ML20155J325
| ML20155J325 | |
| Person / Time | |
|---|---|
| Site: | Fort Calhoun  |
| Issue date: | 06/12/1992 |
| From: | Harsell R, Raakkonen R ABB COMBUSTION ENGINEERING NUCLEAR FUEL (FORMERLY |
| To: | |
| Shared Package | |
| ML20155J310 | List: |
| References | |
| -MECH-CALC-21, 0-MECH-CALC-021, FC05977, FC5977, NUDOCS 9811120105 | |
| Download: ML20155J325 (128) | |
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LIC-98 0140 Enclosure 2 Calculation FC05977 ABB-CE Evaluation of Containment Spray Pump Net Positive Suction Head Accounting for Sump Subcooling
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9811120105 981029 PDR ADOCK 05000285 P PDR ,
CALCULATION COVER SHEET Calculation Preparation, Review CALCULATON NUMBER Calc. Page No. I and Approval e A'45977
Calculation Cover Sheet .
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CALCULATION COVER SHEET Criculition Prep;r tion, Review CALCULATON NUMBER Cile. Pag] N3. 2-and Approval FC05977 Form PED-OP-3.1 Form Page No. 2 of 2 Calculation Cover Sheet FACluTWSYSTEM FCS /5T
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PRODUCTION ENGINEERING DMSION FCd5777 CALCULATION REVISION SHEET REV' l NO. DESCRIPTION / REASON FOR CHANGE i o A*J Aw 4 -
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Evaluation of Containment Spray Pump Net Positive Suction Head
(
Accounting for Sump Sub-Cooling l
Prepared for Omaha Public Power District, Fort Calhoun Station l
Calculation No. : O-MECH-CALC-021 Rev. 00 Safety Related : Yes .X. No ;
Total Pages : 21 Appendices : A6, B24, C53, D21 Microfiche : None j Prepared By: R. B. Harsell M Reviewed By: R. F. Pankkonen I
i VERIFICATION STATUS: COMPLETE n.swar a .am.4 me, man n m.4 m m m 6 m a e.6.
m.s nr .c nea, nahep wmjd lergus nes.
fl.Pa
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c li>I, u-Approved By: F. P. Ferraraccio, Su - w e<== @ -l MZ
Purpose:
To investigate available Net Positive Suction Head (NPSH) of Fort Calhoun Station Containment Spray Pumps acaunting for containment sump liquid.
I sub-cooling.
Method and Results of Review : Independent design review. 'Ihe results of the review were found to be acceptable and consistent with that i of the calculation.
ABB Combustion Engineering Nuclear Services
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l ABMOKUSTION ENGINEERING NUCLEAR SERVICES O-MECH-CALC-021 REV. 00 PAGE 2 cf 21 RECORD OF REVISION l
Revision Date Author Reviewer Approval Extent of Rev.
M 6/12/92 R. Harsell R. Paakkonen F. Ferraraccio Origbd hue r
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ABB-COMBUSTION ENGINEERING NUCLEAR SERVICES M 05977 O-MECH-CALC 421 REV. 00 PAGE 3 of 21 Table of Contents Section East
1.0 INTRODUCTION
4 2.0 SCOPE 4 3,0 REFERENCES 5 4.0 BASIC DATA AND ASSUMPTIONS 6 5.0 ME1110D OF ANALYSIS 7 6.0 RESULTS AND CONCLUSIONS 8 7.0 BODY OF THE CALCULA110N 8 List of Tables 1 Containment Spray System Main Model Runs 8 2 Pipeline Total K Factors 14 3 Headioss Equations for the Containment Spray Pumps 15 4 Available Net Positive Suction Head for the Containment Spray Pumps 16 5 Available Net Positive Suction Head for SI-3B and SI-3C Operating in Parallel 16 6 Composite Flow vs. Configuration 17 List of Figures 1 OPPD CSP NPSH - 2P2H Configuration 18 2 OPPD CSP NPSH - 3P2H Configuration 19 3 OPPD CSP NPSH - 2P1H Configuration 20 4 OPPD CSP NPSH - IP1H Contiguration 21 Appendices A Piping Diagram Al B PIPE-FLO Output B1
'C NET-FLO Output for CSS Main Model Runs C1 D Selected References D1
. 4
i ABB-COMEUSTION ENGINEERING NUCLEAR SERVICES FC O V. 00g9 7 7 O-MECH-CALC-021 PAGE 4 (f 21
1.0 INTRODUCTION
The purpose of this calculation is to document the evaluation of available NPSH (NPSH,) of Fort Calhoun Station's Containment Spray Pumps. His calculation documents the investigative effort to identify additional NPSH, using the model of Reference 3.2 and accounting for containment sump sub-cooling. He minimum sump sub-cooling available is given in Reference 3.14. His results in an additional, but conservative, amount of NPSH,.
2.0 SCDPE Dis calculation applies to the Omaha Public Power District's Fort Calhoun Station I Containment Spray System.
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ABB-COIEUSTION ENGINEERING NUCLEAR SERVICES O-MECH-CALC 421 REV. 00 PAGE 5 of 21
3.0 REFERENCES
fc4CT1~1 3.1 CE Calculation O-MPS-CALC-004 Rev. 01, "He Development of a Hydraulic Computer
.Model of the Containment Spray System at Fort Calhoun Station using the "As-Built" Piping Isometrics and "FLO-SERIES" Hydraulic Analysis Computer Code", dated 6/12/92.
fc4C9a, 3.2 CE Calculation O-MECH-CALC-019 Rev. 01, " Evaluation of Containment Spray Pump Net Positive Suction Head", dated 4/27/92.
3.3 CE Letter O-MPS-91-120, " Containment Spray System Open item Closure", dated 8/23/91.
3.4 CE Letter O-MPS-91-147, " Containment Spray System NPSH Investigation for DBD Open Item Number 42", dated 10/10/91.
3.5 FLO-SERIES Users Manual dated 1990.
3.6 Garay, Paul N., " Pump Application Desk Book", De Fairmont Press, Inc.,1990.
3.7 Safety Guide 1, " Net Positive Suction Head for Emergency Core Cooling and Containment Heat Removal System Pumps", dated 11/2n0.
3.8 MISC-MPS-CALC-015 Revision 0, Quality Assurance SoAware Verification and Validation Report, dated 7-12-91 for PIPE-FLO version 3.91a and NET-FLO version 3.92a.
3.9 . Crane Manual, Technical Paper No. 410, Twenty-Fourth printing,1988.
3.10 Ft. Calhoun Station Unit No.1, Surveillance Test ST-N2-1, " Containment Spray Nozzles",
performed May 1987 3.11 OPPD OSAR 85-33, " Electrical Equipment Qualification Environment Determination", dated ;
3/21/86. Copy attached to Reference 3.2.
3.12 Facsimile from P. Kasztejna (Ingersoll-Rand) to D. Blanchard (ABB) concerning Containment Spray Pumps, received 3/19/92. Copy attached in Appendix D.
3.13 CE Calculation O-MPS-CALC-011 Rev. 00, " Calculation of Spray Initiation Time", dated 10/24/91.
3.14 ABB Inter-Office Correspondence OPS-92-0653, " Evaluation of the Pressure Margin Present Between the Saturation Pressure of the Co=*=la==+ Sump Water and the Containment Pressure
- Post LOCA", dated 5/29/92. Copy attached in Appendix D.
3.15 ASME Steam Tables, dated 1979.
3.16 Ingersoll-Rand Company pump curves N-182A, N-171A, AND N-178A. Copy attached in Appendix D.
l ABB-COMBUSTION ENGINEERING NUCLEAR SERVICES FC 05977 O-MECH-CALC-021 REV. 00
! PAGE 6 cf 21 l
4.0 ' BASIC DATA AND ASSUMMIONS l
4.1 Assumptions 4.1 and 4.3 - 4.8 of Reference 3.1 apply. Dose assumptions are:
4.1.1 ne SIRWT water temperature is 90'F.
4.1.2 Pump elevation is 973.25 ft.
4.1.3 Spray headers "A" and "B" are at 1111.5 ft.
4.1.4 De same ring elevations are used.
4.1.5 ne following pump curve data from Reference 3.16 was used to model the pumps:
l hung Curve No.
SI-3A N-178 A SI-3B N-182 A SI-3C N-171 A 1
4.2 Reference 3.11 allows the use of'63 feet oflevel in the containmant sump for NPSH, determination. Its applicability whistablished in Reference 3.2.
4.3 De NPSH, curve in each of this calculation's Figures is based on Reference 3.12. This curve l is the most recent curve of NPSH, and was, therefore, used in this calculation. Its applicability ,!
- was established in Reference 3.2. !
4.4 Properties of sump liquid are approximated as water and, as such, the properties of Reference 3.15 apply to the sump liquid. 1 l
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AEB-COICUSTION ENGINEERING NUCLEAR SERVICES FC 05977 O-MECH-CALC-021 REV. 00 PAGE 7 cf 21 5.0 METHOD OF ANALYSIS nis calculation is an expansion of Reference 3.2. References 3.1,3.2,3.3, and 3.4 have noted a possible condition resulting in inadequate NPSH for the Containment Spray Pumps (CSP) during the recirculation phase of safety injection, nis calculation uses the n odel developed for Reference 3.2.
He objective of this calculation is to calculate the available NPSH and compare it against the required NPSH. To determine NPSR, various parameters were considered. He parameters of elevation difference, sump level, and CSP suction headloss were considered in Reference 3.2. His calculation, however, expands that calculation by accounting for sump sub-cooling.
He sump sub-cooling arises due to the pressure in containment being greater than the vapor pressure of the sump liquid. He total NPSR is plotted against NPSH, to determine the available NPSH margin.
His Section discusses the methodology in general terms, while Section 7 explains, in detail, the methods employed in this calculation.
5.1 MODEL DEVELOPMENT ne model used in this calculation was developed in Reference 3.2. His included using Reference 3.5. FLO-SERIES has been QA certified by Reference 3.8. He Code Certificates are included in Appendix D.
5.1.1 MODEL MODIFICATION The model of Reference 3.2 was modified to use the manufacturer's pump curve data. A set of runs was performed using the modified model. These runs included the ring data of Reference 3.10. He ring data input to FLO-SERIES was taken from Reference 3.1. He K factors for rings A-F and H-L were taken from Reference 3.1, Appendix G while the K factor for ring G was taken from Appendix T of Reference 3.1. Appendix T accounts for the missing nozzle annotated in Reference 3.10. ne. Piping Project Report showing the respective rings and K factors is located in Appendix B.
5.2 NPSR DETERMINATION l To determine the available NPSH, Equation 1 on page 200 of Reference 3.6 was used.
l NPSH,= , q t Z - Hg, (1) t.y where NPSR = available NPSH
, Pi = containment pressure l
P, = vapor pressure of the water at the pumping temperature; in this case, sump temperature 2.31 = conversion factor from psi to feet of head Z = elevation difference between sump bottom and centerline of pump H,, = suction headloss l l l l
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ABB-COM~USTION ENGINEERING NUCLEAR SERVICES FC 05977 O-MECH-CALC 421 REV. 00 PAGE 8 cf 21 5.3 TEST CASE CONDITIONS ,
Runs were based on allowable CSP /CS header configurations that were developed in Reference 3.13. He configuration runs are listed in Table 1.
TABLE 1 CONTAINMENT SPRAY SYSTEM MAIN MODEL RUNS RUN CONFIGURATION CSS PUMP DISCHARGE l HEADER 1 3P2H SI-3A HDR A SI-3B HDR B SI-3C 2 2P2H SI-3B HDR A '
SI-3C HDR B 3 3P1H SI-3A HDR B SI-3B SI-3C 4 2P1H SI-3A HDR B SI-3B 5 2P1H SI-3A HDR B SI-3C 6 IP1H SI-3A HDR B NOTE: He designation xPyH determines the number of pumps (P) and headers (H).
Results of these runs are found in Appendix C.
6.0 RESULTS Dis calculation shows that crediting only 25% of the available sump liquid sub-cooling NPSH .
and accounting for a 6 foot level in the sump yields positive NPSH margins. Tables 4 and 5 and the Figures show the NPSH, versus NPSH, for various pump flow data points. Table 6 and the Figures show the NPSH, values for the flows determined by FLO-SERIES. De 3P1H configuration is not graphed.
Based on Table 6 and the Figures, OPPD CSPs have sufficient NPSH, providing credit is taken for sump liquid sub-cooling.
7.0 BODY OF THE CALCULATION 7.1 MODEL DEVELOPMENT AND VERIFICATION He explanation of model development is included in Reference 3.1. He base model for this calculation comes from Reference 3.2. He base model, OPPDCS, was copied onto a working l disk as OPPDCSI and run using one set of conditions established in Reference 3.2. The verification run was documented in accordance with FLO-SERIES control procedures; the verification sheet is included in Appendix D. Once the working model was verified, it was modified as described in Section 7.1.1.
ACB-COMEUSTION ENGINEERING NUCLEAR SERVICES O MECH-CALC-021 V. 00 i PAGE 9 cf 21 l l
1 7.1.1 MODEL MODIFICATION He working model was modified in accordance with Reference 3.4 by replacing the test pump data with the manufacturer's pump data. He pump replacement was accomplished by setting up new networks in NET-FLO Network Design & ConFguration. The respective nodes were called up and the proper pump " installed" into the corresponding pipe. He Component Table i Report of Appendit B includes the three pumps used. Components C, D, and E were placed into pipelines 74,75, and 76, respectively. Additionally, for the runs involving only one header, Header A was blocked by the use of " phantom" check valves and 5000 psi for the fixed grade pressure. %1s check valve /high pressure combination resulted in zero flow through Header A. In this way, the system was modified and run in the configurations according to Table 1.
7.2 AVAILABLE NPSH DETERMINATION I As discussed in Section 5.2, NPSH, was determined using Equation 1. In order to calculate NPSH, the terms P , P,, specific gravity, Z, and H are m=7. Reference 3.14 transmitted i
the data pertaining to the conditions in containment that would yield the least, i.e. most conservative, amount of sub-cooling available.
7.2.1 CONTAINMENT PRESSURE (P ) i The values for containment pressure are located in various containment analysis calculations.
He specific containment pressure relevant tr his calculation is given in Reference 3.14 as 16.43 psia.
7.2.2 VAPOR PRESSURE AT SUMP TEMPERATURE (P,)
He vapor pressure is the saturation pressure corresponding to the sump temperature. He sump temperature relevant to this calculation is given in Reference 3.14 as 100.3*F.
7.2.3 P - P, i
Reference 3.14 transmitted the minimum delta P available. His delta P results due to sump sub-cooling and results in additional NPSH,. This differential pressure is stated in Reference 3.14 as 15.47 psi.
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ABM'OMBUS'I10N ENGINEERING NUCLEAR SERVICES O-MECH-CAI4 421 REV. 00 l PAGE 10 of 21 j 1 i 7.2.4 SPECIFIC GRAVITY De specific gravity, as applicable to this case, is defined as SG = ""*'**""'**'"'**"'*
l (2)
P acez acso=r j where p (density at sump temperature of 100.3*F per Reference 3.14) is 61.996 lbm/ft8 from Reference 3.15
. p (density at 60'F) is 62.371 lbm/ft* from Reference 3.15 therefore, .
d.
9 SG =
g = 0.994 (3) 7.2.5 NPSHsuecoouseo Sections 7.2.2 through 7.2.4 are used to calculate the additional NPSH available due to sumo sub-cooling.' He additional NPSH available is NPSHm .wrm = 7 *2.31 = 35.95 feet (4) q i
To maintain conservatism, only 25% , or 8.99 feet, of the NPSHeuscoouseo .will be accounted for in !
this calculation.
- 7.2.6 ELEVATION DIFFERENCE (Z)
The centerline of the CSPs are at 973.25 ft (Assumption 4.1.2) and the bottom of the containment sump is at 994 ft per Reference 3.1. His Z equals 20.75 ft but does not account for any level in the containment sump. Here will, however, be water in the sump which will result in additional level. Reference 3.11 revealed that the height of water in the sump would be approximataly 6.0 ft. His does not account for RCS volume but does' account for SIT
. volume. De resultant Z is 26.75 ft. His calculation shows NPSH, values for both Z =
20.75 feet and Z = 26.75 feet. ~
)( q /3.3 5 ' 2 6 ,TS V I oso $t en x= 4%
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ABB-COMBUS'ITON ENGINEERING NUCLEAR SERVICES FC 05977 O-MECH-CALC-021 REV. 00
' l PAGE 11 of 21 7.2.7 SUCTION HEADLOSS (H,,)
To determine the suction headloss equations for each pump, data for the respective piping ;
2 sections of Reference 3.1 was used to calculate a Total K factor. FLO-SERIES computes two K factors, K, and Kw PIPE-FLO calculates K , based on the valves and fittings " installed" into each pipe section. His K, , is shown on the individual Pipeline Reports which are located in Appendix B. NET-FLO then computes K.,,, using fL/D. De values for f, L (in feet), and !
D (in inches) are also shown on the Pipeline Reports in Appendix B. Equation 5 was used to i calculate Kw. Table 2 compiles the data from the Pipeline Reports and computes a Total K for each pipe section. Equation 6, taken from Reference 3.9, calculates K in terms of different l
size pipes. Using Equation 6, an effective K for the suction side of the respective pump is l
calculated and is shown in Table 3. '
Keoul = K,,g + Kg y , (5)
K,,,33,, ,3,, = Kym, ,jp, ( ')* (6)
Once an effective K factor was determined, Equation 7, taken from page 3-4 of Reference 3.9, was used to calculate the headioss at different flows.
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- f, = O.00259KeoujO (7) d,',,23 7.2.8 SUCTION HEADLOSS (H,,) FOR PUMPS SI-3B and SI-3C OPERATING IN PARALLEL Runs 1-3 result in pumps SI-3B and SI-3C operating in parallel. Derefore, the flow in the common pipelines (108,110, and 112) is essentially doubled. To account for this additional headloss, the resistance for those pipelines has been quadrupled when the CS system is operating in one of the applicable configurations. Equations 10 and 12 represent the headloss equations and Table 3 displays the results in spreadsheet format.
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ABB-COMBUSTION ENGINEERING NUCLEAR SERVICES FC 05977 O-MECH-CALC-021 RET. 00 i
PAGE 12 of 21 7.2.9 AVAILABLE NPSH EQUATION Using Sections 7.2.1 through 7.2.8, the resultant NPSH, equations for each CSP are: ,
l SI-3A NPSH, = 8 . 9 9 + 2 - 2 . 0 8 4
- 10-7 02 (g)
SI-3 B NPSH, = 8 . 9 9 + Z - 2 . 6 57 *10-7 02 (,)
SI-3B (w/SI-3C) NPSH, = 8. 9 9 + Z - 3. 89 9 *10-7 02 (10) i i
SI-3 C NPSH, = 8. 9 9 + Z - 2.7 5 0 *10-7 0 2 (11)
(12)
SI-3C (w/SI-3B)- NPSH, = 8 . 9 9 + Z - 3 . 9 91 *10-7 O 2 4 1
)
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'Ihe effective K factors and headioss equations are included in Table 3. NPSH, calculations for Equations 8 through 12 are in spreadsheet form in Tables 4 and 5. ,
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ABB-COlEUSTION ENGINEERING NUCLEAR SERVICES O-MECH-CALC-021 REV. 00 PAGE 13 ef 21 7.3 FLO-SERIRt INPUT AND OUTPUT 7.3.1 FLO-SERIES INPUT The main CS System network was formed in References 3.1 and 3.2. He network was modified per Section 7.1 of this calculation. He input data consisted of containment sump pressure and prassure at the discharge of the containmaat spray nozzles. Since the nozzles are also in con *=i->=* the pressures are similar. He difference arises due to the 6 foot level in the sump, in accordance with Assumption 4.2. His results in an additional 2.6 psi of pressure at Nodes H69 and H70 using Equation 13.
6 ft*62.12 ft' Paddiefone "
144 inch 2 ft' where 62.12 lbm/ft8 is the density at 90*F (Reference 3.15) 144 inch 2/ft2 converts ft* to inch' He initial pressure input is not important in this application; the only rigid requirement is that the difference between sump and containment spray nozzle pressure be 2.6 psi to account for sump water level.
7.3.2 FLO-SERIES OUTPUT He FLO-SERIES output is contained in Appendix C. He RUN 1 output contains a complete NET-FLO report. His includes a Network Summary Report, a Configured Complete Junction Node Report, and a Complete Pipeline Report. Dese allow the reviewer to verify the node connections and ensure the proper pump was used. For other runs, only the Network Summary Report and Complete Pipeline Report are submitted.
Table 6 list the flows computed by FLO-SERIES and the NPSH, for each run in a composite format.
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FC 0$V77 i ABB-COM~USTION ENGINEERING NUCLEAR SERVICES O-MECH-CALC-021 REV. 00 I PAGE 14 0f 21 Table 2 PIPELINE TOTAL K FACTORS l Total K's for CSP suction pipes. Data is taken from '
Pipeline Reports in Appendix B.
, PIPE # K v&f f L(ft) - D (in) Total K 2 0.236 0.012 7.25 19.25 0.290 l 5 0.618 0.013 18.65 12.39 0.853 '
6 1.662 0.013 26.39 12.39 1.994 7 1.405 0.013 14.85 12.39 1.592 67 0.448 0.013 9.50 12.00 0.572 68 0.000 0.013 5.50 12.00 0.072 69 0.259 0.013 10.43 12.00 0.395 !
107 0.228 0.011 7.20 23.25 0.269 108 0.368 0.012 5.42 23.25 0.402 109 3.022 0.011 140.40 23.25- 3.819 110 3.100 0.011 89.72 23.25 3.609~
111 0.475 0.011 55.86 23.25 0.792 112 0.388 0.011 47.56 23.25 0.658 i
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FC 05977 ABB-COM USTION ENGINEERING NUCLEAR SEP. VICES O-MECH-Calf-021 REY. 00 Tabla 3 PAGE 15 cf 21 HEADLOSS EQUATIONS FOR THE CONTAINMENT SPRAY PUMP Headioss Equations..for CSP SI-3A during Recirculation 1?
Total Kisctors are from Table 24 -
Pipe Diameter Total K in terms of New K 5 12.39 0.853 12.00 0.750 67 12.00 0.572 12.00 0.572 107 23.25 0.269 12.00 0.019 109 23.25 3.819 12.00 0.271 111 23.25 0.792 12.00 0.056 Effective K = 1.668 Suction Head Losses for CSP SI-3A HL = 0.00259 K Q'2/d'4 I HL= 2.084E-07 Q^2 Headiosa Equations ToiaiK fasioisiitrisfotCSESMS.B during Recirculation
! ' MI* - 3 9t#M
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bdiTEbid~2f- ,
l 7 12.39 1.592 12.00 1.401 69 12.00 0.395 12.00 0.395
- 108 23.25 0.402 12.00 0.029
- 110 23.25 3.609 12.00 0.256
- 112 23.25 0.658 12.00 0.047 Effective K = 2.127 K' = 3.121 Suction Head Losses for CSP SI-3B HL = 0.00259 K Q^2/d*4 Single Pump Two Pump HL= 2.657E-07 O*2 3.899E-07 Q^2 Headioss Equations.for CSP Sl?SC during-. Recirculation 4 s s- <
.y g. .;-~,
2 19.25 0.290 12.00 0.044 6 12.39 1.994 12.00 ,
1.755 68 12.00 0.072 12.00 0.072
- 108 23.25 0.402 12.00 0.029
- 110 23.25 3.609 12.00 0.256
- 112 23.25 0.658 12.00 0.047 Effective K = 2.201 K' = 3.196 l Suction Head Losses for CSP SI-3C HL = 0.00259 K Q'2/d*4 Single Pump Two Pump HL= 2.750E-07 Q^2 3.991E-07 Q^2
- refers to those sections of suction pipe which are l shared by pumps 3B and 30. These values for "New K" are quadrupled to determine K' for input to the "H" equation for when CSPs 3B and 30 are operating.
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ABB-COM;USmlON ENGINEERDiG NUCLEAR SERVICES O-MECH-CJ-0Q1 rep. 00O 977 PAGE 16 cf 21 Table 4 AVAILABLE NET POSITIVE SUCTION HEAD FOR THE CONTAINMENT SPRAY PUMPS Based on NPSHac= 8.99 ft Z = 20.75 ft (no level in the sump)
HL = headloss based on appropriate equation from Table 3 NPSHa=NPSHsc + Z - HL = 8.99 + 20.75 - HL ej Flow 2000 2200 2400 2600 2800 3000 3200 NPSHa SI-3A 28.906 28.731 28.539 28.331 28.106 27.864 27.606 NPSHa SI-38 28.677 28.454 28.209 27.943 27.656 27.348 27.019 NPSHa SI-3C 28.640 28.409 28.156 27.881 27.584 27.265 26.924
. , , , , , <f , , gg , ,,, , ~
.s se NPSHr l 14.8 l 16.5 l 18.3 l 20.2 l 22.5 l 24.5 l 27.0 Based on NPSHsc= 8.99 ft Z = 26.75 ft (6 foot level in the sump per Reference 3.11)
HL = headioss based on appropriate equation from Table 3 NPSHa=NPSHsc + Z - HL = 8.99 + 26.75 - HL 2 nl Flow 2000 2200 2400 2600 2800 3000 3200 NPSHa SI-3A 34.906 34.731 34.539 34.331 34.106 33.864 33.606 NPSHa SI-3B 34.677 34.454 34.209 33.943 33.656 33.348 33.019 NPSHa SI-3C 34.640 34.409 34.156 33.881 33.584 33.265 32.924
. , , c ,
up w o m!!gy gg e "s >
~w NPSHr l 14.8 l 16.5 l 12.5 l 20.2 l 22.5 l 24.5 l 27.0 NPSHr is taken from Reference 3.12 _
Table 5 AVAILABLE NET POSITIVE SUCTION HEAD FOR SI-3B AND SI-3C OPERATING IN PARALLEL Available Net Positive Suction Head for CSPs SI-38 & SI-3C Based on NPSHsc= 8.99 ft Z = 20.75 ft and Headioss based on appropriate equation from Table 3 NPSHa=NPSHsc + Z - HL = 8.99 + 20.75 - HL
?l Flow 2000 2200 2400 2600 2800 3000 3200 NPSHa SI-3B 28.18 27.85 27.49 27.10 26.68 26.23 25.75 NPSHa SI-3C 28.14 27.81 27.d4 27.04 26.61 26.15 25.65 geiqq + >< >
, g!( w at ,g gg > syg ,
NPSHr l 14.8 l 16.5 l 18.3 l 20.2 l 22.5 l 24.5 l 27.0 Based on NPSHsc= 8.99 ft Z = 26.75 ft and Headioss based on appropriate equation from Table 3 NPSHa=NPSHsc + Z - HL = 8.99 + 26.75 - HL 2l Flow 2000 2200 2400 2600 2800 3000 3200 NPSHa SI-3B 34.18 33.85 33.49 33.10 32.68 32.23 31.75 NPSHa SI-3C 34.14 33.81 33.44 33.04 32.61 32.15 31.65 m~
NPSHr l 14.8 l 16.5 l 18.3 l 20.2 l 22.5 l 24.5 l 27.0 NPSHr is taken from Reference 3.12
PU 05977 i A"B-COhCUSTION ENGINEERING NUCLEAR SERVICES O-MECH-CALC-021 REV. 00 l PAGE 17 cf 21 1 Table 6 COMPOSITE FLOW vs. CONFIGURATION l NPSHa for CSP flows as computed by FLO-SERIES Using manufacturer's pump curve data of Reference 3.16 NPSHsc = 8.99 ft Pump Configuration Flow NPSHa (ft) NPSHa (ft) Suction (gpm) (Z=0 ft) (Z=6.0 ft) Headioss (ft) 3P2H 2489 28.449 34.449 1.291 4 SI-3A 3P1H 1535 29.249 35.249 0.491 2P1H 2 21 28.803 34.803 0.937 1P1H SUJ3 27.695 33.695 2.045 3P2H I 2566 27.173 33.173 2.567 SI-38 2P2H 3132 25.916 31.916 3.824 3P1H 1563 28.788 34.788 0.952 2P1H 2192 28.463 34.463 1.277 m .
3P2H 2549 27.147 33.147 2.593 SI-3C 2P2H 3115 25.867 31.867 3.873 3P1H 1530 28.806 34.806 0.934 2P1H 2180 28.433 34.433 1.307 Note: Flows listed are the highest flows for the specific pump in the specific configuration.
The FLO-SERIES flow outputs are found in Appendix C.
l 1
)
Figuro 1 OPPD CSP NPSH w/ SUMP.SUB-COOLING ,
m ;
2P2H Configuration g O
5 !
C 34 -------a =------c----- ,- - - - - - - - - - - - - : - - ^ - : - - - - - - - B
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-...............*........t...
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3 z
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24 ...... . . . . . . . . . . .
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s o
10 i
E 1800 2000 2200 2400 2600 2800 3000 3200 3400 .
I FLOW [gpm) $l M :
-6
- - NPSHa @ 6.0 ft
--- N PS H r I NPSHa @ 0 ft o A d j$g!
Pump SI-3B i Pump SI-3C
- g c:
NPSHa taken from SI-3C of Table 5 .
7 < ui Vertical lines represent pump flows y'g 4:
N!
in 2P2H configuration. N:
Figure 2 OPPD CSP NPSH w/ SUMP SUB-COOLING ,
w 3P2H . Configuration g o '
E m
C 34 - - - - - - '. - - - -----
a c---
- - - - .' - g* 5 - - - - - .;- - - - - - :
8 32 - -- '
9.------- ". ----- -=. m ----- -- g
-: - - - - - - + - - - - - - :- - - - - - - ; - - - - - - - g 30 - - - - - -
- - - - - - - - + - - - - - - - :- - - --
-N 28 - - - - - - - i.
yy -...... .....................
h---
I i---- --:-- -- --;--- /
- .i . . . . . . . .It........t 7
. t. . . . . . . . -
24 . .
I - - - - - - -: - - - - - - - - :- - - - - - - :- - - - -
. - - - - - :. - - - - - - - i - - - - - - -
o c/) 22 ~----- '. . .
E
- n. 20 -........' ......'.'....'
7.'-- . . . . . . . . . . ' . . . . . . . . . . . . . . . . . . .n . .
Z 18 .
.........s...
16 .. .. ..
g jg, _...............:........:....
.. z . . . . . . . . :. . . . . . . . . . . . . . . . ; . . . . . . . .. g 12 - - - - - - '. - - - - -:--- - - - - ;. - - - .
S M<
10 3
1800 2000 2200 2400 2600 2800 3000 3200 3400 FLOW (gpm)
{
m
--- N PS H r l NPSHa @ 0 ft + NPSHa @ 6.0 ft g A E9 X
Pump SI-3A '
o Pump SI-3B Pump SI-3C jm$ C C
s .
NPSHa taken from SI-3C of Table 5 e U Vertical lines represent pump flows 3-8< %
in 3P2H configuration. N
Figure 3 OPPD. CSP NPSH w/ SUMP SUB-COOLING c!
g:
2P1H Configuration o
5 C
34 - - - - - - Y - - < ; -ti? - - - - -=-
=^---------6-----b------- g!
- - - - - - - . ' - - - -^ - - q -.*---- - o 32
- 2
} _........... .. .
o
- 28 - - - - -
+.------0 --------i------- ,
+ ---
+ 26 3
{
24 _.......*.....
........t......
2........'.....
2.....
L Z 22 -- - - - - - : - - - - -
o !
CQ -......s....
1 . . . . . . . ;
lo . . . . . . . F [
- ........... .s. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . '
l V ..
. m
.........,.......,.................,.......,........ y -...... ..... 10 n . 5 1800 2000 2200 2400 2600 2800 3000 3200 3400 FLOW (gpm) @ E
--- N PS H r l NPSHa @ 0 ft + NPSHa @ 6.0 ft 6 i X o A mk Pump SI-3A - Pump SI-3B Pump SI-3C s&d m-NPSHa taken from SI-3C of Table 4 g@
e< MO Vertical lines represent pump flows ~gl In 2P1H configuration. N N-i
1 Figure 4 OPPD CSP NPSH w/ SUMP SUB-COOLING t 1P1H Configuration g o I a e 34 ------Y----=-----* =. - -- -~m --- -------- s,-- ------ - 5' o
- a. s _g 32
!E 30 _...... .........................,................. .....
. . . . . . O t I . . . M
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g -.......g........p..... . . , . . . . . . . . . M
,==== 2 8 . . . I 1 i
-...............,...................................... d .f . . . . . . . ..
. . . . . . y
_...... ........................................ ....... . . . . . . . . . . . . g I - - - - - - -: - - - - - - :- - - - - - :- - - - - - - : - - - - - . - - - - - - - - :- --i--------
- E o
Q) 22 . .
. . . . . . . . . . . . r-O,. . . . . . . .
Z 18 - - - - - - ;. - - - - - - - ;- - - - - - M 16
. . . . . . pg j
} . . . . . . . O E
- - - - - - : - - - - - - - - :- - - - - - --i--------
12 -- - - - - - -' '. - - - - - -' - :. - - - - '- - - :- - - -' - - 4 10 1800 2000 2200 2400 2600 2800 3000 3200 3400 FLOW (gpm) % X *
--- N PS H r l NPSHa @ 0 ft + NPSHa @ 6.0 ft Pump SI-3A j@ 3 u
NPSHa taken from SI-3C of Table 4
~
O
*,.-W Vertical h.nes represent pump flow wg of SI-3A. y N
FC 05977 O-MECH-CALC-02I Rev. 00 Page A \ APPENDIX A , PIPING DIAGRAM , 1 A2 Piping Diagram i l l l
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FC 05977 O-MECH-CALC-021 Rev. 00 P:gi B g APPENDIX B PIPE-FLO OUTPUT B2 OPPDCS Piping Project Report B11 Component Table Report B12 Pump Suction Pipeline Reports e t 4
- I
tu uby / t' O-MECH 4ALC-021 Rev. 00 P;gs B 1 ABB Cerburtien Enginscring CLIENT : Omaha Public Power District PIPING PROJECT REPORT JUNE 8, 1992 R. Harsell PROJECT : OPPDCS PIPES : 123 UPDATED: JUNE 8, 1992 OPPD CONTAINMENT SPRAY SYSTEM CSP NPSH EVALUATION W/ SUMP SUBC00 LING 0-MECH-CA14-021 DESIGN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft./sec PRESSURE MIN: 0.00 MAX: 5000.00 PSI IDENTIFIER HATERIAL LENGTH FLUID NAME DESIGN TOTAL SIZE / SCH (ft) TEMP FIDW-RATE K (gal / min) 1 SIRWT EXIT STEEL 74.45 WATER 2.593 20 in/SCH 20 90 deg-F 2 SIRWT HEADER STEEL 7.25 WATER 0.236 20 in/SCH 20 90 deg-F l 3 SIRWT EXIT STEEL 35.75 UATER 1.884 20 in/SCH 20 90 deg-F 4 SIRWT HEADER STEEL 4 WATER 12.521 24 in/SCH 20 90 deg-F ) 5 SI-3A SUCTION SSTEEL 18.65 WATER 0.618 12 in/SCH 10S 90 deg-F 1 6 SI-3C SUCTION SSTEEL 26.39 WATER 1.662 ! 12 in/SCH 105 90 deg-F l 7 SI-3B SUCTION SSTEEL 14.85 WATER 1.405 12 in/SCH 10S 90 deg-F 8 SI-3A DISCHARGE SSTEEL 100.60 WATER 4.062 8 in/SCH 40S 90 deg-F 9 SI-3B DISCHARGE SSTEEL 20.20 WATER 2.937 8 in/SCH 40S 90 deg-F 10 SI-3C DISCHARGE SSTEEL 22.56 WATER 3.218 8 in/SCH 40S 90 deg-F 11 DSCHRG HDR SSTEEL 2.11 WATER 0.259 12 in/SCH 40S 90 deg-F 12 DSCHRC HDR SSTEEL 0.66 WATER 0.580 12 in/SCH 40S 90 deg-F PIPE-FIA by Engineered Software page 1
FC 0597/ O-MECHCALC-021 Rev. 00 Page B3 ABB Combustion Enginscring CLIENT : Omaha Public Power District PIPING PROJECT REPORT JUNE 8, 1992 R. Harsell PROJECT : OPPDCS PIPES : 123 UPDATED: JUNE 8, 1992 IDENTIFIER HATERIAL LENGTH ' FLUID NAME DESIGN TOTAL SIZE / SCH (ft) TEMP FIDW-RATE K (gal / min) 13 DSCHRG HDR SSTEEL 173.70 WATER 1.863 12 in/SCH 40S 90 deg-F 14 A HX INLET SSTEEL 23.16 WATER 2.399 12 in/SCH 40S 90 deg-F 15 B HX INLET SSTEEL 32.16 WATER 4.766 12 in/SCH 40S 90 dog-F 16 A HX OUTLET SSTEEL 15.44 WATER 0.981 12 in/SCH 40S 90 deg-F 17 B HX OUTLET SSTEEL 14.19 WATER 0.792 12 in/SCH 40S 90 deg-F 18 HX CROSS CONECT SSTEEL 12.63 WATER 1.500 12 in/SCH 40S 90 deg-F 19 HX CROSS CONECT SSTEEL 12.27 WATER 1.500 12 in/SCH 40S 90 deg-F 20 SDC DISCHARGE SSTEEL 1 WATER 0.259 12 in/SCH 40S 90 deg-F 21 A HEADER SSTEEL 62.21 UATER 2.435 12 in/SCH 40S 90 deg-F 22 B HEADER SSTEEL 66.47 WATER 2.621 12 in/SCH 40S 90 dog-F 23 A HEADER SSTEEL 3.94 WATER 1.430 8 in/SCH 40S 90 deg-F 24 B HEADER SSTEEL 3.94 WATER 1.627 8 in/SCH 40S 90 deg-F 25 A HEADER SSTEEL 48.53 WATER 1.345 12 in/SCH 40S 90 deg-F 26 A HEADER SSTEEL 52.95 WATER 2.251 12 in/SCH 10S 90 deg-F PIPE-FLO by Engineered Software page 2
O-MECH-CALC 021 Kev. P:geBq ABB Combustion Engineering CLIENT : Omaha Public Power Dist.? f et ' PIPING ' PROJ ECT REPORT TUNE 8, 1992 R. !=rsell PROJECT : OPPDCS-
. PIPES : 123 UPDATED: JUNE 3, 1992 IDENTIFIER MATERIAL LENGTH FLUID NAME DESIGN TOTAL SIZE / SCH .(ft) TEHP FIDW-RATE K (gal / min) 27 A HEADER SSTEEL 2.33 WATER 0.514 12 in/SCH 10S 90 deg-F 28 A HEADER SSTEEL 47.35 WATER 1.295 8 in/SCH 10s 90 deg-F 29 A HEADER- SSTEEL. 52.33 WATER 1.578 l 8 in/SCH 10s 90 dog-F 30 A HEADER' SSTEEL 6.20 WATER 0.257 12 in/SCH 10S 90 deg-F 31 A HEADER SSTEEL 2.05 WATER 0.257 12 in/SCH 10S 90 des-F 32 A HEADER SSTEEL 1 WATER 0.257 12 in/SCH 10S 90 deg-F )
33 PIPE-33 SSTEEL 2.05 WATER 12 in/SCH 10S 90 de5-F 34 A HEADER SSTEEL 4.11 WATER 0.257 12 in/SCH 10S 90 dag-F 35 A HEADER SSTEEL 4.11 WATER 0.257 12 in/SCH 10S 90 deg-F , 36 A HEADER SSTEEL .4.11 WATER 0.257 12 in/SCH 10S 90 deg-F 37 B HEADER SSTEEL 53.38 WATER 2.287 12 in/SCH 10S 90 des-F 38 B HEADER SSTEEL 1 . WATER 0.257 12 in/SCH 10S 90 deg-F 39 B HEADER SSTEEL 55.32 WATER 1.559 8 in/SCH 10S 90 deg-F 40 B HEADER' SSTEEL 51.50 WATER 2.088 8 in/SCH 10S 90 deg-F PIPE-FID by Engineered Software page 3
O-MECil-CALC-021 77 Re PapB$ ABB Combustion Engineering CLIENT : Omaha Public Power District PIPING PROJECT REPORT JUNE 8, 1992 R. Harsell PROJECT : OPPDCS PIPES : 123 UPDATED: JUNE 8, 1992 IDENTIFIER HATERIAL LENGTH FLUID NAME DESIGN TOTAL SIZE / SCH (ft) TEMP FIDV-RATE K (gal / min) 41 B HEADER SSTEEL 4.12 WATER 12 in/SCH 10S 90 deg-F 42 B HEADER SSTEEL 1 WATER 0.257 i 12 in/SCH 10s 90 deg-F 43 B HEADER SSTEEL 0.66 WATER 2.913 1 12 in/SCH 10S 90 deg-F l l 44 B HEADER SSTEEL 3.75 WATER l 12 in/SCH 10S 90 deg-F 45 B HEADER SSTEEL 4.11 WATER 0.257
- 12. in/SCH 10S 90 deg-F 46 B HEADER SSTEEL 4.11 WATER 0.257 12 in/SCH 10S 90 deg-F 47 B HEADER SSTEEL 4.11 WATER 0.237 12 in/SCH 10S 90 deg-F 48 B HEADER SSTEEL 4.11 WATER 0.257 12 in/SCH 10S 90 deg-F 49 RING A SSTEEL 9.18 WATER 1.273 8 in/SCH 10S 90 deg-F 50 RING B SSTEEL 17.55 WATER 1,250 8 in/SCH 10S 90 deg-F 51 RING C SSTEEL 25.48 WATER 1.261 6 in/SCH 10S 90 deg-F 52 RING D SSTEEL 33.24 WATER 1.272 6 in/SCH 10S 90 deg-F 53 RING E SSTEEL 36.63 WATER 1.052 4 in/SCH 10S 90 deg-F 54 RING E2 SSTEEL 0.33 WATER 0.322 4 in/SCH 10S 90 deg-F PIPE-FID by Engineered Software page 4
FCp1qev.00977 O-MECH 4ALC PageB(
'ABB Corbustien Enginasring i
CLIENT : Omaha Public Power District I PIPING PROJECT REPORT JUNE 8, 1992 R. Harsell PROJECT : OPPDCS PIPES : 123 UPDATED: JUNE 8, 1992 IDENTIFIER MATERIAL LENGTH FLUID NAME DESIGN TOTAL SIZE / SCH (ft) TEMP FLOW-RATE K l (gal / min) -55 RING E3 SSTEEL 11.50 WATER 0.338 3 in/SCH 10S 90 des-F 1 56 RING F SSTEEL 5.35 WATER 1.593 4 in/SCH 10S 90 des-F 57 RING G SSTEEL 4.98 WATER 1.267 8 in/SCH 10S 90 des-F 58 RING H SSTEEL 13.45 WATER 1.046 8 in/SCH 10s 90 deg-F 59 RING I SSTEEL 21.56 WATER 1.258 6 in/SCH 10S 90 deg-F 60 RING J SSTEEL 29.45 WATER 1.269-6 in/SCH 10S 90 deg-F , 61 RING K SSTEEL 32.80 WATER 1.050 4-in/SCH 10S- 90 deg-F 62 RING K2 SSTEEL 0.33 WATER 0.322 4 in/SCH 10S 90 deg-F 63 RING K3 SSTEEL 12 WATER 0.335 3 in/SCH 10S 90 deg-F 64 RING L SSTEEL 5.39 WATER 1.587 ) 4 in/SCH 10S 90 de5-F i 65 SPRAY HDR A SSTEEL 0.33 WATER 2.913 12 in/SCH 10S 90 deg-F j l 66 SPRAY HDR A SSTEEL 0.33 WATER 2.913 1 12 in/SCH 10s 90 deg-F 67 SI-3A SUCTION SSTEEL 9.50 WATER 0.448 12 in/SCH 40S 90 deg-F 68 SUCTION SI-3C SSTEEL 5.50 WATER 12 in/SCH 40S 90 deg-F 1 PIPE-FLO by Engineered Software page 5 w -, .
O-MECH {ALC-021 Rrv. 00 Paga B ] ABB Combustion Engineering CLIENT : Omaha Public Power District PIPING PROJECT REPORT JUNE 8, 1992 R. Harsell PROJECT : OPPDCS PIPES : 123 UPDATED: JUNE 8, 1992 IDENTIFIER MATERIAL LENGTH FLUID NAME DESIGN TOTAL SIZE / SCH (ft) TEMP FLOW-RATE K (gal / min) 69 SUCTION SI-3B SSTEEL 10.43 WATER 0.259 12 in/SCH 40S 90 deg-F 70 DISCHARGE HDR SSTEEL 0.66 WATER 0.580 l 12 in/SCH 40S 90 deg-F 1 71 DISCHARGE HDR SSTEEL 0.66 WATER 0.580 l 12 in/SCH 40S 90 deg-F l l 72 DISCHARGE HDR SSTEEL 0.66 WATER 0.580 l 12 in/SCH 40S 90 deg-F l 73 HEADER B SSTEEL 39.52 WATER 0.518 12 in/SCH 40S 90 dog-F 74 PUMP SI-3A SSTEEL 1 UATER 0.333 6 in/SCH 10S 90 deg-F 75 PUMP SI-3B SSTEEL 1 WATER 0.333 l 6 in/SCH 10S 90 deg-F 76 PUMP SI-3C SSTEEL 1 WATER 0.371 6 in/SCH 10S 90 deg-F 77 HX-A SSTEEL 1 WATER 12 in/SCH LOS 90 deg-F 78 HX-B SSTEEL 1 WATER 12 in/SCH 40S 90 deg-F 79 RING A SSTEEL 1 WATER 65.909 6 in/SCH 10S 90 deg-F 80 RING B SSTEEL 1 WATER 99.196 6 in/SCH 10S 90 deg-F 81 RING C SSTEEL 1 WATER 150.980 6 in/SCH 10S 90 deg-F 82 RING D SSTEEL 1 UATER 284.020 6 in/SCH 10S 90 deg-F PIPE-FID by Engineered Software page 6
~~
FC 0
' O-MECH-CALC 41 Rev PcgeB$
ABB Cerbuntien Engin2sring I CLIENT : Omaha Public Power District - 1 PIPING PROJECT REPORT JUNE 8, 1992 R. Harsell PROJECT : OPPDCS PIPES : 123 UPDATED: JUNE 8, 1992 IDENTIFIER HATERIAL LENGTH FLUID NAME DESIGN TOTAL SIZE / SCH (ft) TEMP FIDW-RATE K (gal / min) 83 RING E SSTEEL 1 WATER 463.420
.3 in/SCH 10S 90 de5-F 84 RING F SSTEEL 1 WATER 138.920 4 in/SCH 10s 90 dog-F 85 RING G SSTEEL 1 WATER 58.820 6 in/SCH 10s 90 des-F 86 RING H SSTEEL 1 WATER 107.060 6 in/SCH 10S 90 deg-F 87 RING I SSTEEL 1 WATER 174.330
- 6 in/SCH 10S 90 deg-F 88 RING J SSTEEL . 1 WATER 300.980 4
6 in/SCH 10S 90 dog-F 89 RING K SSTEEL 1 WATER 116.210 3 in/SCH 10S 90 deg-F l J 90 RING L SSTEEL 1 WATER 128.500 l 4 in/SCH 10s 90 deg-F 91 SIRWT STEEL 0.25 WATER 0.500 l 20 in/SCH 20 90 deg-F I 92 SIRWT STEEL 0.25 WATER 0.500 20 in/SCH 20 90 deg-F 93 PIPE-93 SSTEEL 9,000- WATER 4 5400000 1 .5 in/,SCH 80S 90 deg-F i 94 CS RECIRC SSTEEL 23.54 WATER 91.894 2 in/SCH 40S 90 deg-F , 95 CS RECIRC SSTEEL 18 WATER 89.961 2 in/SCH 40S 90 deg-F
- 96 CS RECIRC SSTEEL 8.46 WATER 89.021 !
2 in/SCH 40s 90 deg-F ! PIPE-FI/) by Engineered Software page 7 i 1 l' ' .
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O-MECH 4ALC41 Rev. 00 Pass B g i ABB Conbustion Enginsering CLIENT : Omaha Public Power District
- PIPING PROJECT REPORT JUNE 8, 1992 R. Harsell PROJECT : OPPDCS PIPES : 123 UPDATED: JUNE 8, 1992 IDENTIFIER MATERIAL LENCTH FLUID NAME DESIGN TOTAL SIZE /-SCH (ft) TEMP FIhW-RATE K (gal / min) 97 CS RECIRC SSTEEL 0.60 WATER 3 in/SCH 40S 90 dag-F
.98 COMMON RECIRC SSTEEL 9.40 WATER 0.505 3 in/SCH 40s 90 deg-F 99 COMMON RECIRC SSTEEL 0.66 UATER 0.596 6 in/SCH 40S 90 dog-F 100 CS RECIRC SSTEEL 1 WATER 6 in/SCH 40S 90 deg-F 101 COMMON RECIRC SSTEEL 27.24 WATER 0.894 6 in/SCH 40S 90 des-F 102 COMMON RECIRC SSTEEL 5 WATER 0.596 6 in/SCH 40S 90 des-F 103 COMMON RECIRC SSTEEL 43.25 WATER 2.235 6 in/SCH 40S 90 deg-F 104 COMMON RECIRC SSTEEL' 6 WATER .11.644 4 in/SCH 80S 90 deg-F 105 COMMON RECIRC SSTEEL 24.99 WATER 2.158 6 in/SCH 10S 90 dog-F 106 COMMON RECIRC SSTEEL 21.01 WATER 0.590 6 in/SCH 10s 90 deg-F 107 CS SUMP PIPE STEEL 7.20 WATER 0.228 24 in/SCH 20 90 deg-F 108 CS SUMP PIPE STEEL 5.42 WATER 0.368 20 in/SCH 20 90 dog-F 109 COMMON SUMP LIN STEEL 140.40 WATER 3.022 24 in/SCH 20 90 deg-F 110 COMMON SUMP LIN STEEL 89.72 WATER 3.100 24 in/SCH 20 90 deg-F PIPE-FID by Engineered Software page 8 t . .
FC 059?? O-MECH-CALC 42i Rev. 00 PageBlo ABB Combustion Engineering CLIENT : Omaha Public Power District PIPING PROJECT REPORT JUNE 8, 1992 R. Harsell PROJECT : OPPDCS PIPES : 123 UPDATED: JUNC 8, 1992 IDENTIFIER HATERIAL LENGTH ' uID NAME DESIGN TOTAL SIZE / SCH (ft) TEMP FLOW-RATE K (gal / min) 111 COHHON SUMP LIN STEEL 55.86 WATER 0.475 24 in/SCH 20 , 90 deg-F 112 COHHON SUMP LIN STEEL 47.56 WATER 0.388 14 in/SCH 20 90 deg-F 113 cs recire 3b SSTEEL 0.66 WATER 0.776 2 in/SCH 40S 90 deg-F 114 cs recirc 3c SSTEEL 0.66 WATER 0.776 2 in/SCH 40S 90 deg-F 115 cs recire 3a SSTEEL 0.66 CLIER 0.776 2 in/SCH 40S 90 deg-F 116 cs recire SSTEEL 0.66 WATER 0.560 2 in/SCH 40S 90 deg-F 117 common to sirwt SSTEEL 1 UATER 1.000 6 in/SCH 10S 90 deg-F 118 SI-3C DISCHARGE SSTEEL 1 WATER 8 in/SCH 40S 90 deg-F 119 SI-3B DISCHARGE SSTEEL 1 WATER 8 in/SCH 40S 90 deg-F 120 SI-3A DISCHARGE SSTEEL 1 WATER 8 in/SCH 40S 90 deg-F 121 SUMP ENTRANCE STEEL 0.25 WATER 0.500 24 in/SCH 20 90 des-F 122 SUMP ENTRANCE STEEL 0.25' WATER 0.500 24 in/SCH 20 90 deg-F 123 A1 HEADER SSTEEL 25.28 UATER 1.917 12 in/SCH 40S 90 dog-F PIPE-FLO by Engineered Software page 9
, ,. _ . -_ . .._ . _ . . . _ .._ . m._ . . _ - . . . . . . . . _ _ _ _ . . . . . . . . .._. ._._
PageBgg l COMPONENT TABLE REPORT as of MAY 21, 1992 TABLE NAME: 6 COMPONENT ENTRIES CSS COMPONENTS FOR OPPD CSP NPSH w/ SUBCOOLING
' CODE COMPONENT ID POWER EQUATION A HX-A HEAD IDSS - 1.54E-06
- Q ^ 2 DATA POINTS: 0 gal / min vs. O ft of fluid j-' DATA POINTS: 1500 gal / min vs. 3.476 ft of fluid DATA POINTS: 4000 gal / min' vs.
24.72 ft of fluid B FIDW VALVE HEAD IDSS - 7.99E-07
- Q ^ 2 j DATA POINTS: 0 gal / min vs. O ft of fluid DATA POINTS: 2000 gal / min vs. 3.194 ft of fluid ,
DATA POINTS: 4000 Sal / min vs. 12.776 ft of fluid ' l C SI-3A (pump) HEAD RISE - 500 - 1.01E-07
- Q ^ 2.642 DATA POINTS: 0 gal / min vs. 500 ft of fluid DATA POINTS:-2800 gal / min vs. 370 ft of fluid DATA POINTS: 3200 gal / min vs. 315 ft of fluid D SI-3B (pump) HEAD RISE - 496 - 5.62E-08
- Q ^ 2.713 j
, DATA POINTS: 0 gal / min vs. 496 ft'of fluid ! DATA POINTS: 2800 gal / min vs. 370 ft of fluid DATA POINTS: 3200 gal / min vs. 315 ft of fluid
~
E SI-3C (pump) HEAD RISE - 494 - 4.14E-08
- Q ^ 2.749 DATA POINTS: O gal / min vs. 494 ft of fluid DATA POINTS: ' 2800 : gal / min vs. 370 ft of fluid DATA POINTS: 3200 gal / min vs. -315 ft of fluid i
F flow meter HEAD IDSS - 8.68E-07
- Q ^ 2 DATA POINTS: 0 gal / min vs. O ft of fluid DATA-POINTS:-2000 gal / min vs. 3.46 ft of fluid DATA POINTS: 4500 gal / min vs. 17.51 ft of fluid page 1 Y
O-MECH-CALC 42i Rev. 00 Pcge B l1 , ABB Combustion' Engineering CLIENT : Omaha Public Power District PIPELINE REPORT : SIRWT HEADER MAR 19, 1992 Petraske/ Harsell l PROJECT : OPPDCS DESIGN RULES: VELDCITY MIN: MAX: 1000.00 ft/see i PIPE NO : 2 ------------ PRESSURE MIN:0 MAX: 5000.00 PSI
---- PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES -----------
MATERIAL: STEEL FLUID: VATER at 90.0 des-F SCHEDULE: 20 density: 62.108 lbs/ft*3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois l NOMINAL SIZE: 20 in DESIGN PIDW RATE: l inside diameter: 19.25 in FLUID VEIDCITY: 1 PIPE 12NGTH: 7.25 ft HEAD IDSS: ELEVATION IN: 981.00 ft PRESSURE IN:
-00T: 981.00 ft OUT:
---.--------------------- VALVES AND FITTINGS -------------------------
VALVE NO FFT - 0.012 K - VALUE 1 TEE-RUN 0.236 V&F HEAD IDSS - 0.000 ft V&F TOTAL K - 0.236 4 PIPE-FLO by Engineered Software ;
- 1
FC 05977 O-MECH-CALC-021 Rev. 00 P:ge B G ABB Combustion Engineering CLIENT : Omaha Public Power District PIPELINE REPORT : SI-3A SUCTION MAR 19, 1992 Petraske/ Harsell PROJECT : OPPDCS DESIGN RULES: VEIDCITY MIN: MAK: 1000.00 ft/see PIPE NO : 5 ------------ PRESSURE MIN:0 MAX: 5000.00 PSI
---- PIPE CHARACTERISTICS ------------------- FINID PROPERTIES ------- .---
MATERIAL: SSTEEL FLUIDi WATER at 90.0 des-F SCHEDULE: 105 density: 62.108 lbs/ft^3 abs. roughness: 1.80E-03 in viscosity: 0.7600 contipois NOMINAL SIZE: 12 in DESIGN FIDW RATE: inside M==ater: 12.39 in FIRID VEIDCITY: PIPE IJMGTH: 18.65 ft HEAD IDSS: ELEVATION IN: 980.00 ft PRESSURE IN: OUT: 980.00 ft OUT:
------------------------- VALVES AND FITTINGS -------------------------
K - VALUE VALVE NO FFI - 0.013 ' 1 2
- ELBOW-S 90 de5 0.515 2 GATE 0.103 V&F HEAD IDSS - 0.000 ft V&F 'IOTAL K - 0.618 PIPE-FID by Engineered Software
FC 05 Rev.2,7 7 O-MECH-CALC-021 P;gnB(g ABB Combustion Engineering CLIENT : Omaha Public Power District PIPELINE REPORT : SI-3C SUCTION MAR 19, 1992 Petraske/ Harsell PROJECT : OPPDCS DESIGN. RULES: VEIDCITY MIN: HAX: 1000.00 ft/see PIPE NO : 6 ------------ PRESSURE MIN:0 HAX: 5000.00 PSI
---- PIPE CHARAC 3 RISTICS ------------------- FLUID PROPERTIES -----------
MATERIAL: SSTEEL FLUID: WATER at 90.0 deg-F SCHEDULE: 10S density: 62.108 lbs/ft*3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois NOMINAL SIZE: 12 in DESIGN FIDW RATE: inside diameter: 12.39 in FLUID VEIDCITY: PIPE LENGTH: 26.39 ft HEAD IASS: ELEVATION IN: 981.00 ft PRESSURE IN: OUT: 978.00 ft OUT:
......................... VALVES AND FITTINGS VALVE NO FFT - 0.013 K - VALUE 1 FIX-K VAIEE 0.787 2 3
- E130W-S 90 deg 0.772 3 GATE 0.103 V&F HEAD LOSS - 0.000 ft V&F TOTAL K - 1.662 .
1 1 PIPE-FIA by Engineend Software O
_ ~. .. . . - - - . - _ _ - . _ . _ _ _ _ _ _ _. . _ _ , _ _ _ _ . _ _ , _ _ , _ _ __ ,_ _ __ _,_ O-MECH 42 , PJgn B gy ABB Combustion Engineering CLIENT : Omaha Public Power District PIPELINE REPORT : SI-3B SUCTION MAR 19, 1992 Petraske/ Harsell PROJECT : OPPDCS DESIGN RULES: VEIDCITY MIN: MAK: 1000.00 ft/see PIPE NO : 7 ------------ FRESSURE MIN:0 MAX: 5000.00 PSI
-... PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES ----- .-----
NATERIAL: SSTEEL FIDID: WATER at 90.0 deg-F SCHEDULE: 10S density: 62.108 lbs/ft*3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois NOMINAL SIZE: 12 in DESIGN FIDW RATE: inside diameter: 12.39 in FLUID VEIDCITY: PIPE LDCTH: 14.85 ft HEAD IDSS: ELEVATION IN: 981.00 ft PRESSURE IN: OUT: 979.00 ft OUT:
......................... VALVES AND FITTINGS -------------------------
VALVE NO FFT - 0.013 K - VALUE 1 FIX-K VAIDE 0.787 2 2
- ELBOW-S 90 deg 0.515 3 CATE 0.103 V&F HEAD IDSS - 0.000 ft V&F TOTAL K - 1.405 PIPE-FID by Engineered Software
^ ' ~ - . . , . .
FU 05W / O-MECH-CALC-021 Rev. 00 1 P.g3 B gb ABB Combustion Engineering CLIENT : Omaha Public Power District PIPELINE REPORT : SI-3A SUCTION MAR 19, 1992 Petraske/ Harsell PROJECT : OPPDCS DESIGN RULES: VEIDCITY MIN: HAX: 1000.00 ft/see PIPE NO : 67 ------------ PRESSURE MIN:0 HAX: 5000.00 PSI
.... PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES ------ ----
MATERIAL: SSTEEL FLUID: VATER at 90.0 dog-F SCHEDULE: 40S density: 62.108 lbs/ft^3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois NOMINAL SIZE: 12 in DESIGN FLOW RATE: inside diameter: 12.00 in FLUID VEIACITY: PIPE LENGTH: 9.50 ft HEAD LOSS: ELEVATION IN: 980.00 ft PRESSURE IN: OUT: 973.00 ft OUT:
.................-.-...-- VALVES AND FITTINGS -------------------------
VALVE NO FFT - 0.013 K - VAIDE 1 ELBOW-S 45 dag 0.189 2 ELBOW-S 90 deg 0.259 V&F HEAD IDSS - 0.000 ft .V&F TOTAL K - 0.448 . l l PIPE-FLO by Engineered Software
0-MECH -021 PageBQ j 1 l ABB Combustion Engineering CLIENT : Omaha Public Power District ] 1 PIPELINE REPORT : SUCTION SI-3C MAR 19, 1992 ( Petraske/ Harsell . PROJECT : OPPDCS DESIGN RULES: VEIACITY MIN: MAX: 1000.00 ft/sec l PIPE NO : 68 ------------ PRESSURE MIN:0 MAX: 5000.00 PSI l ..-. PIPE CHARACTERISTICS ------------------- FIAID PROPERTIES --------..- MATERIAL: SSTEEL FLUID: VATER at 90.0 deg-F SCHEDULE: 40S density: 62.108 lbs/ft*3 abs. roughness: 1.80E-03 in viscosity: 0.7600 contipois NOMINAL SIZE: 12 in DESION FIAU RATE: inside diameter: 12.00 in FLUID VEIACITY: PIPE LENGTH: 5.50 ft HEAD 1 ASS: l ELEVATION IN: 978.00 ft PRESSURE IN:
- l OUT: 973.00 ft OUT:
............-...-......-- VALVES AND FITTINGS ------------------------ -
none i i l ' l l I l
\
l I
- 1 t .
l i PIPE-FID by Engineered Software
Pcg3Bjj l ABB Combustion Engineering l i CLIENT : Omaha Public Power District l PIPELINE REPORT : SUCTION SI-3B MAR 19, 1992 Petraske/ Harsell PROJECT : OPPDCS DESIGN RULES: VEIDCITY MIN: MAX: 1000.00 ft/see PIPE NO : 69 ------------ PRESSURE MIN:0 MAX: 5000.00 PSI
---- PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES ------r----
HATERIAL: SSTEEL FLUID: WATER at 90.0 deg-F SCHEDULE: 40S density: 62.108 lbs/ft*3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois . NOMINAL SIZE: 12 in DESICN FIDT RATE: inside diameter: 12.00 in FLUID VEIDCITY: PIPE LENGTH: HEAD IDSS: 1 ELEVATION IN: ' 10.43 979.00 ft ft PRESSURE IN: OUT: 973.00 ft OUT:
------------------------- VALVES AND FITTINCS -------------.-----------
VALVE NO FFT - 0.013 K - VAIRE q 1 ELBOW-S 90 deg 0.259 V&F HEAD IDSS - 0.000 ft V&F TOTAL K - 0.259 I a PIPE-FLO by Engineered Software
VU UD')(( 0-MECil-CALC-021 Rev. 00 1 l Page B g i I ABB Combustion Engineering 1 CLIENT : Omaha Public Po'ver District PIPELINE PIPORT : CS SUMP PIPE HAR 19, 1992 l Petraske/ Harsell l l PROJECT : OPPDCS DESIGN RULES: VELOCITY MIN: HAX: 1000.00 ft/see PIPE NO : 107 ------------ PRESSURE MIN:0 HAX: 5000.00 PSI
---- PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES ------ ----
l MATERIAL: STEEL FLUID: UATER at 90.0 deg-F SCHEDULE: 20 density: 62.108 lbs/ft^3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois NOMINAL SIZE: 24 in DESIGN FLOW RATE: l inside diameter: 23.25 in FLUID VEIDCITY: i PIPE LENGTH: 7.20 ft HEAD IDSS: l ELEVATION IN: 980.00 ft PRESSURE IN: OUT: 980.00 ft OUT: VALVES AND FITTINGS VALVE NO FFT - 0.011 K - VALUE 1 TEE-RUN 0.228 V&F HEAD IDSS - 0.000 ft .V&F TOTAL K - 0.228-l l l l l PIPE-FID by Engineered Sof tware
l FC 05977 O-MECilCALC-021 Rev. 00 P:gi B Qo ABB Combustion Engineering l CLIENT : Omaha Public Power District PIPELINE REPORT : CS SUMP PIPE HAR 19, 1992 Petraske/ Harsell PROJECT : OPPDCS DESIGN RULES: VEIDCITY MIN: MAX: 1000.00 ft/see . PIPE NO : 108 ------------ PRESSURE MIN:0 MAX: 5000.00 PSI l
---- PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES -----------
MATERIAL: STEEL FLUID: WATER at 90.0 deg-F SCHEDULE: 20 density: 62.108 lbs/ft^3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois NOMINAL SIZE: 20 in DESIGN FIDW RATE: inside diameter: 19.25 in FLUID VEIDCITY: PIPE LENGTH: 5.42 ft HEAD IDSS: ELEVATION IN: 982.00 ft PRESSURE IN: OUT: 982.00 ft OUT:
........_-..........----. VALVES AND FITTINCS -------------------------
VALVE NO FFT - 0.012 K - VALUE 1 TEE-RUN 0.236 2 REDUCER seat: 23.25 , appr: 2.00 0.132 V&F HEAD IDSS - 0.000 ft V&F TOTAL K - 0.368 PIPE FLD by Engineered Software
l' O MECH-CALC-021 Rev. 00 l Poge n ') \ l i ABB Combustion Engineering CLIENT : Omaha Public Power District l PIPELINE REPORT : CONMON SUMP LIN MAR 19, 1992 Petraske/ Harsell , PROJECT : OPPDCS DESIGN RULES: VELOCITY MIN: HAX: 1000.00 ft/sec ! PIPE No : 109 ------------ PRESSURE MIN:0 MAX: 5000.00 PSI l
.-.. PIPE CHARACTERISTICS ------------------- FWID PROPERTIES ------ ----
' MATERIAL: STEEL FWID: WATER at 90.0 dog-F -
SCHEDULE: 20 density: 62.108 lbs/ft^3
- . abs. roughness
- 1.80E-03 in viscosity: 0.7600 contipois NOMINAL SIZE: 24 in DESIGN FIDW RATE: '
inside diameter: 23.25 in FLUID VEIDCITY: PIPE LENGTH: 140.40 ft HEAD IDSS: !' ELEVATION IN: 994.00 ft PRESSURE IN: OUT: 982.00 ft OUT: l I '
......................... VALVES' AND FITTINGS -------------------------
VALVE NO FFT - 0.011 K - VALUE l 1 CK-SW-ANG 1.141 2 BUTTERFLY 0.285 l
- 3 2
- ELBOW-S 24 deg 0.276 4 2
- ELBOW-L 90 deg 0.320 5 EXIT 1.000 V&F HEAD IDSS - 0.000 ft V&F TOTAL K - 3.022 i
l i. i 4 PIPE-FID by Engineered Software J
- - , , , . ,y _ -, .
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. - .- - - . _ . _ . _ . - . - . .-. ~ . . . . _ . -
a 0-MECH-CALC 41 Rev,00 P gs B n j ABB Combustion Engineering 4 x CLIENT : Omaha Public Power District PIPELINE REPORT : COMMON SUMP LIN MAR 19, 1992 4 Petraske/ Harsell PROJECT : OPPDCS DESIGN RULES: VEIDCITY MIN: MAX: 1000.00 ft/see . PIPE NO : 110 ------------ PRESSURE MIN:0 MAX: 5000.00 PSI
---- -PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES -----------
MATERIAL: STEEL FLUID: WATER at 90.0 deg-F SCHEDULE: 20 density: 62.108 lbs/ft^3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois NOMINAL SIZE: 24 in DESIGN FLOW RATE: inside diameter: 23.25.in FLUID VEIDCITY: PIPE LENGTH:- 89.72 ft HEAD IDSS: ELEVATION IN: 994.00 ft PRESSURE IN: j OUT: 982.00-ft OUT:
------------------------- VALVE.J AND FITTINGS -------------------------
K - VALUE VALVE NO FFI - 0.011 1.141 1 CK-SW-ANG f 2 BUTTERFLY 0.285 ! 3 2
- ELBOW-L 30 deg 0.195 4 3
- ELBOW-L 90 de5 0.479 ,
1 5 EXIT 1.000 ! I V&F HEAD IDSS - 0.000 ft V&F TOTAL K - 3.100 i I a M 4 1 9 PIPE-FLO by Engineered Software
IFU 05977 O-MECil-CALC-021 Rw. 00 Pcg:s B13 ABB Combustion Engineering CLIENT : Omaha Public Power District PIPELINE REPORT : COMMON SUMP LIN MAR 19, 1992 Petraske/ Harsell PROJECT : OPPDCS DESIGN RULES: VEMCITY MIN: MAX: 1000.00 ft/see PIPE NO : 111 ------------ PRESSURE MIN:0 HAX: 5000.00 PSI
.... PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES ------ ----
HATERIAL: STEEL FLUID: WATER at 90.0 deg-F SCHEDULE: 20 density: 62.108 lbs/ft^3 abs. roughness: 1.80E-03 in viscosity: 0.7600 centipois NOMINAL SIZE: 24 in DESIGN FMW RATE: inside diameter: 23.25 in FLUID VEMCITY: PIPE LENGTH: 55.86 ft HEAD MSS: l ELEVATION IN: 982.00 ft PRESSURE IN: i OUT: 980.00 ft OUT: -
...................-....- VALVES AND FITTINGS -------------------------
VALVE NO FFT - 0.011 K - VAME i 1 ELBOW-L 20 deg 0.087 2 ELBOW-L 90 dag 0.160 1 3 TEE-RUN 0.228 ) l V&F HEAD M SS - 0.000 ft V&F TOTAL K - 0.475 i* PIPE-FLO by Engineered Software
PU U59// O-MECHCALC-021 Rev. 00
, . P gs B 1%
ABB Combustion Engineering CLIENT : Omaha Public Power District PIPELINE REPORT : COMMON SUMP LIN MAR 19, 1992 Petraske/ Harsell PROJECT : OPPDCS DESIGN RULES: VEIDCITY MIN: PIPE NO : 112 MAX: 1000.00 ft/see
------------ PRESSURE MIN:0 MAX: 5000.00 PSI PIPE CHARACTERISTICS ------------------- FLUID PROPERTIES ----- -----
MATERIAL: STEEL FLUID: WATER at SCHEDULE: 20 - 90.0 deE-F abs. roughness: 1.80E-03 in density: 62.108 lbs/ft*3 viscosity: 0.7600 centipois l NOMINAL SIZE: 24 in DESIGN FIDWRATE: l inside diameter: 23.25 in FLUID VEIDCITY: l PIPE LENGTH: 47.56 ft HEAD IDSS* I ELEVATION IN: 992.00 ft PRESSURE IN: ' OUT: 992.00 ft OUT:
---.--------------------- VALVES AND FITTINGS -------------------------
VALVE NO FFI - 0.011 K - VALUE 1 ELBOW-L 90 deg 0.160 2 TEE-RUN 0.228 V&F HEAD IDSS - 0.000 ft V&F TOTAL K - 0.388 l l \ PIPE FID by Engineered Software I l
O-MECHCALC-021 Rev. 00 Page C l l i j APPENDIX C NET-FLO OUTPUT FOR CSS MAIN MODEL RUNS C2 NET-FLO Output for Run 1 C19 NET-FLO Output for Run 2 C26 NET-FLO Output for Run 3 . l C33 NET-FLO Output for Run 4 C40 NET-FLO Output for Run 5 C47 NET-FLO Output for Run 6 i l j I i i l t
~
FC 05977 o-MECH-CALC-021 Rrs. 00 i Pagi C 1 ABB Cctbustien Engintering CLIENT : Omaha Public Power District NETWORK
SUMMARY
REPORTS JUNE 8, 1992 R. Harsell NETWORK NAME : OPPDCS1 DATA FOR PIPES: OPPDCS UPDATED : JUNE 8, 1992 OPPD CSP NPSH W/ SUMP SUBCOOLING 0-MECH-CALC-021 3P2H:3A,3B,3C SUCTION FROM THE SUMP (6 ft) 0.01 4 DEVIATION after 8 ITERATIONS FIXED GRADE
SUMMARY
NETWORK CONNECTION FLOW-RATE FIXED GRADE / NODE. PIPELINE (gal / min ) PRESSURE SOURCE l R1 >>> 79 RING A >>> 1,149.88 >>> 14.70 PSI R2 M> 80 RING B >>> 926.30 >>> 14.70' PSI R3 >>> 81 RING C >>> 740.49 >>> 14.70 PSI . R4 >>> 82 RING D >>> 537.40 >>> 14.70 PSI R7 >>> 83 RING E >>> 108.05 >>> 14.70 PSI R8 >>> 84 RING F .>>> 336.13 >>> 14.70 PSI R9 >>> 85 RING G >>> 1,198.03 >>> 14.70 PSI R10 >>> 86 RING H >>> 875.66 >>> 14.70 PSI R11 >>> 87 RING I >>> 675.80 >>> 14.70 PSI R12 >>> 88 RING J >>> 510.55 >>> 14.70 PSI l R15 >>> 89 RING K >>> 207.66 >>> 14.70 PSI i R16 >>> 90 RING L >>> 338.13 >>> 14.70 PSI H70 <<< 121 SUMP ENTRANCE <<< 7,604.09 <<< 17.30 PS , I l i NET FIDWS IN: 0.01 gal / min l l l l NET-F1h of the FLO-SERIES page 1 d l l-
FC 05977 O-MECH CALC 41 Rev. 00 DEMAND
SUMMARY
PageC3 JUNCTION DEMAND JUNCTION DEMAND NODE (gal / min ) NODE (gal / min ) NET DEMAND IN: 0.00 gal / min 1
)
l l l l l 5 NET-FLO of the FID-SERIES page 2
FU 05977 1 0-MECH-CALC-02i Rev. 00 ! COMPLETE JUNCTION NODE REPORT JUNE 8, 1992 Pags C y NODE COUNT: 81 DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI
. JUNCTION- DEMAND ELEVATION ' HYDRAULIC PRESSURE NODE (gal / min ) (ft) GRADE (PSI)
C1 0 989.00 1,032.58 18.80 PIPES IN: PIPES OUT: 1 SIRWT EXIT i l C10 0 974.00 1,433.68 198.26 PIPES IN: 74 PUMP SI-3A PIPES OUT: 120 SI-3A DISCHARGE , X 93XPIPE-93 l l
- l. C11 0 979.50 1,408.62 185.08 l PIPES IN: 8 SI-3A DISCHARGEPIPES'0UT: 70 DISCHARGE HDR X 93XPIPE-93
~ '
i C12 0 974.00 1,423.93 194.06 PIPES IN: 75. PUMP SI-3B PIPES OUT: 119 SI-3B DISCHARGE C13 0 979.50 1,409.60 185.50 PIPES IN: 9 SI-3B DISCHARGEPIPES OUT: 71 DISCHARGE HDR 1 C14 0 974.00 1,425.13 194.57 PIPES IN: 76 PUMP SI-3C PIPES OUT: 118 SI-3C DISCHARGE C15 0 979.50' 1,'409.60 185.50 PIPES IN:' 10 SI-3C DISCHARGEPIPES OUT: 72 DISCHARGE HDR
- j C16 0 979.50 1,408.16 184.88 PIPES IN: 11 DSCHRG HDR PIPES OUT: 13 DSCHRG HDR 70 DISCHARGE HDR
, NET-FID of the FID-SERIES page 3 l Y l'
FC 05977 l 0-MECH CALC-021 Rev. 00 1 COMPLETE JUNCTION NODE REPORT JUNE 8, 1992 Rae C 5 l NODE COUNT: 81 DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI JUNCTION DElkJD ELEVATION HYDRAULIC PRESSURE NODE (gal /tain ) (ft) CRADE (PSI) 4 l C17 0 979.50 1,409.12 185.30 1 PIPES IN: 71 DISCHARCE HDR PIPES OUT: 11 DSCHRG HDR 72 DISCHARGE HDR , C18 0 997.66 1,377.73 163.93 PIPES IN: 13 DSCHRG HDR PIPES OUT: 14 A HX INLET l 15 B HX INLET l C19 0 993.75 1,372.84 163.50 PIPES IN: 14 A HX INLET PIPES OUT: 77 HX-A C2 0 981.50 1,032.58 22.03 PIPES IN: 1 SIRWT EXIT PIPES OUT: 6 SI-3C SUCTION 2 SIRWT HEADER C20 0 993.75 1,368.32 161.55 PIPES IN: 15 B HX INLET PIPES OUT: 78 HX-B C21 0 995.75 1,350.53 153.02 PIPES IN: 77 HX-A PIPES OUT: 16 A HX OUTLET C22 0 996.75 1,348.37 151.66 ) I PIPES IN: 16 A HX OUTLET PIPES OUT: 18 HX CROSS CONECT , 21 A HEADER : I C23 0 995.75 1,345.92 151.03 l PIPES IN: 78 HX-B PIPES OUT: 17 B HX OUTLET l NET-FID of the FLO-SERIES page 4 l
PU UD')t/ O-MECH-CALC-021 Rev. 00 JUNE 8, 1992 Paga C b COMPLETE JUNCTION NODE REPORT NODE COUNT: 81 DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI JUNCTION DEMAND ELEVATION HYDRAULIC PRESSURE NODE (gal / min ) (ft) GRADE (PSI) C24 0 996.75 1,344.13 149.83 PIPES IN: 17 B HX OUTLET PIPES OUT: 19 HX CROSS CONECT 22 B HEADER C25 0 990.50 1,348.37 154.35 PIPES IN: 18 HX CROSS CONECTPIPES OUT:X 20XSDC DISCHARGE C26 0 990.50 1,344.13 152.52 PIPES IN: 19 HX CROSS CONECTPIPES OUT: X 20XSDC DISCHARGE C27 0 1,008.00 1,329.94 138.85 PIPES IN: 21 A HEADER PIPES OUT: 23 A HEADER C28 0 1,009.00 1,325.18 136.37 PIPES IN: 22 B HEADER PIPES OUT: 24 B HEADER C29 0 1,009.00 1,304.45 127.43 PIPES IN: 23 A HEADER PIPES OUT: 25 A HEADER C3 0 981.50 1,032.62 22.05 PIPES IN: 108 CS SUMP PIPE PIPES OUT: 2 SIRWT HEADER 7 SI-3B SUCTION , C30 0 1,032.00 1,300.81 115.94 PIPES IN: 25 A HEADER PIPES OUT: 26 A HEADER
. NET-FID of the FLO-SERIES page 5 l
l FC 059 7 l O-MECH-CALC-021 Rev. 00 ! COMPLETE JUNCTION NODE REPORT JUNE 8, 1992 Pass C ] NODE COUNT: 81 l DESIGN RULES: PRESSURE MIN: 0.00 HAX: 5000.00 PSI JUNCTION DEMAND ELEVATION ' HYDRAULIC PRESSURE NODE (gal / min ) (ft) CRADE (PSI) C31 0 1,009.00 1,297.76 124.54 PIPES IN: 24 B HEADER PIPES OUT: 73 HEADER B l C32 0 1,036.70 1,295.82 111.76 PIPES IN: 73 HEADER B PIPES OUT: 37 B HEADER l 1,296.11 C33 0 1,074.00 95.80 PIPES IN: 26 A HEADER PIPES OUT: 27 A HEADER 29 A HEADER C34 0 1,074.00 1,295.88 95.70 . . ! PIPES IN: 27 A HEADER PIPES OUT: 28 A HEADER C35 0 1,111.50 1,291.10 77.46 PIPES IN: 28 A HEADER PIPES OUT: 30 A HEADER i C36 0 1,111.50 1,291.16 77.49 PIPES IN: 29 A HEADER PIPES OUT: 65 SPRAY HDR A 66 SPRAY HDR A C37 0 1.,111.50 1,290.95 77.40 PIPES IN: 30 A HEADER PIPES OUT: 31 A HEADER 49 RING A , C38 0 1,111.50 1,290.'93 77.39 PIPES IN: 31 A HEADER PIPES OUT: 32 A HEADER 65 SPRAY HDR A NET-FLO of the FLO-SERIES page 6 l t
FC 05977 O-MECH-CALC-021 Rev. 00 COMPLETE JUNCTION - NODE REPORT JUNE 8, 1992 Pass CT NODE COUNT: 81 DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI JUNCTION DEMAND ELEVATION HYDRAULIC PRESSURE NODE (gal / min ) (ft) GRADE (PSI) C39 0 1,111.50 1,290.85 77.35 PIPES IN: 32 A HEADER PIPES OUT: 33 PIPE-33 66 SPRAY HDR A C4 0 989.00 1,033.56 19.22 PIPES IN: PIPES OUT: 3 SIRWT EXIT C40 0 1,111.50 1,290.83- 77.35 PIPES IN: 33 PIPE-33 PIPES OUT: 34 A HEADER 50 RING B I I
~ '
C41 0 1,111.50 1,290.73 77.30 PIPES IN: 34 A HEADER PIPES OUT: 35 A HEADER l 51 RING C l C42 0 1,111.50 1,290.69 77.29 PIPES IN: 35'A HEADER PIPES OUT: 36 A HEADER 52 RING D f C43 0 1,111.50 1,290.68 77.28 PIPES IN: 36 A HEADER PIPES OUT: 53 RING E i C44 0 1,074.00 1,291.03 93.61 PIPES IN: 37 B HEADER PIPES OUT: 38 8 HEADER j 40 B HEADER C45 0 1,074.00 1,290.93 93.56 PIPES IN: 38 B HEADER PIPES OUT: 39 B HEADER l-j NET-FID of the FID-SERIES page 7 i 6
-
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FC 05977 O-MECH CALC 41 Rev. 00 COMPLETE JUNCTION NODE REPORT JUNE 8, 1992 Page C q
- NODE COUNT
- 81 DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI JUNCTION DEMAND ELEVATION HYDRAULIC PRESSURE NODE (gal / min ) (ft) GRADE (PSI)
C46 0 1,111.50 1,284.66 74.68 PIPES IN: 40 B HEADER PIPES OUT: 41 B HEADER C47 0 1,111.50 1,284.64 74.68 PIPES IN: 41 B HEADER PIPES OUT: 42 B HEADER C48 0 1,111.50 1,285.67 75.12 I PIPES IN: 39 B HEADER PIPES OUT: 43 B HEADER ; C49 0 1,111.50 1,284.45 74.59 PIPES IN: 44 B HEADER PIPES OUT: 45 B HEADER 57 RING G I C5 0 980.00 1,033.56 23,10 PIPES IN: 3 SIRWT EXIT PIPES OUT: 4 SIRWT HEADER C50 0 1,111.50 1,284.22 74.50 l PIPES IN: 45 B HEADER PIPES OUT: 46 B HEADER i 58 RING H l C51 0 1,111.50 1,284.11 74.45 . PIPES IN: 46 B HEADER PIPES OUT: 47 B HEADER I 59 RING I , CS2 0 1,111.50 1,284.07 74.43 PIPES IN: 47 B HEADER PIPES OUI: 48 8 HEADER 60 RING J l r i NET-FLO of the FLO-SERIES page 8 1
L FC 05977 O-MECH CALC-021 Rev. 00 ' I COMPLETE ' JUNCTION NODE REPORT JUNE 8, 1992 Page C \o NODE COUNT: 81-l DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI JUNCTION DEMAND ELEVATION HYDRAULIC PRESSURE NODE (gal / min ) (ft) GRADE (PSI)
- C53 0 1,111.50 1,284.06 74.43 PIPES IN
- 48 8 HEADER PIPES OUT: 61 RING K I
C54 0 1,111.50 1,284.53 74.63 PIPES IN: 42 B HEADER PIPES OUT: 44 B HEADER 43 B HEADER I i C6 0 980.00 1,033.56 23.10 I 1 PIPES IN: 4 SIRWT HEADER PIPES OUT: 5 SI-3A SUCTION l 107 CS SUMP PIPE
~ ~
C60 0 975.00 1,423.84 193.59 PIPES IN: '119 SI-3B DISCHARGEPIPES OUT: 9 SI-3B DISCHARGE i C61 0 975.00 1,425.04 194.10 PIPES IN: 118 SI-3C DISCHARGEPIPES OUT: 10 SI-3C DISCHARGE i C62 0 975.00 1,433.59 197.79 PIPES IN: 120 SI-3A DISCHARGEPIPES OUT: 8 SI-3A DISCHARGE C7 0 973.25' 1,032.51 25.56 PIPES IN: 67 SI-3A SUCTION PIPES OUT: 74 PUMP SI-3A
~
C8 0 973.25 1,031.07 -24.94 j PIPES IN: 68 SUCTION SI-3C PIPES OUT: 76 PUMP SI-3C 1 l C9 0 973.25 1,031.11 24.96 PIPES IN: 69 SUCTION SI-3B PIPES OUT: 75 PUMP SI-3B l
- j. NET-FLO of the FLO-SERIES page 9 f
I i e
O-MECH CALC-021 Rev. 00 COMPLETE JUNCTION NODE REPORT JUNE 8, 1992 Pcge C y NODE COUNT: 81 DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI
. JUNCTION DEMAND ELEVATION HYDRAULIC PRESSURE-NODE (gal / min ) (ft) GRADE (PSI)
H3 0 982.00 1,033.63 22.27 PIPES IN: 109 COMMON SUMP LINPIPES OUT: 111 COMMON SbMP LIN H70 0 994.00 1,033.85 17.19 PIPES IN: 121 SUMP ENTRANCE PIPES OUT: 109 COMMON SUMP LIN 110 COMMON SUMP LIN N3 0 980.00 1,033.58 23.11 PIPES IN: 111 COMMON SUMP LINPIPES OUT: 107 CS SUMP PIPE l N42 0 --- 1,032.99 --- PIPES IN: 110 COMMON SUMP LINPIPES OUT: 112 COMMON SUMP LIN N9 0 980.00 1,032.82 22.78 PIPES IN: 112 COMMON SUMP LINPIPES OUT: 108 CS SUMP PIPE R1 0 1,117.50 1,289.90 74.36 PIPES IN: 49 RING A PIPES OUT: 79 RING A R10 0 1,119.30 1,283.66 70.89 PIPES IN: 58 RING H PIPES OUT: 86 RING H R11 0 1,122.30 1,282.72 69.19 j i
- PIPES IN: 59 RING I PIPES OUT: 87 RING I
.R12 0 1,124.60 1,283.16 68.39 PIPES IN: 60 RING J PIPES OUT: 88 RING J NET-FID of the FLO-SERIES page 10
FC'05977 - 0-MECH-CALC-021 Rev. 00 COMPLETE JUNCTION NODE REPORT JUNE 8, 1992 Page C h NODE COUNT: 81 DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI JUNCTION DEMAND ELEVATION HYDRAULIC PRESSURE NODE -(gal / min ) (ft) GRADE (PSI) R13 0 1,124.50 1,277.87 66.15 PIPES IN: 61 RING K PIPES OUT: 62 RING K2 64 RING L R14 0 1,124.50 1,277.76 66.10 PIPES IN: 62 RING K2 PIPES OUT: 63 RING K3 R15 0 1,127.50 1,276.61 64.31 PIPES IN: 63 RING K3 PIPES OUT: 89 RING K 1 R16 0 1,126.50 1,276.20 64.57 . , PIPES IN: 64 RING L PIPES OUT: 90 RING L R2 0 1,120.90 1,290.05 72.96 PIPES IN: 50 RING B PIPES OUT: 80 RING B R3 0 1,123.50 1,288.95 71.36 PIPES IN: 51 RING C PIPES OUT: 81 RING C j l R4 0 1,125.40 1,289.63 70.83 PIPES IN: 52 RING D PIPES OUT: 82 RING D R5 0 1,125.30 1,286.26 69.42 j PIPES IN: 53 RING E PIPES OUT: 54 RING E2 56 RING F R6 0 1,128.00 1,286.23 68.25 PIPES IN: 54' RING E2 PIPES OUT: 55 RING E3
. NET-FLO of the FLO-SERIES page 11
O-MECH 4ALC 021 Rev. 00 COMPLETE JUNCTION NODE REPORT JUNE 8, 1992 Pqp C l$ NODE COUNT: 81 DESIGN RULES: PRESSURE MIN: 0.00 MAX: 5000.00 PSI JUNCTION DEMAND ELEVATION MYDRAULIC PRESSURE NODE (gal / min ) (ft) GRADE (PSI) R7 0 1,127.70 1,285.91 68.24 PIPES IN: 55 RING E3 PIPES OUT: 83 RING E R8 0 1,127.00 1,284.61 67.98 PIPES IN: 56 RING F PIPES OUT: 84 RING F R9 0 1,115.30 1,283.39 72.50 PIPES IN: 57 RING G PIPES OUT: 85 RING G S1 0 980.00 1,032.96 22.84 -
^~
PIPES IN: 5 SI-3A SUCTION PIPES OUT: 67 SI-3A SUCTION S2 0 979.00 1,031.45 22.62 PIPES IN: 7 SI-3B SUCTION PIPES OUT: 69 SUCTION SI-35 S3 0 978.75 1,031.13 22.59 PIPES IN: 6 SI-3C SUCTION PIPES OUT: 68 SUCTION SI-3C 5 i NET-FLO of the FLO-SERIES page 12
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FC 05977
- 0. MECH-CALC 4X21 Rev. 00 COMPLETE PIPELINE REPORT JUNE 8, 1992 Pagi C g PIPELINE COUNT: 100 DESIGN RULES: .. VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec ;
PIPELINE . FROM TO HEAD-IDSS VEIDCITY FIDW-RATE NO . ID NODE NODE (CAIN) (ft/sec) (gal / min )
'l . SIRWT EXIT C1 C2 0.00 0.00 0.00 _
i 2 SIRWT HEADER C3
- C2 0.04 2.81 2,549.27
'3 SIRWT EXIT, C4 C5 0.00 0.00 0.00 4 SIRWT HEADER C5 C6 0.00 0.00 'O.00 5 SI-3A SUCTION C6 S1 0.60 6.62 2,489.21 6 SI-3C SU' GON C2 S3 1.45 6.78 2,549.27 7 SI-3B SUCTION C3 S2 1.17 6.83 2,565.61 i
8 SI-3A DISCHARGE C62 C11. 24.97 15.96 2,489.21
.9' SI-3B DISCHARGE C60 C13 14.24 16.45 2,565.61
.10'1 SI-3C DISCHARGE- C61 C15 15.44 16.34 2,549.27 11 DSCHRG HDR C17 C16 0.94 14.51 5,114.88 13 DSCHRG HDR C16 C18 30.43 21.57 7,604.09 14 A HX INLET C18 C19 .4.91 10.77 3,798.25 15 'B HX INLET' C18 C20 9.44 10.79 3,805.84
'16 A HX OUTLET C21 C22 2.16 10.77 3,798.25 17 5 HX OUTLET C23 C24 1.79 10.79 3,805.84 18 3X CROSS CONECT C22 C25 0.00 0.00 0.00 19 HX CROSS CONECT C24 C26 0.00 0.00 0.00
- 20. SDC DISCHARGE C25 C26 *** CIASED ***
21- 'A HEADER C22 C27 18.43 10.17 3,798.25
--- WITH COMPONENT F - flow meter-l22 B HEADER - C24 C28 18.95 10.79 3,803.84
--- WITH COMPONENT F - flow meter
. NET-FID of the FID-SERIES page 13
- . - -. . . . - . .n - . _ . ~ . - . ~ . - - ..- .- .. . . . ~ . . . - .
O-MECH 4ALC41 Rev. 00 COMPLETE PIPELINE REPORT JUNE 8, 1992 Page C gf I PIPELINE COUNT: 100 l l, DESIGN RULES: VEIDCITY MIN: 0.00 HAX: 1000.00 ft/sec l i PIPELINE FROM TO HEAD-LOSS VELOCITY FIDW-RATE l NO. ID NODE ' NODE (GAIN) (ft/sec) (gal / min ) 23 _ A HEADER C27 C29 25.49 24.35 3,798.25
- --- WITH COMPONENT B - FIDW VALVE i
- 24 B HEADER- .C28 C31 27.42 24.40 3,805.84
[ --- WITH COMPONENT B - FIDW VALVE l 3.64 25' A HEADER C29 C30 10.77 3,798.25 l 26 A HEADER C30 C33 4.70 10.10 -3,798.25 27 'A HEADER- C33 C34 0.23 5.21 1,957.71 ) l 28 'A HEADER C34 C35 4.78 11.52 1,957.71 ! 29 A HEADER C33 C36' 4.94 10.84 1,840.55 ! 30 A HEADER C35 C37 0.15 5.21 1,957.71 31 A HEADER , C37 C38 0.02 2.15 807.83 l 32 A HEADER C38 C39 0.08 4.41 1,658.60 ! 33 PIPE-33 C39 'C40 0.02 7.05 2,648.37 34 A HEADER C40 C41 0.10 4.58 1,722.08 35 A HEADER. C41 C42 0.03 2.61 981.59 l 36 .A HEADER C42 C43 0.01 1.18 444.19 l 37 B HEADER C32 C44 4.79 10.12 3,805.84 38 B HEADER C44 C45 0.11 5.01 1,883.00 l L 39- B HEADER C45 C48 5.26 11.09 1,883.00' l l- 40 B HEADER C44' C46 6.37 11.32 1,922.d4 i 41 B HEADER C46 C47 0.02 5.12 1,922.84 42 -B HEADER C47 C54 0.11 5.12 1,922.84 43 B HEADER- C48 C54 1.14 5.01 1,883.00 L , TNET-FIA of the FIA-SERIES page 14 i. i. i .. - . . .
FC 05977 O.MECHCALC421 Rev. 00 COMPLETE PIPELINE REPORT JUNE 8, 1992 Pag > C $, PIPELINE COUNT: 100 DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO HEAD;LDSS VELOCITY FLOW-RATE
.NO ID NODE NODE (GAIN) (ft/sec) (gal / min )
44 B HEADER C54 C49 0.08 10.12 3,805.84 45 B HEADER C49 C50 0.23 6.94 2,607.81 46 B HEADER C50 C51 0.10 4.61 1,732.14 47 B HEADER C51 C52 0.04 2.81 1,056.34 48 B HEADER CS2 C53 0.01 1.45 545.79 49 RING A C37 R1 1.05 6.77 1,149.88 50 RING B C40 R2 0.78 5.45 . 926.30 51 RING C C41 R3 1.78 7.48 740.49 52 RING D C42 R4 1.06 5.43 537.E0 53 RING E C43 R5 4.42 10.00 444.19 54 RING E2 R5 R6 0.03 2.43 108.05 55 RING E3 R6 R7 0.32 4.15 108.05 56 RING F R5 R8 1.65 7.56 336.13 57 RING G C49 R9 1.06 7.05 1,198.03 58 RING H C50 R10 0.56 5.16 875.66 59 RING I C51 R11 1.39 6.83 675.80 60 RING J C52 R12 0.91 5.16 510.55 61 RING K C53 R13 6.19 12.28 545.79 62 RING K2 R13 R14 0.12 4.67 207.66 63 RING K3 R14 R15 1.15 7.98 207.66 64 RING L R13 R16 1.67 7.61 338.13 65 SPRAY HDR A C36 C38 0.23 2.26 850.77 NET-FID of the FID-SERIES page 15
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. . - _._.FC 05977 -
O-MECH-CALC-021 Rev. 00 COMPLETE PIPELINE REPORT JUNE 8, 1992 Pagn C g PIPELINE COUNT: 100 DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/sec ) PIPELINE FROM TO HEAD-IDSS VELOCITY FIDW-RATE I NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) l 66 SPRAY HDR A C36 C39 0.31 2.63 989.77 ) 1 67 SI-3A SUCTION S1 C7 0.45 7.06 2,489.21 I 68 SUCTION SI-3C S3 C8 0.06 7.23 2,549.27 69 SUCTION SI-3B S2 C9 0.34 7.28 2,565.61 70 DISCHARGE HDR C11 C16 0.46 7.06 2,489.21 71 DISCHARGE HDR C13 C17 0.48 7.28 2,565.61 72 DISCHARGE HDR CIS C17 0.48 7.23 2,549.27 73 HEADER B C31 C32 1.94 10.79 3,805.84
- 74. PUMP SI-3A C7 C10 ( 401.17) 25.16 2,489.5!1"
--- WITH COMPONENT C - SI-3A 75 PUMP SI-3B C9 C12 ( 392.82) 25.93 2,565.61 i
--- WITH COMPONENT D - SI-3B l 76 PUMP SI-3C C8 C14 ( 394.06) 25.76 2,549.27
--- WITH COMPONENT E - SI-3C 77 HX-A C19 C21 22.31 10.77 3,798.25
--- WITH COMPONENT A - HX-A 78 HX-B C20 C23 22.40 10.79 3,805.84
--- WITH COMPONENT A - HX-A 79- RING A R1 FG 138.32 11.62 1,149.88
--- WITH CHECK VALVE 80 RING B R2 FG 135.07 9.36 926.30
--- WITH CHECK VALVE f 81 RING C R3 FG 131.37 7.48 740.49
--- WITH CHECK VALVE 82 RING D R4 FG 130.15 5.43- 537.40
--- WITH CHECK VALVE 83 RING E R7 FC 124.13 4.15 108.05
--- WITH CHECK VALVE NET-FID of the FLO-SERIES page 16
.. . - . . . .. . .-... .~.. - - ~ . - . . _ . - - . . . . . - ~ .. .... .~ 0-MECH-CALC 41 Rev. 00 COMPLETE PIPELINE REPORT JUNE 8, 1992 Pase C g E PIPELINE COUNT: 100 DESIGN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec PIPELINE FROM TO HEAD-IDSS VEIDCITY FIDW-RATE i
'NO ID NODE ~ NODE . (GAIN) (ft/sec) (gal / min ) I 84 RING F R8 FG 123.53 7.56 336.13 i
--- WITH CHECK VALVE 1 85 RING G R9 FG 134.01 12.11 1,198.03 86 RING H R10 FG 130.28 8.85 875.66- ;
1 87 RING I R11 FC 126.34 6.83 -675.80 88 RING J R12 FG 124.48 5.16 510.55 . 89 RING K R15 FC 115.03 -7.98 207.66 I 1 90 RING L R16 FG 115.62 7.61 338.13 93 PIPE-93 C11 C10 *** CLOSED *** . . 107, CS SUMP PIPE N3 C6 0.02 1.88 2,489.21 108- CS SUMP PIPE N9 C3 0.20 5.64 5,114.88 109 COMMON SUMP LIN H70 H3 0.22 1.88 2,489.21 110 COMMON SUMP LIN- ' M70 N42 0.86 3.86 5,114.88 111 COMMON SUMP LIN H3 N3 0.05 1.88 2,489.21 112 COMMON SUMP LIN N42 -N9 0.17 3.86 5,114.88 118 SI-3C DISCHARGE C14 C61 0.09 16.34 2,549.27 119 SI-35 DISCHARGE C12 C60 0.09 16.45 2,565.61 120 SI-3A DISCHARGE C10 C62 0.09 15.96 2,489.21 121 SUMP ENTRANCE FG ' H70 0.26 5.74 7,604.(9
, NET-FID of the ' FID-SERIES page 17 4
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FC 05977. O-MECH-CALC-021 Rev. 00 ABB Combustion Enginsering - CLIENT : Omaha Public Power District - NETWORK
SUMMARY
REPORTS JUNE 8, 1992 R. Harsell
' NETWORK NAME : OPPDCS1 DATA FOR PIPES: OPPDCS UPDATED : JUNE 8, 1992 OPPD CSP NPSH W/ SUMP SUBC00 LING 0-MECH-CAI4-021 2P2H: 3B & 3C SUCTION FROM THE SUMP (6 ft) 0.00 t DEVIATION after 9 ITERATIOli FIXED GRADE
SUMMARY
NETWORK CONNECTION FLOW-RATE FIXED GRADE / NODE , PIPELINE (gal / min ) PRESSURE SOURCE R1 >>> 79 RING A >>> 951.05 >>> 14.70 PSI R2 >>> 80 RING B >>> 761.70 >>> 14.70 PSI R3 >>> 81 RING C >>>. 606.04 >>> 14.70 PSI R4 >>> 82 RING D >>> 438.26 >>> 14.70 PSI R7 >>> 83 RING E >>> 87.71 >>> 14.70 PSI i R8 >>> 84 RING F >>> 273.24 >>> 14.70 PSI !
>>> >>> l R9 85 RING G 994.00 >>> 14.70 PSI j R10 >>> 86 RING H >>> 721.50 >>> 14.70 PSI R11 >>> 87 RING I >>> 553,71 ->>> 14.70 PSI R12 >>> 88 RING J >>> 416.44 >>> 14.70 PSI i
R15 >>> 89 RING K >>> 168.32 >>> 14.70 PSI l R16 >>> 90 RING L >>> 274.69 >>> 14.70 PSI H70 <<< 121 SUMP ENTRANCE <<< 6,246.65 <<< 17.30 PSI NET FLOWS OUT: 0.01 gal / min NET-FID .of the FID-SERIES page 1 1-i l
1 FQ-GM.ev,J7 O-MECH 4 9 P:g> C 13 DEMAND
SUMMARY
JUNCTION DEMAND JUNCTION DEMAND , NODE (gal / min ) NODE (gal / min ) NET DEMAND IN: 0.00 gal / min J f l l l i
. j i
i l ! l [ 1 i
. l 1
l l 1 l l NET-FLO of the FID-SERIES page 2 9 e
_ _ . . _ _ _ . . . . . _ . . . . ~ . . . ~ . _ . . . _ . _ _ . . _ _ . . - _ _ _ . . - . . _ . _ _ . . _ _ _ _ O-MECH CQ)Gev 0077 Pass C 4 COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 - DESIGN RULES: VELDCITY MIN: 0.00 HAK: 1000.00 ft/sec PIPELINE FROM TO HEAD-IDSS VEIDCITY FIDW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) 1 SIRWT EKIT C1 C2 0.00 0.00 0.00 l 2 SIRWT HEADER C3
- C2 0.05 3.43 3,115.12 3 .SIRWT EKIT C4 C5 0.00 0.00 0.00 4 SIRWT HEADER C5 C6 0.00 0.00 0.00 5 SI-3A SUCTION C6 S1 0.00 0.00- 0.00 6 SI-3C SUCTION C2 S3 2.16 8.29 3,115.12 7 SI-3B SUCTION C3 S2 1.73 8.33 3,131.52 8 SI-3A DISCHARGE C62 C11 0.00 0.00 0.00 ,
9 SI-38 DISCHARCE C60 C13 21.19 20.08 3,131.52 10' SI-3C DISCHARGE C61 C15 23.04 19.97 3,115.12 11 DSCHRG HDR C17 C16 1.40 17.72 6,246.65
.13' DSCHRG HDR C16 C18 20,62 17.72 6,246.65 14 A HK INLET C18 C19 3.31 8.84 3,117.99 15 B HK INLET C18 C20 6.38 8.87 3',128.66 16 A HK OUTLET C21 C22 1.46 8.84 3,117.99 17 5 HK OUTLET C23 C24 1.21 8.87 3,128.66 l
j 18 -HK CROSS CONECT C22 C25 0.00 0.00 0.00 j 19 HK CROSS CONECT C24 C26 0.00 0.00 0.00 20 SDC DISCHARGE C25 C26 *** CIASED *** - 21 A HEADER C22 C27 12.43 8.84~ 3,117.99
--- WITH COMPONENT F - flow mater 22 B HEADER C24 C28 12.82 8.87 3,128.66
--- WITH COMPONENT F - flow meter
. . NET-FID of the FID-SERIES page 3 3 i . - . . .
... . . . . . .. -.- .. = . . _ _ - . _ .
O-MECH 1 , COMPLETE PIPELINE REPORT JUNE 8,1992 l PIPELINE COUNT: 100 - l_ DESICN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec l PIPELINE FROM TO HEAD-IDSS . VEIDCITY FIDW-RATE l NO ID NODE NODE (CAIN) (ft/sec) (gal / min ) l 23 A HEADER C27 C29 17.18 19.99 3,117.99
--- WITH COMPONENT B - FIDW VALVE l 24 B HEADER C28 C31 18.53 20.06 3,128.66 l
--- WITH COMPONENT B - FIDW VALVE 25 A HEADER C29 C30 2.47 8.84 3,117.99 i
26 A HEADER C30 C33 3.18 8.29 3,117.99 27 A HEADER C33 C34 0.16 4.28 1,607.11 28 A HEADER C34 C35 3.24 9.46 1,607.11 29 A HEADER C33 C36 3.35 8.89 1,510.88 30 A HEADER C35 C37 0.10 4.28 1,607.11 l l 31 A HEADER C37 C38 0.01 1.75 656.05 32 A HEADER C38 C39 0.05 3.60 1,354.93 33 PIPE-33 C39 C40 0.01 5.76 2,166.94 34 A HEADER C40 C41 0.07 3.74 1,405.24 35 A HEALER C41 C42 0.02 '2.13 799.20 36 A HEADER C42 C43 0.00 0.96 360.94 37 B HEADER C32 C44 3.24 8.32 3,128.66 38 B HEADER C44 C45 0.07 4.12 1,547.90 l 39 B HEADER C45 C48 3 57 9.11 1,547.90 j \ l 40 B HEADER C44 C46 4.32 9.31 1,580.76 l 41 B HEADER C46 C47 0.02 4.21 1,580.76 i 42- B HEADER C47 C54 0.07 4.21 1,580.76 l 43 B HEADER C48 C54 0.77 4.12 1,547.90 NET-FID of the FLO-SERIES page 4 2 6 l
FC 05977 O-MECH CALC-021 Rev. 00 i Page C 13 COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 DESIGN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec PIPELINE FROM TO HEAD-IASS VEIDCITY F1hW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) 44 B HEADER C54 C49 0.06 8.32 3,128.66 45 B HEADER C49 C50 0.16 5.68 2,134.66 46 B HEADER C50 C51 0.07 3.76 1,413.16 47 B HEADER C51 C52 0.03 2.29 859.45 48 B HEADER CS2 C53 0.01 1.18 443.01 49 RING A C37 R1 0.72 5.60 951.05 50 RING B C40 R2 0.53 4.48 761.70 51 RING C C41 R3 1.20 6.12 606.04 52 RING D C42 R4 0.71 4.43 438.26 53 RING E C43 RS 2.95 8.12 360.94 54 RING E2 R5 R6 0.02 1.97 87.71 55 RING E3 R6 R7 0.21 3.37 87.71 56 PlNG F R5 R8 1.10 6.15 273.24 57 RING G C49 R9 0.73 5.85 994.00 58 RING H C50 R10 0.38 4.25 721.50 59 RING I CSI R11 0.94 5.60 553.71 60 RING J CS2 R12 0.61 4.21 416.44 61 RING K C53 R13 4.11 9.97 443.01 62 RING K2 'R13 R14 0.03 3.79 168.32 63 RING K3 R14 R15 0.77 6.47 168.32 64 RING L R13 R16 1.10 6.18 274.69 65 SPRAY HDR A C36 C38 0.16 1.86 698.88 NET-FID of the FID-SERIES page 5
PU UbV / I' O-MECH-CALC-021 Rev. 00 Pagi C pt COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 , DESIGN RULES: VEMCITY MIN: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO HEAD-MSS VELOCITY FMW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) 66 SPRAY HDR A C36 C39 0.21 2.16 812.00 67 SI-3A SUCTION S1 C7 0.00 0.00 0.00 68 SUCTION SI-3C S3 C8 0.09 8.83 3,115.12 69 SUCTION SI-3B S2 C9 0.50 8.88 3,131.52 70 DISCHARGE HDR C11 C16 0.00 0.00 0.00 ; 1 71 DISCHARGE HDR C13 C17 0.72 8.88 3,131.52 72 DISCHARGE HDR C15 C17 0.71 8.83 3,115.12 73 HEADER B 031 C32 1.32 8.87 3,128.66 74 PUMP SI-3A C7 C10 *** CLOSED *** l
--- WITH COMPONENT C - -
l 75 PUNP SI-3B C9 C12 ( 319.68) 31.65 3,131.52
--- WITH COMPONENT D - SI-3B ,
1 76 PUMP SI-3C C8 C14 ( 321.59) 31.48 3,115.12 !
--- WITH COMPONNTT E - SI-3C l 77 HX-A C19 C21 15.04 8.84 3,117.99
--- WITH COMPONENT A - HX-A 78 HX-B C20 C23 15.14 8.87 3,128.66
-- ~WITH COMPONENT A - HX-A 79 RING A R1 FG 94.62 9.61 951.05
--- WITH CHECK VALVE ,
80 RING B R2 FG 91.33 7.70 761.70
--- WITH CHECK VALVE 81 RING C R3 FG 87.99 6.12 606.04
--- WITH CHECK VALVE 82 RING D R4 FG 86.56 4.43 438.26
--- WITH CHECK VALVE 83 RING E R7 FG 81.79 3.37 87.71
--- WITH CHECK VALVE NET-FM of the FM-SERIES page 6
.. .. ~ . . - . - - .. . - . _ _ . - _ . - . ..- . . . . - . . . . -- - - - . . -
O-MECH fALC421 Rev. 0 j Page C 15 COMPLETE PIPELINE REPORT JUNE 8,.1992 PIPELINE COUNT: 100 ' i DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/sec l PIPELINE FROM TO HEAD-IDSS VEIDCITY FLOW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) J j 84 RING F R8 FG 81.62- 6.15 273.24 1
--- WITH CHECK VALVE 2
- 85 RING G R9 FG 92.25 10.05 994.00 86 RING H R10 FG 88.44 7.29 721.50 87 RING I R11 FG 84,81 5.60 553.71 1 88 RING J R12 FG 82.82 4.21 416.44
- -89 RING K R15 FG 75.57 6.47 168.32
- 1. 90 RING L R16 FG 76.31 6.18 274.69 l 93 PIPE-93 C11 C10 *** CIDSED ***
107 CS SUMP PIPE , N3 C6 0.00 - 0.00 0.00' 108 CS SUMP PIPE N9 C3 0.30 6.88 6,246.65 109 COMMON SUMP LIN H70 H3 0.00 0.00 0.00 110 COMMON SUMP LIN H70 N42 1.28 4.72 6,246.65 111 COMMON SUMP LIN H3 N3 0.00 0.00 0.00 112 COMMON SUMP LIN N42 N9 0.24 4.72 6,246.65 118 SI-3C DISCHARGE C14 C61 0.14 19.97 3,115.12 119 SI-3B DISCHARGE C12 C60 0.14 20.08 3,131.52 120 SI-3A DISCHARGE C10 C62 0.00- 0.00 0.00 121 SUMP ENTRANCE FC H70 0.17 4.72 6,246.65 l
- NET-FID of the FIA-SERIES page 7
. ._. . - . - ~ . .~ . - . . - . ~ . . ~ . . . - - ..--. .-..- . -.-..- .
FC 05977 O-MECH CALC-021 Rev. 00 Page C % ABB Corbustien Enginsering l CLIENT : Omaha Public Power District - i l NETWORK
SUMMARY
REPORTS JUNE 8, 1992 l R. Harsell l NETWORK NAME : OPPDCS1 DATA FOR PIPES: OPPDCS UPDATED : JUNE 8, 1992 OPPD CSP NPSH W/ SUMP SUBC00 LING O-MECH-CALC-021 3P1H:3A,3B,3C HDR B SUCTION FROM THE SUMP (6 ft)
- 0.01 % DEVIATION after 14 ITERATIONS FIXED GRADE
SUMMARY
! NETWORK CONNECTION FLOW-RATE. FIXED GRADE / u NODE PIPELINE (gal / min ) PRESSURE SOURCE l . R1 n> 79 RING A h> 0.00 n> 5,000.00 PSI R2 >n 80 RING B >n 0.00 n> 5,000.00 PSI ! R3 >W 81 RING C >n 0.00 >n 5,000.00 PSI R4 >n 82 . RING D n> 0.00 n> 5,000.00 PSI i l R7 >n 83 RING E >n 0.00 n> 5,000.00 PSI R8 >W 84 RING F n> 0.00 n> 5,000.00 PSI R9 >>> 85 RING G n> 1,447.60 >n 14.70 PSI R10 n> 86 RING H n> 1,063.15 n> 14.70 PSI l R11 n> 87 RING I n> 823.60 n> 14.70 PSI R12 >n 88 RING J >W 624.07 >> 14.70 PSI i R15 n> 89 RING K >n 254.88 n> 14.70 PSI
- R16 >>> 90 RING L n> 414.41 >n 14.70 PSI H70 <<< 121 SUMP ENTRANCE <<< 4,627.72 <<< 17.30 PSI NET FIDWS IN
- 0.01 gal / min I
NET-FLO of the FLO-SERIES page 1 4 l
tb U5977 O-MECHCALC-021 Rev. 00 Page C p I DEMAND
SUMMARY
JUNCTION DEMAND JUNCTION DEMAND NODE (gal / min ) NODE (gal / min ) I NET DEMAND IN: 0.00 gal / min l 6l NET-FID of the FID-SERIES page 2
FC 05977 O-MECH 4ALC-021 Ray. 00 Pcg3 C 'L1 COMPLETE PlPELINE REPORT JUNE 8, 1992
-PIPELINE COUNT: 100 -
DESIGN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec PIPELINE FROM TO HEAD-IDSS VELOCITY FIDW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) 1- SIRWT EXIT C1 C2 0.00 0.00 0.00 2 SIRWT HEADER C3
- C2 0.01 1.69 1,530.20 3 SIRWT EXIT C4 C5 0.00 0.00 0.00 4 SIRWT HEADER CS C6 0.00 0.00 0.00 5 SI-3A SUCTION C6 S1 0.23 4.08 1,534.64 6 SI-3C SUCTION C2 S3 0.53 4.07 1,530.20 7 SI-35 SUCTION C3 S2 0.43 4.16 1,562.89 8 SI-3A DISCHARGE C62 C11 9.58 9.84 1,534.64 9~ SI-35 DISCHARGE C60 C13 5.30 10.02 1,562.89 10 SI-3C DISCHARGE C61 CIS 5.58 9.81 1,530.20
- . 11 DSCHRG HDR C17 C16 0.35 8.77 3,093.08 l 13' DSCHRG HDR C16 C18 11.40 13.12 4,627.72 14 A HK INLET C18 C19 0.00 0.00 0.00 l 15 B HK INLET C18 C20 13.94 13.12 4,627.72 l- 16 A HK OUTLET C21 C22 0.00 0.00 0.00 17 B HK OUTLET C23 C24 . 2.64 13.12 4,627.72 ;
18 HK CROSS CONECT C22 C25 0.00 0.00 0.00 l 19 HK CROSS CONECT C24 C26 0.00 0.00 0.00 l 20 SDC DISCHARGE C25 C26 *** CIDSED *** 21 A HEADER C22 C27 0.00 0.00 0.00
--- WITH COMPONENT F - flow meter *** MODEL OUT OF RANGE ***
22 B HEADER- C24 C28 27.99 13.12 4,627.72 1 --- WITH COMPONENT F - flow meter *** MODEL OUT OF RANGE *** l' NET-FID. of the FID-SERIES page 3 i )
FC 05977 0-MECH-CALC-021 Rev. 00 Paga C 1A ! COMPLETE ' PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 l DESIGN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec j PIPELINE FROM TO HEAD-IDSS VEIDCITY FIDW-RATE l NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) l 23 A HEADER C27 C29 0.00 0.00 0.00
--- WITH COMPONENT B - FIDW VALVE *** MODEL OUT OF RANGE ***
24 B HEADER C28 C31 40.53 29.67 4,627.72
--- WITH COMPONENT B - FIDW VALVE *** MODEL OUT OF RANCE ***
25 A HEADER C29 C30 0.00 0.00 0.00 26 A HEADER C30 C33 0.00 0.00 0.00 27 A HEADER C33 C34 0.00 0.00 0.89 28 A HEADER C34 C35 0.00 0.01 0.89 29 A HEADER C36
- C33 0.00 0.01 0.89 30 A HEADER C35 C37 0.00 0.00 0.89 j 31 A HEADER C37 C38 0.00 0.00 0.89 32 A HEADER C38 C39 0.00 0.00 0.44 33 PIPE-33 C39 C40 0.00 0.00 0.00 34 A HEADER C40 C41 0.00 0.00 0.00 35 A HEADER C41 C42 0.00 0.00 0.00 36 A HEa C42 C43 0.00 0.00 0.00 37 B HEADER C32 C44 7.06 12.31 4,627.72 38 B HEADER C44 C45 0.16 6.09 2,289.70 39 B HEADER C45 C48 7.74 13.48 2,289.70 40 B HEADER C44 C46 9.38 13.76 2,338.02 41 B HEADER C46 C47 0.03 6.22 2,338.02 42 B HEADER C47 C54 0.16 6.22 2,338.02 l 43 B HEADER C48 C54 1.68 6.09 2,289.70 t
NET-FLO of the FLO-SERIES page 4 1
O-MECH-CALC-021 Rev,00 Page C h COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 l DESIGN RULES: VEIhCITY - kW.: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO HEAD-IASS VEIACITY FIhW-RATE NO .. ID NODE NODE (CAIN) (ft/sec) -(gal / min ) 44 B HEADER C54 C49 0.12 12.31 4,627.72
'45 5 HEADER C49 C50 0.35 8.46 3,180.12 46 B HEADER C50 C51 0.16 5.63 2,116.96 47 5 HEADER C51 C52 0.06 3.44 1,293.36 48 B HEADER CS2 C53 0.02 1.78 669.29 49 RING A C37 R1 0.00 0.00 0.00 50- RING B C40 R2 0.00 0.00 0.00
- 51 RING C C41 R3 0.00 0.00 0.00 52- RING D C42 R4 0.00 ,
0.00 0.00 53 RING E C43 R5 0.00 0.00 0.00
~54 RING E2 R5 R6 0.00 0.00 0.00
.55 RING E3 R6 ,R7 0.00 0.00- 0.00 56 RING F R5 R8 0.00 0.00 0.00 57 RING G C49 R9 1.55 8.52 1,447.50 58 RING H C50 R10 0.82 6.26 1,063.15 59 RING I C51 R11 2.06 8.32 823.60 60 RING J C52 R12 1.35 6.31 624.07 61 RING K C53 R13 9.25 15.06 669.29 62 RING K2 R13 R14 0.17 5.74 254.88 63 RING K3 R14 R15 1.72 9.79 254.88 64' RING L R13 R16 2.50 9.33 414.41 65 SPRAY HDR A C38
- C36 0.00 0.00 0.45 i
l
' NET-FIA of the FID-SERIES page 5 l
__. - _...-m_ .._ _ _ __.. _ .. _. . . _ . _ . . _ . . . ~ . . , . . . - . . _ . . _ . _ . _ _ . , O-MECH. [pC-02Qpev. 00977 P:gs C M j COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 . DESIGN RULES: . VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec PIPELINE FROM TO HEAD-LOSS VEIDCITY FLOW-RATE
- NO ID NODE NODE (CAIN) (ft/sec) (gal / min )
i ~ 66 SPRAY HDR A C39
- C36 0.00 0.00 0.44
+ 67 'SI-3A SUCTION S1 C7 0.17 4.35 1,534.64 68 SUCTION SI-3C S3 C8 0.02 4.34 1,530.20 69 SUCTION SI-3B S2 C9 0.13 4.43 1,562.89 l_ 70 DISCHARGE HDR C11 C16 0.17 4.35 1,534.64 i 71 DISCHARGE HDR C13 C17 0.18 4.43 1,562.89 72 DISCHARGE HDR C15 C17 0.17 4.34 1,530.20
.73 HEADER B C31 C32 2.85 13.12 4,627.72
. 74 PUMP SI-3A C7 C10 ( 472.10) 15.51 1,534.64
--- WITH COMPONENT C'- SI-3A 75 PUMP SI-3B C9 C12 ( 468.68) 15.79 1,562.89
--- WITH COMPONENT D - SI-3B
.76 PUMP'SI-3C C8 C14 ( 468.96) 15.46 1,530.20
--- WITH COMPONENT E - SI-3C
. 77 HX-A C19 C21' O.00- . 0.00 0.00
--- WITH COMPONENT A - HX-A *** MODEL OUT OF RANCE ***
78 HX-B- C20 C23 33.13 13.12 4,627.72
--- WITH COMPONENT A - HK-A *** MODEL OUT OF RANGE ***
79 RING A R1 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIDSED BY REVERSE FIAW ***
80 -RING B R2: FG 0.00 0.00 0.00
--- WITH CHECK-VALVE *** CIDSED BY REVERSE FIDW ***
81 RING C R3 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIDSED BY REVERSE FIhW ***
82 RING D . R4 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIDSED BY REVERSE FLOW ***
83 ' RING E R7 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CLOSED BY REVERSE FIAW ***
NET-FID of the FLO-SERIES page 6 9
0-MECH ev Page C 3% COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 DESIGN RULES: VEIACITY MIN: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO HEAD-IASS VELOCITY FIDW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) 84 RING F R8 FG 0.00 0.00 0.00
- - WITH CHECK VALVE *** CIASED BY REVERSE FIDW ***
85 RING G R9 FG 195.65 14.63 1,447,60 86 RING H R10 FG 192.04 10.74 1,063.15 87 RING I R11 FG 187.64 8.32 823.60 88 RING J R12 FG 185.99 6.31 624.07 89 RING K R15 FG 173.29 9.79 254.88 90 RING L R16 FG '173.67 9.33 414.41 93 PIPE-93 C11 C10 *** CIASED *** 107 CS SUMP PIPE - N3 C6 0.01 1.16 1,534.64 108 CS SUMP PIPE N9 C3 0.07 3.41 3,093.08 109 COMMON SUMP LIN H70 H3 0.09 1.16 1,534.64 110 COMMON SUMP LIN H70 N42 0.32 2.34 3,093.08 111 COMMON SUMP LIN H3 N3 0.02 1.16 1,534.64 112 COMMON SUMP LIN N42 N9 0.06 2.34 3,093.08 118 SI-3C DISCHARGE C14 C61 0.03 9.81 1,530.20 l l 119 SI-3B DISCHARGE C12 C60 0.04 10.02 1,562.89 l 120 SI-3A DISCHARGE C10 C62 0.03 9.84 1,534.64 121 SUMP ENTRANCE FG H70 0.10 3.50 4,627.72 i I
)
NET-FLO of the FID-SERIES page 7 i l l l l l
1 0-MECH CALC-021 Rev. 00 P:ge C 33 ABB Combustion Engineering CLIENT : Omaha Public Power District NETWORK
SUMMARY
REPORTS JUNE 8, 1992 R. Harsell NETWORK NAME : OPPDCS1 DATA FOR PIPES: OPPDCS UPDATED : JUNE 8, 1992 OPPD CSP NPSH W/ SUMP SUBC00 LING O-MECH-CALC-021 2P1H:3A & 3B HDR B SUCTION FROM THE SUMP (6 ft) 0.01 % DEVIATION after 14 ITERATIONS FIXED GRADE
SUMMARY
NETWORK CONNECTION FLOW-RATE FIXED GRADE / NODE PIPELINE (gal / min ) PRESSURE SOURCE R1 >>> 79 RING A n> 0.00 >n 5,000.00 PSI R2 >>> 80 RING B >>> 0.00 >n 5,000.00 PSI R3 >> 81 RING C n> 0.00 n> 5,000.00 PSI R4 >n 82 RING D >n 0.00 n> 5,000.00 PSI R7 n> 83 RING E >n 0.00 n> 5,000.00 PSI R8 >n 84 RING F >n 0.00 n> 5,000.00 PSI R9 >>> 85 RING G >n 1,349.79 >>> 14.70 PSI R10 n> 86 RING H n> 989.77 >>> 14.70 PSI R11 >>> 87 RING I n> 765.82 n> 14.70 PSI R12 >n 88 RING J n> 579.73 >n 14.70 PSI R15 >>> 89 RING K >n 236.46 n> 14.70 PSI R16 n> 90 RING L n> 384.63 >n 14.70 PSI H70 <<< 121 SUMP ENTRANCE <<< 4,306.21 <<< 17.30 PSI NET FLOWS IN: 0.01 gal / min NET-FIA of the FID-SERIES page 1
! FU 05977 O-MECH 4ALC-021 Rev. 00 Page C 3q DEMAND
SUMMARY
JUNCTION DEMAND JUNCTION DEMAND NOPF. (gal / min ) NODE (gal / min ) NET DEMAND IN: 0.00 gal / min l l l l I l l l l l NET-FID of the FID-SERIES page 2
- . . . _ _ _ _ _ _ _ . ......__.___.___..m__....~ . . . . . _ . . , . . - _m.__ ..m._ ..
_ _ . , _ . _ __._ FC 05977_. . . O-MECH-CALC 421 Rev. 00 Pegs C 3 f COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE' COUNT: 100 '
. DESIGN RULES: VELOCITY MIN: 0.00 HAX: 1000.00 ft/see i PIPELINE Ml0N TO HEAD-IDSS VEIDCITY FIDW-RATE NO ID NODE NODE (CAIN) (ft/sec) (gal / min )
1 SIRWT EXIT C1 C2 0.00 0.00 0.00 2 SIRWT HEADER C2 C3 0.00 0.00 0.00 3 SIRWT EXIT C4 C5 0.00 0.00 0.00 4 SIRWT HEADER CS C6 0.00 0.00 0.00 5 SI-3A SUCTION C6 S1 0.43 5.63 2,114.64 6 SI-3C SUCTION C2 S3 0.00 0.00 0.00 7 SI-3B SUCTION C3 S2 0.85 5.83 2,191.57 8 SI-3A DISCHARGE C62 C11 18.07 _13.56 2,114.64 9 SI-3B DISCHARGE C60 C13 10.40 14.05 2,191.57 10 SI-3C DISCHARGE C61 CIS -0.00 0.00 .0.00 l 11 DSCHRG HDR C17 C16 0.17 6.22 2,191.57 ' 13 .DSCHRG HDR C16 C18 9.89 12.21 4,306.21 14 A HK INLET C18 C19 0.00 0.00 0.00 15 .B HK INLET C18 C20 12.08 '12.21 4,306.21 I 16 A HX OUTLET C21 C22 0.00 0.00 0.00 17 B HK OUTLET C23 C24 2.29 12.21 4,306.21 18 HX CROSS CONECT C22 C25 0.00 0.00 0.00
- 19. HX CROSS CONECT C24 C26 0.00 'O.00 0.00 20 SDC DISCHARGE C25 C26 *** CIDSED ***
21 A HEADER C22 C27 0.00 0.00 0.00
--- WITH COMPONENT F - flow meter *** HODEL OUT OP RANGE ***
22' B' HEADER C24 C28 24.24 12.21 4,306.21
--- WITH COMPONENT F - flow meter NET-FID of the FID-SERIES '
page 3 i r
fU 059'i7 O MECH CALC 421 Rev. 00 P ge C K COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO HEAD-IASS VEIDCITY FLOW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) 23 A HEADER C27 C29 0.00 0.00 0.00
--- WITH COMPONENT B - FLOW VALVE *** HODEL OUT OF RANCE ***
24 B HEADER C28 C31 35.10 27.61 4,306.21
--- WITH COMPONENT B - FIDW VALVE *** MODEL OUT OF RANGE ***
25 A HEADER C29 C30 0.00 0.00 0.00 l 26 A HEADER C30 C33 0.00 0.00 0.00 27 A HEADER C33 C34 0.00 0.00 0.90 l 28 A HEADER C34 C35 0.00 0.01 0.90 29 A HEADER C36
- C33 0.00 0.01 0.90 30 A HEADER C35 C37 0.00 0.00 0.90 31 A HEADER C37 C38 0.00 0.00 0.90 32 A HEADER C38 C39 0.00 0.00 0.45 33 PIPE-33 C39 C40 0.00 0.00 0.00 34 A HEADER C40 C41 0.00 0.00 0.00 35 A HEADER C41 C42 0.00 0.00 0.00 36 A HEADER C42 C43 0.00 0.00 0.00 37 B HEADER C32 C44 6.12 11.46 4,306.21 38 B HEADER C44 C45 0.14 5.67 2,130.60 39 B HEADER C45 C48 6.71 12.54 2,130.60 1
40 B HEADER C44 C46 8.13 12.81 2,175.61 41 B HEADER C46 C47 0.03 5.79 2,175.61 42 B HEADER C47 C54 0.14 5.79 2,175.61 43 B HEADER C48 C54 1.46 5.67 2,130.60 NET-FLO of the FID-SERIES page 4
FO 05977 O-MECH-CALC-021 Rev. 00 i l Page C 37 ) COMPLETE PIPELINE REPORT JUNE 8, 1992 i PIPELINE COUNT: 100 ' DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO HEAD-IDSS VEIDCITY FLOW-RATE NO ID NODE NODE (CAIN) (ft/sec) (gal / min ) l 44 B HEADER C54 C49 0.10 11.46 4,306.21 45 B HEADER C49 C50 0.30 7.87 2,956.42 46 B HEADER C50 C51 0.13 5.23 1,966.64 47 B HEADER C51 CS2 0.05 3.19 1,200.83 1 48 B HEADER C52 C53 0.01 1.65 621.09 49 RING A C37 R1 0.00 0.00 0.00 50 RING B C40 R2 0.00 0.00 0.00 51 RING C C41 R3 0.00 0.00 0.00 ) 52 RING D C42 R4 0.00 0.00 0.00 l l 53 RING E C43 R5 0.00 0.00 0.00 l 1 54 RING E2 R5 R6 0.00 0.00 0.00 55 RING E3 R6 R7 0.00 0.00 0.00 56 RING F R5 R8 0.00 0.00 0.00 57 RING G C49 R9 1.35 7.95 1,349.79 58 RING H C50 R10 0.71 5.83 989.77 59 RING I C51 R11 1,79 7.74 765.82 60 RING J CS2 R12 1.17 5.86 579.73 61 RING K C53 R13 7.98 13.98 621.09 62 RING K2 R13 R14 0.15 5.32 236.46' 63 RING K3 R14 R15 1.48 9.09 236.46 64 RING L R13 R16 2.16 8.66 384.63 65 SPRAY HDR A C38
- C36 0.00 0.00 0.45 NET-FID of the FLO-SERIES page 5
_. . _ _ m. _ _ _ _ _ _ . . _ _ _ . . _ _ , _ . . . _ _ O-MECHCALC-021 Rev. 00 Page C 3{ COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100
- DESIGN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO~ HEAD-IDSS VEIDCITY FIDW-RATE NO ID . NODE NODE (GAIN) (ft/sec) (gal / min )
66 SPRAY HDR A C39
- C36 0.00 0.00 0.45 6'7 SI-3A SUCTION S1 C7 0.33 6.00 2,114.64 68 SUCTION SI-3C S3 C8 0.00 0.00 0.00 69 SUCTION SI-3B S2 C9 0.25 6.22 2,191.57 70 DISCHARGE,HDR C11 C16 0.33 6.00 2,114.64 71 DISCHARGE HDR C13 C17 0.35 6.22 2,191.57 ;
1 72 DISCHARGE HDR C15. C17 0.00 0.00 0.00 ! 73 HEADER B C31 C32 2.47 12.21 4,306.21 < l 74 PUMP SI-3A C7 C10 ( 435.51) 21.37 2,114.64
--- WITH COMPONENT C - SI-3A 75 PUMP SI-3B C9 C12 ( 428.41) 22.15 2,191.57 !
--- WITH COMPONENT D - SI-3B l
76 PUMP SI-3C C14 C8 *** CIDSED *** l --- WITH COMPONENT E - 77 HK-A C19 C21 0.00 0.00 0.00
--- WITH COMPONENT A - HK-A *** MODEL OUT OF RANGE ***
78 HK-B C20 C23 28.68 12.21 4,306.21
--- WITH COMPONENT A - HK-A *** MODEL OUT OF RANGE ***
i- 79' RING A R1 FC 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIDSED BY REVERSE FIhW .***
80 RING B R2: FG 0.00 0.00 0.00 l --- WITH CHECK VALVE *** CIASED BY REVERSE FIDW *** 81 RING C R3 FG 0.00 0.00 0.00 l --- WITH CHECK VALVE *** CLOSED BY REVERSE FIhW ***
- 82 RING D R4 FC 0.00 0.00 0.00 L --- WITH CHECK VALVE *** CIASED BY REVERSE FIDW *** l
(. ) l 83 RING E R7 FC 0.00 0.00 0.00 l
--- WITH CHECK VALVE *** CIDSED BY REVERSE FIDW ***
i ; I NET-FIA of the FID-SERIES page 6 i l \
FC 05977 0 MECil-CALC-021 Rev. 00 P;p C 39 COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 DESIGN RULES: VEMCITY MIN: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO HEAD-LOSS VEMCITY FLOW-RATE NO ID NODE NODE (CAIN) (ft/sec) (gal / min ) 84 RING F R8 FG 0.00 . 0.00 0.00
--- WITH CHECK VALVE *** CMSED BY REVERSE FLOW ***
85 RING G R9 FG 170.10 13.64 1,349.79 86 RING H R10 FG 166.44 10.00 989.77 87 RING I R11 FG 162.23 7.74 765.82 88 RING J R12 FG 160.50 5.86 579.73 89 RING K R15 FG 149.14 9.09 236.46 90 RING L R16 FG 149.62 8.66 384.63 93 PIPE-93 C11 C10 *** CMSED *** 107 CS SUMP PIPE N3 C6 0.01 1.60 2,114.64 108 CS SUMP PIPE N9 C3 0.04 2.42 2,191.57 109 COMMON SUMP LIN H70 H3 0.16 1.60 2,114.64 110 COMMON SUMP LIN H70 N42 0.16 1.66 2,191.57 111 COMMON SUMP LIN H3 N3 0.04 1.60 2,114.64 112 COMMON SUMP LIN N42 N9 0.03 1.66 2,191.57 118 SI-3C DISCHARGE C14 C61 0.00 0.00 0.00 119 SI-3B DISCHARGE C12 C60 0.07 14.05 2,191.57 120 SI-3A DISCHARGE C10 C62 0.06 13.56 2,114.64 121 SUMP ENTRANCE FG H70 0.08 3.25 4,306.21 NET-FLO of the FM-SERIES page 7
O-MECHCALC41 Rev 00 Pcge C 95 ABB Combustion Engineering CLIENT : Omaha Public Power District ' NETWORK
SUMMARY
REPORTS JUNE 8, 1992 R. Harsell NETWORK NAME : OPPDCS1 DATA FOR PIPES: OPPDCS UPDATED : JUNE 8, 1992 OPPD CSP NPSH W/ SUMP SUBCOOLING O-MECH-CALC-021 2P1H:3A & 3C HDR B SUCTION FROM THE SUMP (6 ft) 0.01 4 DEVIATION after 14 ITERATIONS FIXED GRADE
SUMMARY
NETWORK CONNECTION FIDW-RATE FIXED GRADE / ) NODE PIPELINE (gal / min ) PRESSURE SOURCE R1 >>> 79 RING A >>> 0.00 >>> 5,000.00 PSI - R2 >>> 80 RING B >>> 0.00 >>> 5,000.00 PSI R3 >>> 81 RING C >>> 0.00 >>> 5,000.00 PSI R4 >>> 82 RING D >>> 0.00 >>> 5,000.00 PSI R7 >>> 83 RING E >>> 0.00 >>> 5,000.00 PSI R8 >>> 84 RING F >>> 0.00 >>> 5,000.00 PSI R9 >>> 85 RING G >>> 1,348.31 >>> 14.70 PSI R10 >>> 86 RING H >>> 988.66 >>> 14.70 PSI R11 >>> 87 RING I >>> 764.94 >>> 14.70 PSI R12 >>> 88 RING J >>> 579.06 >>> 14.70 PSI R15 >>> 89 RING K >>> 236.18 >>> 14.70 PSI R16 >>> 90 RING L >>> 384.18 >>> 14.70 PSI H70 < 121 SUMP ENTRANCE < 4,301.34 < 17.30 PSI I NET FLOWS IN: 0.01 gal / min NET-FLO of the FID-SERIES page 1
O-MECHCALC@1 Rev. 00 FC 05977 Page C q( DEMAND
SUMMARY
JUNCTION DEMAND JUNCTION DEMAND NODE (gal / min ) NODE (gal / min ) NET DEMAND IN: 0.00 gal / min I e I NET-FID 'of the FID-SERIES page 2
)
FC 05977 O-MECH-CALC 42i Rev. 00 P;ge C g COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/see , l PIPELINE FROM TO HEAD-LOSS VELOCITY FLOW-RATE i l NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) l 1 SIRWT EXIT C1 C2 0.00 0.00 0.00 2 SIRWT HEADER C3
- C2 0.03 2.40 2,179.91 3 SIRWT EKIT C4 c5 0.00 0.00 0.00 l 4 SIRUT HEADER C5 C6 0.00 0.00 0.00 l 5 SI-3A SUCTION C6 S1 0.44 5.64 2,121.43 6 SI-3C SUCTION C2 S3 1.06 5.80 2,179.91 7 SI-3B SUCTION C3 S2 0.00 0.00 0.00 8 SI-3A DISCHARGE C62 C11 if 18 13.60 2,121.43 9 SI-3B DISCHARGE C60 C13 0.00 0.00 0.00 10 SI-3C DISCHARGE C61 C15 11.30 13.98 2,179.91 !
11 DSCHRG HDR C17 C16 0.17 6.18 2,179.91 13 DSCHRG HDR C16 C18 9.87 12.20 4,301.34 14 A HX INLET C18 C19 0.00 0.00 0.00 15 B HX INLET C18 C20 12.05 12.20 4,301.34 16 A HX OUTLET C21 C22 0.00 0.00 0.00 17 8 HX OUTLET C23 C24 2.29 17.20 4,301.34 18 HX CROSS CONECT C22 C25 0.00 0.00 0.00 19 HX CROSS CONECT C24 C26 0.00 0.00 0.00 20 SDC DISCHARGE C25 C26 *** CLOSED *** 21 A HEADER C22 C27 0.00 0.00 0.00
--- WITH COMPONENT F - flow meter *** HODEL OUT OF RANGE ***
22 B HEADER C24 C28 24.19- 12.20 4,301.34
--- WITH COMPONENT F - flow meter ' NET-FLO of the FLO-SERIES page 3
l N 05977 O-MECH-CALC-021 Rev. 00 , Page C % 3 l COMPLETE PIPELINE REPORT JUNE 8, 1992 l PIPELINE COUNT: 100 - DESIGN RULES: VEIDCITY MIN: 0.00 - MAX: 1000.00 ft/sec I PIPELINE FROM TO HEAD-IDSS VEIACITY FIDW-RATE l NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) l 23 A HEADER C27 C29 0.00 0.00 0.00
--- WITH COMPONENT B - FIhW VALVE *** MODEL OUT OF RANGE ***
I l 24 3 HEADER C28 C31 35.02 27.58 4,301.34 l --- WITH COMPONENT B - FIDW VALVE *** MODEL OUT OF RANCE *** i 25 A HEADER C29 C30 0.00 0.00 0.00 26 A HEADER C30 C33 0.00 0.00 0.00 i l'
- 27 A HEADER C33 C34 0.00 0.00 0.90 28 A HEADER C34 C35 0.00 0.01 0.90 l
29 A HEADER C36
- C33 0.00 0.01 0.90 30 A HEADER C35 C37 0.00 ,
0.00 0.90 l 31 A HEADER C37 C38 0.00 0.00 0.90 ( 32 A HEADER C38 C39 0.00 0.00 0.45 , 1 33 PIPE-33 C39 C40 0.00 -0.00 0.00 l 34 .A HEADER C40 C41 0.00. 0.00 0.00
'35 A HEADER C41 C42 0.00 0.00 0.00 l 36 A HEADER C42 C43 0.00 0.00 0.00 -
L L 37 B HEADER C32 .C44 6.11 11.44 4,301.34 38 8 HEADER C44 C45 .0.13 5.66 2,128.19 39 8 HEADER C45 C48 6.70 12.53 2,128.19
. 40 - B HEADEL C44 C46 8.12 12.79 2,173.15 41 B HEADER C46 C47 0.03 5.78 2,173.15 l
42 B HEADER C47 C54 0.14 5.78 2,173.15 43 B HEADER C48 C54 1.46 5.66 2,128.19 I NET-FLO of the FID-SERIES page 4 l I t-
- O-MECH-CALC-021 Rey,00 Pap C %
COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 ' DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/see PIPELINE FROM TO HEAD-LOSS VEIDCITY FLOW-RATE NO ID NODE NODE (CAIN) (ft/sec) (gal / min ) 44 B HEADER C54 C49 0.10 11.44 4,301.34 45 B HEADER C49 C50 0.30 7.86 2,953.03 46 B HEADER C50 C51 0.13 5.23 1,964.37 47 B HEADER C51 CS2 0.05 3.19 1,199.42 48 B HEADER C52 C53 0.01 1.65 620.36 4 49 RING A C37 R1 0 00 0.00 0.00 50 RING B C40 R2 0.00 0.00 0.00 51 RING C C41 R3 0.00 0.00 0.00 52 RING D C42 R4 0.00 0.00 0.00 53 RING E C43 R5 0.00 0.00 0.00 l
.54 RING E2 R5 R6 0.00 0.00 0.00 55 RING E3 R6 R7 0.00 0.00 0.00 56 RING F R5 R8 0.00 0.00 0.00 57 RING G C49 R9 1.35 7.94 ~1,348.31 s
4 58 RING H CSP R10 0.71 5.82 988.66 59 RING I C51, R11 1.78 7.73 764.94 60 RING J C52 R12 1.17 5.85 579.06 61 RING K C53 R13 7.96 13.96 620.36 62 RING K2 R13 R14 0.15 5.31 236.18 63 RING K3 R14 R15 1.48 9.08 236.18 64 RING L R13 R16 2.15 8.65 384.18 4 65 SPRAY HDR A C38
- C36 0.00 0.00 0.45 NET-FID of the FID-SERIES page 5
O-MECH C 1 P:go C %$ COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100
- DESIGN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec PIPELINE FROM TO HEAD-IDSS VEIDCITY FIDW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min )
66 SPRAY HDR A C39
- C36 0.00 0.00 0.45 67 SI-3A SUCTION S1 C7 0.33 6.02 2,121.43 68 SUCTION SI-3C S3 C8 0.05 6.18 2,179.91 69 SUCTION SI-3B S2 C9 0.00 0.00 0.00 70 DISCHARGE HDR C11 C16 0.33 6.02 2,121.43 ,
1 71 DISCHARGE HDR C13 C17 0.00 0.00 0.00 72 DISCHARGE HDR CIS C17 0.35 6.18 2,179.91 73 HEADER B C31 C32 2.46 12.20 4,301.34 - 74 PUMP SI-3A C7 C10 ( 434.97) 21.44 2,121.43 1
--- WITH COMPONENT C - SI-3A i 75 PUMP SI-3B C9 C12 *** CIDS ED *** '
--- WITH COMPONENT D -
76 PUMP SI-3C C8 C14 ( 428.68) 22.03 2,179.91
--- WITH COMPONENT E - SI-3C 77 HX-A C19 C21 0.00 0.00 0.00
--- WITH COMPONENT A - HX-A *** MODEL OUT OF RANGE ***-
78 HX-B C20 C23 28.62 12.20 4,301.34
--- WITH COMPONENT A - HX-A *** MODEL OUT OF RANGE ***
79 RING A R1 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIDSED BY REVFRSE FLOW ***
80 RING B R2- FC 0.00 0.00 0.00
--- WITH CHECK VALVE *** CLOSED BY REVERSE FIDW ***
81 RING C R3 FC 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIDSED BY REVERSE FIDW ***
82 RING D R4 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIDSED BY REVERSE FIDW ***
'83' RING E R7 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CLOSED BY REVERSE FIDW ***
, NET-FLO of the FID-SERIES page 6 l l l
O-MECH 4ALC 021 Rev. 00 Page C g k COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 ' j { DESIGN RULES: VEMCITY MIN: 0.00 MAX: 1000.00 ft/see l PIPELINE FROM TO HEAD-LOSS VELOCITY FwW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) l 84 RING F R8 FG 0.00 0.00 0.00 t --- WITH CHECK VALVE *** C MSED BY REVERSE FMW *** l l 85 RING G R9 FC 169.73 13.63 1,348.31 l l l 86 RING H R10 FG 166.07 9.99 988.66 ' 87 RING I R11 FG 161.86 7.73 764.94
- . 88- RING J R12 FG 160,13 5.85 579.06 89 RING'K R15 FG 148.79 9.08 236.18 j
[ 90 RING L R16 FG 149.26 8.65 384.18 93 PIPE-93 C11 C10 *** CMS ED *** 107 CS SUMP PIPE , N3 C6 0.01 ' 1.60 2,121.43 108 CS SUMP PIPE N9 C3 0.04 2.40 2,179.91 109 COMMON SUMP LIN H70 H3 0.16 1.60 2,121.43 110 COMMON SUMP LIN H70 N42 0.16 1.65 2,179.91 111 COMMON SUHF LIN H3 N3 0.04 1.60 2,121.43 112 COMMON SUMP LIN N42 N9 0.03 1.65 2,179.91 118 SI-3C DISCHARGE C14 C61 0.07 13.98 2,179.91 119 SI-3B DISCHARGE C12 C60 0.00 0.00 0.00 120 SI-3A DISCHARGE C10 C62 0.06 13.60 2,121.43 121 SUMP ENTRANCE FG H70 0.08 3.25 4,301.34 l l. NET-FLO of the FM-SERIES page 7 l
.. . .- , . _ _ = . - . _ .- - - ~ . _ _ _ . . _
0-MECH 4:ALC-021 Rev. 00 PagiCLQ l , ABB Combustion Engineering 1 l l CLIENT : Omaha Public Power District ~ l l NETWORK
SUMMARY
REPORTS JUNE 8, 1992 l R. Harsell-NE'NORK NAME : OPPDCS1 DATA FOR PIPES: OPPDCS l UPDATED : JUNE 8, 1992 OPPD CSP NPSH W/ SUMP SUBC00 LING 0-MECH-CALC-021 4 1P1H: 3A HDR B SUCTION FROM THE SUMP (6 ft) 0.01 % DEVIATION after 15 ITERATIONS i FIXED GRADE'
SUMMARY
1 NETWORK CONNECTION FIDW-RATE FIXED GRADE / ! NODE PIPELINE (gal / min ) PRESSURE SOURCE l R1 >n 79 RING A n> 0.00 n> 5,000.00 PSI R2 n> 80 RING B n> 0.00 n> 5,000.00 PSI R3 n> 81 RING C >n 0.00 n> 5,000.00 PSI l R4 >n 82 RING D >n 0.00 >n 5,000.00 PSI R7 n> 83 RING E n> 0.00 >n 5,000.00 PSI l l R8 >n 84 RING F >>> 0.00 n> 5,000.00 PSI l R9 >n '85 RING G n> 995.19 n> 14.70 PSI I i R10 >n 86 RING H n> 722.41 n> - 14.70 PSI ! R11 >n 87 RING I n> 554.44 n> 14.70 PSI R12 >n 88 RING J n> 416.99 n> 14.70 PSI R15 n> 89 RING K >n 168.56 n> 14.70 PSI R16 >n 90 RING L >n 275.07 n> 14.70 PSI ; H70 <<< 121 SUMP ENTRANCE <<< 3,132.66 <<< 17.30 PSI l NET FIhWS IN: 0.00 gal / min l t NET-FID of the FID-SERIES page 1
~
FC 05977 0-MECH-CALC-021 Rev. 00 PageCy$ DEMAND
SUMMARY
JUNCTION DEMAND JUNCTION DEMAND
- NODE (gal / min ) NODE (gal / min )
NET DEMAND IN: 0.00 gal / min f l l l' [ , i l l NET-FIA of the FIA-SERIES page 2 4
. . _ _ _ - . _ _ _ _ - . _ _ _ . _ _ _ . _ . . ~ . . . _ . _ _ _ _ _ . _ ~ _ _ _ _ . _ . _ _ _ _ _ ~ . . _ _ . _ _
0-MECH ,C 00 PageC9% COMPLETE PIPELINE REPORT JUNE 8, 1992 l PIPELINE COUNT: 100 DESIGN RULES: t'2DCITY MIN: 0.00 , MAX: 1000.00 ft/see PIPELINE FROM TO HEAD-IDSS VELOCITY FIDU-RATE ! NO ID NODE NODE (CAIN) (ft/sec) (8al/ min ) 1 SIRWT IIIT C1 C2 0.00 0,00 0.00 2 SIRWT H1'ADER C2 C3 0.00 0.00 0.00 3 SIRWT E1IT C4 C5 0.00 0.00 0.00 4 SIRWT HEADER C5 C6 0.00 0.00 0.00 5 SI-3A SUCTION C6 S1 0.94 8.33 3,132.66 6 S'I-3C SUCTION C2' S3 0.00 0.00 0.00 7 SI-3B SUCTION C3 S2 0.00 0.00 0.00 8 SI-3A DISCHABCE C62 C11 39.41 20.09 3,132.66 9 SI-3B DISCHARGE C60 C13 0.00 0.00 0.00 10 SI-3C. DISCHARGE C61 C15 0.00 0.00 0.00 11' DSCHRG HDR C17 C16 0.00 0.00 0.00 13 DSCHRG HDR C16 C18 5.29 8.88 3,132.,66 14 A Hi INLET CIS C19 0.00 0.00 0.00 15 B HX INLET C18 C20 6.40 8.88 3,132.66 . 16 A HX OUTLET C21 C22 0.00 0.00 0.00 17 B HX OUTLET C23 C24 _1.22 8.88 3,132.66 l 18 HK CROSS CONECT- C22 C25 0.00 0.00 0.00 19 HK CROSS CONECT C24 C26 0.00 0.00 0.00 20 SDC DISCHARGE C25 C26 *** CIASED *** 21 A HEADER C22 C27 0.00 0.00 0.00
--- WITH COMPONENT F - flow meter *** MODEL OUT OF RANGE *+*
22 B HEADER C24 C28 12.85 8.88 3,132.66
--- WITH COMPONENT F - flow meter NET-FID of the FID-SERIES page 3 h
L
- - - - ,, - , ~ ,
. . . . . . . . . _ .- -- -- .- .- ..-. _..~_ - ...~.- .. . - . . _ -
0-MECHCALC421 Rev. 00 Page C $5 i COMPLETE PIPELINE REPORT JUNE 8, 1992
! PIPELINE COUNT: 100 -
I DESICN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec $ PIPELINE FROM TO HEAD-LOSS VEIDCITY FIhW-RATE NO ID NODE NODE (CAIN) (ft/sec) (gal / min ) 4 23 A HEADER C27 C29 0.00 0.00 0.00
--- WITH COMPONENT 5 - FIAW VALVE *** MODEL OUT OF RANGE ***
l 24 B HEADER C28 C31 18.58 20.09 3,132.66
--- WITH COMPONENT B - FIDW VALVE i
.j 25 A HEADER C29 C30 0.00 0.00 0.00 ] 26 A HEADER C30 C33 0.00 0.00 0.00 27 A HEADER C33 C34 0.00 0.00 0.66
, 28 A HEADER C34 C35 0.00 0.00 0.66
'29 A HEADER C36
- C33 0.00 0.00 0.66
- 30 A HEADER C35 C37 0.00 0.00 0.66 i 31 A HEADER C37 C38 0.00 0.00 0.66
) i j- 32 A HEADER C38 C39 0.00 0.00 0,33 l j 33 PIPE-33 C39 C40 0.00 0.00 0.00 34 A HEADER C40 C41 0.00 0.00 0.00
.35 A HEADER C41 C42 0.00 0.00 0.00 1
36 A HEADER C42 C43 0.00 0.00 0.00 l
- I 37 B HEADER C32 C44 3.25 8.33 3,132.66 38 B HEADER C44- C45 0.07 4.12 1,549.88 39 B HEADER C45' C48 3.58 9.12 1,549.88
[ 40 B HEADER C44 C46 4.33 9.32 1.582.78 41 B' HEADER C46 C47 0.02 4.21 1,582.78
'42 B HEADER C47 C54 0.07 4.21 1,582.78 43 5 HEADEk C48 C54 0.77 4.12 1,549.88 4
NET-FLO of the FIA-SERIES page 4 v 9 w = , e -- - ,-v v-- -- , s.
l FC 05977 O-MECH-cal &O2i Rev. 00 Paso C 5 \ COMPLETE PIPELINE
- REPORT JUNE 8, 1992
' PIPELINE COUNT: 100 DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/sec PIPELINE FROM TO HEAD-LOSS VEIDCITY FIDW-RATE l NO ID NODE NODE (CAIN) (ft/sec) (gal / min ) l i
44 B HEADER C54 C49 0.06 8.33 3,132.66 45 B IIEADER C49 C50 0.16 5.69 2,137.47 46 B HEADER C50 C51 0.07 3.76 1,415.06 i l
'47 5 HEADER C51 C52 0.03 2.29 860.62 l '
'48 5 HEADER C52 C53 0.01 1.18 443.63 2
!- 49 RING A C37 R1 0.00 0.00 0.00 50 RING B C40 R2 0.00 0.00 0.00 l 51 RING C C41 R3 0.00 0.00 0.00 . , 52' RING D C42 R4 0.00 0.00 0.00 l . l '53 RING E C43 R5 0.00 0.00 0.00 ! l 54 RING E2 R5 R6 0.00 0.00 0.00 l 55 RING E3 R6 R7 0.00 0.00 0.00 l -56 RING F R5 'R8 0.00 0.00 0.00 l '57 RING G C49 R9 0.74 5.66 995.19 58 RING H C50 R10 0.38 4.25 722.41 l- 59 RING I C51 R11 0.94 5.60 554.44 60 RING J CS2 R12 0.61 4.21 416.99 61 RING K. C53 R13 4.12 9.98 443.63 [ 62 RING K2 R13 R14 0.08 3.79 168.56 i
'63- RING K3 R14 R15 0.77* 6.48 168.56 i-64- RING L R13' R16 1.11 6.19 275.07
! '65- SPRAY HDR A C38
- C36 0.00 0.00 0.33 i
w ' - NEToFID of the FID-SERIES page 5
,,y
- FC 05977 0.MECHCALC421 Rev. 00 Pags c 5 s.
COMPLETE PIPELINE REPORT JUNE.8, 1992 PIPELINE COUNT: 100 DESIGN RULES: VELOCITY MIN: 0.00 MAX: 1000.00 ft/sec l PIPELINE FROM TO HEAD-IASS VEIDCITY FLOW-RATE NO ID NODE NODE (GAIN) (ft/sec) (gal / min ) l l 66 SPRAY HDR A C39
- C36 0.00 0.00 0.33 67 SI-3A SUCTION S1 C7 0.71 8.88 3,132.66 68 SUCTION'SI-3C S3 C8 0.00 0.00 0.00 69 SUCTION SI-3B- S2 C9 0.00 0.00 0.00 L 70 DISCHARGE HDR C11 C16 0.72 8.88 3,132.66 71 DISCHARGE HDR C13 C17 0.00 0.00 0.00 72 DISCHARGE HDR C15 C17 0.00 0.00 0.00 73 HEADER B C31 C32 1.32 8.88 3,132.66
! 74 PUMP SI-3A C7 C10 ( 319.47 31.66 3,132.66 I
--- WITH COMPONENT C - SI-3A i
75 PUMP SI-3B C9 C12 *** CIDS ED *** -
--- WITH COMPONENT D -
76 PUMP SI-3C C14 C8 *** CIDSED *** l
--- WITH COMPONENT E -
77 HX-A C19 C21 0.00 'O.00 0.00
--- WITH COMPONENT A - HX-A *** MODEL OUT OF RANGE ***
78 HX-B C20 C23 15.18 8.88 3,132.66
--- WITH COMPONENT A - HX-A 79 RING A R1 FC 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIASED BY REVERSE FIhW ***
80 RING B R2 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIASED BY REVERSE FIDW ***
81 RING C R3 FG 0.00 0.00 0.00
--- WITH CHECK VALVE ~ *** CLOSED BY REVERSE FIhW ***
82 RING D R4 FG 0.00 0.00 0.00 l --- WITH CHECK VALVE *** CIASED BY REVERSE FIDW *** l 83 RING E R7 FC 0.00 0.00 0.00 l --- WITH CHECK VALVE *** CIASED BY REVERSE FLOW *** l i NET-FID of the FIA-SERIES page 6 I l
O-MECH 4ALC-G21 Rev. 00 l COMPLETE PIPELINE REPORT JUNE 8, 1992 PIPELINE COUNT: 100 DESIGN RULES: VEIDCITY MIN: 0.00 MAX: 1000.00 ft/sec PIPELINE FROM TO HEAD-IDSS VEIDCITY FLOW-RATE NO ID NODE NODE (CAIN) (ft/sec) (gal / min ) 84 RING F R8 FG 0.00 0.00 0.00
--- WITH CHECK VALVE *** CIDSED BY REVERSE FIDW ***
85 RING G R9 FG 92.47 10.06 995.19 86 RING H R10 FC 88.67 7.30 722.41 87 RING I R11 FG 85.03 5.60 554.44 88 RING J R12 FG 83.04 4.21 416.99 89 RING K R15 FG 75.78 6.48 168.56 90 RING L R16 FG 76.52 6.19 275.07 93 PIPE-93 C11 C10 *** CIDSED *** 107 CS SUMP PIPE , N3 C6 0.02 2.37 3,132.66 108 CS SUMP PIPE N9 C3 0.00 0.00 0.00 109 COMMON SUMP LIN H70 H3 0.35 2.37 3,132.66 110 COMMON SUMP LIN H70 N42 0.00 0.00 0.00 111 COMMON SUMP LIN H3 N3 0.08 2.37 3,132.66 112 COMMON SUMP LIN N42 N9 0.00 0.00 ~0.00 118 SI-3C DISCHARGE C14 C61 0.00 0.00 0.00 119 SI-3B DISCHARGE C12 C60 0.00 0.00 0.00 120 SI-3A DISCHARGE C10 C62 0.14 20.09 3,132.66 121 SUMP ENTRANCE FG H70 0.04 2.37 3,132.66 NET-FID of the FID-SERIES page 7
. . . - . - - . . . - - -~ - - -. . --
0-MECH 4ALC-021 Rev. 00 Page D g APPENDIX D SELECTED REFERENCES l D2 Reference 3.12 i D5 Reference 3.14 D16 Reference 3.16 D19 FLO-SERIES Code Cealficates D21 Model Verification Checklist e 4 4 0
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I FC 05977 O-MECH-CALC-021 Rw. 00 , PgeD'l T N G E R S O .L L - R A N D ) EPD ENGINEERING . 942 MEMORIAL PARKWAY NEW JERSEY PHILLIPSBURG, DATE: Ik M A1tc kh
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0-MECH-CALC 021 Rw. 00 PegeDE A BR ED I 7%EDED ASEA BROWN BOVERI i . l !- Inter. Office Correspondence l l ' i- ) . To: R. Harsell From: M. Petraska l OPS-92-0653 1 F. P. Ferraraccio
- l. -
May 29, 1992 l 1
.xc: M. J. Gancarz -
- - R. C. Whipple I i J. J. Herbst
- M. D. Michonski QRC (2) - Permanent i
) i
References:
- 1) ABB CE Calculation No. 002-AS91-C-001 Rev.00, "OPPD Maximum Safe Hot Leg LOCA Containment Analysis" guards , Dated 9-5-91. s.
3 l 2) ABB CE Calculation No. 002-NT90-C-012 Rev. 00. {- " Evaluation of LOCA Long Term Containment Response for Fort Calhoun Station", Dated 11-l_ 26-90. 1
- 3) Omaha Public Ponar District Fort ,Calhoun
; Station Updated Final. Safety Analysis Report, i R2, Dated 7-91..
p Graphs and Data Tables Developed from CONTRANS
Enclosure:
1) Case #AVQC, Case #0SNVBV97, and Case #AGTL. i
Subject:
EVALUATION 0F THE PRESSURE MARGIN PRESENT BETWEEN THE SATURATION PRESSURE OF THE CONTAINMENT SUMP WATER AND THE CONTAINMENT PRESSURE - POST LOCA. This meno is in response to your request to transmit the results of' , a review of Omaha Public Power District's Fort Calhoun Station containment transient analysis. This review ' was conducted to support the containment spray pump Net Positive Suction Head available (NPSHa) investigation. The containment analysis runs are from the NRC approved code CONTRANS. .This code simulates the pressure and temperature
' response in the containment following a derign basis event. The output of this analysis code includes the containment pressure, sump water temperature, and various other containment parameters as a function of time during an event.
_ _ _ _ .mm _._ _ _ _ _ _ _ . _ _ _ _ _ . _ . _ _ _ . . _ - _ _ _ _ . . . _ __ _. .. _ . _ . 3 . _ . .FC 05977 ._ < o-MECH-CALC-021 Rsv. 00 Page D b 4 1 1 i t l It is from this data, specifically the sump water temperature, that the saturation pressure of the sump water can be determined. The
- CONTRANS analysis runs chosen from References (1) and (2) are
? either the analysis of record, Case #AVQC (Reference 3) , or provide
- a scenario where the sump temperature would be maximized and the >
- containment pressure minimized, Case #AGTL and Case #0SNVBV97
) I (Reference 1 and 2). j' case #AVQC utilizes 1 spray header with spray water at 105'F and updated Shutdown Cooling Heat Exchanger data. Case #AGTL is the , i same as Case #AVQC except it has a revised decay heat input, a ; i spray flow of 2510 GPM and 2 spray headers. Case #0SNVBV97 is a I best estimate maximum safeguards case. It should be noted that all ' 1 these cases are LOCA cases. The Main Steam Line Break cases of record in Reference (3) were not reviewed since the transient l f calculations are terminated prior to the time of the receipt of the l i Recirculation Actuation Signal (RAS) . Since the MSLB case does not j l have any data post RAS it is impossible to predict the pressure response in containment. Note also that the cases reviewed were run to a maximum of 100,000 seconds, predictions of sub-cooling beyond that time were not possible. The curves and tables developed in Enclosure (1) use the data taken directly from the CONTRANS case output and the ASME Steam Tables. The containment pressure is a direct output of the code while the.P saturation pressure of the sump water was developed using the temperature given by CONTRANS, and the corresponding saturation pressure from the ASME Steam Tables. This provided data for the containment pressure and the sump water saturation pressure. These two sets of data were then plotted and the minimum pressure 4 differential determined. I The minimum differential pressure is being sought because it minimizes the amount of Net Positive Suction Pressure available to the containment spray pump during an event. This result is the goal of the evaluation this document is supporting. In evaluating the curves and data tables in Enclosure (1) it can be i seen that the minimum pressure differential between the containment sump saturation pressure and the' total containment pressure, after the initiation of Recirculation Actuation Signal, is 15.47 psi. In each of the cases RAS is not achieved until after 1400 seconds into the transient. Therefore, any pressure differentials before this time are not considered in this evaluation. This occurs during the maximum safe guards case, Case #0SNVBV97, with all safety injection pumps running and two spray headers, with fan coolers. The minimum pressure differential occurs with the total containment pressure of 16.43 psia at 99650 seconds, and sump water at 100.3'F. It should be noted that case #0SNVBV97 never has sump water in excess of 212'F . In the three cases investigated, the sump temperature was maintained below 212'F except in Case #AVQC, between 18520 and 79520 seconds. In that case the sump water does reach the saturation point of water, at 14.7 psia, and 212*F , but the containment pressure in this range is maintained above 38.26 psia.
o-MECHCALC42i Rev. 00 Pege D 7 i l 4 This provides a margin of over-pressure, from the containment pressure to the saturation pressure of the sump water, of 23 psi. This information is provided simply to illustrate that the water does exceed the saturation temperature at 14.7 psia, but there is sufficient over-pressure on the water to maintain it in a sub-cooled state. At all times in the three analyses there are large margins of containment pressure in excess of the saturation pressure of the sump water. Therefore the minimum differential pressure,15.47, is achieved in Case #0SNVBV97, at 99650 seconds. The enclosed data has been Quality. Assured in accordance with the QAPM guidelines. Should you have any q)2estions, please do not hesitate to contact myself at X5485, or Mike Gancarz at x4600. QAStatus: Verred The safety related design Inhxmation contained in this document has been reviewed and satisfies (where ap:dicabk) theitems contained on check-list (s) 4 -. - .and - of theQuality , Assurance liocedures Manual.This review is so certified, independentileviewer N.J b Data _ (o - / - 9 SL , DocumentRw.No. - O - l l I l l l 4 e
.OPPD LOCA CONTAINMENT PRESSURE vs TIME.
; Case # OSNVBV97 I
PR(SSURE, psia . 60- -
.50 .
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- TIME, SECONDS (Thousands) c8o !
E iT8 e$ Sump Saturated *34
---- Containment "27 7 80!
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O MECH 4A, 5 FQ421Q2v.377 l Pzgs D A OPS-92-0653 Enclosure (1) , page 2 of 8 l
- l OPPD LOCA CONTAINMENT Pft"vs TIME 1 Case # OSNVBV97 CONTAINMENT SUMP SAT.
WATER, F PRESS.PStA DELTA.P A., ,4 Q.j*'#* .Q,y __ TIME.SEC PRESS. PSIA j 0.0 90.0 14.70 0.69 14.01 0.2 90.5 16.78 0.71 16.07 0.4 914 19.23 0.78 18.45 1.3 111.8 28.03 1.34 26.69 2.8 135.1 38.00 2.54 35.46 3.8 148.0 43.49 3.54 39.95 4.8 159.9 48.54 4.73 '43.81 5.8 169.9 5102 5.98 47.04 7.8 183.9 59.86 8.18 51.68 l i 8.8 188.0 62.10 8.95 53.15 10.8 192.7 64.69 - 9.89 54.8
-12.8 194.3 66.07 10.23 55.84 18.8 194.0 65.85 10.17 55.68 20.8 1917 65.72 10.10 55.62 28.8 192.6 65.28 9.87 55.41 38.8 191.1 64.91 9.56 55.35 l
68.8 190.5 62.74 9.44 513 88.8 192.0 60.87 9.75 51.12 98.8 192.6 60.03 9.87 - 50.16 112.8 193.1 58.77 9.97 48.8 122.8 1912 57.92 9.99 47.93 132.8 1914 57.11 10.04 47.07 152.8 193.6 55.60 10.08 45.52 172.8 193.5 . , . 54.20 10.06 44.14 192.8 193.3 52.91 10.02 42.89 210.8 '193.0 51.81 9.95 41.86 248.8 192.1 49.42 9.75 39.67 288.8 190.8 46.89 9.50 37.39 308.8 190.0 45.71 9.34 36.37 338.8 188.6 43.93 9.06 34.87 368.8 187.1 42.20 8.77 33.43 388.8 186.1 41.13 8.58 32.55 , 428.8 184.0 . 38.95 8.20 30.75 448.8 183.0 37.92 8.02 29.9 468.8 '181.9 37.03 7.83 29.2 488.8 180.9 35.99 7.66 28.33 l 530.0 178.7 34.13 7.29 26.84 j 730.0 169.2 27.56 5.88 21.68 i 830.0 165.0 25.17 5.34 19.83 930.0 161.0 2140 4.85 18.55 l 1030.0 157.4 22.10 4.45 17.65 I 1180.0 152.5 .20.77 3.95 16.82 ! 1380.0 146.7 18.97 3.42 15.55 1530.0 145.4 18.99 3.29 15.7 I 1730.0 144.7 19.04 3.25 15.79 1930.0 144.1 18.97 3.21 15.76 l 2390.0 142.5 18.72 3.08 15.64 2840.0 140.9 18.50 2.96 15.54 3890.0 137.0 18.15 2.67 15.48
-_ ~ - -- -. _ _ . . . . . . _ .- . _. ..
O MECH. CALC 421 Rev. 00 Pags D go OPS-92-0653 Enclosure (1) page 3 of 8 OPPD LOCA CONTAINMENT PIT vs11ME Caso # OSNV8V97 CONTAINMENT SUMP SAT. TIME.$EC WATal.F PfESS. PSIA PRESS. PSIA DELTA P 4640.0 134.3 17.97 2.49 15.48 5240.0 132.3 17.85 2.36 15.49 6290.0 129.0 17.68 2.16 15.52 7640.0 125.3 17.51 1.96 15.55 8240.0 123.8 17.44 1.88 15.56 9290.0 1 21.5 17.34 1J6 15.58 10850.0 118.5 17.22 1.62 15.6 I 12650.0 115.7 17.12 1.50 15.62 13650.0 114.4 17.07 1.45 15.62 18650.0 109.9 16.91 1.27 15.64 21650.0 108.2 16.84 1.21 15.63 25650.0 106.6 16.78 1.15 15.63 ' 29650.0 105.6 16.73 1.12 1S.61 39650.0 103.9 16.64 1.06 15.58 49650.0 102.8 16.58 1.03 15.55 59650.0 102.0 1634 1.00 15.54 69650.0 1013 16.50 0.99 15.51 79650.0 101.0 16.47 0.98 - 15.49 89650.0 100.6 16.45 0.96 15.49 99650.0 100.3 16.43 0.96 15.47 - 100000.0 100.2 16.43 0.95 15.48 , l t
i. OPPD LOCA CONTAl.NMENT PRESSURE vs TIME Case # AVQC PRESSURE, psia . 80 ? i 60 4 t 1 1 i 40 - 20 - O 0 10 20 30 40 60 60 70 80 90 100 @ TIME, SECONDS (Thousands) m E U b
*U O O >
P f os M M e
---- Containment Sump Saturated 18i' ce :r 8- O t N
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FC 05977 O-MECHCALC.021 Rev. 00 Pegs D @ OPS-92-0653 Enclosure (1) page 5 of 8 OPPD LOCA CONTAINMENT P/T vsTIME Case # AVOC CONTAtNMENT SUMP SAT. TIME.SEC WATER. F PRESS. PSIA PRESS. PSIA DELTA.P 0.0 120.0 17.70 1.89 16.01 0.2 119.9 19.39 1.69 17.70 0.4 121.4 21.79 1.76 20.03 1.3 134.5 30.06 2.50 28.16 2.8 153.2 40.80 4.02 36.78 3.8 164.0 46.42 5.21 41.21 4.8 174.1 51.61 6.58 45.03 ; 5.8 182.7 56.23 7.97 48.26 l 7.8 194.9 63.35 10.36 52.99 l 8.8 198.5 65.74 11.17 54.57 10.8 202.6 68.60 12.16 56.44 12.8 203.9 70.17 12.49 57.68 18.8 204.1 70.35 12.54 57.81 20.8 204.1 70.34 12.54 57.80 28.8 204.0 70.37 12.51 57.86 l 38.8 203.8 70.52 12.46 58.06 l 68.8 202.5 71.19 12.14 59.05 ) 88.8 201.4 71.82 11.86 59.96 ! 98.8 200.8 72.13 11.72 60.41 j 112.8 199.9 72.49 11.50 60.99 122.8 199.3 72.77 11.36 61.41 132.8 198.6 73.07 11.20 ' 61.87 152.8 197.3 73.71 10.90 62.81
, 172.8 197.4 74.06 10.92 63.14 192.8 198.1 74.25 11.08 63.17
. 210.8 198.7 74.43 11.22 63.21 248.8 199.4 74.35 11.38 62.97 288.8 199.9 74.18 11.50 62.68 308.8 200.0 7194 11.53 62.41 338.8 200.2 7160 11.57 62.03 1 368.8 200.2 73.08 11.57 61.51 388.8 200.1 72.72 11.55 61.17 428.8 199.9 72.03 11.50 60.53 448.8 199.9 71.68 11.50 60.18 468.8 199.7 71.33 11.45 59.88
^
488.8 199.6 71.00 11.43 59.57 530.0 199.3 70.34 11.36 58.98 730.0 197.9 67.17 11.03 56.14 830.0 197.1 65.70 10.85 54.85 930.0 196.3 64.33 10.67 53.66 1030.0 195.3 62.50 10.45 52.05 1180.0 193.9 59.87 10.15 49.72 1380.0 191.9 56.74 9.72 47.02 1530.0 190.4 54.69 9.41 45.28 1730.0 188.4 52.31 9.02 43.29 1930.0 186.3 50.30 8.62 41.68
, 2360.0 182.2 46.87 7.89 38.98 2860.0 178.0 43.92 7.18 36.74 3860.0 - 183.0 43.60 8.02 35.58
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YO 05977 O-MECH-CALC 421 Rsv. 00 l P:gs D (3 t OPS-92-0653 Enclosure (1) page 6 of 8 l OPPD LC CA CONTAINMENT P/T vs TIME j Case # AVQC l CONTAINMENT SUMP SAT. TIME,SEC WATER. F PRESS. PSIA PRESS. PSIA DG.TA. P , 4260.0 184.9 43.48 8.37 35.11 l 5260.0 189.5 43.15 9.24 33.91 l 6260.0 193.4 42.89 10.04 32.85 7260.0 196.8 42.69 10.78 31.91 8260.0 %99.4 42.52 11.38 31.14 ( 9260.0 202.3 42.37 12.08 30.29 l 10320.0 204.6 42.23 12.66 29.57 12320.0 208.3 42.11 13.65 28.46 13520.0 210.0 42.08 14.12 27.96 ! 18520.0 215.3 42.04 15.68 26.36 ! 21520.0 217.2 42.00 16.27 25.73 l 25520.0 218.9 41.91 16.82 25.09 l 29520.0 ' 219.8 41.75 17.12 24.63 l 39520.0 220.2 41.14 17.25 23.89 L 49520.0 219.1 40.39 16.89 23.50 59520.0 217.4 39.64 16.34 23.30 69520.0 215.5 38.92 15.75 23.17 l 79520.0 213.7 38.26 15.19 23.07 89520.0 211.9 37.66 14.66 23.00 , 99520.0 210.2 37.12 14.18 22.94
- l 100000.0 210.1 37.00 14.15 22.94 1
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OPPD LOCA. CONTAINMENT PRESSURE vs TIME Case # AGTL
~
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---- Containment Sump Saturated 18 T2 aw , $.
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ru 05977 O-MECH CALC.021 Rav. 00 P:ss D )5 OPS-92-0653 OPPD LOCA CONTAINMENT P/T vs TIME Enclosure (1) Case # AGT1. Page 8 of 8 CONTAINMENT SUMP SAT. TIME.SEC WATER. F PRESS. PSIA PRESS PSIA DELTA.P 0.00 120.0 , 17.70 1.69 16.01 0.17 119.9 19.39 1.69 17.702 0.37 121.4 21.79 1.76 20.03 1.30 134.5 30.66 2.3 28.16 2.80 153.2 40.80 4.02 36.78 1 80 164.0 46.42 5.22 41.2 4.80 174.1 51.61 6.58 45.03 5.80 182.7 56.23 7.97 48.26 7.80 194.9 6135 10.36 52.99 8.80 198.5 65.74 11.17 54.57 10.80 202.6 68.00 12.16. 56.44 12.80 203.9 70.17 12.48 57.69 18.80 204.1 70.35 12.54 57.81 20.80 204.1 70.34 12.54 57.8 28.80 204.0 70.37 12.51 57.86 38.80 203.8 70.52 12.46 58.06 68.80 202.5 71.19 12.13' 59.06 88.80 201.4 71.82 11.86 59.96 98.80 200.8 72.13 11.71 60.42 112.80 199.9 72.49 11.50 60.99 122.80 199.3 72.77 11.36 61.41 132.80 198.6 73.07 11.19 61.88 152.80 197.3 73.70 10.89 62.81 172.80 196.2 74.34 ,10.65 63.69
. .192.80 197.4 74.41 10.92 63.49 -
210.80 198.4 74.51 11.15 63.36
' 248.80 199.8 74.23 11.48 62.75 288.80 200.9 73.87 11.74 62.13 308.80 201.3 73.54' 11.84 61.7 338.80 201.7 73.06 11.94 61.12 368.80 202.0 72.42 12.01 00.41 388.00 202.1 71.98 12.03' 59.95 428.80 -
202.2 ' 71.13 12.06 59.07 448.80 202.3 - 70.70 12.08 58.62 468.80 202.3 70.27 12.08 58.19 488.00 202.3 69.86 -12.08 57.78 530.00 202.2 60.05 12.06 58.99 730.00 201.3 05.22 11.84 53.38 830.00 200.6 63.46 11.67 51.79 930.00 199.9 61.83 11.50 50.33 1030.00 199.0 59.82 11.29 48.53 1180.00 197.5 56.71 10.94 45.77 1380.00 195.2 53.14 10.43 42.71 1530.00 193.4 50.88 10.04 40.84 1730.00 190.9 48.31 9.52 38.79 1930.00 188.4 46.14 9.02 37.12 2360.00 183.6 42.44 8.13 34.31 . 2860.00 181.2 40.29 7.71 32.58 3860.00 185.9 40.09 8.55 31.54 4260.00 187.6 39.94 8.87 31.07 5000.00 190.5 39.69 9.44 30.25 i - -
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PU U5977 l O-MECH 4ALC-021 Rev. 00 Page D t\ I I CilECKLIST FOR FLO-SERIES VERIFYING RUNS Preparer Reviewer Task A /2// Original Database Model OU VC S 4^ M/t' Taken f rom Cale l) - e 014
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