0 0 0 2-0201B-3 Tee 2F Tee 2E O O O O 2-0201B-4 Tee 2E Tee 2D 0 0 0 0 2-0201B-5 Tee 2D Tee 2C 0 0 0 0 2-0201C-1 Tee 2C Noz2C 0 0 0 0 2-0201C-2 Noz2C Ram 2C 0 0 0 0 2-0201D-1 Tee 2D Noz2D 0 0 0 0 2-0201D-2 Noz2D Ram 2D 0 0 0 0 2-0201E-1 Tee 2E Noz2E O O O O 2-0201E-2 Noz2E Ram 2E O O O O 2-0201F-1 Tee 2F Noz2F 0 0 0 0 2-0201F-2 Noz2F Ram 2F 0 0 0 0 2-0201G-1 Tee 2G Noz2G 0 0 0 0 2-0201G-2 Noz2G Ram 2G 0 0 0 0 2-1006A-1 Dis 10A T1032A 5128
- 14.56 0.044 0.101 2-1006A-2 T1032A T1006A 5128
- 14.56 7.206 8.306 2-1006B-1 Dis 10B T1032B 5121
- 14.54 0.044 0.101 2-1006B-2 T1032B T1006B 5121
- 14.54 7.195 8.282 2-1006C-1 Dis 10C T1032C 5060
- 14.37 0.269 0.624 2-1006C-2 T1032C T1006C 4911
- 13.94 6.927 7.659 2-1006D-1 Dis 10D T1032D 5072
- 14.4 0.270 0.627 2-1006D-2 T1032D T1006D 4924
- 13.98 6.946 7.702 2-1008A-1 T1006B InHXA 4633 6.46 1.604 0.932 2-1008A-2 T1006B <-> T1006A 487.6 0.680 0.0d1 0.002 2-1008A-3 T1006A T1008A 5616 7.83 11.17 5.427 1008B-1 T1006D T1008B 5361 7.475 10.99 $ 013 2-1008B-2 T1006C T1006D 436.9 0.609 0 0.002 2-1008B-3 T1006C InHXB 4474 6.237 1.556 0.822 2-1009A-1 OutHXA T1008A 4633 6.46 0.099 0.229 2-1009A-2 T1008A T1010A 10249
- 14.29 0.535 1.241 2-1009A-3 T1010A Red 1012A 20084
- 28 19.67 49.16 2-1009B-1 OutHXB T1008B 4474 6.237 0.092 0.215 2-1009B-2 T1008B ,
T1010B 9835
- 13.71 0.450 1.045 2-1009B-3 T1010B Red 1012B.O O O O 2-1010 T1010B <-> T1010A 9835
- 13.71 4.963 11.52 2-1012A-1 Red 1012A V28A 20084
- 35.31 11.99 19.75 2-1012A-2 V28A V29A 20084
- 40.09 47.09 109.3' 2-1012A-3 V29A RecircA 20084
- 38.75 35.77 66.62 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A(o
- ._ - ~ _ _ . -. . __ ._ _ _ - _ . . _ _ _ _ _ . . _ __ _ _ . _ _ . _ _ _ _ _ _ _ _ _ _ _ _ . _
LINEDP PIPELINES -LSL-FULL 09/25/98' P2PELIME FROM TO FLOW VEL dP H1 gpm ft/sec psi a ft 2-1012B-1 Red 1012B V28B 0 0 0 0 2-1012B-2 V28B V29B 0 0 0 0 2-1012B-3 V29B RecircB 0 0 0 0 2-1015A-1 X-223A Tee 10A-1 10249 7.751 2.182 2.314 2-1015A-2 Tee 10A-1 Red 10A 5128 3.878 0.142 0.329 2-1015B-1 X-223B Tee 10B-1 10133 7.663 2.165 2.276 2-1015B-2 Tee 10B-1 Red 10B 5060 3.827 0.140 0.325 2-1016A-1 Red 10A Tee 10A-2 5128 11.94 (1,819 ) 0.948 2-1016A-2 Tee 10A-2 Suc10A 5128 11.94 0.365 2.347 2-1016B-1 Tee 10A-1 Tee 10B-2 5121 11.92 (1.185 ) 2.749 2-1016B-2 Tee 10B-2 Suc10B 5121 11.92 0.464 2.247 2-1016C-1 Red 10B Tee 10C-2 5060 11.78 (1.199 ) 2.677 2-1016C-2 Tee 10C-2 Suc10C 5060 11.78 0.390 2.115 2-1016D-1 Tee 10B-1 Tee 10D-2 5072 11.81 (1.969 ) 0.760 2-1016D-2 Tee 10D-2 Suc10D SG72 11.81 0.344 2.138 2-1025-1 B <-> A 265( 2.122 0 0.001 2-1025-10 I <-> X-223B 12016 9.598 0.007 0.017 2-1025-11 J <->I 12026 9.088 0.182 0.422 2-1025-12 K <-> J 12016 9.598 0.008 0.019 2-1025-13 L <-> K 1153 0.921 0.001 0.003 2-1025-14 M <-> L 1153 0.872 0.005 0.011 2-1025-15 X-226 <-> M 1153 0'921
. 0 0 2-1025-16 N <-> X-226 1153 0,921 0.001 0.003 2-1025-17 O <-> N 1153 0.872 0.002 0.004 2-1025-18 P <-> 0 1153 0.921 0 0 2-1025-19 P Q 9696 7.745 'O.0'05 0.012
'2-1025-2 C <-> B ,2656 2.009 0.033 0.076 2-1025-20 Q R 9696 7.333 0.108 'O 252 2-1025-21 R X-224B 9696 7.745 0.005 0.011 2-1025-22 X-224B X-225 3546 2.832 0.015 0.035 2-1025-23 X-225 S 3546 2.832 0.005 0.013 2-1025-24 S T 3546 2.682 0.018 0.042 2-1025-25 T X-224A 3546 2.832 0.013 0.0'30 2-1025-26 U <-> X-224A 2656 2.122 0 0
.2-1025-2.7 V <-> U 2656 2.009 0.009 0.021 2-1025-28 A <-> V 2656 2.122 0 0.001 2-1025-3 D <-> C 2656 2.122 0.007 0.017 2-1025-4 D E 8366 6.682 0.004 0.009 2-1025-5 E F 8366 6.327 0.090 0.208' 2-1025-6 F X-223A 8366 6.682 0.004 0.008 PIPE-FLO-rev 4.11 Calc. No QDC-1000-M-0454, Rev. 1. Attachment A Page A~l
LINEUP PIPELINES -LSL-FULL 09/25/98 PIPEL2NE FROM TO FLOW VEL dP H1 ' gpm ft/sec psi a ft 2-1025-7 G <-> X-223A 1883 1.504 0.002 0.004 2-1025-8 H <-> G 1883 1.424 0.004 0.008
.2-1025-9 X-223B <-> H 1883 1.504 0.005 0.012
- - 2-1032A T1032A T1032-1 closed 0 0 0 2-1032B-1 T1032B R1032B closed 0 0 0 2-1032C-1 T1032C R1032C 149.8
- 16.28 135 306 2-1032C-2 R1032C T1079-1 149.8 6.504 0.155 0.360 2-1032D T1032D T1079-1 148.3
- 16.12 135.2 306.4 2-1079 T1079-1 T1079-2 298
- 12.94 21.11 24 2-1079-1 T1079-2 Torus 2 298 1.213 (8.401 ) 0 2-1318-1 X-226 Red 13 0 0 0 0 ;
2-1318-2 Red 13 Tee 13 0 0 0 0 2-1318 Tee 13 RCIC2 0 0 0 0 2-1401-1 X-224A Teel 4A 6202 8.522 (0.409 ) 2.92 l 2-1401-2 Teel 4A Red 14A 6202 8.522 0.051 0.118 2-1401-3 Red 14A Suc14A 6202 10.9 0.005 0.012 l 2-1402-1 X-224B Teel 4B 6150 8.45 (0.437 ) 2.856 2-1402-2 Teel 4B Red 14B 6150 8.45' O.049 0.113 2-1402-3 Red 14B Suc14B 6150 10.81 0.007 0.017 i 2-1403-l' Dis 14A RedCSA 6202
- 17.61 70.66 83.14 !
2-1403-2 RedCSA V24A- 6202
- 25.26 1.296 1.339 l
i 2-1403-3 V24A InletA 6202
- 26.67 16.85 29.79 2-1404-1 Dis 14B RedCSB 6150
- 17.46 76.78 91.6 2-1404-2 RedCSB ' InletB 6150
- 26.45 17.06 34.36 2-2302-1 X-225 Red 23-1 0 0 0 0 2-2302 Red 23-1 Tee 23 C 0 0 0 2-2302-3 Tee 23 Red 23-2 0 0 0 0 2-2302-4 Red 23-2 HPCI2 0 0 0 0 Break-A RecircA Break-A 20084
- 38.75 10.03 23.29 Break-B RecircB Break-B 0 0 0 0 i l
HXA InHXA 'CutHXA 4633 6.366 9.468 4.267 i HXB InHXB OutHXB 4474 6.146 9.344 3.979 LA-1 X-204A ZA 0 0 0 0
--- strainer --- dP: --- Hl:
. LA-2 ZA A 0 0 0 0 LB-1 X-204B .
ZB 11022
- 13.34 (0.398 ) 7.076 strainer --- dP: 3.036 --- Hl: 7.047 j LB-2 ZB D 11022
- 12.16 0.386 1.896 i~
-LC-1 X-204C ZC 10863
- 13.15 (0.485 ) 6.874 I --- strainer --- dP: 2.949 --- Hl: 6.845 LC-2. ZC K 10863 11.98 0.363 1.842 i
' PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Anaclunent A, Page AB w gi3 y w y-w- ir -.r- ' ' - ' -
LINEUP PIPELINES LSL-FULL 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft LD-1 .. X-204D ZD 10849
- 13.14 (0.493 ) 6.856 ,
--- strainer -*- dP: 2.941 --- Hl: 6.827 j LD-2 ZD P 10849 11.97 0.361 1.837
{ Pmp10A Suc10A Dis 10A 5128
- 14.56 (144.5 ) (335.3)
--- RHR Pump --- dP: (144.5) --- Hl: (335.3)
Pmp10B Suc10B Dis 10B 5121
--- RHR Pump --- dP: (145) --- Hl: (336.7)
- 14.54 (145 ) (336.7)
Pmp10C Suc10C Dis 10C 5060 (149.7
--- RHR Pump --- dP: (149.7) --- Hl: (347.5)
- 14.37 ) (347.5)
Pmp10D Suc10D Dis 10D 5072 (148.8
--- RHR Pump --- dP: (148.9) --- Hl: (345.4)
- 14.4 ) (345.4)
Pmp14A Suc14A Dis 14A 6202
- 17.61 (170.7 ) (396.2)
--- CS Pump --- dP: (170.7) --- Hl: (396.2)
Pmp14B Suc14B Dis 14B 6150 (174.2
--- CS Pump --- dP: (174.2, --- Hl: (404.4)
- 17.46 ) (404.4)
SpargerA InletA CSOutA 6002
- 25.81 82.19 190.8 SpargerB InletB CSOutB 5950
- 25.59 80.78 187.5 l j
i l 1 I 4 l t l i ^ PIFE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A'I
Comp ny: Comed LSL-CAV l ProjCct: ! by: Doug Collina 09/25/98 l LINEUP REPORT rev: 09/25/98 l LINELIST: SHORT DEVIATION: 0.0001 % l i datedi 09/25'/98 after: 13 iterations l Volumetric flow rates require constant fluid properties in all pipelines. Fluid properties in the first specification were used. NODE DEMAND NODE DEMAND gpm gpm Suc14A >>> 5400 Suc14B >>> 5400 FLOWS IN: 0 gpm FLOWS OUT: 10800 gpm NET FLOWS OUT: 10800 gpm PIPELINE FLOW PRESSURE SET gpm SOURCE psia Break-A >>> 20095 >>> Break-A 14.7 2-1079-1 >>> 298.1 >>> Torus 2 14.7 LB-1 <<< 10507 <<< X-204B 14.7 LC-1 <<< 10355 <<< X-204C 14.7 LD-1 <<< 10330 <<< X-204D 14.7 FLOWS IN: 31192 gpm FLOWS OUT: 20393 gpm NET FLOWS IN: 10799 gpm PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page Ato
LINEUP NODES LSL-CAV 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm poi a ft A 559.5
- 15.04 594.4 B 559.5
- 15.04' 594.4 Break-A 605.5 p 14,7 639.6 Break-B 605.5
- 135.3 919.5 C 559.5
- 15.06 594.5 D 559.5
- 15.06 594.5 Dis 10A 555.58
- 158.3 923.1 Dis 10B 555.58
- 158.3 923.1 l Dis 10C 555.58
- 163 933.9 Dis 10D 555.58
- 163 933.9 E 559.5
- 15.06 594.5 F 559.5
- 14.97 594.2 ;
G 559.5
- 14.97 594.2 H 559.5
- 14.97 594.2 HPCI2 556.08 16.54 594.5 I 559.5
- 14.98 594.3 InHXA 566,79
- 149.5 913.8 InHXB 566.79
- 154.2 924.8 J 559.5
- 15.16 594.7 K 559.5
- 15.17 594.7 L 559.5
- 15.17 594.7 M 559.5
- 15.18 594.7 N 559.5
- 15.18 594.7 Noz2C 623.25
- 127.6 919.5 Noz2D 623.25
- 127.6 919.5 Noz2E 623.25
- 127.6 919.5 Noz2F 623.25
- 127.6 919.5 Noz2G 623.25
- 127.6 919.5 0 559.5
- 15.10 594.7 OutRXA 584.5
- 140 909.5 OutHXB 584.5
- 144.9 920.8 P 559.5
- 15.18 594.7 Q 559.5
- 15.18 594.7 R 559.5
- 15.09 594.5 R1032C 563 .
- 27.57 627 Ram 2C 634.23
- 122.9 919.5 .
Ram 2D 634.23
- 122.9 919.5 Ram 2E 634.23
- 122.9 919.5 - -
Ram 2F 634.23
- 122.9 919.5 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page All
_ _ . - . - . . . _ - . _ _ ._ . . . - . . _ . . . . . _ . . . . . ~. _ _ _ _ __ .-. . . _ _ _ . _ . - _ _ LINEUP NODES LSL-CAV 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft Ram 2G 634.23
- 122.9 919.5 RCIC2 556.83 16.33 594.7 RecircA 605.5
- 24.75 662.9 RecircB 605.5
- 135.3 919.5 Red 1012A 581
- 119.7 858.8 Red 1012B 580.67
- 146 919.5 Red 10A 562.25
- 12.64 591.6 Red 10B 562.25
- 12.67
. 591.7 Red 13 561.46 14.33 594.7 Red 14A 555.63 15.71 592.1 Red 14B 555.63 15.76 592.2 Red 23-1 562.25
- 13.88 594.5
. Red 23-2 556.08 16.54 594.5 5 559.5
- 15.06 594.5 :
Suc10A 555.58 14.09 588.3 ) Suc10B 555.58 13.5 586.9 Suc10C 555.58 13.47 586.9 Suc10D 555.58 14.43 589.1 i Suc14A 555.63 > 5400 15.71 592.1 Suc14B -555.63 > 5400 15.76 592.2 l T 559.5
- 15.05 594.4 T1006A 564
- 151.1 914.7 T100GB 564
- 151.1 914.7 T1006C 564
- 155.8 925.6 i T1006D 564
- 155.8 -
925.6 T1008A 584.5
- 139.9 909.3 T1008B 584.5
- 144.8 920 6 T1010A 584.5
- 139.4 908 T1010B 584.5
- 144.3 919.5 T1032A 555.58
- 158.3 923 T1032B 555.58
- 158.3 923 i T1032C 555.58
- 162.7 933.3 T1032D 555.58
- 162.7 933.3 1
T1079-1 563
- 27.42 626.6 T1079-2 588 6.299 602.6 Tee 10A-1 562.25
- 12.78 591.9 -
Tee 10A-2 557.08 14.46 590.6 Tee 10B-1 562.25
- 12.81 592 - '
Tee 10B-2 556.75 13.96 589.2 PIPE-FLO.rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page All
. a - _ . -. . . . - _ . _ = - . _ . -. - -
09/25/98 l NODE ELEVAT20N DEMAND PRESSURE H GRADE J ft gpm psi a ft Tee 10C-2* 55'6.79 13.86 589 Tee 10D-2 556.92 14.77 591.2 Tee 13 557.33 16.11 594.7 Teel 4A 555.63 15.75 592.2 Tee 14B 555.63 15.8 592.3 Tee 23 562.67 13.7 594.5 Tee 2C 610
- 133.4 919.5 Tee 2D 610
- 133.4 919.5 Tee 2E 610
- 133.4 919.5 Tee 2F. 610
- 133.4 919.5 Tee 2G .610
- 133.4 919.5 Torus 2 568.5 p 14.7 602.6 U 559.5
- 15.04 594.4 V 559.5
- 15.04 594.4 V28A 589.08
- 107.7 839 V28B 591.25
- 141.4 919.5 V29A 589.08
- 60.55 729.6 V29B 591.25
- 141.4 919.5 X-204A 568.5 11.16 594.4 X-204B 568.5 p 14.7 602.6 X-204C 568.5 p 14.7 602.6 X-204D 568.5 p 14.7 602.6 X-223A 559.5
- 14.96 594.2 X-223B 559.5
- 14.97 594.3 X-224A 559.5 15.04 .
'594.4 X-224B 559.5 15.08 594.5 X-225 559.5
- 15.07 594.5 X-226 559.5 15.18 594.7 ZA 560.5
- 14.61 594.4 ZB 560.5
- 15.38 596.2
'ZC 560.5
- 15.46 596.4 ZD 560.5
- 15.47 596.4 L
1 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Anaclunent A, Page AG
LINEUP PIPELINES -LSL-CAV 09/25/98 PIPELINE FRGM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-0201A-1 RecircA Tee 2L closed 0 0 0 2-0201B-1 RecircB Tee 2F 0 0 0 0 2-0201B-2 Tee 2F Tee 2G 0 0 0 0 2-0201B-3 Tee 2F Tee 2E O O O O 2-0201B-4 Tee 2E Tee 2D 0 0 0 0 l 1 2-0201B-5 Tee 2D Tee 2C 0 0 0 0 I l 2-0201C-1 Tee 2C Noz2C 0 0 0 0 2-0201C-2 Noz2C Ram 2C 0 0 0 0 2-0201D-1 Tee 2D Noz2D 0 0 0 0 2-0201D-2 Noz2D Ram 2D 0 0 0 0 2-0201E-1 Tee 2E Noz2E O O O O 2-0201E-2 Noz2E Ram 2E O O O O 2-0201F-1 Tee 2F Noz2F 0 0 0 0 2-0201F-2 Noz2F Ram 2F 0 0 0 0 2-0201G-1 Tee 2G Noz2G 0 0 0 0 2-0201G-2 Noz2G Ram 2G 0 0 0 0 2-1006A-1 Dis 10A T1032A 5131
- 14.57 0.044 0.102 i 1006A-2 T1032A T1006A 5131
- 14.57 7.21 8.315 1
l 2-1006B-1 Dis 10B T1032B 5124
- 14.55 0.044 0.101 2-1006B-2 T1032B T1006B 5124
- 14.55 7.199 8.291 2 1006C-1 Dis 10C T1032C 5063
- 14.37 0.269 0.624 .
2-1006C-2 T1032C T1006C 4913
- 13.95 6.931 7.668 2-1006D-1 Dis 10D T1032D 5075
- 14.41 0.270 0.627 2-1006D-2 T1032D T1006D 4927'
- 13.99 6.949 7.71 2-1008A-1 T1006B InHXA 4636 6.463 1.604 0.933 2-1008A-2 T1006B <-> T1006A 487.9 0.680 0.001 0.002 2-1008A-3 T1006A T1008A 5619 7.834 11.17 5.433 2-1008B-1 T1006D T1008B 5364 7.479 10.99 5.019 2-1008B-2 T1006C T1006D 437.2 0.610 0 0.002 2-1008B-3 T1006C InHXB 4476 6.24 1.557 0.823 2-1009A-1 OutHXA T1008A 4636 6.463 0.099 0.230 2-1009A-2 T1008A T1010A 10255
- 14.3 0.535 1.242 2-1009A-3 T1010A Red 1012A 20095
- 28.02 19.69 49.21 2-1009B-1 OutHXB T1008B 4476 6.24 0.093 0.215 2-1009B-2 T1008B T1010B 9840
- 13.72 0.451 1.046
.2-1009B-3 T1010B Red 1012B.O O O O 2-1010 T1010B <-> T1010A 9840
- 13.72 4.968 11.53 '
2-1012A-1 Red 1012A V28A 20095
- 35.32 12 19.77 2-1012A-2 V28A V29A 20095
- 40.11 47.14 109.4' 2-1012A-3 V29A RecircA 20095
- 38.77 35.8 66.69 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page AM
LINEUP PIPELINES LSL-CAV 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1012B-1 Red 1012B V28B 0 0 0 0 2-1012B-2 V28B V29B 0 0 0 0 2-1012B-3 V29B RecircB 0 0 0 0 2-1015A-1 X-223A Tee 10A-1 10255 7.755 2.183 2.317 2-1015A-2 Tee 10A-1 Red 10A 5131 3.881 0.142 0.329 l 2-1015B-1 X-223B Tee 10B-1 10138 7.667 2.167 2.279 2-1015B-2 Tee 10B-1 Red 10B 5063 3.829 0.140 0.326 , 2-1016A-1 Red 10A Tee 10A-2 5131 11.95 (1.818 ) 0.949 2-1016A-2 Tee 10A-2 Suc10A 5131 11.95 0.366 2.35 2-1016B-1 Tee 30A-1 Tee 10B-2 5124 11.93 (1.184 ) 2.752 2-1016B-2 Tee 10B-2 Suc10B 5124 11.93 0.465 2.25 2-1016C-1 Red 10B Tee 10C-2 5063 11.79 (1.198 ) 2.68 2-1016C-2 Tee 10C-2 Suc10C 5063 11,79 0.391 2.117 2-1016D-1 Tee 10B-1 Tee 10D-2 5075 11.82 (1.969 ) 0.761 2-1016D-2 Tee 10D-2 Suc10D 5075 11.82 0.345 2.14 2-1025-1 B <-> A 1990 1.59 0 0 2-1025-10 I <-> X-223B 11876 9.485 0.007 0.017 2-1025-11 J <->I 11876 8.902 0.178 0.412 l 2-1025-12 K <-> J 11876 9.485 0.008 ' l 0.018 2-1025-13 L <-> K .421 1.215 0.002 0.006 2-1025-14 M <-> L 1521 1.15 0.000 0.019 2-1025-15 X-226 <-> M 1521 1.215 0 0 l 2-1025-16 N <-> X-226 1521 1.215 0.002 0.006 2-1025-17 0 <-> N 1521 1.15 0.003 0.007 2-1025-18 P <-> 0 1521 1.215 0 0 2-1025-19 P Q 8810 7.036 0.'004 0.010 2-1025-2 C <-> B 1990 1.505 0.019 0.044 2-1025-20 0 R 8810 6.663 0.090 0.209 2-1025-21 R X-224B 8810 7.036 0.004 0.009 2-1025-22 X-224B X-225 3410 2.723 0.014 0.032 2-1025-23 X-225 S 3410 2.723 0.005 0.012 2-1025-24 S T 3410 2.579 0.017 0.039 2-1025-25 T X-224A 3410 2.723 0.012 0.028 2-1025-26 U <-> X-224A 1990 1.59 0 0 2-1025-27 V <-> U 1990 1.505 0.005 0.012 2-1025-28 A <-> V .1990 1.59 0 0 2-1025-3 D <-> C 1990 1.59 0.004 0.010 l 2-1025-4 D E 8517 6.803 0.004 0.010
~
2-1025-5 E F 8517 6.441 0.093 0.216 2-1025-6 F X-223A 8517 6.803 0.004 0.009 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Anaciunent A Page At6
. _ _m __. ._ _ _ _ . _ _ _ _ . . _ _ _ _ _ . _ _ __ ._ __
LINEUP P3PELINES - LSL-CAV 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1025-7 G <-> X-223A 1738 1.388 0.002
, 0.004 2-1025-8 H <-> G 1738 1.314 0.003 0.007 2-1025-9 X-223B <-> H 1738 1.388 0.005 0.011 2-1032A T1032A T1032-1 closed 0 0 0 2-1032B-1 T1032B R1032B- closed 0 0 0 2-1032C-1 .T1032C R1032C 149.8
- 16.29 135.1 306.3 2-1032C-2 R1032C T1079-1 149.8 6.507 0.155 0.360 2-1032D T1032D T1079-1 148.3
- 16.13 135.3 306.7 2-1079 T1079-1 T1079-2 298.1
- 12.95 21.12 24.02 2-1079-1 T1079-2 Torus 2 298.1 1.214 (8.401 0
)
2-1318-1 X-226 Red 13 0 0 0 0
.2-1318-2 Red 13 Tee 13 0 0 0 0 2-1318-3 Tee 13 RCIC2 0 0 0 0 2-1401-1 X-224A Teel 4A 5400 7.419 (0.713 ) 2.216 2-1401-2 Teel 4A Red 14A 5400 7.419 0.039 0.090 2-1401-3 Red 14A Suc14A 5400 9.493 0.004 0.009 2-1402-1 X-224B Tee 14B- 5400 7.419 (0.718 ) 2.204 2-1402-2 Teel 4B Red 14B 5400 7.419 0.038 0.087 2-1402-3 Red 14B Suc14B 5400 9.493 0.006 0.013 2-2302-1 X-225 Red 23-1 0 0 0 0 2-2302-2 Red 23-1 Tee 23 0 0 0 0 2-2302-3 Tee 23 Red 23-2 0 0 0 0 2-2302-4 Red 23-2 HPCI2 0 0 0 0 Break-A RecircA Break-A 20095
- 3 .77 10.05 23.32 Break-B RecircB Break-B 0 0 0 0 HXA InHXA OutHXA 4636 6.369 9.47 4.272 HXB InHXB OutHXB 4476 6.15 9.345 3.983 LA-1 X-204A ZA 0 0 0 0
--- strainer --- dP: --- Hl:
LA-2 ZA A 0 0 0 0 LB-1 X-204B ZB 10507
- 12.72 (0.676 ) 6.431 strainer --- dP: 2.759 --- Hl: 6.404 LB-2 ZB D 10507 11.59 0.312 1.723 LC-1 X-204C ZC 10355
- 12.54 (0.756 ) 6.246
--- strainer --- dP: 2.679 --- Hl: 6.22 LC-2 ZC K 10355 11.42 0.290 1.674 LD-1 X-204D
. ZD . 10330
- 12.51 (0.763 ) 6.216 strainer --- dP: 2.667 --- Hl: 6.19 .
LD-2 ZD P 10330 11.4 0.287 1.666 4 Pmp10A Suc10A Dis 10A 5131
- 14.57 (144.2 '
) (334.8P
--- RHR Pump --- dP: (144.2) --- Hl: (334.8)
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page Al(a
, .- - . = . - . - . _ _ . _ _~_=. . _ . - . ..
LINEUP PIPELINES LSL-CAV 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft Pmp10B Suc10B Dis 10B 5124 (144.8
--- RHR Pump --- dP: - ( 14 4 . 8 ) --- Hl: (336.2)
- 14.55 ) (336.2)
Pmp10C Suc10C' Dis 10C 5063
- 14.37 (149.5 ) (347.1)
--- RHR Pump --- dP: (149.5) --- Hl: (347.1)
Pmp10D Suc10D Dis 10D 5075 (148.6
--- RHR Pump --- dP: (148.6) --- Hl: (344.9)
- 14.41 ) (344.9)
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 i
l l l 1 l'
~
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page AL'l l
I Comp *my: . Comed' Projset: LSL-3RHR
.by: Doug Collins 09/25/98
-LINEUP REPORT rev: 09/25/98 LINELIST: SHORT- DEVIATION: 5.59e-005 %
dated: 09/25'/98 after: 13 iterations Volumetric flow rates require constant fluid properties in all pipelines. Fluid properties-in the first specification were used. : NODE DEMAND NODE DEMAND
. gpm gpm InletA >>> 200 InletB >>> 200 FLOWS IN: 0 gpm FLOWS OUT: 400 gpm NET FLOWS OUT: 400 gpm PIPELINE FLOW PRESSURE SET gpm SOURCE psia Break-A' >>> 16391 >>> Break-A 14.7 SpargerA >>> -6010 >>> CSoutA 14.7 SpargerB . >>> 5958 >>> CSoutB- 14.7 2-1079-1 >>> ' 257.1 >>> Torus 2 14.7 LB-1 - <<< 9753 <<< X-204B 14.7 LC-1 <<< 9632 <<< X-204C 14.7 LD-1 <<< 9630 <<< X-204D 14.7 FLOWS IN: 29015 gpm FLOWS OUT: 28616 gpm NET FLOWS IN: 399 gpm i
PIPE-FLO rev 4.11 Calc.'No. QDC-1t,00-M-0454, Rev. 1. Attachment A Page Ai6
LINEUP NODES .LSL-3RHR 09/25/98 J NODE ELEVATIOM. DEMAND PRESSURE H GRADE ft gpm psi a ft A 55'9.5
- 15.49 595.5 B 559.5
- 15.49 595.5 Break-A 605.5 p 14.7 639.6 Break-B 605.5
- 97.62 832.1 C 559.5
- 15.54 595.6 CSOutA 647.5 p 14.7 681.6 CSOutB 647.5 p 14.7 681.6 D 559.5
- 15.55 595.6 Dis 10A 555.58
- 118.4 830.4 Dis 10B 555.58
- 114 820.3 1
I , Dis 10C '555.58
- 126.5 849.3 l Dis 10D 555.58
- 126.6 849.3 Dis 14A 555.63
- 186 987.4 Dis 14B 555.63
- 189.6 995.8 E 559.5
- 15.55 5 S:5. 6 F 559.5
- 15.49 595.5 G 559.5
- 15.49 595.5 H 559.5
- 15.49 595.5 HPCI2 556.08 16.9B 595.5 I 559.5
- 15.49 595.5 InHXA 566.79
- 109.1 820 InHXB 566.79
- 117 838.4 InletA 647.5 > 200
- 97.09 872.9 InletB 647.5 > 200
- 95.67 869.6 J 559.5
- 15.62 -
'595.8 K 559.5
- 15.63 595.8 L 559.5
- 15.63 595.8 M 559.5
- 15.63 595.8 N 559.5
- 15.63 595.8 Noz2C 623.25
- 89.98 832.1 Noz2D 623.25
- 89.98 832.1
.Noz2E 623.25
- 89.98 832.1 Noz2F 623.25
- 89.98 832.1 Noz2G 623.25
- 89.98 832.1 0 559.5 .
- 15.63 595.8 OutHXA 584.5
- 100.9 818.7 .
OutHXB 584.5
- 107.3 833.6 P 559.5
- 15.63 A
595.8 - - Q 559.5
- 15.62 595.8 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page. Ad
LINEUP NODES - LSL-3RHR
,09/25/98 NODE ELEVATION DEMP.ND PRESSURE H GRADE ft gpm psi a ft R 559.5
- 15.52 595.5 R1032C 563
- 24.91 620.8 Ram 2C 634.23
- B5.25 832.1 Ram 2D 634.23
- 85.25 832.1 l
Ram 2E 634.23
- 85.25 832.1-Ram 2F 634.23
- 85.25 832.1 Ram 2G 634.23
- 85.25 832.1 RCIC2 556.83 16.78 595.8 RecircA 605.5
- 21.38 655.1 RecircB 605.5
- 97.62 832.1
. Red 1012A 581
- B8.12 785.5 Red 1012BL 580.67
- 108.3 832.1 Red 10A 562.25
- 13.83 594.4 Red 10B 562.25
- 12.97 592.4 Red 13 561.46 14.78 595.8 Red 14A 555.63 15.84 592.4 Red 14B 555.63 15.9 592.5 Red 23-1 562.25
- 14.32 595.5 Red 23-2 556.08 16.98 595.5 RedCSA 636.5
- 115.3 904.1 RedCSB 642.25
- 112.8 904 S 559.5
- 15.5 595.5 Suc10A 555.58 15 590.4 Suc10B 555.58 16.88 594.8
.Suc10C 555.58 13.4 586.7
-Suc10D 555.58 14.54 589.3 Suc14A 555.63 15.83 592.4 Suc14B 555.63 15.9 592.5 T 559.5
- 15.49 595.5 T1006A 564 '
- 110.4 820.3 T1006B 564
- 110.4 820.3 T1006C 564
- 118.6 839.4 T1006D 564
- 118.6 839.4 T1008A 584.5
- 100.9 818.7 T1008B 584.5 -
- 107.2 833.4 T1010A 584.5
- 100.7 818.3 -
T1010B 584.5
- 106.7 832.1
~ T1032A 555.58
- 118.4 830.3 - '
T1032B 555.58
- 114 820.3 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A2.0
. - . . . . ~ . . . - - . -- _-. . . ~ . . . - _ . ... . -
l' LINEUP NODES LSL-3RHR 09/25/98 NODE ELEVATION DEMAND PRESSURE ft H GRADE gpm psi a ft i T1032C 555.58
- 126.2 848.6 T1032D 555.58
- 126.2 848.6 T1079-1 563
- 24.8 620.6 T1079-2 588 6.299 602.6 Tee 10A-1 562.25
- 14 594.8 Tee 10A-2 557.08' 15.57 593.2 j Tee 10B-1 562.25
- 13.14 592.8 Tee 10B-2 556.75 16.37 1
594.8 I Tee 10C-2 556.79 13.96 589.2 Tee 10D-2 556.92 15.05 591.9 Tee 13 557.33 16.56 595.8 Teel 4A 555.63 15.89 592.5 Teel 4B 555.63 ~15.95 592.7 Tee 23 562.67 14.14 595.5 Tee 2C 610
- 95.6B 832.1 Tee 2D 610
- 95.68 832.1 Tee 2E 610
- 95.68 832.1 Tee 2F 610
- 95.68 832.1
{ Tee 2G 610
- 95.68 832.1 Torus 2 568.5 p 14.7 602.6 U 559.5
- 15.48 595.4 V 559.5
- 15.49 595.5 V24A 638.17
- 114 902.7 V28A 589.08
- 78.96 772.4 V28B 591.25
- 103.8 .
832.1 V29A 589.08
- 47.'59 699.5 V29B 591.25
- 103.8 832.1 X-204A 568.5 11.62 595.5 X-204B 568.5 p 14.7 602.6 X-204C 568.5 p 14.7 602.6 X-204D 568.5 p 14.7 602.6 X-223A 559.5
- 15.49 595.5 X-223B 559.5
- 15.49 595.4 X-224A 559.5 15.48 595.4 X-224B 559.5 .'
15.52 595.5 l X-225 559.5
- 15.51 595.5 -
X-226 559.5 15.63 595.8 ZA 560.5
- 15.06 - '
l 595.5 l ZB 560.5
- 15.76 597.1 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A 2.1
, ..__,m.. _ . _ _ .. ., . . _ _ . _ _ , - _ . - . _ . . . . _ _ , _ _ _ _ . . . . . . _ , , _ _ . , . . . _ . . . _ _ . . _ _ _ . . __.
. LINEUP NODES
- LSL-3RHR: , '
09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE-ft gpm psi a ft ZCi 560.5
- 15.82 597.2 -
ZD 560.5
- 15.82' 597.2 !
a i
.i l
4 a i s t 4 4 7 k +
' PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A22.
LINEUP PIPELINES LSL-3RHR l 09/25/98 i PIPELYNE FROM TO FLOW VEL dP M1 g gpm ft/sec psi a ft I l- 2-0201A-1 RecircA Tee 2L closed 0' O O j 2-0201B-1 RecircB Tee 2F 0 0 0 0 2-0201B-2 Tee 2F Tee 2G 0 0 0 0 l 2-0201B-3 Tee 2F Tee 2E O O O O 2-0201B-4 Tee 2E Tee 2D 0 'O. 0 0 f 2-0201B-5 Tee 2D Tee 2C 0 0 0 0 2-0201C-1 Tee 2C Noz2C 0 0 0 0 2-0201C-2 Noz2C Ram 2C 0 0 0 0 2-0301D-1 Tee 2D Noz2D 0 0 0 0 2-0201D-2 Noz2D Ram 2D. 0 0 0 0
- 2-0201E-1 Tee 2E Noz2E O O O O 2-0201E-2 Noz2E Ram 2E O O O O i 2-0201F-1 Tee 2F Noz2F 0 0 0 0 2-0201F-2 Noz2F Ram 2F 0 0 0 0 2-0201G-1 Tee 2G Noz2G 0 0 0 0 2-0201G-2 Noz2G Ram 2G 0 0 0 0 2-1006A-1 Dis 10A T1032A 5619
- 15.95 0.052 0.121 2-1006A-2 T1032A T1006A 5619
- 15.95 7.922 9.97 2-1006B-1 Dis 10B T1032B 0 0 0 0 1
2-1006B-2 T1032B T1006B 0 0 0 0 2-1006C-1 Dis 10C T1032C 5508
- 15.64 0.318 0.738 2-1006C-2 T1032C T1006C 5379
- 15.27 7.586 9.189 2-1006D Dis 10D T1032D 5521
- 15.67 0.319 0.741 2-1006D-2 T1032D T1006D 5393
- 15.31 7.607 9.237 2-1008A-1 T1006B InHXA 2514 3.505 1.321 0.277 2-1008A-2 T1006A T1006B 2514 3.505 0.027 0.062 2-1008A-3 T1006A T1008A 3105 4.329 9.548 1.663 2-1008B-1 T1006D T1008B 5872 8.187 11.42 6.013 2-1008B-2 T1006C T1006D 479.2 0.668 0.001 0.002 2-1008B-3 T1006C InHXB 4900 6.831 1.626 0.985 2-1009A-1 OutHXA T1008A 2514 3.505 0.029 0.068 2-1009A-2 T1008A T1010A 5619 7.834 0.161 0.375 2-1009A-3 T1010A Red 1012A 16391
- 22.85 12.6 32.76 2-1009B-1 OutHXB T1008B 4900 6.831 0.111 0.257 2-1009B-2 T1008B T1010B 10772
- 15.02 0.540
, 1.253 2-1009B-3 T1010B ' Red 1012B 0 0 0 0 1 2-1010 T1010B <-> T1010A 10772
- 15.02 5.948 13.81 2-1012A-1 Red 1012A V28A 16391
- 28.81 9.162 13.19 2-1012A-2 V2 8A - V29A 16391
- 32.71 31.37 72.81' 2-1012A-3 V29A ~RecircA 16391
- 31.63 26.21 44.41 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A23
__ . _ _ _ .- __ _ ____._ ._m ._ LINEUP PIPELINES LSL-3RHR I
- 09/25/98 PIPELINE FROM TO FLOW VEL dP M1 gpm ft/see psi a ft 2-1012B-1 ,
Red 1012B V28B 0 0 0 0 2-1012B-2 V28B V29B- 0 0 0 0 2-1012B-3 V29B RecircB 0 . 0 0 0 , 2-1015A-1 X-223A Tee 10A-1 5619 4.249 1.486 0.699 i. l 2-1015A-2 Tee 10A-1 Red 10A 5619 4.249 0.170 0.395 2-1015B-1 X-223B Tee 10B-1 11029 8.341 2.346 2.695 2-1015B-2 Tee 10B-1 Red 10B 5508 4.166 0.166 0.385 2-1016A-1 Red 10A Tee 10A-2 5619
- 13.08 (1.138 ) 1.136
! 2-1016A-2 Tee 10A-2 Suc10A 5619
- 13.08 0.567 2.816
[. 2-1016B-1 Tee 10A-1 Tee 10B-2 0 0 0 0 j 2-1016B-2 Tee 10B-2 Suc10B 0 0 0 0
)
2-1016C-1 Red 10B Tee 10C-2 5508
- 12.83 (0.986 ) 3.172 2 k l016C-2 Tee 10C-2 Suc10C 5508
- 12.83 0.557 2.504 I 2-1016D-1 Tee 10B-1 Tee 10D-2 5521
- 12.86 (1.909 ) 0.899 4
2-1016D-2 Tee 10D-2 Suc10D 5521
- 12.86 0.513 2.53 2-1025-1 B <-> A 3155 2.52 0 0.001 2-1025-10 I <-> X-223B 10050 8.027 0.005 0.012 !
2-1025-11 J <-> I 10050 7.601 0.128 0.298 2-1025-12 K <-> J 10050 8.027 0.006 0.013 ! 2-1025-13 L <-> K 418 0.334 0 0 2-1025-14 M <-> L 418 0~.316 0 0.002 2-1025-15 X-226 <-> M 418 0.334 0 0 i ! 2-1025-16 N <-> X-226 418 0.334 0 0 l 2-1025-17 0 <-> N 418 0.316 0 0 l 1025-18 P <-> 0 418 0.334 0 0 l 2-1025-19 P Q 9212 7.358 0.0b5 0.011 ( 2-1025-2 C <->B 3155 2.386 0.045 0.105 2-1025-20 Q R 9212 6.967 0.098 'O.228 l 2-1025-21 R X-224B 9212 7.358 0.004 0.010 2-1025-22 X-224B X-225 3054 2.44 0.011 0.026 2-1025-23 X-225 S 3054 2.44 0.004 0.009 2-1025-24 S T 3054 2.31 0.014 0.032 2-1025-25 T X-224A 3054 2.44 0.010 0.022 2-1025-26 U <-> X-224A 3155 2.52 0 0.001 ! 2-1025-27 V <-> U 3155 2.386 0.012 0.029 i i 2-1025-28 A <-> V 3155 2.52 0 0.001 l 2-1025-3 D <-> C 3155 2.52 0.010 0.024 2-1025-4 D E 6598 5.27 0.003 0.006 2-1025-5 E F 6598 4.99 0.057 0.131' 2-1025-6 F X-223A 6598 5.27 0.002 0.005 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A14 I
LINEUP PIPELINES 4SL-3RHR 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/sec psi a ft 2-1025-7 X-223A G 979 0.782 0 0.001 2-1025-8 G H 979 0.740 0.001 0.002 2-1025-9 H X-223B 979 0.782 0.001 0.003 2-1032A T1032A T1032-1 closed 0 0 0 2-1032B-1 T1032B R1032B closed 0 0 0 2-1032C-1 T1032C R1032C 129.2
- 14.05 101.3 227.7 2-1032C-2 R1032C T1079-1 129.2 5.611 0.116 0.269 2-1032D T1032D T1079-1 127.9
- 13.91 101.4 228 2-1079 T1079-1 T1079-2 257.1 11.17 18.5 17.94 2-1079-1 T1079-2 Torus 2 257.1 1.047 (8.401 ) 0 2-1318-1 X-226 Red 13 0 0 0 0 2-1318-2 Red 13 Tee 13 0 0 0 0 2-1318-3 Tee 13 RCIC2 0 0 0 0 2-1401-1 X-224A Tee 14A 6210 8.532 (0.406 ) 2.927 2-1401-2 Teel 4A Red 14A 6210 8.532 0.051 0.119 2-1401-3 Red 14A Suc14A 6210 10.92 0.005 0.012 2-1402-1 X-224B Teel 4B 6158 8.46 (0.434 ) 2.863 2-1402-2 Tee 14B Red 14B 6158 8.46 0.049 0.113 2-1402-3 Red 14B Suc14B 6158 10.82 0.007 0.017 2-1403-1 Dis 14A RedCSA 6210
- 17.63 70.74 83.33 2-1403-2 RedCSA V24A 6210
- 25.29 1.298 1.342 2-1403-3 V24A InletA 6210
- 26.71 16.88 29.86 2-1404-1 Dis 14B RedCSB 6150
- 17.48 76.87 91.81 2-1404-2 RedCSB InletB 6158
- 26.48 17.1 34.44 2-2302-1 X-225 Red 23-1 0 0 0 0 2-2302-2 Red 23-1 Tee 23 0 0 0 0 2-2302-3 Tee 23 Red 23-2 0 0 0 0 2-2302-4 Red 23-2 HPCI2 0 0 0 'O Break-A RecircA Break-A 16391
- 31.63 6.684 15.51 Break-B RecircB Break-B 0 0 0 0 HXA InHXA OutHXA 2514 3.454 8.171 1.256 HXB InHXB OutHXB 4900 6.732 9.686 4.773 LA-1 X-204A ZA 0 0 0 0
--- strainer --- dP: --- Hl:
LA-2 ZA A 0 0 0 0 LB-1 X-204B . ZB 9753 11.81 (1.059 ) 5.541
--- strainer --- dP: 2.377 --- Hl: 5.518 LB-2 ZB D 9753 10.76 0.209 1.485 LC-1 X-204C ZC 9632 11.66 (1.118 ) 5.404 ' ' --- strainer --- dP: 2.318 --- Hl: 5.381 LC-2 ZC K 9632 10.63 0.193 1.448 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A25'
. . .- . _ _ . . . _ . . _ _ . _ . . ~ . _ . . . . .._ .._.. .. _ _ _ _. _..~. _ _ _ _ . . _ . . . _ _ . . .
LINEUP PIPELINES Lst.3RHR 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm .ft/see psi a ft LD-1 X-204D ZD 9630 11.66 (1.119 ) 5.402
--- strainer -'- dP: 2.317 --- Hl: 5.379 LD-2 ZD P 9630 10.62 0.193 1.447 Pmp10A Suc10A Dis 10A 5619
- 15.95 (103.4 ) (240)
--- RHR Pump --- dP: (103.4) --- Hl: (240)
Pmp10B Suc10B Dis 10B closed 0 0 0
--- RHR Pump --- dP: --- Hl:
Pmp10C Suc10C Dis 10C 5508 (113.1
-- .RHR Pump --- dP: (113.1) --- Hl: (262.6)
- 15.64 ) (262.6)
Pmp10D Suc10D Dis 10D 5521
--- RHR Pump --- dP: (112) --- Hl: (260)
- 15.67 (112 ) (260)
Pmp14A Suc14A Dis 14A 6210 (170.2
--- CS Pump --- dP: (170.2) --- Hl: (395)
- 17.63 ) (395)
Pmp14B Suc14B Dis 14B 6158 (173.7
--- CS Pump --- dP: (173.7) --- Hl: (403.3)
- 17.48 ) (403.3)
SpargerA InletA CSoutA 6010
- 25.85 82.39 191.3 SpargerB InletB CSOutB 5958
- 25.62 80.97 188 I
4 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A2(o
Comp;ny: bomEd 4 ProjGets SF-DG I by: Doug Collina 09/25/98 l l LINEUP REPORT rev: 09/25/98 LINELIST: SHORT DEVIATION: 7.45e-005 % dated:'09/25/98 after: 9 iterations volumetric flow rates require constant fluid pr6perties in all pipelines. Fluid properties in the first specification were used. NODE DEMAND NODE DEMAND gpm gpm InletA >>> 200 FLOWS IN: 0 gpm FLOWS OUT: 200 gpm l NET FLOWS OUT: 200 gpm PIPELINE FLOW PRESSURE SET gpm SOURCE psia SpargerA >>> 6026 >>> CSOutA 14.7 2-0201H-2 >>> 2286 >>> Ram 2H 14.7 2-0201J-2 >>> 2287 >>> Ram 2J 14.7 2-0201K-2 >>> 2292 >>> Ram 2K 14.7 2-0201L-2 >>> 2321 >>> Ram 2L 14.7 2-0201M-2 >>> 2313 >>> Ram 2M 14.7 LB-1 <<< 6147 <<< X-204B 14.7 LC-1 <<< 5792 <<< X-204C 14.7 LD-1 <<< 5785 <<< X-204D 14.7 FLOWS IN: 17724 gpm FLOWS OUT: 17525. gpm NET FLOWS IN: 199 gpm PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page Arl
LINEUP NODES . Sp.DG 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft A 559.5
- 17.37 599.8 B 559.5
- 17.37 599.8 Break-A 605.5
- 42.72 704.7 C 559.5
- 17.37 599.8 CSoutA 647.5 p 14.7 681.6 D 559.5
- 17.37 599.8 Dis 10A' 555.58-
- 107 804 Dis 10B 555.58
- 107 804 Dis 14A 555.63
- 186.7 989.1 E 559.5
- 17.37 599.8 F 559.5
- 17.34 599.7 G 559.5
- 17.36 599.8 H 559.5
- 17.39 599.9 HPCI2 556.08 18.92 600 I 559.5
- 17.45 600 InHXA 566.79
- 97.14 792.3 InletA 647.5 > 200
- 97.55 873.9 J 559.5
- 17.51 600.1 K 559.5
- 17.51 600.1 L 559.5
- 17.51 600.1 M 559.5
- 17.51 600.1 N 559.5
- 17.51 600.1 Noz2H 623.25
- 32.31 698.3 Noz2J 623.25
- 32.33 698.3 Noz2K 623.25 -
- 32.38 698.4 Noz2L 623.25
- 32.72 699.2 Moz2M 623.25
- 32.62 699 0 559.5
- 17.51 600.1 OutHXA 584.5
- 87.2 786.9 P 559.5
- 17.51 600.1 Q 559.5
- 17.51 600.1 R 559.5
- 17.48 600.1 Ram 2H 634.23 p 14.7 668.4
, Ram 2J 634.23 p 14.7 668.4 Ram 2K 634.23 . p 14.7 668.4 l Ram 2L 634.23 p 14.7 668.4 . 1 Ram 2M 634.23 p 14.7 668.4 RCIC2 556.83 18.66 600.1 - - RecircA 605.5
- 42.72 704.7 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A16
. - . . . . -- ~ .. . ~ . - - . . _ . - . _ - . . - - . . . . - . . - . . . . . . - LINEUP NODES SF-DG 09/35/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft- gpm psi a ft Red 1012A 581
- 80.96 768.9 I Red 10A 562.25
- 14.72 596.4 Red 13 561.46 16.67 600.1 Red 14A 555.63 17.71 596.7-Red 23-1 '562.25
- 16.26 600 l Red 23-2 556.08 18.92 600 RedCSA 6 3 6 . .E
- 115.8 905.3 S 559.5
- 17.43 600 l Suc10A 555.58 15.81 592.3 Suc10B 555.58 15.06 590.5
-Suc14A 555.63 17.71 596.7 T 559.5.
- 17.39 599.9 T1006A 564
- 98.84 793.4 T1006B 564
- 98.85 793.4 i T1008A 584.5
- 87.07 786.6 T1010A 584.5
- 86.4 785.1 T1032A 555.58
- 107 803.9 T1032B 555.58
- 107 803.9
-Tee 10A-1 562.25
- 14.9- 596.8 Tee 10A-2 557.08 16.43 595.2 Tee 10B-2 556.75 15.78 593.4 Tee 13 557.33 18.45 600.1 Teel 4A 555.63 17.77 596.9 Tee 23 562.67 16.08 600 Tee 2H 610
- 38.61 699.6 Tee 2J 610
- 38.63 699.7 Tee 2K 610
- 38.69 699.8 Tee 2L 610
- 39.04 700.6 Tee 2M 610
- 39 700.5 U 559.5
- 17.37 599.8 V 559.5
- 17.37 599.8 V24A 638.17
- 114.5 904 V28A 589.08
- 74.66 762.4 V29A 589.08
- 59.22 726.6 X-204A 568.5' .
13.49 599.8 X-204B 568.5 p 14.7 602.6 . X-204C 568.5 p 14.7 602.6 X-204D 568.5 p 14.7 602.6 - - X-223A 559.5
- 17.34 599.7
. PIPE-FLO rev'4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A2.9
LINEUP NODES sp.pg-09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE fC- gpm psi a ft
;X-223B' 599.5 17.45 600 X-224A 559.5 17.37 599.8 X-224B 559.5 17.48 600.1 X-225 559.5 *' 17.44 600 X-226 559.5 17.51 600.1 l l
ZA 560.5
- 16.94 599.8 ZB 560.5
- 17.2 600.4 ZC 560.5
- 17.3 600.7 ZD 560.5
- 17,31 - 600.7 i
l l 4 4 PIPE-FLO rev.4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A30
LINEUP PIPELINES .SF-DG 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-0201A-1 RecircA Tee 2L 11498 7.248 3.676 4.033 2-0201A-2 Tee 2L Tee 2M 2313 2.354 0.039 0.091 2-0201A-3 Tee 2L Tee 2K 6864 6.986 0.353 0.820 2-0201A-4 Tee 2K Tee 2J 4572 4.654 0.059 0.137 2-0201A-5 Tee 2J Tee 2H 2286 2.326 'O.015 0.034 2-0201H-1 Tee 2H Noz2H 2286 6.968 6.301 1.376 l 2-0201H-2 Noz2H Ram 2H 2286 9.307 17.61 29.9 2-0201J-1 Tee 2J Noz2J 2287 6.972 6.301 1.377 2-0201J-2 Noz2J Ram 2J 2287 9.312 17.63 29.93 I 2-0201K-1 Tee 2K Noz2K 2292 6.987 6.304 1.383 2-0201K-2 Noz2K Ram 2K 2292 9.332 17.68 30.06 2-0201L-1 Tee 2L Noz2L 2321 7.077 6.322 1.425 2-0201L-2 Noz2L Ram 2L 2321 9.452 18.01 30.84 2-0201M-1 Tee 2M Noz2M 2313 7.05 6.383 1.566 2-0201M-2 Noz2M Ram 2M 2313 9.416 17.92 30.61 l 2-1006A-1 Dis 10A T1032A 5753
- 16.33 0.055 0.127 2-1006A-2 T1032A T1006A 5753
- 16.33 8.13 10.45 2-1006B-1 Dis 10B T1032B 5745
- 16.31 0.055 0.127 2-1006B-2 T1032B T1006B 5745
- 16.31 8.117 10.42 2-1008A-1 T1006B InHXA 5198 7.246 1.707 1.172 2-1008A-2 T1006B <-> T1006A 547.5 0.763 0.001 0.003 .
2-1008A-3 T1006A T1008A 6300 8.784 11.77 6.828 2-1009A-1 OutHXA T1008A 5198 7.246 0.124 0.289 2-1009A-2 T1008A T1010A 11498
- 16.03 0.672 1.561 2-1009A-3 T1010A Red 1012A 11498
- 16.03 5.443 16.13 2-1010 T1010A T1010B closed 0 0 0 2-1012A-1 Red 1012A V28A 11498
- 20.21 6.293 6.527 2-1012A-2 V28A V29A 11498
- 22.95 15.44 '35.84 2-1012A-3 V29A RecircA 11498
- 22.19 16.51 21.9 2-1015A-1 X-223A Tee 10A-1 11498 8.696 2.439 2.91 2-1015A-2 Tee 10A-1 Red 10A 5753 4.351 0.178 0.414 2-1015B-1 X-223B Tee 10B-1 closed 0 0 0 2-1016A-1 Red 10A Tee 10A-2.5753
- 13.4 (1.714 1.191
)
2-1016A-2 Tee 10A-2 Suc10A 5753
- 13.4 0.625 2.951
1016B-1 Tee 10A-1 Tee 10B-2 5745
- 13.38 (0.879 ) 3.459 2-1016B-2 Tee 10B-I Suc10B 5745
- 13.38 0.713 2.826 2-1025-1 B <-> A 1019 0.814 0 0 2-1025-10 I <-> X-223B 6369 5.087 0.002 0.005 2-1025-11 J <-> I 6369 4.817 0.053 0.123' 2-1025-12 K <-> J 6369 5.087 0.002 0.006 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Page A31 Attachment A
LINEUP PZPELINES - SF-DG 09/25/98
~ PIPELINE FROM TO FLOW VEL dP M1 !
gpm ft/sec psi a ft 2-1025 L <-> K 577.3 0.461 0 0 2-1025-14 M <-> L 577.3 0.437 0.001 0.003 ! 2-1025-15 X-226 <->M 577.3 0.461 0 0 2-1025-16 N <-> X-226 577.3 0.461 0 0 2-1025-17 O <-> N 577.3 0.437 0 0.001 2-1025-18 P <-> 0. 577.3 0.461 0- 0 2-1025-19 .P Q 5208 4.16 0.002 0.004 2-1025-2 C <-> B 1019 0.770 0.005 0.012 2-1025-20 Q R 5208 3.939 0.032 0.075 2-1025-21 R X-224B 5208 4.16 0.001 0.003 2-1025-22 X-224B X-225 5208 4.16 0.032 0.075 2-1025-23 X-225 S 5208 4.16 0.012 0.027 2-1025-24 S T 5208 3.939 0.038 0.089 2-1025-25 T X-224A 5208 4.16 0.028 0.065 2-1025-26 U <-> X-224A 1019 0.814 0 0 2-1025-27 V <-> U 1019 0.770 0.001 0.003 2-1025-28 A <-> V 1019 0.814 0 0 2-1025-3 D <-> C 1019 0.814 0.001 0.003 2-1025-4 D E 5129 4.096 0.002 0.004 2-1025-5 E F 5129 3.879 0.035 0.081 2-1025-6 F X-223A 5129 4.096 0.001 0.003 2-1025-7 G <-> X-223A 6369 5.087 0.020 0.046 2-1025-8 H <-> G 6369 4.817 0.036 0.083 2-1025-9 X-223B <->H 6369 5.087 0.060 0.139 2-1032A T1032A T1032-1 closed 0 0 0 2-1032B-1 T1032B R1032B closed 0 0 0 2-1318-1 X-226 Red 13 ,0 0 0 0 2-1318-2 Red 13 Tee 13 0 0 0 0 2-1318-3 Tee 13 RCIC2 0 0 0 0 2-1401-1 X-224A Tee 14A 6226 8.555 (0.400 ) 2.943 2-1401-2 Teel 4A ' Red 14A 6226 8.555 0.051 0.119 2-1401-3 Red 14A Suc14A 6226 10.95 0.005 0.012 2-1402-1 X-224B Teel 4B closed 0 0 0 2-1403-1 Dis 14A RedCSA 6226
- 17.68 70.93 83.78 2-1403-2 RedCSA V24A 6226
- 25.35 1.301 1.349 2-1403-3 V24A InletA 6226
- 26.78 16.95 30.02 2-2302-1 X-225 Red 23-1 0 0 0 0 2-2302-2 Red 23-1 Tee 23 0 0 0 0 2-2302-3 Tee 23 Red 23-2 0 0 0 0
~ ~
2-2302-4 Red 23-2 HPCI2 0 0 0 0 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A32.
LINEUP PIPELINES SF-DG 09/25/98 PIPEL2NE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft Break-A RecircA Break-A 0 0 0 0 HXA InHXA OutHXA 5198 7.141 9.943 5.37 LA-1 X-204A ZA 0 0 0 0
--- strainer --- dP: --- Hl:
LA-2 ZA A 0 0 0 0 LB-1 X-204B ZB 6147 7.443 (2.498 ) 2.201 strainer --- dP: 0.944 --- Hl: 2.192 LB-2 ZB D 6147 6.782 (0.177 ) 0.590 LC-1 X-204C ZC 5792 7.012 (2.605 ) 1.954
--- strainer --- dP: 0.838 --- Hl: 1.946 LC-2 ZC K 5792 6.39 (0.205 ) 0.524 ~ LD - l ' X-204D ZD 5785 7.004 (2.607 ) 1.95 strainer --- dP: 0.836 --- Hl: 1.941 LD-2 ZD P 5785 6.382 (0.206 ) 0.523 Pmp10A Suc10A Dis 10A 5753
- 16.33 (91.22 ) (211.7)
, --- RHR Pump --- dP: (91.22) --- Hl: (211.7) Pmp10B Suc10B Dis 10B 5745
- 16.31 (91.95 ) (213.4)
--- RHR Pump --- dP: (91.95) --- H1: (213.4)
Pmp14A Suc14A Dis 14A 6226
- 17.68 (169 ) (392.4)
--- CS Pump --- dP: (169) --- Hl: (392.4).
SpargerA InletA CSOutA 6026
- 25.92 82.85 192.3 1
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A33
. Company: Comed SHRT-NEW Projset:
by: Doug Collina 09/25/98 LINEUP. REPORT rev: 09/25/98 LINELIST: SHRT-NEW DEVIATION: 0.0001 % dated: 09/25/98 after: 12 iterations , volumetric flow rates require constant fluid properties in all pipelines. Fluid properties in the first specification were used. NODE DEMAND NODE DEMAND gpm- gpm InletA >>> 200 InletB >>> 200 ' FLOWS IN: 0 gpm FLOWS OUT: 400 gpm NET FLOWS OUT: 400 gpm PIPELINE FLOW PRESSURE SET gpm SOURCE psia Break-A >>> 20156 >>> Break-A 14.7 i SpargerA >>> 6024 >>> CSoutA 14.7 SpargerB >>> 5971~ >>> CSOutB 14,7 ; 2-1079-1 >>> 298.9 >>> Torus 2 14.7 LA-1 <<< 8161 <<< X-204A 14.7 ' LB-1 <<< 8263 <<< X-204B 14.7 LC-1 <<< 8270 <<< X-204C 14.7 LD-1 <<< 8156 <<<- X-204D 14.7 1 I FLOWS IN: 32850 gpm FLOWS OUT: 32450 gpm NET FLOWS- IN: 400 gpm ; i- ) I l l 1 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page AM
LINEUP NODES SHRT-NEW 09/25/98 L -NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft lL A 559.5
- 17.11 599.2 B 559.5
- 17.-11 l
599.2 Break-A 605.5 p 14.7 639.6 Break-B 605.5
- 136 921.2 C 559.5
- 599.2 i
17.09 CSOutA 647.5 p 14.7 681.6 CSOutB 647.5 p 14.7 681.6 l D 559.5
- 17.09 599.2 Dis 10A- 555.58
- 159.1 924.8 Dis 10B 555.58
- 159.1 924.8 Dis 10C 555.58
- 163.8 935.7 l Dis 10D 555.58
- 163.8 935.7 Dis 14A: 555.63
- 186.6 988.8 Dis 14B 555.63
- 190.2 997.2 E 559.5
- 17.08 599.2 F 559.5
- 16.95 598.8 i G 559.5
- 16.95 598.8 H 559.5
- 16.95 598.8 HPCI2 556.08 18.54 599.1 I 559.5
- 16.95 598.8 InHXA 566.79
- 150.2 915.4 InHXB 566.79
- 155 926.5 InletA 647.5 > 200
- 97.48 873.8 InletB 647.5 > 200
- 96.04 870.4 J 559.5
- 17.08 599.2 K 559.5
- 17.09 599.2 L 559.5
- 17.09' 599.2 M 559.5
- 17.11 599.2 N 559.5
- 17.11 599.2 Noz2C 623.25
- 128.4 921.2 Noz2D 623.25
- 128.4 921.2 Noz2E 623.25
- 128.4 921.2 i
Noz2F 623.25
- 128.4 921.2 Noz2G 623.25
- 128.4 921.2 0 559.5 .
- 37.11 599.2 i
l OutHXA 584.5
- 140.7 911.1 -
l OutHXB 584.5
- 145.6 922.5 P 559.5
- 17.12 599.2 - -
Q 559.5
- 17.11 599.2 l'
l . PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A3T 4
LINEUP NODES SHRT-EEW 09/25/98 NODE ELEFATION DEMAND PRESSURE ft H GRADE gpm . psi a ft i R 559.5
- 17.07 599.1 R1032C. 563
- 27.63 ' 627.1 Ram 2C 634.23 + 123.7 921.2 Ram 2D B34.23
- 123.7 921.2
. Ram 2E 634.23
- 123.7 921.2 Ram 2F 634.23
- 123.7 921.2 Ram 2G 634.23-
- 123.7 921.2 RCIC2 556.83 18.26 599.2 RecircA 605.5
- 24.81 663.1 RecircB 605.5
- 136 921.2 Red 1012A 581
- 120.3 860,1 Red 1012B 580.67
- 146.7 921.2 Red 10A 562.25
- 14.61 596.2 Red 10B 562.25
- 14.63 596.2 Red 13 561.46 16.26 599.2 Red 14A 555.63 17.41 596.1 Red 14B 555.63 17.44 596.1 Red 23-1 562.25
- 15.88 599.1 Red 23-2 556.08 18.54 599.1 RedCSA 636.5
- 115.7 905.1 RedCSB 642.25
- 113.2 905 S 559.5-
- 17.06 5-99.1 Suc10A 555.58 16.06 592.9 Suc10B 555.58 15.46 591.5 Suc10C 555.58 15.43 -
591.4 Suc10D 555.58 16.39 593.6 Suc14A 555.63 17.41 596 Suc14B 555.63 17.44 596.1 T 559.5
- 17.06 599.1 T1006A 564
- 151.8 916.4 T1006B 564
- 151.8 916.4 T1006C 564
- 156.5 927.4 T1006D 564 + 156.5 927.4 T1008A 584.5
- 140.6 910.9 T1008B 584.5 .
145.5 922.3 T1010A 584.5
- 140.1 909.6 .
T1010B 584.5
- 145.1 921.2 T1032A 555.58
- 159 924.7 - ~
T1032B 555.58
- 159 924.7 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A%
^ ~ ~ _ . - . . - - .- -- - - - - - '
l LINEUP NODES JHRT-NEW l 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ft l T1032C '555.58
- 163.5 935.1 i T1032D' 555.58
- 163.5 935.1 T1079-1 563
- 27.47 1 626.8 j T1079-2 588 6.299 602.6 l
Tee 10A-1 562.25
- 14.76 596.5 l- Tee 10A-2 557.08 16.43 595.2 Tee 10B-1 562.25
- 14.77 596.5 Tee 10B-2 556.75 15.93 593.7 Tee 10C-2 556.79 15.82 593.5
. Tee 10D-2 556.92 16.74 595.8 i Tee 13 557.33 18.04 599.2 !
Teel 4A 555.63 17.47 596.2 Teel 4B 555.63 17.49 596.2 [ Tee 23 562.67 15.7 599.1 Tee 2C 610
- 134.1 921.2 Tee 2D 610
- 134.1 921.2 Tee 2E 610
- 134.1 921.2 Tee 2F 610
- 134.1 921.2 Tee 2G 610
- 134.1 921.2 Torus 2 568.5 p 14.7- 602.6 U 559.5
- 17.07 599.1-V 559.5
- 17.11 599.2 V24A 638.17
- 114.4 903.8 V28A 589.08
- 108.2 840.3 V28B 591.25
- 142.2 -
'921.2 V29A 589.08
- 60.78 730.2
.V29B 591.25
- 142.2 921.2 X-204A 567.5 p 14.7 601.6 X-204B 567.5 p 14.7 601.6 X-204C 567.5 p 14.7 601.6 X-204D 567.5 p 14.7 601.6 X-223A 559.5
- 16.95 598.8 X-223B 559.5
- 16,95 598.8 X-224A 559.5 17.06 599.1 X-224B 559.5 .' 17.06 599.1 X-225 559.5
- 17.06 599.1 s X-226 559.5 17.11 599.2 ZA 560.5
- 17.13 600.3 - -
ZB 560.5
- 17.12 600.2 P!PE-FLO.rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A14
.. ...-..- ~ . - . - . . . - - . . . = - . - . - - -- . -
--.- -- ~---~--~
i i LINEUP NODES ..SHRT-NEW 09/25/98 NODE ELEVATION DEMAND PRESSURE H GRADE j .- ft gpm- psi,a
. ft j '= ZC-
, 56'O.5-
- 17,12 600.2 l ZD' 560.5 -*- 17.13 600.3 i.
l I b' i-
.)
s l
- f. ' ,
' PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A3B
LINEUP PIPELINES SHRT-MEW 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-0201A-1 RecircA Tee 2L closed 0 0 0 2-0201B-1 htecircB Tee 2F 0 0 , 0 0 2-0201B-2 Tee 2F Tee 2G 0 0 0 0 2-0201B-3 Tee 2P Tee 2E O O O O 2-0201B-4 Tee 2E Tee 2D 0 0 0 0 2-0201B-5 Tee 2D Tee 2C 0 0 0 0 2-0201C-1 Tee 2C Noz2C 0 0 0 0 2-0201C-2 Noz2C Ram 2C 0 0 0 0 2-0201D-1 Tee 2D Noz2D 0 0 0 0 2-0201D-2 Noz2D Ram 2D 0 0 0 0 2-0201E-1 Tee 2E Noz2E O O O O 2-0201E-2 Noz2E Ram 2E O O O O 2-0201F-1 Tee 2F Noz2F 0 0 0 0 2-0201F-2 Noz2F Ram 2F 0 0 0 0 2-0201G-1 Tee 2G Noz2G 0 0 0 0 2-0201G-2 Noz2G Ram 2G 0 0 0 0 2-1006A-1 Dis 10A T1032A 5147
- 14.61 0.044 0.102 2-1006A-2 T1032A T1006A 5147
- 14.61 7.231 8.365 2-1006B-1 Dis 10B T1032B 5139
- 14.59 0.044 0.102 2-1006B-2 T1032B T1006B 5139
- 14.59 7.221 8.341 2-1006C-1 Dis 10C T1032C 5078
- 14.42 0.271 0.628 2-1006C-2 T1032C T1006C 4928
- 13.99 6.951 7.714 2-1006D-1 Dis 10D T1032D 5091
- 14.45 0.272 0.631 2-1006D-2 T1032D T1006D 4942
- 14.03 6.969 7.757 2-1008A-1 T1006B InHXA 4650 6.483 1.607 0.939 2-1008A-2 T1006B <-> T1006A 489.4 0.682 0'.001 0.002 2-1008A-3 T1006A T1008A 5636 7.858 11.19 5.466
.2-1008B-1 T1006D T1008B 5380 7.501 11.01 5.049 2-1008B-2 T1006C T1006D 438.5 0.611 0 0.002 2-10088-3 T1006C InHXB 4490 6.259 1.559 0.828 2-1009A-1 OutHXA T1008A 4650 6.483 0.100 0.231 2-1009A-2 T1008A T1010A 10286
- 14.34 0.538 1.25 2-1009A-3 T1010A Red 1012A 20156
- 28.1 19.82 49.51 2-10098-1 OutHXB T1008B 4490 6.259 0.093 0.216 2-1009B-2 T1008B T1010B 9870
- 13.76 0.453 1.052 2-10098-3 T1010B ' Red 1012B 0 0 0 0 2-1010 T1010B <-> T1010A 9870
- 13.76 4.999 11.6 i- 2-1012A-1 Red 1012A V28A 20156
- 35.43 12.05 19.89 2-1012A-2 V28A V29A 20156
- 40.23 47.42 110.1' 2-1012A-3 V29A RecircA 20156
- 38.89 35.98 67.09 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A31
LINEUP PIPELINES - SHRT-NEW 09/25/98 PIPELINE- FROM TO FLOW VEL dP M1 gpm ft/sec psi a ft 2-1012B-1 Red 1012B V28B 0 0 0 0 2-1012B-2 Y28B V29B 0 0 0 0 2-1012B-3 V29B RecircB 0 0 0 0 2-1015A-1 X-223A Tee 10A-1 10286 7.779 2.189 2.331 2-1015A-2 Tee 10A-1 Red 10A 5147 0.143
.'.892 0.331 2-1015B-1 X-223B Tee 10B-1 10169 7.691 2.172 2.293 2-1015B-2 Tee 10B-1 Red 10B 5078 3.841 0.141 0.328 2-1016A-1 Red 10A Tee 10A-2 5147 11.98 (1.816 i
) 0.955 2-1016A-2 Tee 10A-2 Suc10A 5147 11.98 0.372 2.364 2-1016B-1 Tee 10A-1 Tee 10B-2 5139 11.97 (1.177 ) 2.768 2-1016B-2 Tee 10B-2 Suc10B 5139 11.97 0.471 I
2.263 i 2-1016C-1 Red 10B Tee 10C-2 5078 11.83 (1.19 ) 2.697 2-1016C-2 Tee 10C-2 Suc10C 5078 11.83 0.396 2.13 2-1016D-1 Tee 10B-1 Tee 10D-2 5091 11.85 (1.967 ) 0.765 2-1016D-2 Tee 10D-2 Suc10D 5091 11.85 0.350 2.153 2-1025-1 A B 1993 1.592 0 0 l 2-1025-10 I <-> X-223B 10199 8.146 0.005 0.012 ! 2-1025-11 J <-> I 10199 7.713 0.132 0.306 2-1025-12 K <->J 10199 8.146 0.006 0,014 2-1025-13 L <-> K 1929 1.541 0.004 0.009 2-1025-14 M <-> L 1929 1.459 0.013 0.030 2-1025-15 X-226 <-> M 1929 1.541 0 0 l 2-1025-16 N <-> X-226 1929 1.541 0.004 0.009 2-1025-17 0 <-> N 1929 3.459 0.005 0.011 2-1025-18 P <-> 0 1929 1.541 0 0 2-1025-19 P Q 6227 4.974 0.002 0.005 2-1025-2 B C 1993 1.507 0.019 0.044
~2-1025-20 Q R 6227 4.71 0.046 0.106 2-1025-21 R X-224B 6227 4.974 0.002 0.005 2-1025-22 X-224B X-225 56.31 0.045 0 0 I 2-1025-23 X-225 S 56.31 0.045 0 0 1 2-1025-24 S T 56.31 0.043 0 0 2-1025-25 T X-224A 56.31 0.045 0 0 2-1025-26 U <-> X-224A 6167 4.926 0.002 0.005 2-1025-27 V <-> U 6167 4.664 0.045 I 0.104 ,
2-1025-28 A
<-> V 6167 4.926 0.002 0.005 l 2-1025-3 C D 1993 1.592 0.004 '
0.010 2-1025-4 D E 10256 8.192 0.006 0.014 2-1025-5 E F 10256 7.757 0.133 0.310' 2-1025-6 F- X-223A 10256 8.192 0.005 0.012 1 PIPE-FLO rev 4.11 Calc No. QDC-1000-M-0454, Rev. 1. Attachment A Page AMO 1 l 1
._. __ __ m . _ _ _ _ _- . .- _ . _ . . _ . __ . _ _ __ ,___
LINEUP PIPELINES SMRT-NEW 09/25/98 PIPELINE FROM TO FLOW VEL dP H1 gpm ft/sec psi a ft 2-1025-7 , G <-> X-223A 29.69 0.024 0 0
~
2-1025-8 H <-> G 29.69 0.022 0 0 L 2-1025-9 X-223B <-> H 29.69 . 0.024 0 0 2-1032A T1032A T1032-1 closed 0 0 0 2-1032B-1 T1032B R1032B closed 0 0 0 2-1032C-1 T1032C R1032C 150.2
- 16.34 135.9 307.9 2-1032C-2 R1032C T1079-1 150.2 6.525 0.156 0.362 l 2-1032D T1032D T1079-1 148.7
- 16.17 136 308.3 2-1079 T1079-1 T1079-2 298.9
- 12.98 21.17 24.15 2-1079-1 T1079-2 Torus 2 298.9 1.217 (8.401 ) 0 2-1318 X-226 Red 13 0 0 0 0 2-1318 Red 13 Tee 13 0 0 0 0 2-1318-3 Tee 13 RCIC2 0 0 0 0 2-1401-1 X-224A Teel 4A 6224 8.551 (0.401 ) 2.94 2-1401-2 Teel 4A Red 14A G224 8.551 0.051 0.119 2-1401-3 Red 14A- Suc14A 6224 10.94 0.005 0.012 2-1402-1 X-224B Tee 14B 6171 8.479 (0.429 ) 2.875 l
2-1402-2 Teel 4B Red 14B 6171 8.479 0.049 0.114 2-1402-3 Red 14B Suc14B 6171 10.85 0.007 0.017 2-1403-1 Dis 14A RedCSA 6224
- 17.67 70.9 83.71 2-1403-2 RedCSA V24A 6224
- 25.34 1.3 1.348 2-1403-3 V24A InletA 6224
- 26.77 16,94 29.99 2-1404-1 Dis 14B RedCSB 6171
- 17.52 77.04 92.21 2-1404-2 RedCSB InletB 6171
- 26.54 17.16 34.59 2-2302-1 X-225 Red 23-1 0 0 0 0 2-2302-2 Red 23-1 Tee 23 0 0 0 0 2-2302-3 Tee 23 Red 23-2 0 0 0 0 2-2302-4 Red 23-2 HPCI2 0 0 0 0 Break-A RecircA Break-A 20156
- 38.89 10.11 23.46 Break-B RecircB Break-B 0 0 0 0 HXA InHXA OutHXA 4650 6.388 9.481 4.298 HXB InHXB OutHXB 4490 6.168 9.356 4.007 LA-1 X-204A ZA 6161 9.88 (2.431 ) 1.357
--- strainer --- dP: 0.577 --- Hl: 1.34 LA-2 ZA A 8161 9.003 0.017 1.04 LB-1 X-204B .' ZB 8263 10 (2.419 ) 1.385
--- strainer --- dP: 0.589 --- Hl: 1.368 LB-2 ZB D 8263 9.116 0.028 1.066 l LC-1 X-204C 2C 8270 10.01 (2.418 )
! 1.387, ,
--- strainer'--- dP: 0.590 --- Hl: 1.37 LC-2 ZC 'K 8270 9.124 0.029 1.068.
PIPE-FLO rev 4.11 Calc No. QDC-1000-M-0454, Rev. 1. Attachment A Page A'il
- . . .. - - .. .. - . - _ . = .-- - -. - . . - -
LINEUP PIPELINES SHRT-NEW 09/25/98 PIPELIME FROM TO FLOW VEL dP H1 gpm ft/see psi a ft LD-1 X-204D ZD 8156 9.875 (2.432 ) 1.356
--- strainer - *- dP: 0.577 --- Hl: 1.339 LD-2 ZD P 8156 8.999 0.017 1.039 Pmp10A Suc10A Dis 10A 5147
- 14.61 (143 ) (332)
--- RHR Pump --- dP: (143) --- Hl: (332) ;
Pmp10B l Suc10B Dis 10B 5139 (143.6
--- RHR Pump --- dP: (143.6) --- Hl: (333.3)
- 14.59 ) (333.3) l' Pmp10C Suc10C Dis 10C 5078
- 14.42 (148.3 ) (344.3)
--- RHR Pump --- dP: (148.3) --- Hl: (344.3) )-
Pmp10D Suc10D Dis 10D 5091
- 14.45 (147.4 ) (342.1)
--- RHR Pump --- dP: (147.4) --- Hl: (342.1)
Pmp14A Suc14A Dis 14A 6224
- 17.67 (169.2 ) (392.8)
--- CS Pump --- dP: (169.2) --- Hl: (392.8)
Pmp14B Suc14B Dis 14B 6171
- 17.52 (172.8 ) .(401.1)
--- CS Pump --- dP: (172.8) --- Hl: (401.1)
SpargerA InletA CSoutA- 6024
- 25.91 82.78 192.2 l SpargerB InletB CSOutB 5971
- 25.68 81.34 188.8
]
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A%
Comp:ny: Comed Projset: LSL-FEW by: Doug Collins 09/28/98 LINEUP REPORT rev: 09/28/98 LINELIST: SHORT DEVIATION: 9.le-005 % dated: 09/25'/98 after: 13 iterations Volumetric flow rates require constant fluid properties in all pipelines. Fluid properties in the first specification were used, j 1 NODE DEMAND NODE DEMAND 9Pm gpm Suc14A >>> 5650 Suc14B >>> 5650 FLOWS IN: 0 gpm FLOWS OUT: 11300 gpm NET FLOWS OUT: 11300 gpm PIPELINE FLOW PRESSURE SET gpm- SOURCE psia Break-A >>> '20091 >>> Break-A 14.7 2-1079-1 >>> 298.1 >>> Torus 2 14.7 LB-1 <<< 10673 <<< X-204B 14.7 LC-1 <<< 10519 <<< X-204C 14.7 LD-1 <<< 10498 <<< X-204D 14.7 FLOWS IN: 31690 gpm l FLOWS OUT: 20389 gpm ; NET FLOWS IN: 11301 gpm I l l l ,. l PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A93
.- . . _ . . . . .- - ...-_.-_~ ._.... .. . . . - . _ ~ - . - - _ ~ . .
LINEUP NODES - LSL-FEW 09/28/9E NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm. psi a , ft i L A 559.5
- 14.92 594.1 B 559.5
- 14.92 =594.1 Break-A 605.5 p 14.7 639.6 Break-B 605.5
- 135.3 919.5 .
_C 559.5
- 14.95 594.2 D 559.5
- 14.95 594.2 Dis 10A 555.58
- 158.3 923 j Dis 10B 555.58
- 158.3 923
. Dis 10C 555.58
- 162.9 933.8 1
I Dis 10D 555.58
- 163 933.8 E 559.5
- 14.95 594.'2 !
F. 559.5
- 14.86 594 G 559.5
- 14.85 594 H 559.5
- 14.86 594-HPCI2 556.08 16.43 594.2 l- I 559.5
- 14.87 594 InHXA 566.79
- 149.4 913.7 InHXB 566.79
- 154.2 924.7 J 559.5
- 15.05 594.4
'K 559.5
- 15.06 594.5 I L 559.5
- 15.06 594.5 M 559.5.
- 15.07 594.5 N 559.5
- 15.07 594.5 Noz2C 623.25
- 127.6 919.5 Noz2D 623.25
- 127.6 919.5 No:2E 623.25
- 127.6 919.5 Noz2F 623.25
- 127.6 919.5 No:2G 623.25
- 127.6 919.5 0 559.5
- 15.07 594.5 OutHXA 584.5
- 140 909.4
- l. OutHXB 584.5
- 144.8 920.7 P 559.5
- 15.07 594.5 Q 559.5
- 15.07 594.5 R 559.5
- 14.97 594.3 R1032C 563
- 27.57 627 Ram 2C 634.23
- 122.9 919.5 .
- Ram 2D 634.23
- 122.9 919.5
, Ram 2E 634.23
- 122.9 919.5 -
- l Ram 2F 634.23
- 122.9 919.5 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page AVI
- . - . .- . . . ~ . -. ~_~ . - . - . - - . _ - . - . ..
LINEUP NODES LSL-FEW 09/28/98 NODE ELEVATION DEMAND PRESSURE H GRADE ft gpm psi a ' ft Ram 2G 634.23
- 122.9 919.5 RCIC2 556.83 16.22 594.5 RecircA 605.5
- 24.74 662,9 RecircB 605.5
- 135.3 919.5 Red 1012A 581
- 119.6 858.7 Red 1012B 580.67
- 145.9 919.5 Red 10A 562.25
- 12.53 591.3 Red 10B 562.25
- 12.56 591.4 Red 13 561.46 14.22 594.5 Red 14A 555.63 15.5 591.6 Red 14B 555.63 15.55 591.7 Red 23-1 562.25
- 13.77 594.2 L- Red 23-2 556.08 16.43 594.2 S 559.5
- 14.95 594.2 Suc10A 555.58 13.98 588 Suc10B 555.58 13.39 586.7 Suc10C 555.58 13.36 586.6 Suc10D 555.58 14.32 588.8 Suc14A 555.63 > 5650 15.49 591.6 Suc14B 555.63 > 5650 15.55 591.7 T 559.5 * .
14.93 594.2 T1006A 564
- 151 914.6 T1006B 564
- 151 914.6 T1006C 564
- 155.7 925.5 T1006D 564
- 155.7 .
925.5 T1008A 584.5
- 139.9 909.2 T1008B 584.5
- 144.8 920.5 T1010A 584.5
- 139.3 907.9 T1010B 584.5
- 144.3 919.5 T1032A 555.58
- 158.2 922.9 T1032B 555.58
- 158.2 922.9 T1032C 555.58
- 162.7 933.2 l- T1032D 555.58
- 162.7 933.2 l -T1079-1 563
- 27.42 626.6 l
T1079-2 588 . 6.299 602.6 Tae10A 562.25
- 12.67 591.7 .
Tee 10A-2 557.08 14.35 590.4 Tee 10B-l' 562.25
- 12.7 591.7 - -
Tee 10B-2 556.75 13.86 588.9 PIPE-FLO rev 4.11 ~ Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page AMS" l y
- .. . - - - - . . .. - _ .~. ~.- . . - ~ . . - . . . .. . - . --- .-.
LINEUP NODES - LSL-FEW l 09/28/98 NODE ELEVAT80N. DEMAND PRESSURE H GRADE
.ft gpm psi a ft i
l Tee 10C-2 596.79 13.75 588.7 Tee 10D-2 556.92 14.67 591 L Tee 13 557.33- 16 594.5 Teel 4A 555.63 15.54 591.7 Teel 4B 555.63 15.59 591.8
. Tee 23 562.67 13.59 594.2 Tee 2C 610.
- 133.3 919.5 Tee 2D 610
- 133.3 919.5 Tee 2E 610
- 133.3 919.5 Tee 2F 610
- 133.3 919.5 Tee 2G 610
- 133.3 919.5 Torus 2 568.5 p 14.7 602.6 U 559.5
- 14.92 594.1 V 559.5
- 14.92 594.1 V28A 589.08
- 107.7 839 V28B 591.25
- 141.4 919.5 V29A 589.08
- 60.54 729.6 V29B 591.25
- 141.4 919.5 X-204A 568.5 11.05 594.1 X-204B 568.5 p 14.7 602.6 X-204C 568.5 p 14.7 602.6 X-204D 568.5 p 14.7 602.6 X-223A 559.5
- 14.85 594 X-223B 559.5
- 14.86 594 X-224A 559.5 14.92 594.1 X-224B 559.5 14.97 594.2
.X-225 559.5
- 14.95' 594.2 X-226 559.5 15.07 594.5 ZA 560.5
- 14.49 594.1 ZB 560.5
- 15.29 596 ZC 560.5
- 15.37 596.2 ZD 560.5
- 15.38 596.2 l-PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1- Attachment A Page A%
l
LINEUP PIPELINES LSL-FEW 09/28/98 j (' PIPELINE FROM TO FLOW VEL dP H1 l gpm ft/see psi a ft )
~
2-0201A-1 RecircA Tee 2L closed 0 0
' 0 2-0201B-1 RecircB Tee 2F 0 0 0 0 !
i 2-0201B-2 Tee 2F Tee 2G 0 0 0 l 0 l: 2-0201B-3 Tee 2F Tee 2E O O O O 2-0201B-4 Tee 2E Tee 2D 0 0 0 0 2-0201B-5 Tee 2D Tee 2C 0 0 0 0 2-0201C-1 Tee 2C Noz2C 0 0 0 0 0201C-2 Noz2C Ram 2C 0 0 0. 0 2-0201D-1 Tee 2D Noz2D 0 0 0 0 2-0201D-2 Noz2D Ram 2D 0 0 0 0 2-0201E-1 Tee 2E Noz2E O O O O 2-0201E-2 Noz2E Ram 2E O O O O 2-0201F-1 Tee 2F Noz2F 0 0 0 0 2-0201F-2 Noz2F Ram 2F 0 0 0 0 2-0201G-1 Tee 2G Noz2G 0 0 0
, 0 2-0201G-2 Noz2G Ram 2G 0 0 0 0 2-1006A-1 Dis 10A T1032A 5130
- 14.56 0.044 0.102 l 2-1006A T1032A T1006A 5130
- 14.56 7.208 8.312 2-1006B-1 Dis 10B T1032B 5123
- 14.54 0.044 0.101 2-1006B-2 T1032B T1006B 5123
- 14.54 7.198 8.288 2-1006C-1 Dis 10C T1032C 5062
- 14.37 l
0.269 0.624 2-1006C-2 T1032C T1006C 4912
- 13.95 6.93 7.665 2-1006D-1 Dis 10D T1032D 5074
- 14.41 0.270 0.627 2-1006D-2 T1032D T1006D 4926
- 13.99 6.948 7.708 2-100BA-1 T1006B InHXA 4635 6.462 1.604 0.933 2-1008A-2 T1006B <-> T1006A 487.8 0.680 0.001 0.002 2-1008A-3 T1006A T1008A 5618 7.833 11.17 5.431 2-1008B-1 T1006D T1008B 5363 7.477 10.99 5.017 2-1008B-2 'T1006C T1006D 437.1 0.609 0 0.002 2-1008B-3 T1006C InHXB 4475 6.239 1.556 0.823 2-1009A-1 OutHXA T1008A 4635 6.462 0.099 0.230 2-1009A-2 T1008A T1010A 10253
- 14.29 0.535 1.242 2-1009A-3 T1010A Red 1012A 20091
- 28.01 19.68 49.19 1009B-1 OutRXB T1008B 4475 6.239 0.093 0.215 2-1009B-2 T1008B T1010B 9838
- 13.72 0.450 1.046 2-1009B-3 T1010B '
Red 1012B 0 0 0 0 2-1010 T1010B <-> T1010A 9838
- 13.72 '
i 4.967 11.53 j 2-1012A-1 . Red 1012A V28A 20091
- 35.32 11.99 19.76 2-1012A-2 V28A V29A 20091
- 40.1 47.12 109.4 '
2-1012A-3 V29A RecircA 20091
- 38.77 35.79 66.66.
PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page AM 1
LINEUP PIPELINES LSL-FEW e 09/28/98 I PIPELINE FROM TO FLOW VEL dP H1 gpm ft/see psi a ft 2-1012B-1 Red 1012B V28B 0 0 0 i
, 0 !
2-10128-2 V28B V29B 0 0 0 0 2-1012B-3 V29B RecircB U 0 0 t 0 2-1015A-1 X-223A Tee 10A-1 10253 7.754 2.183 2.316 l 2-1015A-2 Tee 10A-1 Red 10A 5130 3.88 0.142 ! 0.329 2-1015B-1 X-223B Tee 10B-1 10136 7.666 2.166 2.278 l 2-1015B-2 Tee 10B-1 Red 10B 5062 3.828 l 0.140 0.326 i 2-1016A-1 Red 10A Tee 10A-2 5130 11.95 (1.819 ) 0.949 2-1016A-2 Tee 10A-2 Suc10A 5130 11.95 0.366 2.349 2-1016B-1 Tee 10A-1 Tee 10B-2 5123 11.93 (1.184 ) 2.751 2-1016B-2 Tee 10B-2 Suc10B 5123 11.93 0.465 2.249 2-1016C-1 Red 10B Tee 10C-2 5062 11.79 (1.198 ) 2.679 2-1016C-2 Tee 10C-2 Suc10C 5062 11.79 0.390 2.116 l 2-1016D-1 Tee 10B-1 Tee 10D-2 5074 11.82 (1.969 ) 0.760 2-1016D-2 Tee 10D-2 Suc10D 5074 11.82 0.344 2.139 2-1025-1 B <-> A 2207 1.763 0 0 l 2-1025-10 I <-> X-223B 11923 9.523 0.007 0.017 2-1025-11 J <-> I 11923 9.017 0.179 0.416 2-1025-12 K <-> J 11923 9.523 0.008 0.018 2-1025-13 L <-> K 1405 1.122 0.002 0.005 2-1025-14 M <-> L 1405 1.062 0.007 0.016 1 2-1025-15 X-226 <-> M 1405 1.122 0 0 2-1025-16 N <-> X-226 1405 1.122 0 002 0.005 2-1025-17 O <-> N 1405 1.062 0.003 0.006 2-1025-18 P <-> 0 1405 1.122 0 0 2-1025-19 P Q 9093 7.263 0.00'5 0.011 2-1025-2 C <-> B 2207 1.669 0.023 0.053 2-1025-20 Q R 9093 6.877 0.096 d.222 2-1025-21 R X-224B 9093 7.263 0.004 0.010 2-1025-22 X 224B X-225 3443 2.75 0,014 0.033 2-1025-23 X-225 S 3443 2.75 0.005 0.012 l 2-1025-24 S T 3443 2.604 0.017 0.040 l 2-1025-25 T X-224A 3443 2.75 0.07.2 0.028 2-1025-26 U <-> X-224A 2207 1.763 0 0 2-1025-27 V <-> U 2207 1.669 0.006 l 0.015 . 2-1025-28 A
<-> V 2207 1.763 0 0 2-1025-3 D <-> C 2207 1.763 0.005 0.012 l 2-1025-4 D E 8466 6.762 0.004 0.010
. 2-1025-5 E F 8466 6.403 0.092
~ '
0.213 2-1025-6 .F ~X-223A 8466 6.762 0.004 0.009 PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A%S
LINEUP PIPELINES LSL-FEW 09/28/98 l P2PELINE FROM TO FLOW VEL dP H1 gpm ft/sec psi a ft 2-1025-7 G <-> X-223A 1787 1.427
, 0.002 0.004 2-1025-8 H <-> G 1787 1.351 0.003 0.007 2-1025-9 X-223B <-> H 1787 1.427 0.005 0.011 2-1032A T1032A T1032-1 closed 0 0 0 2-1032B-1 T1032B R1032B closed 0 0 0 2-1032C-1 T1032C R1032C 149.8
- 16.29 135.1 306.2 2-1032C-2 R1032C T1079-1 149.8 6.506 0.155 l 0.360 2-1032D T1032D T1079-1 148.3
- 16.13 135.3 306.6 2-1079 T1079-1 T1079-2 298.1
- 12.95 21.12 24.01 l 2-1079-1 T1079-2 Torus 2 298.1 1.214 (8.401 ) 0 I 2-1318-1 X-226 Red 13 0 0 0 0 2-1318-2 Red 13 Tee 13 0 0 0 0 2-1318-3 Tee 13 RCIC2 0 0 0 0 2-1401-1 X-224A Tee 14A 5650 7.763 (0.623 ) 2.425 2-1401-2. Teel 4A Red 14A 5650 7.763 0.042 0.098 2-1401-3 Red 14A Suc14A 5650 9.932 0.004 0.010 2-1402-1 X-224B Tee 14B 5650 7.763 (0.628 ) 2.412 2-1402-2 Teel 4B Red 14B 5650 7.763 0.041 0.096 2-1402-3 Red 14B Suc14B 5650 9.932 0.006 0.014 2-2302-1 X-225 Red 23-1 0 0 0 0 2-2302-2 Red 23-1 Tee 23 0 0 0 0 2-2302-3 Tee 23 Red 23-2 0 0 0 0 2-2302-4 Red 23-2 HPCI2 0 0 0 0 Break-A RecircA Break-A 20091
- 38.77 10.04 23.31 Break-B RecircB Break-B 0 0 0 0 HXA InHXA OutHXA 4635 6.368 '9.4'69 4.271 HXB InHXB OutHXB .4475 6.149 9.345 3.981 LA-1 X-204A ZA 0 0 0 'O strainer --- dP: --- Hl:
LA-2 ZA A 0 0 0 0 LB-1 X-204B ZB 10673
- 12.92 (0.588 ) 6.635 strainer --- dP: 2.847 --- Hl: 6.608 LB-2 ZB D 10673 11.78 0.335 1.778 LC-1 X-204C ZC 10519
- 12.73 (0.670 ) 6.445 strainer --- dP: 2.765 --- Hl: 6.417 LC-2 ZC K 10519 11.6 0.313 1.727 LD-1 X-204D '
ZD 10498
- 12.71 (0.681 ) 6.419 strainer --- dP: 2.754 --- Hl: 6.392 .
LD-2 ZD P 10498 11.58 0.310 1.72 Pmp10A Suc10A Dis 10A 5130
- 14.56 (144.3 ) (335) - -
--- RHR Pump --- dP: (144.3) --- Hl: (335)
PIPE-FLO rev 4.11 Calc. No. ODC-1000-M-0454, Rev. 1. Attachment A Page AT}
l LINEt?P PIPELINES -Lgt.FEW 09/28/98 PIPEL2NE- FROM TO FLOW VEL dP H1 gpm ft/see psi a ft Pmp10B Suc10B' Dis 10B 5123
- 14.54 (144.9 ) (336.3)
--- RHR Pump - *- dP: (144.9) --- Hl: (336.3)
Pmp10C Suc10C Dis 10C 5062
- 14.3i (149.6 ) (347.2)
--- RHR Pump ---.dP: (149.6)~--- Hl: (347.2)
Pmp10D Suc10D. Dis 10D 5074
- 14.41 (148.6 ) (345)
--- RHR Pump --- dP: (148.6) --- Hl: (345) j Pmp14A Suc14A Dis 14A closed 0 0 0 l
--- CS Pump --- dP:
--- Hl:
l; Pmp14B Suc14B Dis 14B- closed 0 0 0 l --- CS Pump --- dP: --- Hl: l'
-1 i
s
- PIPE-FLO rev 4.11 Calc. No. QDC-1000-M-0454, Rev. 1. Attachment A Page A50 (Rat)
rnoas can so oun noon rax No.: assesssrso, es-es.,7 esiss, p.e7 C-, 0.. NN' , * ].
. . C&
September 24, 1992 Ms. Sharon Eldridge Commonwealth Edison Company Rural Route i 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 loss-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 4 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 ID 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 design record file,and evidence of verification of this letter is included in the GE DRF-T23-00692. Sincerely, 3 f S. Mintz cc: 91 ' J. E. Torbeck C. T. Young I i Pay 4 1/F W. J. E.,Nash
Calc. No. QDC-1000-M-0454, Rev 4 Attachment C
, Page CL ne three points listed in Design input 4.4 for NPSHR versus flow can be plotted and curve fit (See page J2).' This quadratic interpolation of these three points was detennined as follows:
The NPSHR was defined as a quadratic function: 2 NPSHR = AQ + BQ + C Where Q is the flow rate (gpm) and A, B and C are unknown constants. The following 3 points are defined in Design input 4.4:
- 1. Q=4000 and NPSHR = 25.0 l
- 2. Q=5000 and NPSHR = 30.0 I
- 3. Q=6012 and NPSHR = 40.9 '
Substituting these values into the equation listed above will yield a system of equations: , 4. A(4000)' + B(4000) + C = 25.0 4 5. A(5000)* + B(5000) + C = 30.0 1 6 A(6012)* + B(6012) + C = 40.9 ! This system of equations can be solved for the values of A, B and C: s 4 A = 2.868 x 10 B = -0.0208 i C = 62.35 Substituting these values back into the equation from above yields the quadratic interpolation of NPSHR
- venus Dow:
4 2 NPSHR = (2.868 x 10 )Q -(0.0208I)Q + 62.35 f This curve along with the three data points from Design input 4.4 are shown in the plot on the next page. l l
Chart 1 G z NPSHR Versus Flow P O e 60 7' NPSHR = 2.868E-EQ' - 0.020E IQ + 62.35 > 5 50 j 40 J ~U.
} . _ _ _ _... _
N 30 .- - NPSHR (feet)
,_ Curve Fit of NPSHR (feet) n.
z a
- i. t 20 10 b:
't -
0 1000 2000 3000 4000 5000 6000 7000 8000 o 1 Flow (Q)(gpm) DE P -t i 3'0 s C
, Page 1
__ _ _ _- _ _ .- ~. - - . -- - - CIlc. No. QDC-1000-M-0454, Rev.1. Attachment D Page D1 Table D SF-LSL: 4 RHR/2 CS Injection CS (New Design Basis) CS (Old Design Basis) Available Credited Pool Pool Pool Specific Required Required Time Pressure Pressure Temp Volume Py Flow NPSHR Z-h, Pressure Margin Flow NPSHR Z-h, Pressure Margin (sec) (psig) (psig) (deg. F) (ft'/?b) (psia) (gpm) (feet) (psig) (gpm) (feet) (feet) (feet) (feet) (psig) - (feet) 12 21.6 8.0 112.6 0 016175 1.376 38 23.4 80 t32.7 0.016260 2.391 47 23 2. 8.0 133 6 0.016263 2.448 6224 43.93 6.29 3.82 9.79 6202 43.60 0.74 6.05 4.57 60 23.1 ' 80 133.6 0016263 2.448 6224 43.93 6.29 3.82 9.79 6202 43.60 0.74 6.05 4.57 80 20 8 80 134.2 0 016266 2.487 6224 43.93 6.29 3.86 9.70 6202 43.60 0.74 6.09 4.48 109 18.3 8.0 135.7 0.016274 2.587 6224 43.93 6.29 3.95 9.49 6202 43.60 0.74 6.18 4 27 129 16.8 8.0 137.4 0.016281 2.704 6224 43.93 6.29 4.06 9.24 6202 43.60 0.74 6.29 4.02 146 15.3 80 138 6 0.016287 2.789 6224 43.93 6.29 4.14 9.06 6202 43.60 0.74 6.36 3 84 166 13.5 8.0 140.3 0 016295 2.915 6224 43.93 6.29 4.26 8.79 6202 43.60 0.74 6 48 3.57 188 11.3 80 141.8 0.016302 3.029 6224 43.93 6.29 4.36 8.54 6202 43.60 0.74 6.59 3.32 209 9.2 8.0 142.8 0.016307 3.106 6224 43.93 6.29 4.44 8.37 6202 43.60 0.74 6 66 3 15 239 6.9 2.5 143 9 0.016313 3.195 6224 43.93 6.29 4.52 -4.74 6202 43 60 0.74 6.74 -9.96 276 5.2 2.5 145.1 0.016319 3.293 6224 43.93 6.29 4.61 -4.96 6202 43.60 0.74 6.83 -10 18 311 4.2 2.5 146 0 0.016323 3.368 6224 43.93 6.29 4.68 -5.13 6202 43.60 0.74 6.90 -10.35 352 3.4 2.5 147.0 0 016328 3.454 6224 43.93 6.29 4.76 -5.32 6202 43.60 0.74 6 98 -10.54 394 3.1 2.5 147.7 0.016332 3.515 6224 43.93 6.29 4.82 -5.46 6202 43.60 0.74 7.04 -10 68 441 3.1 2.5 148 4 0.016335 3.577 6224 43.93 6.29 4.88 -5.60 6202 43.60 0.74 7.10 -10.82 491 3.2 2.5 149.2 0 016339 -3 648 6224 43.93 6.29 4.95 -5.75 6202 43.60 0.74 7.16 -10.97 516 3.3 2.5 149.5 0.016341 3.676 6224 43.93 6.29 4.97 -5 82 6202 43.60 0.74 7.19 -11.04 566 3.3 2.5 150.2 0 016344 3.741 6224 43.93 6.29 5.03 -5.96 6202 43 60 0.74 7.25 -11.18 600 3.4 2.5 150.7 0 016347 3.787 6224 43.93 6.29 5.08 -6.07 6202 43.60 0.74 7.29 -11.29
t I Calc. No. QDC-1000-M-0454, Rev.1. Attachment D Page D2 (Final) Old Strainer Design Basis vs. New Design Basis (NRC Bulletin 96-03) j 25 r # - , 20
\\ .
_ Available Pool Pressure , cm o.
- - - Credited Pool Pressure i
[o 15 a CS Req. Press. (New DB) ' 3 O CS Req. Press. (Old DB) 2 n. c E
.E 10 2
e , O -..... .... . .. . .. .. .... . . . . . ., A ,-. r, e r' OEG31 C :: [] O CU 5 ; a:.
, , ,, . _ ; m ,
a . . . . a O ^ s
. t 0
10 100 1000 t i Time (aeconds) ' i, l t
) Calc. No. QDC-1000-M-0454. R;v.1.' Attachm nt E Page E1 a t Table E SF-LSL: 4 RHR/2 CS fnjection CS Available Pool Pool Specific Required Time Pressure Temp ',olume Pv Flow NPSHR Z-h, Pressure Margin { (sec) (psig) (deg. F) (ft*/lb) (psla) (gpm) (feet) (feet) (psig)
! (feet) 12 21.6 112.6 0.016175 1.376 38 23.4 132.7 0.016260 2.391 47 23.2 133.6 0.016263 2.448 5650 36.33 1.83 2.48 48.52 60 23.1 133.6 0.016263 2.448 5650 36 33 1.83 2.48 48.29 80 20.8 134.2 0.016266 2.487 5650 36 33 1.83 2.52 42.83 109 18.3 135.7 0.016274 2.587 5650 36.33 1.83 2.61 36.77 129 16.8 137.4 0.016281 2.704 5650 36.33 1.83 2.72 33.01 146 15.3 138.6 0.016287 2.789 5650 36.33 1.83 2.80 29.32 166 13.5 140.3 0.016295 2.915 5650 36.33 1.83 2.92
' 24.83 188 11.3 141.8 0.016302 3.029 5650 36.33 1.83 '3.03 19.42 209 9.2 142.8 0.016307 3.106 5650 36.33 1.83 3.10 14.33 A8
- Calc. No. QDC-1000-M-0454, Rev.1. Attachment E Page E2 (Final)
Figure E 25 150.0 p%%
/
\ .
20 \ ' 140.0
% / .e .-
a Available Pool Pressure - - . 5 O CS Required Pressure
- c E 15 , 130.0 g
[ Pool Temperature , g E ,' e
- l
- 2 E , m E r N a
= '
j 10 , 120 0 $ o - t
,' 8 9
5 110 0 C C C 0 100 0 1 10 100 1000 Time (seconds) i
l -. l-~ . - [ t-i i-1 i l l j l ATTACHMENT C SVP 98-316 GE Report, GENE-637-022-0893, DRF F23-00711, September,1993, Quad Cities l Nuclear Power Station, Units 1 and 2," Evaluation of the Minimum Post-LOCA Heat Removal Requirements to Assure Adequate NPSH for the Core Spray and LPCI/ Containment Cooling Pumps" i-I- L l i I' e
- -}}