ML12088A432
| ML12088A432 | |
| Person / Time | |
|---|---|
| Site: | Indian Point  |
| Issue date: | 03/23/2005 |
| From: | CSI Technologies |
| To: | Entergy Nuclear Northeast, Atomic Safety and Licensing Board Panel |
| SECY RAS | |
| Shared Package | |
| ML12088A422 | List: |
| References | |
| RAS 22102, 50-247-LR, 50-286-LR, ASLBP 07-858-03-LR-BD01 040711-01, Rev 0 | |
| Download: ML12088A432 (47) | |
Text
ENT000073 Submitted: March 28, 2012
(
IndianPoint Indian Unit 33 Point Unit CHECWORKS Power CHECWORKS Power Uprate UprateAnalysis Analysis CalculationNo.
. Calculation 040711-01 No. 040711-01 Revision00 Revision For-Use Issued For-Use Issued March 23, March 23,2005 2005
(
prepared preparedfor:
for:
Entergy Entergy Nuclear Nuclear Northeast Northeast 295 Broadway Suite 3 295 Broadway Suite 3 PO Box 308 PO 308 Buchanan, NY 1051 1-0308 Buchanan, NY 10511-0308 ENTERGY NUCLEAR NORTHEAST ENN-DC-149 prepared by:
2 0 ACCEPTED AS NOTED RESUBMITIAL NOT REQUIRED I TECHNOLOGIES, INC.
o ACCEPTED AS NOTEDRESUBMITIAL REQUIRED 105 E. Main St., Suite 215 E tt Dundee, IL 60118 Dundee, IL 60118
cs/ TECHNOLOGIES. INC.
CSI TECHNOLOGIES, INC . IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Uprate AnalysisAnalysis
( Table of Table of Contents Contents 1
1.. INTRODUCTION ..............................................................................................................................................
INTRODUCTION.............................................................................................................................................. 22 2
2.. ........................................................................................................................................................... 33 PURPOSE...........................................................................................................................................................
PURPOSE 3.
- 3. ................................................................................................................................................................ 44 SCOPE ................................................................................................................................................................
SCOPE 4.
- 4. ASSUMPTIONS AND ASSUMPTIONS AND MODELING MODELING DECISIONS ......................................................................................... 55 DECISIONS .........................................................................................
5 5.. METHODOLOGY ............................................................................................................................................ 77 METHODOLOGY ............................................................................................................................................
5.1.
5.1. INPUTSPU INPUT SPU GLOBAL GLOBALDATA ...........................................................................................................................
DATA........................................................................................................................... 77 5 .2.
5.2. REDEFINITION OF REDEFINITION CHECWORKS LINES OF CHECWORKS .................................................................................................... , .. 11 LINES ................................................................................................. 11 5.3.
5.3. UPDATE UPDATE MODELBASED MODEL BASEDON ON SPUSPU OPERATIONAL OPERATIONALOR CONFIGURATION OR CONFIGURATION CHANGES CHANGES ........................................ 12
........................................ 12 5.4.
5.4. UPDATE UPDATE NETWORK NETWORK FLOW FLOW ANALYSIS ANALYSIS DEFINITIONS ......................................................................................
D E F I N ~ ~ ~......................................................................................
ONS 12 12 5.5.
5.5. IMPLEMENT IMPLEMENT THE ADVANCED THE ADVANCED RUN RUNDEFINITION DEFINITION ...........................................................................................
........................................................................................... 13 13 5.6.
5.6. PERFORM PERFORM WEARRATE WEAR RATEANALySIS ANALYSIS ............................................................................................................... 15
............................................................................................................... 15 5.7.
5.7. QUANTIFY QUANTIFY EFFECTOF EFFECT STRETCH OF STRETCH POWERUPRATE POWER ........................................................................................
UPRATE ........................................................................................ 15 15 6
6.. .........................................................................................................................................................
RESULTS ......................................................................................................................................................... 16 RESULTS 16 6.1.
6.1. COMPONENT COMPONENT LEVELWEARRATE LEVEL WEAR RATE CHANGES CHANGES DUE TO DUE TO SPUSPU...........................................................................
........................................................................... 16 16 6.2.
6.2. STEAM CYCLE STEAM CYCLELEVEL LEVELWEAR WEARRATE CHANGESDUE RATE CHANGES DUE TO TO SPU ........................................................................ 16 SPU ........................................................................ 16 7
7.. .................................................................................................................................................
REFERENCES................................................................................................................................................. 17 REFERENCES 17
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APPENDIX A: A: CHECWORKS MODELED MODELED LINES ..............................................................................................
LINES.............................................................................................. 19 19 ApPENDIX CHECWORKS APPENDIX B: COMPONENT LEVEL LEVELWEAR WEAR RATE RATE CHANGES CHANGES DUE TO SPU SPU ........................................................ 33 33 ApPENDlxB: COMPONENT APPENDIX APPENDlXC: c: STEAM CYCLE CYCLE LEVEL LEVELWEAR WEAR RATE CHANGES CHANGES DUE TO SPU SPU ..................................................... 35 35 ATTACHMENT ATTACHMENT A: REFERENCED A: REFERENCED CORRESPONDENCE CORRESPONDENCE AND COMMUNICATIONS .......................................................
COMMvNICATtONS....................................................... 39 39 Calculation No Calculation . 040711.01. Revision No. 040711-01, Revision 00 Page 11 of Page 44 of 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. /NC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Analysis Uprate Analysis
( 1.
- 1. Introduction Introduction This calculation This calculation documents documents the the revision of the revision of the Indian Indian Point Point Unit Unit 33 CHECWORKS CHECWORKS model model to predict to Flow-Accelerated Corrosion predict Flow-Accelerated Corrosion (F (FAC) wear rate AC) wear rate changes changes duedue to to Stretch Stretch Power Power Uprate (SPU).
Uprate (SPU). TheThe Indian Indian Point Point Unit SPU will Unit 33 SPU will change change feedwater feedwater andand steam steam flow flow rates, rates, temperatures, and temperatures, and enthalpies, enthalpies, which turn change in turn which in change local local chemistry chemistry values.
values. AllAll of of these these factors affect factors affect wear wear rates rates due due to to F FAC.
AC. AsAs aa result result of the uprate, of the some lines uprate, some lines will experience will experience accelerated rates accelerated of FAC, while rates ofFAC, while others others will have reduced will have reduced rates.
rates. The The impact impact on on each each line line depends on depends on the the complex complex interaction interaction of of changes changes in in flow flow rate, rate, pressure, temperature, pressure, temperature, enthalpy, steam enthalpy, steam quality, quality, and and chemistry chemistry on on the the F FAC degradation mechanism.
AC degradation mechanism.
Indian Point Indian Point 33 had had previously developed aa CHECWORKS previously developed CHECWORKS model of FAC-susceptible model ofFAC-susceptible piping. However, the piping. However, the previous previous model model did did not not address address the the changes changes that that will will result result from from Appendix K Appendix K Uprate Uprate and and Stretch Stretch Power Power Uprate.
Uprate. This calculation details This calculation details the the process process required to required to revise the CHECWORKS revise the CHECWORKS model model so that it so that it correctly correctly reflects reflects all all plant plant power power levels (the levels (the original original power level, Appendix power level, Appendix K K Uprate, Uprate, and and Stretch Stretch Power Power Uprate).
Uprate). Also Also documented are the changes in FAC wear rates due to the SPU.
documented are the changes in F AC wear rates due to the SPU.
Note that historical Note that historical (pre-uprate (pre-uprate and and Appendix Appendix K Uprate) operating K Uprate) operating conditions conditions remain remain within the within the model, model, associated associated to to the the applicable applicable operating operating cycles.
cycles. The The SPU SPU operating operating conditions are conditions are associated associated to to the the calendar calendar time time that that those those conditions conditions are are scheduled scheduled to to occur, starting occur, starting inin Cycle Cycle 14 In this
[7.3.1]. In 14 [7.3.1]. this way, way, the the model's models predictions predictions ofof total current total current and future and future wear will be wear will be as as accurate accurate asas possible because the possible because the predictions predictions will will bebe based based on on
( both historical both historical and and expected expected future future operating operating conditions.
conditions.
i Calculation No.
Calculation No. 040711-01, Revision 00 040711-01, Revision Page 2 Page of 44 2 of 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. /NC. IP3 CHECWORKS Power IP3 CHECWORKS PowerUprate Uprate Analysis Analysis
( 2.
- 2. Purpose Purpose The purposes The purposes of of the the power power uprate uprate analysis analysis in in CHECWORKS CHECWORKS are are as follows:
as follows:
- To quantify To quanti@ changes changes in in FFAC wear rates AC wear rates due due to to the the Stretch Power Uprate Stretch Power Uprate (both (both increases and increases and decreases).
decreases).
- 0 gain the To gain To the ability ability to to describe describe the the effects effects of of power on FFAC-susceptible uprate on power uprate AC-susceptible piping in piping in the the Licensing Licensing Submittal.
Submittal.
- To ensure To ensure that that the the CHECWORKS CHECWORKS model model reflects reflects current current plant plant conditions conditions going going forward.
forward.
(
Calculation No.
Calculation No. 040711-01, 040711-01, Revision Revision 00 Page Page 33 of 44 of44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. /NC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis
( 3.
- 3. Scope Scope The scope The scope of this power of this power uprate uprate analysis analysis was was the the entire entire Indian Indian Point Point 33 CHECWORKS CHECWORKS model including model including allall modeled modeled lines lines and and components [7.2]. No components [7.2]. analysis was No analysis was performed performed on on plant lines plant lines and and components components thatthat were were not part of not part the CHECWORKS of the CHECWORKS model model This analysis This analysis was was performed performed using using CHECWORKS CHECWORKS FAC FAC version 1.OG.
version 1.0G.
Assumptions and Assumptions and modeling modeling decisions decisions made made during during this this analysis analysis are are documented documented inin Section 4.
Section The methodology
- 4. The methodology employed employed during during this analysis is this analysis is detailed detailed in in Section Section 5.
5.
Results obtained Results obtained areare listed listed in in Section Section 66 and in the and in the Appendices.
Appendices. Finally, Finally, Section Section 77 includes aa list includes list of of all all references references used used in in this this analysis.
analysis.
Calculation No. 040711-01, Calculation No. 040711-01, Revision Revision 00 Page Page 44 of 44 of44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. INC. CHECWORKS Power IP3 CBECWORKS IP3 Uprate Analysis Power Uprate Analysis
( 4.
- 4. Assumptions and Assumptions and Modeling Modeling Decisions Decisions The following The following assumptions assumptions and and modeling modeling decisions decisions apply apply to to the the updated updated CHECWORKS CHECWORKS model.
model.
4.1.
4.1. All data in All data in the CHECWORKS model the CHECWORKS model received received as as input input (the (the as-received as-received model) model)
[7.2] was
[7.2] assumed to was assumed to be complete and be complete and accurate.
accurate.
4.2.
4.2. An exception was An exception was made made toto Assumption Assumption 4.1 4.1 in in one one case.
case. TheThe CHECWORKS CHECWORKS HBD in HBD in the the input input model had the model had the Boiler Boiler Feed Feed Pump modeled as Pump modeled as an an electric electric pump pump instead of instead of aa steam steam driven driven pump.
pump. The The CHECWORKS CHECWORKS HBD HBD was was corrected corrected to to portray the Boiler portray the Boiler Feed Feed Pump Pump as as aa steam steam driven driven pump.
pump.
4.3.
4.3. Because the Because the Boiler Boiler Feed Pump was Feed Pump remodeled as was remodeled as aa steam steam driven driven pump pump as as discussed in discussed in Section Section 4.2, 4.2, Steam Steam CycleCycle Data Data was was input input for for the the original original power power level level in addition to the Appendix K and SPU power levels for in addition to the Appendix K and SPU power levels for this location. Flow rate this location. Flow rate was obtained was obtained from from the the original original HBDHBD [7.1.1].
[7.1.1]. Feed Feed PumpPump Turbine Turbine drain drain pressure pressure and enthalpy and enthalpy was was notnot shown shown on on the the original original HBD; HBD; therefore, therefore, the the original original pressure pressure and enthalpy and enthalpy was was assumed assumed to to be be equivalent equivalent to to the the SPU SPU pressure pressure andand enthalpy enthalpy as as shown on shown on the the SPU SPU HBDHBD [7.1.3].
[7.1.3]. Note that this Note that assumption has this assumption has little little impact impact onon the model the model as as nono components components in in the the Feed Feed Pump Pump Turbine Turbine draindrain are are modeled.
modeled.
( 4.4.
4.4. For aa number For number oflines of lines onon the the SPU SPU HeatHeat Balance Balance Diagram Diagram [7.1.3]
[7.1.3] and and Appendix Appendix K K Heat Balance Heat Balance Diagram [7.1.2], thermodynamic Diagram [7.1.2], thermodynamic and and flow flow values (pressure, values (pressure, enthalpy, and enthalpy, and flow flow rate) rate) were listed separately were listed separately for for the steam phase the steam phase andand the water the water phase phase oror for for each each train in aa parallel train in parallel train configuration. The train configuration. The overall overall flow flow rate, rate, pressure, pressure, andand enthalpy enthalpy of of these lines were these lines were calculated calculated and and entered entered in in the the CHECWORKS Steam CHECWORKS Steam Cycle Cycle (see(see Section Section 5.1.3).
5.1.3). The The combined combined flow flow rate rate was was calculated as calculated as the the sum sum of of the the liquid liquid andand steam steam flow flow rates rates (or (or the the sum sum of of multiple multiple trains), the trains), the combined combined pressure pressure waswas calculated calculated as as the the average average of of all all pressures, pressures, andand the enthalpy the enthalpy was was calculated calculated as as the the weighted weighted average average ofliquid of liquid andand steam steam enthalpy enthalpy (or the (or the weighted average of weighted average of multiple multiple trains).
trains). These These calculations calculations were were performed performed based on based on EPRI's EPRIs Guidelines Guidelines for for Plant Plant Modeling Modeling and and Evaluation Evaluation of of Component Component Inspection Data [7.6].
Inspection Data [7.6].
4.5.
4.5. Plant period Plant period datadata was was estimated estimated for for the the cycle cycle where where the the SPU SPU will occur. Start will occur. Start and and end dates end dates were estimated based were estimated based on on anticipated anticipated datesdates [7.3.1].
[7.3.1]. An estimation of An estimation of operating hours operating hours was was calculated calculated fromfrom these these dates dates based based on on calendar calendar days.
days. TheThe Water Treatment Water Treatment for for this this cycle cycle waswas modeled modeled as equivalent to as equivalent to the the most most recent recent complete operating complete operating cycle.
cycle. The The model model can can be be updated updated with with actual actual values values forfor these these inputs when inputs when thisthis data data becomes becomes available.
available.
4.6.
4.6. Due to Due to the the use use ofof the the Advanced Advanced Run Run Definition Definition feature feature in in this this model, which is model, which is required for required for accurate accurate modeling modeling of of the the power power uprate condition, CHECWORKS uprate condition, CHECWORKS Calculation No.
Calculation Revision 00 040711-01, Revision No. 040711-01, Page 55 of Page of 44 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis Analysis FAC FA Version 1.00 C Version 1.OG cannot cannot accurately accuratelyrepresent represent the the operating operating conditions conditions in in tees tees
( that combine that combine or or split split flow. In order flow. In order to to maintain maintain simplicity simplicity inin the the CHECWORKS CHECWORKS model, tees model, tees were were modeled modeled with with aa flow flow rate rate equal equal toto the the highest highest flow flow rate rate present present inin the tee.
the tee. Therefore, Therefore, thethe predicted predicted wear wear rates rates for for tees tees should should bebe used used with with caution.
caution.
4.7.
4.7. The flow The flow rate rate in in the the Feedwater Feedwater Pump Pump Recirculation Recirculation lines lines was was shown shown as as zero zero on on the SPU the SPU Heat Heat Balance Balance [7.1.3]
[7.1.3] and and Appendix Appendix K K Heat Heat Balance Balance [7.1.2].
C7.1.21. In general Ingeneral flow through flow through such such lines lines is is zero zero under under normal normal operation, operation, so so aa heat heat balance balance is is not not aa good source good source for for determining determining this this flow.
flow. Therefore, Therefore, an an assumption assumption was was made made that that the flow the flow rate rate under SPU and under SPU and Appendix Appendix K K conditions conditions was was equivalent equivalent to to the the flow flow rate under rate under original original pre-uprate pre-uprate conditions conditions asas defined defined in in the the input input CHECWORKS CHECWORKS model (the model (the as-received as-received model) [7.2]. Note model) [7.2]. Note that that all all components components in in these these lines lines are are constructed with constructed with FFAC-resistant material, so AC-resistant material, this assumption so this assumption has has little little to no impact to no impact on wear on wear rate rate predictions.
predictions.
(i, Calculation Calculation No.
No. 04071 1-01, Revision 040711-01, Revision 00 Page Page 6 of of 44 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis Analysis
( 5.
- 5. Methodology Methodology Additional input Additional input data data was was entered entered intointo the the CHECWORKS CHECWORKS model model to to model model thethe power power uprate. A uprate. A number number oftasks of tasks were were required required to to convert convert thethe previous previous Indian Indian Point Point Unit Unit 33 model into model into aa format format that that was was compatible compatible with with aa power power uprate.
uprate. The The following following section section describes the describes the tasks tasks performed performed to to enter enter power power uprate uprate data data and and toto convert convert the the model model into into aa form compatible form compatible withwith multiple multiple power power levels.
levels.
5.1.
5.1. Input SPU Input SPU Global Global DataData Additional CHECWORKS Additional CHECWORKS Power Power Levels Levels representing representing thethe SPUSPU andand Appendix Appendix K K operating conditions operating conditions werewere defined defined in in the the model model andand associated associated to to the the applicable applicable Plant Period.
Plant Period. The The following following sections sections detail detail the the steps steps involved involved in in this this task.
task.
5.1.1. CHECWORKS 5.1.1. CHECWORKS Heat Heat Balance Balance Diagram Diagram The CHECWORKS The CHECWORKS Heat Heat Balance Balance Diagram Diagram (HBD)
(HBD) was was reviewed reviewed to to ensure ensure that it that it correctly correctly portrayed portrayed plant plant configuration.
configuration. The The CHECWORKS CHECWORKS HBD HBD was compared was compared to to the the plant Heat Balance plant Heat Balance Diagrams Diagrams [7.1] [7.1] and and flow flow
[7.3.3]. A diagrams [7.3.3].
diagrams discrepancy was A discrepancy was noted noted and and corrected corrected as as discussed discussed inin Section 4.2 Section 4.2 Power Level 5.1.2. Power 5.1.2. Level Data Data
( A Plant A Plant Power Power Level Level is is defined defined forfor each each power level at power level at which which thethe plant is plant is operated for operated for aa significant significant period period of of time.
time. Two Two newnew power power levels levels were were added to added to the the model model representing representing the the SPU SPU and and Appendix Appendix K K conditions.
conditions.
Table 5.1 Table 5.1 lists lists all all power levels in power levels in the the model model and and thethe operating operating cycles cycles to to which they which they apply.
apply.
Table 5.1 Table 5.1 Power Power Level History Level History Power Power Operating Cycles Notes Level (%) (MWt) 100.00 100.00 3045.3 3045.3 Cycles 1-12A Cycles 1-12A Power Level Original Power Original Level 101.12 101.12 3079.4 3079.4 Cycles 12B-13 Cycles 12B-13 Appendix K Uprate Appendix K Uprate 104.95 104.95 3196.0 3196.0 Cycle Cycle 14 14 to to End End of of Life Life Stretch Stretch Power Power Uprate Uprate (SPU)
(SPU)
Data Data was was entered entered for for the the new new power power levels levels on on the the Power Level Form Power Level Form in in accordance with the CHECWORKS User's Guide [7.5].
accordance with the CHECWORKS User's Guide [7.5].
Table 5.2 Table 5.2 summarizes Appendix K summarizes Appendix K power power level level input input data data and and the the source source of of this this data.
data.
(
Calculation No. 040711-01, Calculation No. 040711-01, Revision Revision 0 Page 7 of Page 7 44 of44
cs/ TECHNOLOGIES, INC.
CSI TECHNOLOGIES, /NC. CHECWORKS Power IP3 CHECWORKS IP3 Uprate Analysis Power Uprate Analysis
(
Table 5.2 Table 5.2 Appendix Appendix K K Power Power LevelLevel Input Input DataData Power Level CHECWORKS Field Reference 101.12%
I Steam Rate Steam Rate (Mlblhr)
(Mlbh) I 13.186870 13.186870 I 7.1.2 7.1.2 1 Pressure (psia)
Pressure (psia) 774.4 774.4 7.1.2 7.1.2 Temp (F)
Temp (F) 5 14.5 7.1.2 I
514.5 7.1.2 Blowdown Rate Blowdown Rate (Mlblhr)
(Mlb/hr) I 0.057785 0.057785 I 7.1.2 7.1.2 Carryover (%)
Carryover (%) 0.08 0.08 7.1.2 7.1.2 Feedwater Vent Feedwater Rate (%)
Vent Rate (%) xX 7.5 7.5 Reheater Vent Reheater Vent Rate Rate (%)
(%) xX 7.5 7.5 Moisture Separator Moisture Separator Carryunder Carryunder (%) (%) xX 7.5
7.5 Notes
Appendix K Uprate. 3079.4 MWt x - Field should be left blank for a PWR.
Table 5.3 Table summarizes SPU 5.3 summarizes SPU power level input power level input datadata and and the the source of this source of this data.
data.
Table 5.3 Table SPU Power 5.3 SPU Power LevelLevel Input Input Data Data Power Level CHECWORKS Field Reference 104.95%
I Steam Steam Rate Rate (Mlblhr)
( Mlbh) I 13.783800 13.783800 I 7.1.3 7.1.3 I Pressure (psia) 760.4 7.1.3 Temp (F) 512.4 7.1.3 Blowdown Rate (Mlblhr) 0.057785 7.1.3 Carryover (%) 0.08 7.1.3 Feedwater Vent Rate (%) x 7.5 Reheater Vent Rate (%) x 7.5 Moisture Separator Carryunder (%) x 7.5 Notes: Stretch Power Uprate. 3196 MWt xx -- Field Field should should be left blank be left blank for aa PWR.
PWR.
Steam Cycle 5.1.3. Steam 5.1.3. Cycle Data Data Steam Cycle Steam Cycle Data Data isis used used by CHECWORKS to by CHECWORKS to calculate calculate chemistry chemistry conditions during wear rate analysis. It is also used to calculate operating conditions during wear rate analysis. It is also used to calculate operating conditions when conditions when the the Advanced Advanced Run Run Definition Definition feature feature isis implemented implemented (see (see Section 5.5). Steam cycle data was entered for each heat balance item for Section 5.5). Steam cycle data was entered for each heat balance item for the SPU the SPU power level and power level and the the Appendix Appendix K K power power level.
level. All data was All data was entered in accordance with EPRIs Guidelines for Plant Modeling and entered in accordance with EPRI's "Guidelines for Plant Modeling and Evaluation of Evaluation of Component Component Inspection Inspection Data" Data [7.6][7.61 and and the the CHECWORKS CHECWORKS Calculation No.
Calculation 040711-01, Revision No. 040711-01, Revision 0 Page 88 of Page of 44 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. INC. CHECWORKS Power IP3 CHECWORKS IP3 Power Uprate Uprate Analysis Users Guide User's Guide [7.5]. Table 5.4
[7.5]. Table 5.4summarizes summarizes AppendixAppendix K K steam steam cycle cycle input input
( data and data and thethe source source of this data.
of this data.
Table 5.4 Table Appendix K 5.4 Appendix K Steam Steam CycleCycle Input Input Data Data 1 Flow Rate Enthalpy Pressure Temp HBD Item Location Reference (Mlb/hr) (Btu/Ibm) (psia) (F)
FWHTR 1 Tube side outlet X X X 425.0 7.1.2 FWHTR 2 Tube side outlet X X X 374.7 7.1.2 FWHTR 3 Tube side outlet X X X 296.6 7.1.2 FWHTR 4 Tube side outlet X X X 243.0 7.1.2 FWHTR 5 Tube side outlet X X X 196.4 7.1.2 FWHTR 6 Tube side outlet X X X 155.3 7.1.2 Driven steam and drain SPUMP 1 enthalpy and pressure 0.147147 976.3 1.0 X 7.1.2 Moist Sep & Moist PreSep MSEP 1 Drains 2 0.922509 355.9 199.8 X 7.1.2 Heater Drain Tank exiting TANK 1 steam 0 338.7 197.7 X Note 4 TANK 2 Blowdown tank exiting steam 0 502.9 761.2 X Note 4 RHTR 1 Reheater Drain 0.954357 506.5 623.3 X 7.1.2 Conditions in line (Presep HPEXTLINE 1 Outlet to FWH 5)3 0.935949 1148.2 200.9 X 7.1.2 HPEXTLINE 2 Conditions in line to FWH 6 0.751563 1138.6 361.4 X 7.1.2
(
i e
LPEXTLINE 1 Conditions in line to FWH 4 0.531280 1197.4 74.54 x 7.1.2 LPEXTLINE 2 Conditions in line to FWH 3 0.447417 1075.7 31.29 X Note 5 LPEXTLINE 3 Conditions in line to FWH 2 0.458881 906.1 12.80 x Note 5 LPEXTLINE 4 Conditions in line to FWH 1 0.771656 907.0 5.55 X Note 5 xx = No value
= No value entered entered (not(not required required by by CHECWORKS).
CHECWORKS).
(1)
(1) The The HBD HBD ItemItem name name is is automatically automatically generated generated byby CHECWORKS.
CHECWORKS. Feedwater Feedwater heaters heaters are are numbered numbered sequentially sequentially in in reverse reverse flow flow order.
order. Feedwater Feedwater Heater Heater 11 is is the the feedwater feedwater heater heater closest closest toto the the steam steam generator generator (equivalent (equivalent to to heater heater 36 36 atat Indian Indian Point Point 3).
3). Extraction Extraction lines lines are are numbered numbered sequentially sequentially in in order order of of decreasing decreasing pressure.
pressure.
(2)
(2) MSEP MSEP 11 represents represents the the conditions conditions in in both both the the moisture moisture separator separator andand moisture moisture pre-separator pre-separator drain drain lines lines as as recommended recommended by by EPRI EPRI Guidelines Guidelines [7.6].
[7.6].
(3)
(3) HPEXTLINE HPEXTLINE 1 1 is is aa fictitious fictitious high-pressure high-pressure extraction extraction line line representing representing thethe steam steam lines lines between between thethe pre-pre-separator and m separator and ain separator main separator as as recommended recommended by by EPRI EPRI Guidelines Guidelines [7.6].
[7.6].
(4) Flow (4) Flow rate rate is is for for exiting exiting steam steam flow flow and and was was entered as zero entered as zero asas recommended recommended by by EPRI EPRI Guidelines Guidelines [7.6].
[7.6].
Pressure and enthalpy were obtained from the Appendix K PEPSE model [7.1.2].
Pressure and enthalpy were obtained from the Appendix K PEPSE model [7.1.2].
(5)
(5) Enthalpy Enthalpy was was calculated calculated as as the the weighted average of weighted average of the the steam steam andand liquid liquid phases.
phases. Steam Steam phase phase enthalpy enthalpy was was obtained directly from obtained directly from thethe PEPSE PEPSE diagram diagram as as the the enthalpy enthalpy after after moisture moisture removal removal inin the the LP LP Turbine.
Turbine. Liquid Liquid phase phase enthalpy was calculated as the enthalpy of saturated liquid at the pressure given on the PEPSE diagram [7.1.2].
enthalpy was calculated as the enthalpy of saturated liquid at the pressure given on the PEPSE diagram [7.1.2].
Table Table 5.5 5.5 summarizes summarizes SPU SPU steam steam cyclecycle input input data data andand the source of the source of this data.
data.
('"
Calculation Calculation No.
No. 040711-01, 040711-01, Revision Revision 00 Page Page 99 of 44 of44 I -
cs/TECHNOLOGIES, CSI TECHNOLOGIES, INC. /NC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Analysis Uprate Analysis
(
Table 5.5 Table SPU Steam 5.5 SPU Steam Cycle Cycle InputInput DataData 1 Flow Rate Enthalpy Pressure Temp HBD Item Location Reference (Mlb/hr) (Btu/lbm) (psia) (F)
FWHTR 1 Tube side outlet x x x 430.4 7.1.3 FWHTR 2 Tube side outlet x x x 377.3 7.1.3 FWHTR 3 Tube side outlet x x x 298.3 7.1.3 FWHTR 4 Tube side outlet x x x 245.2 7.1.3 FWHTR 5 Tube side outlet x x x 198.0 7.1.3 FWHTR 6 Tube side outlet x x x 156.9 7.1.3 Driven steam and drain SPUMP 11 SPUMP enthalpy and pressure 0.160926 974.8 1.0 x 7.1.3 Moist Sep & Moist PreSep MSEP 11 MSEP Drains 2 1.097732 358.7 207.2 x 7.1.3 Heater Drain Tank exiting TANK 11 TANK steam 0 342.5 203.3 x Note 4 TANK 22 TANK Blowdown tank exiting steam 0 502.8 760.4 x Note 4 RHTR 11 RHTR Reheater Drain 0.870169 504.5 620.3 x 7.1.3 Conditions in line (Presep HPEXTLINE 1 Outlet to FWH 5)3 HPEXTLINE 0.984482 1147.3 208.3 x 7.1.3 HPEXTLINE 22 Conditions in line to FWH 6 HPEXTLINE 0.852604 1155.1 388.6 x 7.1.3 LPEXTLINE 1 LPEXTLINE 1 Conditions in line to FWH 4 0.548842 1197.6 77.28 x 7.1.3 LPEXTLINE LPEXTLINE 2 2 Conditions in line to FWH 3 0.472533 1076.5 32.42 x Note 5
( LPEXTLINE 3 LPEXTLINE 3 Conditions Conditions in in line line to to FWH FWH 2 0.475753 I 905.9 2 I 0.475753 905.9 13.27 13.27 xX Note 5 Note 5 LPEXTLINE 4 LPEXTLINE Conditions in 4 Conditions inlineto line to FWH I F W H 11 0.790585 0.790585 I 905.2 905.2 5.76 5.76 xX Note 5 Note 5 xx == No No value value entered entered (not(not required required by by CHECWORKS).
CHECWORKS).
(1)
(1) The The HBD HBD ItemItem name name is is automatically automatically generated generated by by CHECWORKS.
CHECWORKS. Feedwater Feedwater heaters heaters are are numbered numbered sequentially sequentially in in reverse reverse flow flow order.
order. Feedwater Feedwater Heater is the Heater 11 is the feedwater feedwater heater heater closest closest to to the the steam steam generator generator (equivalent (equivalent to to heater heater 36 36 atat Indian Indian Point Point 3).
3). Extraction Extraction lines lines are are numbered sequentially i numbered sequentially inn order order ofof decreasing decreasing pressure.
pressure.
(2) MSEP (2) MSEP 11 represents represents the the conditions conditions in in both both the the moisture moisture separator separator and and moisture moisture pre-separator pre-separator draindrain lines lines as as recommended recommended by EPRI Guidelines byEPRl Guidelines [7.6].[7.6].
(3)
(3) HPEXTLINE HPEXTLINE 1 1 is is aa fictitious fictitious high-pressure high-pressure extraction extraction line line representing representing the the steam steam lines lines between between the the pre-pre-separator and main separator and main separator separator as as recommended recommended by by EPRI EPRl Guidelines Guidelines [7.6].
[7.6].
(4) Flow (4) Flow rate rate is is for for exiting exiting steam steam flowflow andand was was entered entered asas zero as recommended zero as recommended by by EPRI EPRl Guidelines Guidelines [7.6].
[7.6].
Pressure Pressure and and enthalpy enthalpy werewere obtained obtained fromfrom the the SPU SPU PEPSE PEPSE model model [7.1.3].
[7.1.3].
(5)
(5) Enthalpy Enthalpy was was calculated calculated as as the the weighted average of weighted average of the steam and the steam and liquid liquid phases.
phases. Steam Steam phase phase enthalpy enthalpy was was obtained obtained directly directly from from thethe PEPSE PEPSE diagram diagram as as the the enthalpy enthalpy after after moisture moisture removal removal inin the the LPLP Turbine.
Turbine. Liquid Liquid phase phase enthalpy enthalpy was was calculated calculated as as the enthalpy of the enthalpy of saturated saturated liquid liquid at at the the pressure pressure given given on on the the PEPSE PEPSE diagram diagram [7.1.3].
[7.1.3].
5.1.4.
5.1.4. Plant Plant Period Period Data Data Each power level identified Each power level identified in Table 5.1 in Table 5.1 was was associated associated to to the the correct correct operating operating cycle cycle or or cycles.
cycles. The Appendix K The Appendix K Uprate Uprate start start date date waswas obtained obtained through correspondence with plant personnel [7.3.3]. The SPU is through correspondence with plant personnel [7.3.3]. The SPU is i
scheduled scheduled for for the start of the start of Cycle Cycle 14. 14. To To include include this this power power level level inin the the Calculation No.
Calculation 040711-01, Revision No. 040711-01, Revision 00 Page Page 10 10 of of 44 44
CS/TECHNOLOGIES, CSI TECHNOLOGIES, INC. /NC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Uprate Analysis Analysis model, plant model, plant periods periods were were created created that that have have notnot yet yet occurred.
occurred. StartStart dates, dates,
( end dates, end dates, operating operating hours, hours, andand chemistry chemistry datadata was was estimated estimated for for these these periods (see periods (see Section 4.5).
Section 4.5).
5.2.
5.2. Redefinition of Redefinition CHECWORKS Lines of CHECWORKS Lines The CHECWORKS The CHECWORKS model model waswas prepared prepared for for use use ofof the the Advanced Advanced Run Run Definition Definition (see Section (see Section 5.5).
5.5). This This task task consisted consisted of of redefining redefining the the CHECWORKS CHECWORKS lines lines within the within the model model so that all so that all components components on on aa given given line line are are subject subject to to the the same same thermodynamic conditions.
thermodynamic conditions. Appendix Appendix A contains aa listing A contains listing ofof all all lines lines that that appear appear in the in the CHECWORKS CHECWORKS model. model.
For conservatism, For conservatism, the the tee tee where where flow flow raterate changed changed was was associated associated to to the the line line having the having the greatest greatest flow flow rate.
rate. Note Note thatthat the the model model willwill over-predict over-predict the the wear wear for for some sections some sections oftees of tees (see (see Section Section 4.6).
4.6).
Figure 5-1 Figure illustrates the 5-1 illustrates the procedure procedure used used to to group group components components into into lines.
lines. In the Inthe diagram, seven diagram, seven lines lines exist, exist, each each with with aa different different percentage percentage of the total of the total flow.
flow. Note Note that the that the tee is grouped tee is grouped with with the the line line number number seeing seeing thethe greatest greatest percentage percentage of of flow.
flow.
Figure 5-1 Figure 5-1 Diagram Diagram of Line Redefinition of Line Redefinition Procedure Procedure I EQUIPMENT OUTPUT EQUIPMENT OUTPUT I
100% FLO\.!
~l
~
- 2 #3 #4
- 4
- 1 i1 2 %
25%
~l 2 %
~O
- #5 II 2'
~5% .6
~to\).7 Calculation No.
Calculation 040711-01, Revision No. 040711-01, Revision 00 Page 11 Page 11 of of 44 44 II
_I_
Cs/TECHNOLOGIES, CSI TECHNOLOGIES, INC. /NC. IP3 CHECWORKS Power IP3 CBECWORKS Power Uprate Uprate Analysis Analysis Components were Components were grouped grouped into into lines lines by comparing the by comparing input CHECWORKS the input CHECWORKS
( model [7.2]
model [7.2] withwith FAC isometrics [7.7]
FAC isometrics [7.7] and and flow flow diagrams diagrams [7.3.3].
[7.3.3]. New lines were New lines were given names given names according according to to the the naming convention, below.
naming convention, below.
AA-BB.CC D AA-BB.CCD AA AA System Abbreviation
= System Abbreviation BB.CC = Multi-digit BB.CC Multi-digit code code to to identify identifl aa plant line or plant line or location location D
D Brief line description
= Briefline
= description Note that the Note that the AA-BB.CC AA-BB.CC portion portion of of the the line line name name corresponds corresponds to to the the plant line plant line name and name and component component name name prefix prefix asas taken taken from from thethe flow flow diagrams diagrams [7.3.3]
[7.3.3] and and FAC isometrics FAC isometrics [7.7]. [7.7]. NewNew lineline names names werewere created created as as required required by by CHECWORKS, not CHECWORKS, where plant not where plant line line names names changed.
changed. Therefore, Therefore, some some lines lines contain components contain components with with different different component component name name prefixes, prefixes, butbut inin general general thethe component prefix component prefix and and line line name name agree.
agree. Note Note that that if if the the AA-BB.CC AA-BB.CC portion portion ofof the the line name line name was was notnot unique unique for for CHECWORKS CHECWORKS purposes, purposes, an an underscore followed underscore followed by aa I, by 1 ,2, 2 , 33 etc.
etc. was was added added to to this this portion portion of of the line name.
the line name.
For example, For example, line line name name "CD-01.IA CD-01.lA FWH FWH 31A 31A to F W H 32A" to FWH 32A is is plant line name plant line name CD-O1.lA in CD-01.1A in the the Unit Unit 33 Condensate Condensate systemsystem from from Feedwater Feedwater Heater Heater 31A3 1A toto Feedwater Heater Feedwater Heater 32A.
32A.
('
5.3.
5.3. Update Model Update Model Based Based on SPU SPU Operational Operational or or Configuration Configuration Changes Changes With an With uprate in an uprate in power, power, lineslines with with partial operation may partial operation may increase increase or or decrease decrease their operation their operation frequency fiequency (such (such asas additional additional trains trains inin operation operation or or bypass lines bypass lines now operated now operated duringduring fullfull power). Additionally, uprates power). Additionally, uprates may may callcall for for design design changes that changes that maymay result result in in piping piping configuration configuration changes.
changes.
No operational No operational or or configuration configuration changeschanges occurred occuTed due due to to the the SPU SPU [7.3.2].
[7.3.2].
5.4.
5.4. Update Network Update Network Flow Flow Analysis Definitions Analysis Definitions Network Network FlowFlow Analysis Analysis (NFA) (NFA) is is aa module module within within CHECWORKS CHECWORKS that that calculates calculates flow rate, flow rate, pressure drops, temperature pressure drops, temperature changes, changes, and and steam steam quality quality changes changes based based on piping on piping configuration configuration and and source/sink source/sink conditions.
conditions. NFA NF A is is used where operating used where operating conditions are conditions are not completely known.
not completely known. A A different different setset ofof source/sink source/si& conditions conditions is is entered for entered for each each NFANFA per per power level. Additional power level. Additional inputinput data data must must be added to be added to each NFA each NF A to reflect the to reflect the SPU SPU andand Appendix Appendix K K power levels identified power levels identified in in Section Section 5.1.2.
5.1.2.
The Indian The Indian PointPoint 33 CHECWORKS CHECWORKS model model diddid not not contain contain any any NFA definitions; NF A definitions; therefore, therefore, no no updates updates to to the model were the model were performed performed duringduring this task [7.2].
this task [7.2].
Calculation No.
Calculation Revision 0 040711-01, Revision No. 040711-01, Page 12 Page of 44 12 of44
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cs/ TECHNOLOGIES,INC.
CSI TECHNOLOGIES, /NC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate UDrate Analysis Analvsis 5.5.
5.5. Implement the Implement the Advanced Advanced Run Run Definition Definition
( This task This task involved involved aa redefinition redefinition of of the the source source in in which which CHECWORKS CHECWORKS obtains obtains thermodynamic conditions (pressure, enthalpy, temperature, thennodynamic conditions (pressure, enthalpy, temperature, and quality) and and quality) and flow flow rate conditions rate conditions for for aa component.
component. Previously Previously all all thennodynamic thermodynamic and and flow flow rate rate conditions had conditions had been been entered entered individually individuallyfor for each each component component on on the the component component data fonns.
data forms. However, However, the the component component fonn form allows allows only only oneone set set ofthennodynamic of thermodynamic and flow and flow rate rate conditions conditions to to be be entered entered (i.e.
(i.e. from from one one power power level).
level). Therefore, Therefore, use use of the of the component component fonn form as as the the input input forfor thermodynamic thermodynamic and and flow flow rate rate conditions conditions is is not valid, not valid, asas itit does does not not reflect reflect bothboth pre-uprate pre-uprate and and post-uprate post-uprate conditions.
conditions.
Instead, thermodynamic Instead, thermodynamic and and flow flow conditions conditions were were entered entered globally globally (see (see Section Section and linked 5.1) and 5.1) linked to to components components through through the the association association of of aa line line to to the the CHECWORKS RBD CHECWORKS HBD (except (except Z-type Z-type lines).
lines). The The following following sectionssections detail detail the the steps perfonned steps performed to to implement implement the the Advance4 Advanced Run Run Definition.
Definition.
5.5.1. Enter 5.5.1. Enter Flow Flow Factors Factors On the On the CHECWORKS CHECWORKS RBD HBD level, level, flow flow rates rates areare expressed expressed in in totals totals rather rather than for than for each each train.
train. ForFor example, example, feedwater feedwater flow flow rate rate might might be be entered entered as as 10 million 10 million pounds pounds per per hour, hour, where where eacheach train train of of aa three-train three-train system system sees sees million pounds 3.33 million 3.33 pounds per per hour.
hour. As As aa result, result, flow flow multipliers multipliers had had toto be be entered for entered for the the lines lines so that the so that the actual actual flow flow raterate isis used used to to calculate calculate wearwear rate at rate at the the component component level. level. Thus Thus forfor each each lineline aa flow flow multiplier, multiplier, or or flow flow
( factor, was factor, calculated. The was calculated. The flow factor is flow factor is used used to to adjust adjust thethe CHECWORKS CHECWORKS HBD RBD calculated calculated flow flow rate.
rate. The The calculated calculated flow flow factor factor forfor each each lineline was was entered entered on on the the ARD ARD form.
fonn.
There There are are some some exceptions exceptions to to the the use use ofof flow flow factors.
factors. The The first first is is for for lines lines and and flowflow segments segments where where NFA NF A would would be be used used to to calculate calculate operating operating conditions conditions and and flow flow rate.
rate. For For these these the the train train flow flow is is directly directly entered entered intointo the the NFANF A definitions.
definitions. Therefore, Therefore, these these lines lines the the assigned assigned flow flow factor factor is 1.O.
is 1.0.
Other Other exceptions exceptions are are made made for for some some lines lines andand flow flow segments segments where where the the ARD ARD form fonn is is used used as as the the source source of of operating operating conditions.
conditions. I n some In some cases, cases, if if the the input input source source (PEPSE (PEPSE or or HBD)
RBD) already already listedlisted flow flow rate rate per per train, train, then then the the flow flow factor factor is is set set to to 11.0
.O and and thethe train train flow flow raterate isis entered.
entered.
Flow Flow factors factors were were calculated calculated by by consulting consulting the the CHECWORKS CRECWORKS HBD, RBD, the the plant plant heatheat balance balance diagrams diagrams [7.1],[7.1], and and thethe flow flow diagrams diagrams [7.3.3].
[7.3.3]. Flow Flow factors factors for for each each line line appear appear in in Appendix Appendix A. A.
5.5.2. Enter D 5.5.2. Enter uty Factors Duty Factors The The duty duty factor factor is is used used to to specie specify the the fraction fraction of of the the total total plant plant operating operating hours that a given line was in operation. For full-time lines, the duty hours that a given line was in operation. For full-time lines, the duty factor factor is is 11.0.
.O. ForFor part-time part-time lines, lines, the the duty duty factor factor is is set set to to aa value value lessless than than one based on operation. For example, if line has full flow half of the one based on operation. For example, if a line has full flow half of the time time and and zerozero flow flow halfhalf ofof the the time, time, then then thethe lines lines would would be be modeled modeled with with full flow and the duty factor would be set to 0.5. Use of the duty factor is full flow and the duty factor would be set to 0.5. Use of the duty factor is Calculation No. 040711-01, Calculation No. 040711-01, Revision Revision 00 Page Page 1313 of of 44 44
-- I^I -I -- -I
cs/ TECHNOLOGIES, CSI TECHNOLOGIES, /NC.
INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis Analysis in accordance in accordance with with thethe recommendations recommendations of of the the EPRl EPRI Guidelines Guidelines for for Plant Plant
( Modeling and Evaluation of Component Modeling and Evaluation of Component Inspection Data [7.6]. Inspection Data [7.6].
Duty factors Duty factors were were taken taken from from thethe input input CHECWORKS CHECWORKS model model [7.2]. Duty
[7.2]. Duty factors for factors for each each line line appear appear in in Appendix Appendix A. A.
Complete Advanced 5.5.3. Complete 5.5.3. Advanced Run Run Defmition Definition Form Form for for Z-Z-Type Type LinesLines Lines not Lines not associated associated to to the the CHECWORKS CHECWORKS HBD HBD are are called called Z-type Z-type lines.
lines.
Because they Because they areare not not associated associated to to the the HBD, HBD, CHECWORKS CHECWORKS cannot cannot automatically calculate chemistry and operating automatically calculate chemistry and operating conditions for these conditions for these lines.
lines.
Therefore, when Therefore, when usingusing the the ARD ARD function, h c t i o n , the the user user must must input input notnot only only flow factors and duty factors but also thermodynamic flow factors and duty factors but also thermodynamic conditions, flow conditions, flow rate, and rate, and chemistry chemistry conditions conditions for for each each operating operating cycle.
cycle.
Z-type lines Z-type lines were were created created due due toto limitations limitations in in the the CHECWORKS CHECWORKS HBD. HBD.
In these cases, the computer model does not In these cases, the computer model does not obtain the data from the obtain the data f ro m the correct location correct location on on the the HBD, HBD, or or the the CHECWORKS CHECWORKS program program did did not not allow allow the correct the correct data data to to be be entered.
entered. For For example, example, there there isis no no global global input input into into CHECWORKS to CHECWORKS to specify specify thethe pressure, pressure, temperature, temperature, enthalpy, enthalpy, or or quality quality in in feedwater heater feedwater heater draindrain lines.
lines. Instead Instead the the model model calculates calculates the the conditions conditions in in the shell the shell side side drain drain as being equivalent as being equivalent to to tube tube side side heater heater outlet.
outlet. ThisThis isis incorrect, so incorrect, the CHECWORKS so the CHECWORKS HBD HBD was was notnot used used as the source as the source of of operating conditions operating conditions for for heater heater drain drain lines. Instead, operating lines. Instead, operating conditions conditions for heater for heater draindrain lines lines were were entered entered on on the the ARD ARD form. form.
Appendix A Appendix A lists all the lists all the lines in the lines in the model model and and includes includes whether whether or or not not the the line is line is aa Z-type Z-type line.line.
For Z-type For Z-type lines,lines, thermodynamic thermodynamic data data andand flow flow rate rate was obtained from was obtained from thethe Heat Balance Heat Balance Diagrams Diagrams [7.1]. [7.1].
5.5.4. Set 5.5.4. Set Wear Wear Rate Rate Analysis Analysis SourceSource of of Data Data Option Option The The CHECWORKS CHECWORKS model model allows allows the user to the user to specify specify the the source source of of component component operatingoperating conditions. Component operating conditions. Component operating conditions conditions can can come from come from one one of of four four locations:
locations: the the CHECWORKS CHECWORKS HBD, HBD, the the Component Component form, form, an an NFA, NF A, or or the the ARD.
ARD. During During wear wear rate rate analysis, analysis, CHECWORKS CHECWORKS can can use use the the operating operating conditions conditions storedstored at at the the component component level (COMP),
level ("COMP"), determine determine the operating conditions the operating conditions basedbased upon upon steam steam cycle data cycle data and and Advanced Advanced Run Run Definition Definition Flow Flow Factors Factors (HBD),
("HBD"), use use thethe operating operating conditions conditions enteredentered on on the the Advanced Advanced Run Run Definition Definition form form only only
("ARD"), or (ARD), or toto use use thethe operating operating conditions conditions calculated calculated usingusing an an NFA NFA (NFA).
("NFA"). For For allall cases, cases, thethe option option NFA->HBD->ARD->COMP "NFA->HBD->ARD->COMP" was was selected.
selected. This This directs directs CHECWORKS CHECWORKS to to preferentially preferentially use use Network Network Flow Flow Analysis Analysis first first (if it exists (ifit exists for for the the line),
line), followed followed by by the the ARD ARD (for (for Z-type Z-type lines),
lines), the the HBDHBD (for (for all all remaining remaining lines),
lines), andand finally finally the the component.
component.
( The The option option NFA->HBD->ARD->COMP "NFA->HBD->ARD->COMP" was was selected selected for for all all lines lines since since the the model model includes includes multiple multiple power power levels.
levels.
Calculation No.
Calculation No. 04071 1-01, Revision 040711-01, Revision 00 Page Page 1414 of of 44 44
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CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. INC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Uprate Analysis Analysis 5.6.
5.6. Perform Wear Perform Wear Rate Rate Analysis Analysis
( Wear Rate Wear Rate Analysis Analysis (WRA)
(WRA) is is aa module module within within CHECWORKS CHECWORKS that that provides provides predicted wear predicted wear rates rates and and remaining remaining service service lives lives for for each each modeled modeled component.
component.
WRA was WRA was run runonon every every component component so that the so that the predicted predicted wear wear rates rates include include the the SPU conditions.
SPU conditions. WRA includes an WRA includes an error-trapping error-trapping routine, routine, so that discrepancies so that discrepancies will be will be identified identified and and corrected.
corrected. WRA WRA was was performed performed successfully successfully without without error.
error.
5.7.
5.7. Quanti@ Effect Quantify Effect of Stretch Power of Stretch Power Uprate Uprate An analysis An analysis waswas performed performed to to calculate calculate thethe change change in in CHECWORKS CHECWORKS predictedpredicted wear rates wear rates due due toto the the SPU SPU conditions.
conditions. Wear Wear Rate Rate Analysis Analysis was was performed performed forfor two two periods representing periods representing the the original original power power level level and and the the SPU SPU power power level.
level. The The water water treatment for treatment for these these two periods was two periods was modeled modeled as identical, so as identical, wear rate so wear rate changes changes areare due to due to SPU SPU conditions conditions only.
only. In both cases, Inboth cases, Wear Wear Rate Rate Analysis Analysis was was performed performed using Pass 22 methods, using Pass methods, where where predictions predictions are are calibrated calibrated to to inspection inspection history.
history.
The analysis The analysis obtained obtained bothboth actual actual results results and and percentage percentage differences differences for for representative components representative components and and lines lines so that detailed so that detailed comparisons comparisons could could be made.
be made.
The analysis The analysis was was limited limited to to non-Chromium non-Chromium containing containing components components only,only, so so average values average values would would notnot be be skewed skewed by by these these components.
components. In In addition addition the the changes due changes due to to SPU SPU forfor some some of of the the dominant dominant parameters parameters affecting affecting FFAC wear AC wear rates (temperature, rates (temperature, steamsteam quality, quality, and flow rate) and flow rate) were were determined.
determined.
(
Calculation No.
Calculation No. 040711-01, 040711-01, Revision Revision 0 0 Page Page 1515 of of 44 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. INC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Uprate Analysis Analysis
( 6.
- 6. Results Results 6.1.
6.1. Component Level Component Level Wear WearRate Rate Changes Changes due due to SPU to SPU An analysis An analysis waswas perfonned performed on on aa sample sample ofof some some of of the components in the components in the the model model most susceptible most susceptible to to FAC.
FAC. Pass Pass22 Wear Wear Rate Rate Analysis Analysis waswas perfonned performed at at the the pre-pre-uprate, original uprate, original power power level level and and the SPU power the SPU power level.
level. The The samples samples were were determined as detennined as follows:
follows:
- 0 The five The five components components in in the the model model with with the the highest highest wear wear rates rates for for the the original, pre-uprate original, pre-uprate powerpower level level were were selected.
selected.
- 0 The five The five components components that that experienced experienced thethe greatest greatest percent percent increase increase inin wear wear rate due rate due toto the the SPUSPU (excluding (excluding chromium chromium containing containing components).
components).
The results The results of of this this analysis analysis appear appear inin Appendix Appendix B B 6.2.
6.2. Steam Cycle Steam Cycle Level Level Wear Wear Rate Rate Changes Changes due due to SPU to SPU An analysis An analysis waswas perfonned performed comparing comparing Steam Steam Cycle Cycle Level Level changes changes inin wear wear rate rate predictions due predictions due to to the SPU. Lines the SPU. Lines with with similar similar thennodynamic thermodynamic conditions conditions were were grouped together grouped together and and thethe average average component component wearwear rate rate was was calculated calculated for for each each grouping, called grouping, called aa Steam Steam Cycle Cycle Location.
Location. In In addition addition some some ofof the the dominant dominant parameters affecting FAC parameters affecting FAC wear wear rates rates (temperature, (temperature, steam steam quality, quality, and and flow flow rate) rate)
( were determined. The were detennined. The results results of of this analysis appear this analysis appear inin tabular form in tabular fonn in Appendix Appendix C. In C. I addition, results n addition, results are are summarized summarized on on aa steam steam cycle cycle drawing drawing inin Appendix Appendix C. C.
Calculation No.
Calculation No. 040711-01, 040711-01, Revision Revision 00 Page Page 16 of 44 16 of 44
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CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis Analysis
(, 7.
- 7. References References 7.1.
7.1. Indian Point Indian Point 33 Heat Heat Balance Balance Diagrams Diagrams 7.1.1. Original 7.1.1. Original HBD, HBD, 3045.3 3045.3 MWt:
MWt: NewNew York York Power Authority Indian Power Authority Indian Point Point 33 Nuclear Power Nuclear Power Plant Plant Heat Heat Balance Balance "F", 5/29/90.
F, 5/29/90.
77.1.2. Appendix K
.1.2. Appendix K HBD, HBD, 3079.4 3079.4 MWt:
MWt: Indian Indian Point Point 33 Nuclear Nuclear Power Power Plant Plant Benchmark tuned to 3- 19-03 Plant Data, Sheets 1-6, Run date "Benchmark tuned to 3-19-03 Plant Data", Sheets 1-6, Run date 1/ 10/2005.
111012005.
7.1.3. Stretch 7.1.3. Stretch Power Power Uprate Uprate HBD, HBD, 3196 3 196 MWt:
MWt: Indian Indian Point Point 33 Nuclear Nuclear Power Power Plant "Uprate Plant Uprate 3168 3 168 Core Core Power Power w/ w/0.5% Margin, Sheets 0.5% Margin", Sheets 1-6, 1-6, S&W S&W Calc Calc 59379-HU(S)-OOl Rev.
59379-HU(S)-001 Rev. 0, Attachment 8.15.
0, Attachment 8.15.
7.2.
7.2. Indian Point Indian Point 33 CHECWORKS CHECWORKS FAC FAC model, model, input input model model (as-received),
(as-received), electronic electronic files provided files provided toto CSI CSI on on 10/512004.
10/5/2004.
7.3.
7.3. Referenced Correspondence Referenced Correspondence and and Communications Communications (see (see Attachment Attachment A) A) 7.3.1. Email 7.3.1. Email from from Harry Hartjen (lP3)
Harry Hartjen (IP3) to to Daniel Daniel R.R. Poe Poe (CSI (CSI Technologies),
Technologies),
dated 10/1212004, dated 10/12/2004,regarding regarding SPUSPU implementation implementation dates, dates, CSI CSI Doc.
Doc. No.No.
( 04071 111.
04071111.
7.3.2. Email 7.3.2. from Harry Email from Harry Hartjen (IP3) to Hartjen (lP3) to Daniel Daniel R.R. Poe Poe (CSI (CSI Technologies),
Technologies),
dated 10/18/2004, regarding dated 10/18/2004, regarding operational operational and and configuration configuration changes changes due due toto SPU, SPU, CSI CSI Doc.
Doc. No.
No. 04071 113.
04071113.
7.3.3.
7.3.3. Email Email from from Ron Ron Macina Macina (IP3)
(lP3) to to Brian Brian Trudeau Trudeau (CSI (CSI Technologies),
Technologies), dated dated 1/10/2005, regarding 111012005, regarding addition addition a1al Heat Heat Balance Balance Diagrams Diagrams and and uprate uprate start start dates, dates, CSI CSI Doc.
Doc. No No 04071 140.
04071140.
7.4.
7.4. Indian Indian Point Point 33 Erosion Erosion Corrosion Corrosion Inspection Inspection Flow Flow Diagrams Diagrams Condensate Condensate & & Boiler Boiler Feed Feed Pump Pump Suction, Dwg No.
Suction, Dwg No. EC-F-20 183 Sh.
EC-F-20183 Sh. 1, 1, Rev.
Rev. 11 Condensate Condensate & & Boiler Boiler Feed Feed Pump Pump Suction, Dwg No.
Suction, Dwg No. EC-F-20 183 Sh.
EC-F-20183 Sh. 2, 2, Rev.
Rev. 22 Boiler Boiler Feedwater, Dwg No.
Feedwater, Dwg No. EC-F-20 193, Rev.
EC-F-20193, Rev. 22 Extraction Extraction Steam, Dwg No.
Steam, Dwg No. EC-F-20203 EC-F-20203 Sh. Sh. 1, 1, Rev.
Rev. 1 1 Extraction Extraction Steam, Steam, Dwg Dwg No.No. EC-F-20203 EC-F-20203 Sh. Sh. 2, 2, Rev.
Rev. 1 1 Heater Heater Drains Drains && Vents, Dwg No.
Vents, Dwg No. EC-F-20223 EC-F-20223 Sh. Sh. 1, 1, Rev.
Rev. 1 1
Heater Heater Drains & Vents, Drains & Vents, Dwg DwgNo. No. EC-F-20223 EC-F-20223 Sh. 2, 2, Rev.
Rev. 1 1
Moisture Moisture Separator and Reheater Separator and Reheater Drains Drains & & Vents, Vents, Dwg No. EC-F-20233 Dwg No. EC-F-20233 Sh. Sh. 1, 1, Rev.
Rev. 11 Moisture Separator and Reheater Drains & Vents, Dwg No. EC-F-20233 Sh. 2, Rev.
Moisture Separator and Reheater Drains & Vents, Dwg No. EC-F-20233 Sh. 2, Rev. 11 7.5.
7.5. CHECWORKS "CHECWORKS Flow-Accelerated Flow-Accelerated Corrosion Corrosion Application, Application, Version Version 1LOG .OG User User Guide, Document TR- 103198-P1-R1, October 2000.
Guide," Document TR-I03198-PI-R1, October 2000.
Calculation No.
Calculation No. 040711-01, 040711-01, Revision Revision 0 Page Page 17 of 44 17 of 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INC. INC. CHECWORKS Power IP3 CHECWORKS IP3 Power Uprate Uprate Analysis Analysis 7.6.
7.6. CHECWORKSSteamlFeedwater "CHECWORKS StedFeedwater Application, Application, Guidelines Guidelines for for Plant Plant Modeling Modeling
( and Evaluation and Evaluation of of Component Component Inspection Inspection Data",
Data, Doc.
Doc. No. Final Report, 1009599, Final No. 1009599, Report, September 2004.
September 2004.
7.7.
7.7. Indian Point Indian Point 33 F FAC Isometrics and AC Isometrics and Plan/Section PldSection Drawings Drawings Dwg No.
Dwg EC-H-5000, Rev.
No. EC-H-5000, Rev. 33 Dwg No.
Dwg EC-H-50038, Rev.
No. EC-H-50038, Rev. 22 Dwg No. EC-H-5001, DwgNo. EC-H-5001, Rev.
Rev. 44 Dwg No. EC-H-50039, DwgNo. EC-H-50039, Rev.
Rev. 33 Dwg No.
Dwg Rev. 11 EC-H-5002, Rev.
No. EC-H-5002, Dwg No.
Dwg EC-H-50040, Rev.
No. EC-H-50040, Rev. 33 Dwg No.
Dwg EC-H-5004, Rev.
No. EC-H-5004, Rev. 22 Dwg No.
Dwg EC-H-50041, Rev.
No. EC-H-50041, Rev. 33 Dwg No.
Dwg EC-H-5005, Rev.
No. EC-H-5005, Rev. 22 Dwg No.
Dwg EC-H-50042, Rev.
No. EC-H-50042, Rev. 22 Dwg No.
Dwg EC-H-5006, Rev.
No. EC-H-5006, Rev. 11 Dwg No.
Dwg EC-H-50045, Rev.
No. EC-H-50045, Rev. 11 Dwg No.
Dwg EC-H-5007, Rev.
No. EC-H-5007, Rev. 22 Dwg No.
Dwg EC-H-50046, Rev.
No. EC-H-50046, Rev. 22 Dwg No.
Dwg EC-H-5008, Rev.
No. EC-H-5008, Rev. 22 Dwg No.
Dwg EC-H-50047, Rev.
No. EC-H-50047, Rev. 22 Dwg No.
Dwg EC-H-50061, Rev.
No. EC-H-50061, Rev. 11 Dwg No.
Dwg EC-H-50048, Rev.
No. EC-H-50048, Rev. 22 Dwg No.
Dwg EC-H-50062, Rev.
No. EC-H-50062, Rev. 11 Dwg No. EC-H-50060, Rev. 11 Dwg No. EC-H-50060, Rev.
Dwg No.
Dwg EC-H-50064, Rev.
No. EC-H-50064, Rev. 11 Dwg No.
Dwg EC-H-50072, Rev.
No. EC-H-50072, Rev. 11 Dwg No.
Dwg EC-H-50071, Rev.
No. EC-H-50071, Rev. 22 Dwg No.
Dwg EC-H-50074, Rev.
No. EC-H-50074, Rev. 11 Dwg No.
Dwg EC-H-50081, Rev.
No. EC-H-50081, Rev. 22 Dwg No.
Dwg EC-H-50075, Rev.
No. EC-H-50075, Rev. 11 Dwg No.
Dwg EC-H-50082, Rev.
No. EC-H-50082, Rev. 33 Dwg No.
Dwg EC-H-50076, Rev.
No. EC-H-50076, Rev. 11 Dwg No.
Dwg EC-H-50082, Rev.
No. EC-H-50082, Rev. 33 Dwg No.
Dwg EC-H-50077, Rev.
No. EC-H-50077, Rev. 11 Dwg No.
Dwg EC-H-50009, Rev.
No. EC-H-50009, Rev. 11 Dwg No.
Dwg EC-F-50078, Rev.
No. EC-F-50078, Rev. 11 Dwg No.
Dwg EC-H-50010, No. EC-H-500 Rev. 22 10, Rev. Dwg No.
Dwg EC-H-50079, Rev.
No. EC-H-50079, Rev. 22 Dwg No.
Dwg EC-H-500 11, No. EC-H-500 11, Rev.
Rev. 11 Dwg No.
Dwg EC-H-50080, Rev.
No. EC-H-50080, Rev. 22 Dwg No.
Dwg EC-H-50012, Rev.
No. EC-H-50012, Rev. 22 Dwg No.
Dwg EC-H-50084, Rev.
No. EC-H-50084, Rev. 33 Dwg No.
Dwg EC-H-50014, Rev.
No. EC-H-50014, Rev. 11 Dwg No.
Dwg EC-H-50085, Rev.
No. EC-H-50085, Rev. 11 Dwg No.
Dwg EC-H-500 15, Rev.
No. EC-H-50015, Rev. 22 Dwg No.
Dwg EC-H-50086, Rev.
No. EC-H-50086, Rev. 11 Dwg No.
Dwg EC-H-500 16, Rev.
No. EC-H-50016, Rev. 22 Dwg No.
Dwg EC-H-50087, Rev.
No. EC-H-50087, Rev. 11 Dwg No. EC-H-50017, DwgNo. EC-H-50017, Rev.
Rev. 22 Dwg No. EC-H-50088, Rev.
Dwg No. EC-H-50088, Rev. 11 Dwg No. EC-H-50018, DwgNo. EC-H-50018, Rev.
Rev. 22 Dwg NO.
Dwg A-20 1862 No. A-201862 Dwg No.
Dwg EC-H-50020, Rev.
No. EC-H-50020, Rev. 22 Dwg NO.A-201881 DwgNo. A-20 188 1 Dwg No.
Dwg EC-H-50021, Rev.
No. EC-H-50021, Rev. 22 Dwg NO.
Dwg A-202 112 No. A-202112 Dwg No.
Dwg EC-H-50022, Rev.
No. EC-H-50022, Rev. 22 Dwg NO.
Dwg A-202 110 No. A-20211O Dwg No.
Dwg EC-H-50029, Rev.
No. EC-H-50029, Rev. 11 Dwg NO.
Dwg A-202 113 No. A-202113 Dwg No.
Dwg EC-H-50030, Rev.
No. EC-H-50030, Rev. 11 Dwg NO.
Dwg A-202 111 No. A-202111 Dwg No. EC-H-50031, DwgNo. EC-H-50031, Rev.
Rev. 22 Dwg NO.
Dwg A-201869 No. A-201869 Dwg No.
Dwg EC-H-50035, Rev.
No. EC-H-50035, Rev. 22 Calculation No.
Calculation 04071 1-01, Revision No. 040711-01, Revision 00 Page 18 Page of 44 18 of 44
_. I_ I
CS/TECHNOLOGIES, CSI TECHNOLOGIES, INC.INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis Analysis
(
Appendix A Appendix A CHECWORKS Modeled CHECWORKS Modeled Lines Lines
(
(
Calculation No. 040711-01, Calculation No. 040711-01, Appendh , Revision Appendix A A, Revision 00 Page Page 19 of 44 19 of 44
/. .-- 1 Ch C::t, IECHNOLOGIES, INC.
tECHNOLOGIES, INC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Analysis Uprate Anlllysis Op Steam Flow Flow Duty CHECWORKS line Name line Description . Cond Cycle DIagram No. S L N Factor Factor ource oc. o.
EC-F-20183 EC-F-20183 CD-O1.1A FWH CD-01.1A FWH 31A 31A to to FWH FWH 32A 32A Cond: FW Cond: FW Heater Heater 31 31A to FW A to FW Heater Heater 32A 32A SH. 1 SH.1 HBD HBD 8 8 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-01 .lB FWH CD-01.1B FWH 31B 31B to to FWH FWH 32B 32B Cond: FW Cond: FW Heater Heater 31 31B to FW B to FW Heater Heater 32B 32B SH. 1 SH.1 HBD HBD 8 8 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-O1.1C FWH CD-01.1C FWH 31C 31C to to FWH FWH 32C 32C Cond: FW Cond: FW Heater Heater 31 31C to FW C to FW Heater Heater 32C 32C SH. 1 SH.1 HBD HBD 8 8 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-02.11 SGBD HX3 CD-02.11 SGBD HX3 to to FWH FWH HDR HDR Cond:
Cond: FW FW Heaters Heaters 32 32 Outlet Outlet Header Header to SG Blowdown to SG Blowdown HX HX 33 SH. 2 SH.2 HBD HBD 7 7 0.038 1.000 0.038 1.000 EC-F-20183 EC-F-20183 CD-02.1A FWH CD-02.1A FWH 32A 3% to to HDR HDR Cond: FW Cond: FW Heater Heater 32A 32A to to Header Header SH. 1 SH.1 HBD HBD 7 7 0.333 1.000 0.333 1.000 EC-F-20183
- EC-F-20183 CD-02.1B CD-02.1 FWH 32B B FWH 32B to to HDR HDR Cond: FW Cond: FW Heater Heater 32B 32B to to Header Header SH. 1 SH.1 HBD HBD 7 7 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-02.1C FWH CD-02.1C FWH 32C 32C to to HDR HDR Cond: FW Cond: FW Heater Heater 32C 32C toto Header Header SH. 1 SH.1 HBD HBD 7 7 0.333 i 1.000 0.333 1.000 Cond: FW Cond: FW Heaters Heaters 32 32 Outlet Outlet Header Header Between Between 32B 32B EC-F-20183 EC-F-20183 CD-02.2 FWH CD-02.2 FWH 3232 OUT OUT HDR HDR Connection and Connection and 32C 32C Connection Connection SH. 1 SH.1 HBD HBD 7 7 0.667 1.000 0.667 1.000 Cond: FW Cond: FW Heaters Heaters 32 32 Outlet Outlet Header Header Between Between 32C 32C EC-F-20183 EC-F-20183 CD-02.3 FWH CD-02.3 FWH 3232 OUT OUT HDR HDR Connection and Connection and Takeoff Takeoff toto SG S G Blowdown Blowdown HX HX 33 SH. 1 SH.1 , HBD HBD 7 7 1.000 1.000 1.000 1.000 Cond: FW Cond: FW Heaters Heaters 32 32 Outlet Outlet Header Header Between Between Takeoff Takeoff to to EC-F-20183 EC-F-20183 CD-02.4 FWH CD-02.4 FWH 3232 OUT OUT HDR HDR SG Blowdown SG Blowdown HX HX 33 and and Return Return from SG Blowdown from SG Blowdown HX HX 33 SH. 2 SH.2 HBD HBD 7 7 0.962 1.000 0.962 1.000 Cond: FW Cond: FW Heaters Heaters 32 32 Outlet Outlet Header Header Between Between Return Return from from EC-F-20183 EC-F-20183 CD-02.5 FWH CD-02.S FWH 3232 OUT OUT HDR HDR SG Blowdown SG Blowdown HX HX 3 and 33C 3 and 33C Takeoff Takeoff SH. 2 SH.2 HBD HBD 7 7 1.000
- 1.000 1.000 1.000 Cond: FW Cond: FW Heaters Heaters 32 32 Outlet Outlet Header Header Between 33C Takeoff Between 33C Takeoff EC-F-20183 EC-F-20183 CD-02.6FWH CD-02.6 FWH 3232 OUT OUT HDR HDR and 33B and Takeoff 33B Takeoff SH. 2 SH.2 HBD HBD 7 7 1.000 0.667 1.000 0.667 EC-F-20 183 EC-F-20183 CD-02.8A HDR CD-02.8A HDR to to FWH FWH 33A 33A Cond: FW Cond: FW Heaters Heaters 32 32 Outlet Outlet Header Header to to FW FW Heater Heater 33A 33A SH. 2 SH.2 HBD HBD 7 7 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-02.8B HDR CD-02.8B HDR toto FWH FWH 33B 33B Cond: FW Cond: FW Heaters Heaters 32 32 Outlet Outlet Header Header to to FW FW Heater Heater 33B 338 SH. 2 SH.2 HBD HBD 7 7 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-02.8C HDR CD-02.8C HDR toto FWH FWH 33C 33C Cond: FW Cond: FW Heaters Heaters 32 32 Outlet Outlet Header Header to to FW FW Heater Heater 33C 33C SH. 2 SH.2 HBD HBD 7 7 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-02.9 FWH CD-02.9 FWH HDR HDR to to SGBD SGBD HX3 HX3 SG Blowdown Cond: SG Cond: Blowdown HX HX 3 3 to to FW FW Heaters Heaters 32 32 Outlet Outlet Header Header SH. 2 SH.2 HBD HBD 7 7 0.038 1.000 0.038 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, Appendix A, Revision 00 A, Revision Page 20 Page of 44 20 of 44
rc- -- . -.
CSI C~, fECHNOLOGIES, fECHNOLOGIES, INC. INC. CHECWORKS Power IP3 CHECWORKS IP3 Power Uprate Uprate Analysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle Diagram No. S L N Factor Factor ource oc. o.
EC-F-20183 EC-F-20183 CD-03.1A FWH CD-03.1A FWH 33A33A to to FWH FWH 34A 34A Cond: FW Cond: FW Heater Heater 33A 33A to FW Heater to FW Heater 34A 34A SH. 2 SH.2 HBD H8D 6 6 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-03.1B FWH CD-03.18 FWH 33833B to to FWH FWH 348 34B Cond: FW Cond: FW Heater Heater 33B 338 to FW Heater to FW Heater 34B 348 SH. 2 SH.2 HBD HBD 6 6 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-03.1C CD-03.1 FWH 33C C FWH 33C toto FWH FWH 34C 34C Cond: FW Cond: FW Heater Heater 33C to FW 33C to FW Heater Heater 34C 34C SH. 2 SH.2 HBD HBD 6 6 0.333 1.000 0.333 1.000 EC-F-20183 EC-F-20183 CD-04.1A FWH CD-04.1A FWH 34A34A to to FWH FWH 35A 35A Cond: FW Cond: FW Heater Heater 34A 34A to to FW FW Heater Heater 35A 35A SH. 2 SH.2 HBD HBD 5 5 1.ooo 0.333 1.000 0.333 EC-F-20 183 EC-F-20183 CD-04.1B CD-04.1 FWH 34B B FWH 34B to to FWH FWH 35B 358 Cond: FW Cond: FW Heater Heater 34B to FW 348 to FW Heater Heater 35B 35B SH. 2 SH.2 HBD HBD 5 5 1.ooo 0.333 1.000 0.333 EC-F-20183 EC-F-20183 CD-O4.1C CD-04.1 FWH 34C C FWH 34C to FWH 35C to FWH 35C Cond: FW Cond: FW Heater Heater 34C 34C to to FW FW Heater Heater 35C 35C SH. 2 SH.2 HBD HBD 5 5 1.ooo 0.333 1.000 0.333 EC-F-20183 EC-F-20183 CD-05.1A FWH CD-05.1A FWH 35A35A to to HDR HDR Cond: FW Cond: FW Heater Heater 35A to Header 35A to Header SH. 2 SH.2 HBD HBD 4 4 1.000 0.333 1.000 0.333 EC-F-20183 EC-F-20183 CD-05.1B CD-05.1 FWH 35B B FWH 358 to to HDR HDR Cond: FW Cond: FW Heater Heater 35B 358 to to Header Header SH. 2 SH.2 HBD HBD 4 4 1.000 0.333 1.000 0.333 EC-F-20183 EC-F-20183 CD-05.1C CD-05.1 FWH 35C C FWH 35C to to HDR HDR Cond: FW Cond: FW Heater Heater 35C 3% toto Header Header SH. 2 SH.2 HBD HBD 4 4 0.333 1.000 0.333 1.000 Cond: FW Cond: FW Heaters 35 Outlet Heaters 35 Outlet Header Header Between Between 35B358 EC-F-20183
- EC-F-20183 CD-05.3 FWH CD-05.3 FWH 3535 OUT OUT HDRHDR Connection and Connection and 35C 35C Connection Connection SH. 2 SH.2 HBD HBD 4 4 0.667 1.000 0.667 1.000 Cond: FW Cond: FW Heaters Heaters 35 35 Outlet Outlet Header Header Between Between 35C35C EC-F-20 183 EC-F-20183 CD-05.4 FWH CD-05.4 FWH 3535 OUT OUT HDR HDR Connection and Connection and Heater Heater Drain Drain Pump Discharge Connection Pump Discharge Connection SH.2 SH.2 HBD HBD 4 4 ,1.000 1.000 1.000 1.000 Cond: FW Cond: FW Heaters Heaters 35 35 Outlet Outlet Header Header Between Between Heater Heater Drain Drain Pump Discharge Pump Discharge Connection Connection and and Boiler Boiler Feed Feed Pump Pump Inlet Inlet EC-F-20183 EC-F-20183 CD-06.1 FWH CD-06.1 FWH 35 35 OUT OUT HDR HDR Tee Tee SH. 2 SH.2 Z-type Z-type 3 3 1.000 1.000 1.000 1.000 Cond: FW Cond: FW Heaters Heaters 35 35 Outlet Outlet Header Header to to Boiler Boiler Feed Feed Pump Pump EC-F-20183 EC-F-20183 CD-06.2A HDR CD-06.2A HDR toto BFP BFP 3131 31 31 SH. 2 SH.2 Z-type Z-type 3 3 0.500 1.000 0.500 1.000 Cond: FW Cond: FW Heaters Heaters 35 35 Outlet Outlet Header to Boiler Header to Boiler Feed Feed Pump Pump EC-F-20183 EC-F-20183 CD-06.2B HDR CD-06.2B HDR toto BFP BFP 3232 32 32 SH. 2 SH.2 Z-type Z-type 3 3 0.500 1.000 0.500 1.000 Ext Steam:
Ext Steam: HPHP Extraction Extraction from from HP HP Turbine Turbine toto FW FW Heater Heater EC-F-20203 EC-F-20203 EX-01.1HP EX-01.1 HP EXT EXT toto FWH FWH 3636 HDR HDR 36 Inlet 36 Inlet Header Header (Line (Line 11 of of 2)
- 2) Sh. 11 Sh. HBD HBD 17 17 0.500 1.000 0.500 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, Appendix A, Revision 00 A, Revision Page 21 of Page 21 of 44 44
-\ -
\
fECHNOLOGIES, INC.
C,=" (ECHNOLOGIES, /NC. CHECWORKS Power Uprate IP3 CHECWORKS Auaiysis Uprate AUalysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle Diagram No. S L N Factor Factor ource oc. o.
Ext Steam:
Ext Steam: HPHP Extraction Extraction from from HPHP Turbine Turbine to to FW FW Heater Heater EC-F-20203 EC-F-20203 EX-01.2 HP EX-01.2 HP EXT EXT to to FWH FWH 36 36 HDR HDR 36 Inlet 36 Inlet Header Header (Line (Line 2 2 of of 2)
- 2) Sh. 11 Sh. HBD HBD 17 17 0.500 0.500 1.000 1.000 Ext Steam:
Ext Steam: HPHP Extraction Extraction Header Header Between Between HP HP Turbine Turbine EC-F-20203 EC-F-20203 EX-01.3 HP EX-01.3 HP EXT EXT FWH FWH 36 36 HEADER HEADER Outlet Outlet Tee Tee and and FWFW Heater Heater 36C36C Takeoff Takeoff Sh. 11 Sh. HBD HBD 17 17 1.000 1.000 1.000 1.000 Ext Steam:
Ext Steam: HPHP Extraction Extraction Header Header Between Between FW FW Heater Heater 36C 36C EC-F-20203 EC-F-20203 EX-01,4 HP EXT EX-01.4 HP EXT FWH FWH 36 36 HEADER HEADER Takeoff Takeoff and and FWFW Heater Heater 36B 368 Takeoff Takeoff Sh. 1 Sh.1 HBD HBD 17 17 0.667 1.000 0.667 1.000 EC-F-20203 EC-F-20203 EX-01.5A HP EX-01.5A HP EX E X HDR HDR to to FWH FWH 36A 36A Ext Steam: HP Ext Steam: HP Extraction Extraction Header Header to FW Heater to FW Heater 36A 36A Sh. 1 Sh.1 HBD HBD 17 17 0.333 1.000 0.333 1.000 EC-F-20203 EC-F-20203 EX-01.5B HP EX-01.5B HP EX E X HDR HDR to to FWH FWH 36B 36B Ext Steam:
Ext Steam: HPHP Extraction Extraction Header Header to to FW FW Heater Heater 36B 368 Sh. 1 Sh.1 HBD HBD 17 17 0.333 1.000 0.333 1.000 EC-F-20203 EC-F-20203 EX-01.5C HP EX-01.5C HP EX E X HDR HDR to to FWH FWH 36C Ext Steam:
36C Ext Steam: HPHP Extraction Extraction Header Header to FW Heater to FW Heater 36C 36C Sh. 1 Sh.1 HBD HBD 17 17 0.333 1.000 0.333 1.000 Ext Steam:
Ext Steam: Moist Moist PreSeparator PreSeparator 2A 2A toto Feedwater Feedwater Heater Heater 35 35 EC-F-20203 EC-F-20203 EX-02.1 PSEP 2A EX-02.1 PSEP 2A 10" to 35 1 0 to HDR 35 HDR Inlet Header Inlet Header (10-lnch OD Line)
(10-inch OD Line) Sh. 1 Sh.1 Z-type Z-type 18 18 0.250 1.000 0.250 1.000 Ext Steam:
Ext Steam: Moist PreSeparator 11B Moist PreSeparator to Feedwater B to Feedwater Heater Heater 35 EC-F-20203 35 EC-F-20203 EX-02.11 PSEP1 EX-02.11 PSEPlB 14" to B 14" to 35 35 HDR HDR Inlet Header Inlet Header (14-lnch (14-inch OD OD Line)
Line) Sh. 1 Sh.1 Z-type Z-type 18 18 0.500 0.500 1.000 1.000 Ext Steam:
Ext Steam: Moist Moist PreSeparator B and 2B PreSeparator 11Band 28 Outlet Outlet Tee Tee to to Feedwater Heater Feedwater Heater 35 35 Inlet Inlet Header Header (Upstream (Upstream of of 14" 14" EC-F-20203 EC-F-20203 PSEP 11B&2B EX-02.12 PSEP EX-02.12 B&2B to to 35 35 HDR HDR Connection)
Connection) Sh. 1 Sh.1 Z-type Z-type 18 18 0.500 0.500 1.000 1.000 Ext Steam:
Ext Steam: Moist PreSeparator 11B Moist PreSeparator Bandand 2B 28 Outlet Outlet Tee Tee to to Feedwater Heater Feedwater Heater 35 35 Inlet Inlet Header Header (Downstream (Downstream of 14" of 14" EC-F-20203 EC-F-20203 EX-02.13 PSEP EX-02.13 PSEP 11B&2B B&2B to to 35 35 HDR HDR Connection)
Connection) Sh. 11 Sh. Z-type Z-type 18 18 0.500 0.500 1.000 1.000 Ext Steam:
Ext Steam: FWFW Heater 35 Inlet Heater 35 Inlet Header Header Between Between Moist Moist EC-F-20203 EC-F-20203 EX-02.14 FWH EX-02.14 FWH 3535 HEADER HEADER PreSeparator Outlets PreSeparator Outlets and and FWFW Heater Heater 35C 35C Takeoff Takeoff Sh.1 Sh.1 Z-type Z-type 18 18 1.000 1.000 1.000 1.000 Steam: FW Ext Steam:
Ext FW Heater Heater 35 Inlet Header 35 Inlet Header Between Between FW FW EC-F-20203 EC-F-20203 EX-02.15 FWH EX-02.15 FWH 35 35 HEADER HEADER Heater 35C Heater Takeoff and 35C Takeoff and FW FW Heater Heater 35B Takeoff 358 Takeoff Sh. 11 Sh. Z-type Z-type 18 18 0.667 1.000 0.667 1.000 Ext Steam:
Ext Steam: FWFW Heater Heater 35 35 Inlet Inlet Header Header toto Feedwater Feedwater EC-F-20203 EC-F-20203 EX-02.16 HDR EX-02.16 HDR 3535 to to FWH FWH 35A 35A Heater 35A Heater 35A Sh. 1 Sh.1 Z-type Z-type 18 18 0.333 1.000 0.333 1.000 Ext Steam:
Ext Steam: FWFW Heater Heater 35 35 Inlet Inlet Header Header toto Feedwater Feedwater EC-F-20203 EC-F-20203 EX-02.17 HDR EX-02.17 HDR 3535 to to FWH FWH 35B 358 Heater 35B Heater 35B Sh. 11 Sh. 2-type Z-type 18 18 0.333 1.000 0.333 1.000 Ext Steam:
Ext Steam: FWFW Heater Heater 35 35 Inlet Inlet Header Header toto Feedwater Feedwater EC-F-20203 EC-F-20203 EX-02.18 HDR EX-02.18 HDR 35 to FWH 35 to FWH 35C 35C Heater 35C Heater 35C Sh. 1 Sh.1 Z-type Z-type 18 18 0.333 1.000 0.333 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, Revision 00 A, Revision Appendix A, Page 22 Page of 44 22 of 44
if- h CS, {ECHNOLOGIES, c~. /ECHNOLOGIES,INC. INC. CHECWORKS Power IP3 CHECWORKS IP3 Power Uprate Uprate Analysis Analysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle DIagram No. S L N Factor Factor ource oc. o.
Ext Steam:
Ext Steam: Moist Moist PreSeparator PreSeparator 1A 1A toto Feedwater Feedwater Heater Heater 35 35 EC-F-20203 EC-F-20203 EX-02.2 PSEP EX-02.2 PSEP 1A 10" to 35 I O " to 35 HDR Inlet Header Inlet Header (10-lnch (IO-Inch ODOD Line)
Line) Sh. 1 Sh.1 Z-type 18 18 0.250 1.000 0.250 1.000 Steam: Moist Ext Steam:
Ext Moist PreSeparator PreSeparator2A 2A toto Feedwater Feedwater Heater Heater 35 EC-F-20203 35 EC-F-20203 EX-02.4 PSEP2A EX-02.4 PSEP2A 14"14" toto 35 HDR 35 HDR Inlet Header Inlet Header (14-lnch (14-Inch ODOD Line)
Line) Sh. 1 Sh.1 Z-type Z-type 18 18 0.500 1.000 0.500 1.000 Ext Steam:
Ext Steam: Moist Moist PreSeparator PreSeparator 11A and 2A A and 2A Outlet Outlet Tee Tee to to Feedwater Heater Feedwater Heater 35 35 Inlet Inlet Header Header (Upstream (Upstream ofof 14" 14" EC-F-20203 EC-F-20203 PSEP 1A&2A EX-02.6 PSEP EX-02.6 1A&2A to to 35 35 HDR HDR Connection)
Connection) Sh. 1 Sh.1 Z-type Z-type 18 18 0.500 1.000 0.500 1.000 Steam: Moist Ext Steam:
Ext Moist PreSeparator PreSeparator 1A 1A and and 2A 2A Outlet Outlet Tee Tee to to Feedwater Heater Feedwater Heater 3535 Inlet Inlet Header Header (Downstream (Downstream of of 14" 14" EC-F-20203 EC-F-20203 PSEP 11A&2A EX-02.7 PSEP EX-02.7 A&2A to to 35 35 HDR Connection)
Connection) Sh. 1 Sh.1 Z-type 18 18 0.500 1.000 0.500 1.000 Ext Steam:
Ext Steam: Moist Moist PreSeparator PreSeparator2B 2B toto Feedwater Feedwater Heater Heater 35 35 EC-F-20203 EC-F-20203 EX-02.8 PSEP 2B EX-02.8 PSEP 28 10" to 35 I O " to 35 HDR HDR Inlet Header Inlet Header (10-lnch (10-Inch ODOD Line)
Line) Sh.1 Sh.1 Z-type 18 18 0.250 1.000 0.250 1.000 Ext Steam:
Ext Steam: Moist Moist PreSeparator PreSeparator 11B B toto Feedwater Feedwater Heater 35 EC-F-20203 Heater 35 EC-F-20203 EX-02.9 PSEP 11B EX-02.9 PSEP 1 0 to B 10" to 35 35 HDR HDR Inlet Header Inlet Header (10-lnch (IO-Inch ODOD Linel Line) Sh. 1 Sh.1 Z-type .
Z-type 18 18 0.250 1.000 0.250 1.000 Ext Steam:
Ext Steam: LPLP Extraction No. 12 Extraction No. 12 from from LPLP Turbine Turbine 33 33 to to FW FW EC-F-20203 EC-F-20203 EX-03.1A LP EX-03.1A LP EXT EXT 12 12 toto FWH FWH 34A 34A Heater 34A Heater 34A Sh.2 Sh.2 HBD HBD 21 21 0.333 1.000 0.333 1.000 Steam: LP Ext Steam:
Ext LP Extraction No. 12 Extraction No. 12 from from LPLP Turbine Turbine 32 32 to to FW FW EC-F-20203 EC-F-20203 EX-03.1B LP EX-03.1B LP EXT EXT 12 12 toto FWH FWH 34B 348 Heater 34B Heater 34B Sh. 2 Sh.2 HBD HBD 21 21 0.333 1.000 0.333 1.000 Ext Steam:
Ext Steam: LPLP Extraction Extraction No.
No. 12 12 from from LPLP Turbine Turbine 31 to FW 31 to FW EC-F-20203 EC-F-20203 EX-03.1C EX-03.1 C LP LP EXT EXT 12 12 to to FWH 34C FWH 34C Heater 34C Heater 34C Sh. 2 Sh.2 HBD HBD 21 21 0.333 1.000 0.333 1.000 Ext Steam:
Ext Steam: LPLP Extraction No. 14 Extraction No. 14 from from LPLP Turbine Turbine 33 33 to to EC-F-20203 EC-F-20203 EX-04.1 LPEX14 EX-04.1 LPEX14 toto FWH33A FWH33A HDR HDR Header Upstream Header Upstream of of FW FW Heater Heater 33A 33A Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LPLP Extraction Extraction Header Header Upstream Upstream ofof FW FW Heater Heater EC-F-20203 EC-F-20203 EX-04.11 LPEX EX-04.11 LPEX FWH FWH 33B 33B ININ HDR HDR 33B 33B Sh. 2 Sh.2 HBD HBD 22 22 0.333 1.000 0.333 1.000 Steam: LP Ext Steam:
Ext LP Extraction Extraction Header Header to to FW FW Heater Heater 33B (Line 11 EC-F-20203 338 (Line EC-F-20203 EX-04.13 LP EX-04.13 LP EXT EXT 3232 to to FWH FWH 33B 33B of 2)
Of 2) Sh.2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LPLP Extraction Extraction Header Header to to FW FW Heater 33B (Line Heater 33B 2 EC-F-20203 (Line 2 EC-F-20203 EX-04.14 LP EX-04.14 LP EXT EXT 3232 to to FWH FWH 33B 33B of 2) of2J Sh. 2 Sh.2 HBD HBD 22 22 0.167 0.167 1.000 1.000 Ext Steam:
Ext Steam: LPLP Extraction No. 14 Extraction No. 14 from from LPLP Turbine Turbine 31 31 to to EC-F-20203 EC-F-20203 EX-04.15 LPEX14 EX-04.15 LPEX14 to to FWH33C FWH33C HDR HDR Header Header Upstream Upstream of of FW FW Heater Heater 33C 33C Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LPLP Extraction No. 13 Extraction No. 13 from from LPLP Turbine Turbine 31 31 to to EC-F-20203 EC-F-20203 EX-04.16 LPEX13 EX-04.16 LPEX13 to to FWH33C FWH33C HDR HDR Header Header Upstream Upstream of of FW FW Heater Heater 33C 33C Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 CalculationNo.
Calculation 040711-01, Appendix No. 040711-01, Appendix A, A, Revision Revision 00 Page 23 Page of 44 23 of 44
CSa It'ECHNOLOGIES, C~, ECHNOLOGIES, INC. INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Analysis Uprate Analysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle Diagram No. S L N Factor Factor ource oc. o.
Ext Steam:
Ext Steam: LP LP Extraction Extraction Header Header Upstream Upstream of of FW FW Heater Heater EC-F-20203 EC-F-20203 EX-04.18 LPEX EX-04.18 LPEX FWH FWH 33C 33C IN HDR IN HDR 33C 33C Sh. 2 Sh.2 HBD HBD 22 22 0.333 1.000 0.333 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction No. 13from No.13 from LP LP Turbine Turbine 33 33 to to EC-F-20203 EC-F-20203 EX-04.2 LPEX13 EX-04.2 LPEX13 to to FWH33A FWH33A HDR HDR Header Upstream Header Upstream ofof FW FW Heater Heater 33A 33A Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Steam: LP Ext Steam:
Ext LP Extraction Extraction Header Header to to FW FW Heater Heater 33C 33C (Line (Line 11 EC-F-20203 EC-F-20203 EX-04.21 LP EX-04.21 LP EXT EXT 31 31 to to FWH FWH 33C 33C of 2)
Of 2) Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction Header Header to to FW FW Heater Heater 33C 33C (Line (Line 22 EC-F-20203 EC-F-20203 EX-04.22 LP EX-04.22 LP EXT EXT 31 31 to to FWH FWH 33C 33C of 2) of 2) Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction Header Header Upstream Upstream of of FW FW Heater Heater EC-F-20203 '
EC-F-20203 EX-04.4 LPEX EX-04.4 LPEX FWH FWH 33A 33A ININ HDR HDR 33A 33A Sh. 2 Sh.2 HBD HBD 22 22 0.333 1.000 0.333 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction Header Header to to FW FW Heater Heater 33A 33A (Line (Line 11 EC-F-20203 EC-F-20203 EX-04.6 LP EX-04.6 LP EXT EXT toto FWH FWH 33A33A of 2) of 2) Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction Header Header to to FW FW Heater Heater 33A 33A (Line (Line 22 EC-F-20203 EC-F-20203 EX-04.7 LP EX-04.7 LP EXT EXT toto FWH FWH 33A33A of 2) of 2) Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction No. 14 from No.14 from LP LP Turbine Turbine 32 32 to to EC-F-20203 EC-F-20203 EX-04.8 LPEX14 EX-04.8 LPEX14 to to FWH33B FWH33B HDR HDR Header Upstream Header Upstream ofof FW FW Heater Heater 33B 33B Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction No. 13 from No.13 from LP LP Turbine Turbine 32 to 32 to EC-F-20203 EC-F-20203 EX-04.9 LPEX13 EX-04.9 LPEXI 3 toto FWH33B FWH33B HDR HDR Header Upstream Header Upstream ofof FW FW Heater Heater 33B 338 Sh. 2 Sh.2 HBD HBD 22 22 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction No. 16 from No.16 from LP LP Turbine 33 to Turbine 33 to FW FW EC-F-20203 EC-F-20203 EX-05.1A LP EX-05.1A LP EXT EXT 16 16 to to FWH FWH 32A 32A Heater 32A Heater 32A Sh. 2 Sh.2 HBD HBD 23 23 0.167 1.000 0.167 1.000 Steam: LP Ext Steam:
Ext LP Extraction Extraction No. 16 from No.16 from LP LP Turbine Turbine 32 32 to to FW FW EC-F-20203 EC-F-20203 EX-05.1B LP EX-05.1B LP EXT EXT 16 16 to to FWH FWH 32B 32B Heater 32B Heater 32B Sh. 2 Sh.2 HBD HBD 23 23 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction No. 16 from No.16 LP Turbine from LP Turbine 31 31 to to FW FW EC-F-20203 EC-F-20203 EX-05.1C LP EX-05.1C LP EXT EXT 16 16 to to FWH FW H 32C 32C Heater 32C Heater 32C Sh. 2 Sh.2 HBD
, HBD 23 23 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction No. 15 from No.15 LP Turbine from LP Turbine 33 33 to to FW FW EC-F-20203 EC-F-20203 EX-05.2A LP EX-05.2A LP EXT EXT 15 15 to to FWH FWH 32A 3% Heater 32A Heater 32A Sh. 2 Sh.2 HBD HBD 23 23 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LP LP Extraction Extraction No. 15 from No.15 LP Turbine from LP Turbine 32 to FW 32 to FW EC-F-20203 EC-F-20203 EX-05.2B LP EX-05.2B LP EXT EXT 15 to FWH 15 to FWH 32B 32B Heater 32B Heater 328 Sh. 2 Sh.2 HBD HBD 23 23 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LPLP Extraction Extraction No. 15 from No.15 from LP LP Turbine Turbine 31 31 to to FW FW EC-F-20203 EC-F-20203 EX-05.2C LP EX-05.2C LP EXT EXT 15 15 to to FWH FWH 32C 32C Heater 32C Heater 32C Sh. 2 Sh.2 HBD HBD 23 23 0.167 1.000 0.167 1.000 Ext Steam:
Ext Steam: LPLP Extraction Extraction No. 19 from No.19 from LP LP Turbine Turbine 33 to FW 33 to FW EC-F-20203 EC-F-20203 EX-O6.1A LP EX-06.1A LP EXT EXT 19 19 to to FWH FWH 31A 31A Heater 31A Heater 31A Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, A, Revision Appendix A, Revision 00 Page 24 Page of 44 24 of 44
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cb tECHNOLOGIES, INC.
C~, tECHNOLOGIES, INC. CHECWORKS Power IP3 CHECWORKS IP3 Power Uprate Uprate Analysis Analysis Op Steam ty CHECWORKS Line Name Line Description O. Flow N Cond Cycle FFIOtW FDUt tagram o. S L N ac or ac or ource oc. o.
Ext Steam:
Ext Steam: LP LP Extraction No. 19 Extraction No. 19 from from LP LP Turbine Turbine 32 32 to to FW FW EC-F-20203 EC-F-20203 EX-O6.1B LP EX-OS.1B LP EXT EXT 1919 to to FWH FWH 31B 318 Heater 31B Heater 31B Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Ext Steam: LP Extraction No. 19 from LP Turbine 31 to FW EC-F-20203 Ext Steam: LP Extraction No. 19 from LP Turbine 31 to FW EC-F-20203 EX-O6.1C LP EX-OS.1C LP EXT EXT 19to 19 to FWH FWH 31C31C Heater 31C Heater 31C Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Ext Steam:
Ext Steam: LP LP Extraction No. 17 Extraction No. 17 from from LP LP Turbine Turbine 33 33 to to FW FW EC-F-20203 EC-F-20203 EX-06.2A LP EX-OS.2A LP EXT EXT 17 17 to to FWH FWH 31A 31A Heater 31A Heater 31A Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Ext Steam:
Ext Steam: LP LP Extraction No. 17 Extraction No. 17 from from LP LP Turbine Turbine 32 32 to to FW FW EC-F-20203 EC-F-20203 EX-06.2B LP EX-OS.2B LP EXT EXT 17 17 to to FWH FWH 31B 318 Heater 31B Heater 31B Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Ext Steam:
Ext Steam: LP LP Extraction No. 17 Extraction No. 17 from from LP LP Turbine Turbine 31 31 to to FW FW EC-F-20203 EC-F-20203 EX-06.2C LP EX-OS.2C LP EXT EXT 17 17 to to FWH FWH 31C31C Heater 31C Heater 31C Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Steam: LP Ext Steam:
Ext LP Extraction No. 20 Extraction No. 20 from from LP LP Turbine 33 to Turbine 33 to FW FW EC-F-20203 EC-F-20203 EX-06.3A LP EX-OS.3A LP EXT EXT 20 20 to to FWH FWH 31A 31A Heater 31A Heater 31A Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Ext Steam:
Ext Steam: LP LP Extraction No. 20 Extraction No. 20 from from LP LP Turbine Turbine 32 32 to to FW FW EC-F-20203 EC-F-20203 EX-06.3B LP EX-OS.3B LP EXT EXT 20 20 to to FWH FWH 3131BB Heater 31B Heater 31B Sh. 2 Sh.2 HBD HBD 24 24 , 0.083 . 1.000 0.083 1.000 Ext Steam:
Ext Steam: LP LP Extraction No. 20 Extraction No. 20 from from LP Turbine 31 LP Turbine 31 to to FW FW EC-F-20203 EC-F-20203 EX-06.3C LP EX-OS.3C LP EXT EXT 20 20 toto FWH FWH 31C31C Heater 31C Heater 31C Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Steam: LP Ext Steam:
Ext LP Extraction Extraction No. 18 from No. 18 from LP LP Turbine Turbine 33 33 to to FW FW EC-F-20203 EC-F-20203 EX-06.4A LP EX-OS.4A LP EXT 18 to EXT 18 to FWH FWH 31A31A Heater 31A Heater 31A Sh. 2 Sh.2 HBD HBD 24 24 0.083 . 1.000 0.083 1.000 Ext Steam:
Ext Steam: LP LP Extraction No. 18 Extraction No. 18 from from LP Turbine 32 LPTurbine 32 to to FW FW EC-F-20203 EC-F-20203 EX-06.4B LP EX-OS.4B LP EXT EXT 18 18 to to FWH FWH 31B31B Heater 31B Heater 31B Sh. 2 Sh.2 HBD HBD 24 24 0.083 1.000 0.083 1.000 Ext Steam:
Ext Steam: LP LP Extraction No. 18 Extraction No. 18 from from LP LP Turbine Turbine 31 31 to to FW EC-F-20203 FW EC-F-20203 EX-06.4C LP EX-OS.4C LP EXT EXT 18 to FWH 18 to FWH 31C31C Heater 31C Heater 31C Sh. 2 Sh.2 HBD
- HBD 24 24 0.083 1.000 0.083 1.000 Feed:Boiler Feed: Boiler Feed Feed Pump Pump 3131 Discharge Discharge to to Recirculation Recirculation FW-01 .lA BFP FW-01.1A BFP 31 31 to RCIRC T to RCIRC T Takeoff Takeoff EC-F-20193 EC-F-20193 Z-type Z-type 22 0.500 1.000 0.500 1.000 Feed: Boiler Feed: Boiler Feed Feed Pump Pump 3232 Discharge Discharge to to Recirculation Recirculation FW-01 .lB FW-01.1 BFP 32 B BFP 32 to RCIRC T to RCIRC T Takeoff Takeoff EC-F-20193 EC-F-20193 2-type Z-type 22 0.500 1.000 0.500 1.000 Feed: Boiler Feed: Boiler Feed Feed Pump Pump 3131 Discharge Discharge Between Between Recirculation Takeoff Recirculation Takeoffand and Boiler Boiler Feed Feed Pump Discharge Pump Discharge FW-01.2A BFP31 RCIRC T to HDR FW-01.2A BFP31 RCIRC T to HDR Header EC-F-20193 Z-type ,
22 0.500 1.000 0.500 1.000 Feed: Boiler Feed: Boiler Feed Feed Pump Pump 3232 Discharge Discharge Between Between Recirculation Takeoff Recirculation Takeoff and and Boiler Boiler Feed Feed Pump Pump Discharge Discharge FW-01.28 BFP32 FW-01.2B BFP32 RCIRC RCIRC T T to to HOR HDR Header Header EC-F-20193 Z-type Z-tvpe 22 0.500 1.000 0.500 1.000 Calculation No.
Calculation No. 040711-01, Appendix A, 040711-01, Appendix A, Revision Revision 00 Page 25 Page 44 of 44 25 of
cb, tECHNOLOGIES, C~, IECHNOLOGIES,INC. /NC. CHECWORKS Power IP3 CHECWORKS IP3 Power Uprate Uprate Analysis Analysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle DIagram No. S L N Factor Factor ource oc. o.
Feed: Boiler Feed: Boiler Feed Feed Pump Pump Discharge Discharge Header Header Between Between FW-01.3 BFP FW-01.3 BFP DISCHARGE DISCHARGE HDR HDR Pumps Outlet Pumps Outlet Tee Tee and and FW FW Heater Heater 36C 36C Takeoff Takeoff EC-F-20193 EC-F-20193 Z-type Z-type 2 2 1.000 1.000 1.000 1.000 Feed: Boiler Feed: Boiler Feed Feed Pump Pump Discharge Discharge Header Header Between Between FWFW FW-01.4 BFP FW-01.4 BFP DISCHARGE DISCHARGE HDR HDR Heater 36C Heater 36C Takeoff Takeoff and and FW FW Heater Heater 36B 368 Takeoff Takeoff EC-F-20193 EC-F-20193 Z-type Z-type 2 2 0.667 1.000 0.667 1.000 Feed:Boiler Feed: Boiler Feed Feed Pump Pump Discharge Discharge Header Header to to Feedwater Feedwater FW-01.6A BFP FW-01.6A HDR to BFP HDR to FWH FWH 36A 36A Heater 36A Heater 36A EC-F-20193 EC-F-20193 Z-type Z-iype 2 2 0.333 1.000 0.333 1.000 Feed: Boiler Feed: Boiler Feed Feed Pump Pump Discharge Discharge Header Header to to Feedwater Feedwater FW-01.6B BFP FW-01.6B BFP HDR HDR toto FWH FWH 36B 368 Heater 36B Heater 36B EC-F-20193 EC-F-20193 Z-type Z-type 2 2 0.333 1.000 0.333 1.000 Feed: Boiler Feed: Boiler Feed Feed Pump Pump Discharge Discharge Header Header to to Feedwater Feedwater FW-01.6C BFP FW-01.6C BFP HDR HDR toto FWH FWH 36C 36C Heater 36C Heater 36C EC-F-20193 Z-type EC-F-20193 Z-type 2 2 0.333 0.333 1.000 1.000 FW-02.1A FWH FW-02.1A FWH 36A36A to to SG HDR SG HDR Feed: Feedwater Feed: Feedwater Heater Heater 36A 36A to S G Inlet to SG Inlet Header Header EC-F-20193 ' HBD EC-F-20193 HBD 1 1 0.333 0.333 1.000 1.000 FW-02.1B FW FWH 36B
-02.1 B FWH 368 to to SG HDR SG HDR Feed: Feedwater Feed: Feedwater Heater Heater 36B 36B to to SG Inlet Header SG Inlet Header EC-F-20193 HBD EC-F-20193 HBD 1 1 0.333 0.333 1.000 1.000 FW-02.1C FWH FW-02.1C FWH 36C36C to S G HDR to SG HDR Feed: Feedwater Feed: Feedwater Heater Heater 36C 36C to SG Inlet to SG Inlet Header Header EC-F-20193 HBD EC-F-20193 HBD 1 1 0.333
.0.333 1.000 1.000 Feed: SG Inlet Feed: SG Inlet Header Header Between Between FW FW Heater Heater 36B 368 FW-02.3 SG FW-02.3 S G INLET INLET HEADER HEADER Connection and Connection and FW FW Heater Heater 36C 36C Connection Connection EC-F-20193 EC-F-20193 HBD HBD 1 1 0.667 1.000 0.667 1.000 Feed: SG Feed: SG Inlet Inlet Header Header Between Between FW FW Heater Heater 36C 36C FW-02.4 SG INLET FW-02.4 SG INLET HEADER HEADER Connection and Connection and SG SG 31 31 Takeoff Takeoff EC-F-20193 EC-F-20193 HBD HBD 1 1 1.000 1.000 1.000 1.000 SG Inlet Feed: SG Feed: Inlet Header Header Between Between SG SG 31 Takeoff and 31 Takeoff and SG S G 32 32 FW-02.5 SG FW-02.5 SG INLET INLET HEADER HEADER Takeoff Takeoff EC-F-20193 EC-F-20193 HBD HBD 1 1 0.750 1.000
- 0.750 1.000 Feed: SG Feed: Inlet Header SG Inlet Between SG Header Between SG 3232 Takeoff Takeoff and and S SGG 34 34 FW-02.6 SG FW-02.6 SG INLET INLET HEADER HEADER Takeoff Takeoff EC-F-20193 EC-F-20193
- HBD HBD 1 1 0.500 1.000 0.500 1.000 FW-02.8A FW-02.8A SGSG HDR HDR toto SG SG 31 31 Feed: SG Feed: Inlet Header SG Inlet Header to to S G 31 SG 31 EC-F-20193 EC-F-20193 HBD HBD 1 1 0.250 0.250 ' 1.000 1.000 FW -02.8B SG FW-02.8B HDR to SG HDR to SG SG 32 32 Feed: SSG Feed: G Inlet Inlet Header Header to to SG SG 32 32 EC-F-20193 EC-F-20193 HBD
- HBD 1 1 0.250 0.250 1.000 1.000 FW-02.8C SG FW-02.8C SG HDR to SG 34 HDR to SG 34 Feed: SG Feed: Inlet Header SG Inlet to SG Header to SG 34 34 EC-F-20193 EC-F-20193 HBD
- HBD 1 1 0.250 0.250 1.000 1.000 FW-02.8D SG FW-02.8D HDR to SG HDR to SSGG 33 33 Feed: SG Feed: Inlet Header SG Inlet Header to to SG SG 33 33 EC-F-20193 EC-F-20193 HBD HBD 1 1 0.250 0.250 1.000 1.000 Feed:
Feed: Boiler Boiler Feed Feed Pump Pump 3131 Recirculation From BFP Recirculation From BFP 31 31 FW-04.1A FW-04.1A BFP BFP 31 RECIRC 31 RECIRC Discharge Discharge Line Line to to Drain Drain Collecting Collecting Tank Tank 3131 EC-F-20193 EC-F-20193 Z-type Z-type 2 2 1.000 0.020 1.000 0.020 Feed:
Feed: Boiler Boiler Feed Feed Pump Pump 3232 Recirculation From BFP Recirculation From BFP 32 32 FW-04.1 FW-04.1B B BFP BFP 3232 RECIRC RECIRC Discharge Line to Discharge Line to Drain Drain Collecting Collecting Tank Tank 3131 EC-F-20193 EC-F-20193 Z-type Z-type 2 2 1.000 0.020 1.000 0.020 EC-F-20223 EC-F-20223 HD-01 .lA FWH HD-01.1A FWH 36A 36A to to HD HD TK TK Heater Dr:
Heater Dr: FW FW Heater Heater 36A 36A Drain Drain to to Heater Heater Drain Drain Tank Tank Sh.
Sh. 1 1 Z-type Z-type 11 11 0.333 0.333 1.000 1.000 Calculation 040711-01, Appendix No. 040711-01, Calculation No. Appendix A, A, Revision Revision 00 Page 26 Page 26 of of 44 44
cb, 'ECHNOLOGIES, INC.
C~, II ECHNOLOGIES, INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Awlysis Uprate Alt41ysis Op Steam Flow Flow Duty CHECWORKS Une Name Une Description . Cond Cycle Diagram No. Source Loc. No. Factor Factor EC-F-20223 EC-F-20223 HD-O1.1B FWH HD-01.18 FWH 368 36B to to HD HD TK TK Heater Dr: FW Heater Dr: FW Heater Heater 368 36B Drain Drain to to Heater Heater Drain Drain Tank Tank Sh. 1 Sh.1 Z-type Z-tvoe 11 11 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-O1.1C HD-01.1 FWH 36C C FWH 36C to to HD HD TK TK Heater Dr:
Heater FW Heater Dr: FW Heater 36C 36C Drain Drain to to Heater Heater Drain Drain Tank Tank Sh. 1 Sh.1 Z-type Z-type 11 11 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-03.1A FWH HD-03.1A FWH 35A to HD 35A to HD TK TK Heater Dr: FW Heater Dr: FW Heater Heater 35A 35A Drain Drain to to Heater Heater Drain Drain Tank Tank Sh. 1 Sh.1 Z-type
- Z-tvoe 12 12 0.333 1.000 0.333 1,000 EC-F-20223 EC-F-20223 HD-03.1B FWH HD-03.18 FWH 358 to HD 358 to HD TK TK Heater Dr: FW Heater Dr: FW Heater Heater 358 Drain to 358 Drain to Heater Heater Drain Drain Tank Tank Sh. 1 Sh.1 Z-type Z-tvoe 12 12 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-03.1C FWH HD-03.1C FWH 35C 35C to to HD HD TK TK Heater Dr:
Heater Dr: FW FW Heater 35C Drain Heater 35C Drain to to Heater Heater Drain Drain Tank Tank Sh. 1 Sh.1 Z-type Z-tvoe 12 12 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-04.1A FWH HD-04.1A FWH 34A 34A to to FWH FWH 33A 33A Heater Dr: FW Heater Dr: FW Heater Heater 34A 34A Drain to FW Drain to FW Heater Heater 33A33A Sh. 2 Sh.2
- Z-type 13 13 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-04.16 FWH HD-04.18 FWH 348 348 to to FWH FWH 338 338 Heater Dr: FW Heater Dr: FW Heater Heater 348 34B Drain Drain to to FW FW Heater Heater 338338 Sh. 2 Sh.2 Z-type Z-tvoe 13 13 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-04.1C HD-04.1 FWH 34C C FWH 34C to to FWH FWH 33C 33C Heater Dr: FW Heater Dr: FW Heater Heater 34C 34C Drain Drain to to FW FW Heater Heater 33C33C Sh. 2 Sh.2 Z-type
- Z-tvoe 13 13 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-O6.1A FWH HD-06.1A FWH 33A to FWH 33A to FWH 32A 32A Heater Dr: FW Heater Dr: FW Heater Heater 33A 33A Drain to FW Drain to FW Heater Heater 32A32A Sh.2 Sh.2 Z-type Z-tvoe 14 14 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-O6.1B FWH HD-06.18 FWH 338 33B to to FWH FWH 328 32B Heater Dr: FW Heater Dr: FW Heater Heater 338 33B Drain Drain to to FW FW Heater Heater 32B328 Sh. 2 Sh.2 Z-type Z-type 14 14 0.333 1.000 0.333 1.000 EC-F-20223 EC-F-20223 HD-O6.1C HD-06.1 FWH 33C C FWH to FWH 33C to FWH 32C 32C Heater Dr:
Heater Dr: FW FW Heater Heater 33C 33C Drain Drain to to FW FW Heater Heater 32C32C Sh.2 Sh.2 Z-type Z-type 14 14 0.333 1.000 0.333 1.000 Heater Dr: FW Heater Dr: FW Heater Heater 32A 32A Drain Drain to to Tee Tee Upstream Upstream ofof FW FW EC-F-20223 EC-F-20223 HD-08.1A FWH HD-OB.1A FWH 32A 32A to to FWH FWH 31A 31A Heater 31A Heater 31A Sh. 2 Sh.2 Z-type Z-tvoe 15 15 0.333 1.000 0.333 1.000 Heater Dr:
Heater Dr: FW FW Heater Heater 32B 328 Drain Drain to to Tee Tee Upstream Upstream ofof FW FW EC-F-20223 EC-F-20223 HD-08.1B FWH HD-OB.1B FWH 32B 326 to to FWH FWH 31B 318 Heater 31B Heater 316 Sh. 2 Sh.2 Z-type Z-type 15 15 0.333 1.000 0.333 1.000 Dr: FW Heater Dr:
Heater FW Heater Heater 32C 32C Drain Drain to to Tee Tee Upstream Upstream of of FW FW EC-F-20223 EC-F-20223 HD-08.1C FWH HD-OB.1C FWH 32C 32C to to FWH FWH 31C 31C Heater 31C Heater 31C Sh. 2 Sh.2 Z-type Z-type 15 15 0.333 . 1.000 0.333 1.000 Dr: FW Heater Dr:
Heater FW Heater Heater 32A 32A Drain Drain from from Tee Tee Upstream Upstream ofof EC-F-20223 EC-F-20223 HD-09.3A FWH HD-09.3A FWH 32A 32A to to FWH FWH 31A 31A FW Heater FW Heater 31A 31A to to FW FW Heater Heater 31A 31A (Line (Line 11 of of 2)
- 2) Sh. 2 Sh.2 Z-type Z-tvoe 15 15 0.167 1.000 0.167 1.000 Heater Dr:FW Heater Dr: FW Heater Heater 32B 32B Drain Drain from from Tee Tee Upstream Upstream ofof EC-F-20223 EC-F-20223 HD-09.3B FWH HD-09.3B FWH 32B 326 to to FWH FWH 31318 B FW Heater FW Heater 31318 to FW B to FW Heater Heater 31 31B (Line 11 of B (Line of 2)
- 2) Sh. 2 Sh.2 Z-type Z-tvoe , 15 15 0.167 1.000 0.167 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, Appendix A, Revision 00 A, Revision Page 27 Page of 44 27 of 44
.--- /--. --a cb, ,ECHNOLOGIES, C!:t. I ECHNOLOGIES, INC./NC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate llaiysis Abalysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle Diagram No. Source L oe. No. Factor Factor Heater Dr:
Heater FW Heater Dr: FW Heater 32C 32C Drain Drain from Tee Upstream from Tee Upstream of of EC-F-20223 EC-F-20223
-ID-09.3C FWH HD-09.3C FWH 32C32C to to FWH FWH 31C31C FW Heater FW Heater 31C 31C to to FW FW Heater 31C (Line Heater 31C of 2)
(Line 11 of 2) Sh.2 Sh.2 Z-type Z-type 15 15 0.167 1.000 0.167 1.000 Heater Dr:
Heater Dr: FW FW Heater Heater 32A 32A Drain Drain from Tee Upstream from Tee Upstream of of EC-F-20223 EC-F-20223 iD-09.4A FWH HD-09.4A FWH 32A32A to to FWH FWH 31A31A FW Heater FW Heater 31A 31A to to FW FW Heater Heater 31A 31A (Line (Line 22 of of 2)
- 2) Sh. 2 Sh.2 Z-type Z-type 15 15 0.167 1.000 0.167 1.000 Heater Dr: FW Heater Dr: FW Heater Heater 32B 32B Drain Drain from from Tee Tee Upstream Upstream of of EC-F-20223 EC-F-20223 dD-09.4B FWH HD-09.4B FWH 32B to FWH 328 to FWH 31B31B FW Heater FW Heater 31B 318 to to FW FW Heater Heater 31B 318 (Line (Line 22 of of 2)
- 2) Sh. 2 Sh.2 Z-type Z-type 15 15 0.167 1.000 0.167 1.000 Dr: FW Heater Dr:
Heater FW Heater Heater 32C 32C Drain Drain from from Tee Tee Upstream Upstream of of EC-F-20223 EC-F-20223 HD-09.4C FWH HD-09.4C FWH 32C32C to to FWH FWH 31C31C FW Heater FW Heater 31C 31C to to FW FW Heater Heater 31C 31C (Line (Line 2 2 of of 2)
- 2) Sh. 2 Sh.2 Z-type Z-type 15 15 0.167
... 0.167 1.000 1.000 EC-F-20223 EC-F-20223 HD-1O.lA HD HD-10.1A HD TK TK to to HD HD PMP PMP 3131 Heater Dr: Heater Heater Dr: Heater Drain Drain Tank Tank to to Heater Heater Drain Drain Pump Pump 31 31 Sh. 11 Sh. HBD HBD 10 10 0.500 1.000 0.500 1.000 EC-F-20223 EC-F-20223 HD-10.18 HD HD-10.1B HD TK TK to to HD HD PMP PMP 3232 Heater Dr:Heater Heater Dr: Heater Drain Drain Tank Tank to to Heater Heater Drain Drain Pump Pump 32 32 Sh. 1 Sh.1 HBD HBD 10 10 0.500 1.000 0.500 1.000 Heater Dr:Heater Heater Dr: Heater Drain Drain Pump Pump 3131 Discharge Discharge to to Heater Heater EC-F-20223 EC-F-20223 HD-11.1A HD PMP HD-11 .lA HD PMP 3131 to to HDR HDR Drain Pump Drain Pump Discharge Discharge Header Header Sh. 1 Sh.1 HBD HBD 9 9 , 0.500 1.000 0.500 1.000 Heater Dr:
Heater Dr: Heater Heater Drain Drain Pump Pump 3232 Discharge Discharge to to Heater Heater EC-F-20223 EC-F-20223 HD-11.1B HD HD-11.1B HD PMP PMP 3232 to to HDR HDR Drain Pump Drain Pump Discharge Discharge Header Header Sh. 1 Sh.1 HBD HBD 9 9 0.500 1.000 0.500 1.000 Dr: Heater Heater Dr:
Heater Heater Drain Drain Pump Pump Discharge Discharge Header Header to to Connection with Connection Condensate System with Condensate System at at FW FW Heater Heater 3535 EC-F-20223 EC-F-20223 HD-12.2A HD HD-12.2A HD PMP PMP HDR HDR to to CD SYS Outlet CD SYS Outlet Header Header Sh. 1 Sh.1 HBD HBD 9 9 1.000 1.000 1.000 1.000 Moist Sep Moist Dr: Moist Sep Dr: Moist Separator Separator 33A 33A Drain Drain to to Header Header (Line (Line 11 EC-F-20233 EC-F-20233 MSD-O1.11A 11 MSEP MSD-01.11A MSEP 33A33A toto HDR HDR 3)
Of 3) of Sh. 1 Sh.1 Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Dr: Moist Sep Dr: Moist Separator Separator 33A 33A Drain Drain to to Header Header (Line (Line 2 2 EC-F-20233 EC-F-20233 MSD-O1.11A 2 MSD-01.11A 2 MSEP MSEP 33A 33A toto HDR HDR 3)
Of 3) of Sh. 1 Sh.1 Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Dr: Moist Sep Dr: Moist Separator Separator 33A 33A Drain Drain to to Header Header (Line 3 EC-F-20233 (Line 3 EC-F-20233 MSD-O1.11A 3 MSD-01.11A 3 MSEP MSEP 33A 33A toto HDR HDR 3)
Of 3) of Sh. 1 Sh.1 Z-type Z-type 19 19 1.ooo 0.056 1.000 0.056 Moist Sep Moist Dr: Moist Sep Dr: Moist Separator Separator 33B 338 Drain Drain to to Header Header (Line (Line 11 EC-F-20233 EC-F-20233 MSD-01.116 MSD-01.11 MSEP 33B 1 MSEP B 1 338 toto HDR HDR 3)
Of 3) of Sh. 2 Sh.2 Z-type Z-type 19 19 1.ooo 0.056 1.000 0.056 Moist Sep Moist Dr: Moist Sep Dr: Moist Separator Separator 33B 338 Drain Drain to to Header Header (Line (Line 2 2 EC-F-20233 EC-F-20233 MSD-01.11B MSD-01.11 2 MSEP B 2 MSEP 33B 338 toto HDR HDR 3)
Of 3) of Sh. 2 Sh.2 Z-type Z-type 19 19 0.056 1.ooo 0.056 1.000 Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator 33B 33B Drain Drain to to Header Header (Line (Line 3 3 EC-F-20233 EC-F-20233 MSD-Ol.11B MSD-O 3 MSEP 1.11 B 3 MSEP 33B 33B toto HDR HDR 3)
Of 3) of Sh. 2 Sh.2 2-type Z-type 19 19 0.056 1.ooo 0.056 1.000 CalculationNo.
Calculation 040711-01, Appendix No. 040711-01, A, Revision Appendix A, Revision 00 Page 28 Page of 44 28 of44
F - -\
CS, tECHNOLOGIES, C~, tECHNOLOGIES, INC. INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Auaiysis Altiltysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle Diagram No. S L N Factor Factor ource oe. o.
Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator 33A 33A Drain Drain Header Header Upstream Upstream EC-F-20233 EC-F-20233 WSD-O1.12A MSEP MSD-01.12A MSEP 33A DR HDR 33A DR HDR of Takeoff of Takeoff to to Moist Moist Separator Separator Drain Drain Tank Tank Sh. 1 Sh.1 Z-type Z-type 19 19 1.000 0.111 1.000 0.111 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 338 Drain Header 338 Drain Header Upstream Upstream EC-F-20233 EC-F-20233 MSD-01.128 MSEP MSD-01.128 MSEP 33833B DR DR HDR HDR of Takeoff to of Takeoff to Moist Moist Separator Separator Drain Drain Tank Tank Sh.2 Sh.2 Z-type Z-type 19 19 0.111 1.000 0.111 1.000 Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator 33A 33A Drain Drain Header Header toto Moist Moist EC-F-20233 EC-F-20233 MSD-01.13A HDR to MSD-O1.13A HDR to MSEP MSEP TK TK 33A 33A Separator Separator Drain Drain Tank Tank 33A 33A Sh. 1 Sh.1 Z-type Z-type 19 19 1.000 0.167 1.000 0.167 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 338 Drain Header 33B Drain Header toto Moist Moist EC-F-20233 EC-F-20233 MSD-01 .I MSD-01.138 HDR to 38 HDR to MSEP MSEP TK 33B Separator TK 338 Separator Drain Drain Tank 338 Tank 338 Sh. 2 Sh.2 Z-type Z-type 19 19 0.167 1.000 0.167 1.000 Moist Sep Moist Sep Dr: Moist Separator Dr: Moist Separator Drain Drain Tank Tank 33A to Heater 33A to Heater EC-F-20233 EC-F-20233 MSD-O1.14A TK MSD-01.14A TK 33A to HD 33A to HD TKTK Drain Tank Drain Tank Sh. 1 Sh.1 Z-type Z-type 19 19 0.167 1.000 0.167 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator Drain Drain Tank Tank 338 to Heater 33B to Heater EC-F-20233 EC-F-20233 MSD-O1.14B TK MSD-01.148 TK 338 33B to to HD HD TKTK Drain Tank Drain Tank Sh. 2 Sh.2 Z-type Z-type 19 19 1.000 0.167 1.000 0.167 Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator 31A 31A Drain Drain to to Header Header (Line (Line 1I EC-F-20233 EC-F-20233 MSD-O1.1A 11 MSEP MSD-01.1A MSEP 31A to HDR 31A to HDR 3)
Of 3) of Sh. 1 Sh.1 Z-type
- Z-type 19 19 1.000 0.056 1.000 0.056 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 31A 31A Drain to Header Drain to Header (Line (Line 22 EC-F-20233 EC-F-20233
Of 3) 1 Sh. 1 Sh. Z-type Z-~e 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 31A 31A Drain Drain to to Header Header (Line (Line 33 EC-F-20233 EC-F-20233 MSD-O1.1A 33 MSEP MSD-01.1A MSEP 31A to HDR 31A to HDR 3)
Of 3) of Sh. 1 Sh.1 Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator 318 31B Drain to Header Drain to Header (Line (Line 11 EC-F-20233 EC-F-20233 MSD-O1.1B 11 MSEP MSD-01.18 MSEP 31831B to HDR to HDR 3)
Of 3) of Sh. 2 Sh.2 Z-type '
Z-type 19 19 0.056 0.056 1.000 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator 31B Drain Separator 318 Drain to to Header Header (Line (Line 22 EC-F-20233 EC-F-20233 MSD-O1.1B 2 MSD-01.18 2 MSEP MSEP 318316 to HDR to HDR 3)
Of 3) of Sh. 2 Sh.2 Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator 31B Drain Separator 318 Drain to to Header (Line 33 EC-F-20233 Header (Line EC-F-20233 MSD-O1.1B 33 MSEP MSD-01.18 MSEP 318 to HDR 31B to HDR 3)
Of 3) of Sh.2 Sh.2 Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 31A 31A Drain Drain Header Header Upstream Upstream EC-F-20233 EC-F-20233 ,
MSD-O1.2A MSEP MSD-01.2A MSEP 31A DR HDR 31A DR HDR of Takeoff of Takeoff toto Moist Moist Separator Separator Drain Drain Tank Tank Sh. 1 Sh.1 Z-type Z-type 19 19 0.111 1.000 0.111 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 318 Drain Header 31B Drain Header Upstream Upstream EC-F-20233 EC-F-20233 MSD-01.28 MSEP MSD-01.28 MSEP 318 DR HDR 318 DR HDR of Takeoff of Takeoff toto Moist Moist Separator Separator Drain Drain Tank Tank Sh. 2 Sh.2 Z-type Z-type 19 19 0.111 1.000 0.111 1.000 Moist Sep Moist Sep Dr:Dr:Moist Moist Separator Separator 31A 31A Drain Drain Header Header toto Moist Moist EC-F-20233 EC-F-20233 MSD-O1.3A HDR MSD-01.3A HDR to to MSEP MSEP TK TK 31A 31A Separator Drain Separator Drain Tank Tank 31A 31A Sh.1 Sh.1 Z-type Z-type 19 19 0.167 1.000 0.167 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 318 Drain Header 31B Drain Header toto Moist Moist EC-F-20233 EC-F-20233 MSD-01.38 HDR MSD-01.38 HDR to to MSEP MSEP TK 31B TK 318 Separator Drain Separator Drain Tank 31B Tank 318 Sh. 2 Sh.2 Z-type Z-type 19 19 0.167 0.167 1.000 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, Appendix A, A, Revision Revision 00 Page of 44 29 of Page 29 44
Cb ,IECHNOLOGIES, C~, I ECHNOLOGIES, INC. INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Anct,ysis Anrlysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle DIagram No. Source Loc. No. Factor Factor Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator Drain Drain Tank Tank 31A 31A toto Heater Heater EC-F-20233 EC-F-20233 WSD-O1.4A TK MSD-01.4A TK 31A 31A to to HD HD TK TK Drain Tank Drain Tank Sh. 1 Sh.1 Z-type Z-type 19 19 0.167 1.000 0.167 1.000 Moist Sep Moist Sep Dr: Moist Separator Dr: Moist Separator Drain Drain Tank Tank 31 31B B to to Heater Heater EC-F-20233 EC-F-20233 WSD-01.48 TK MSD-01.4B TK 31B 318 to HD TK to HD TK Drain Tank Drain Tank Sh. 2 Sh.2 Z-type Z-type 19 19 0.167 1.000 0.167 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 32A 32A Drain Drain to to Header Header (Line (Line 11 EC-F-20233 EC-F-20233 MSD-O1.6A 11 MSEP MSD-01.6A MSEP 32A32A to HDR to HDR 3)
Of 3) of Sh. 11 Sh. Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Dr: Moist Sep Dr: Moist Separator Separator 32A 32A Drain Drain to to Header Header (Line (Line 2 2 EC-F-20233 EC-F-20233 MSD-O1.6A 2 MSD-01.6A 2 MSEP MSEP 32A32A to HDR to HDR 3)
Of 3) of Sh. 11 Sh. Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 32A 32A Drain Drain to to Header Header (Line (Line 3 EC-F-20233 3 EC-F-20233 MSD-O1.6A 33 MSEP MSD-01.6A MSEP 32A32A to HDR to HDR 3)
Of 3) of Sh. 1 Sh.1 Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator 32B 32B Drain Drain to to Header Header (Line (Line 11 EC-F-20233 EC-F-20233 MSD-O1.6B 11 MSEP MSD-01.6B MSEP 328328 to HDR to HDR 3)
Of 3) of Sh. 2 Sh.2 Z-type Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator 32B 32B Drain Drain to to Header Header (Line (Line 2 2 EC-F-20233 EC-F-20233 MSD-O1.6B 2 MSD-01.6B 2 MSEP MSEP 32B328 to HDR to HDR 3)
Of 3) of Sh. 2 Sh.2 2-type
- Z-type 19 19 0.056 1.000 0.056 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 32B 328 Drain Drain to to Header Header (Line (Line 3 EC-F-20233 3 EC-F-20233 MSD-O1.6B 3 MSD-01.6B MSEP 32B 3 MSEP 32B to HDR to HDR 3)
Of 3) of Sh. 2 Sh.2 Z-type Z-type 19 19 1.000 0.056 1.000 0.056 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 32A 32A Drain Drain Header Header Upstream Upstream EC-F-20233 EC-F-20233 MSD-O1.7A MSEP MSD-01.7A MSEP 32A32A DRDR HDR HDR Takeoff to of Takeoff of to Moist Moist Separator Separator Drain Drain Tank Tank Sh. 1 Sh.1 Z-type Z-type 19 19 0.111 1.000 0.111 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 32B Drain Header 328 Drain Header Upstream Upstream EC-F-20233 EC-F-20233 MSD-O1.7B MSEP MSD-01.7B MSEP 32B32B DRDR HDR HDR of Takeoff of Takeoff toto Moist Moist Separator Separator Drain Drain Tank Tank Sh.2 Sh.2 Z-type Z-type 19 19 0.111 1.000 0.111 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator 32A 32A Drain Drain Header Header to to Moist Moist EC-F-20233 EC-F-20233 MSD-O1.8A HDR MSD-01.8A HDR toto MSEP MSEP TK TK 32A 32A Separator Drain Separator Drain Tank Tank 32A 32A Sh.1 Sh.1 Z-type Z-type 19 19 0.167 1.000 0.167 1.000 Moist Sep Moist Dr:Moist Sep Dr: Moist Separator Separator 32B 32B Drain Drain Header Header to to Moist Moist EC-F-20233 EC-F-20233 MSD-01.88 HDR MSD-01.88 HDR toto MSEP MSEP TK TK 32B 32B Separator Drain Separator Drain Tank Tank 32B 328 Sh.2 Sh.2 2-type
. Z-type 19 19 1.000 0.167 1.000 0.167 Moist Sep Moist Sep Dr:Dr: Moist Moist Separator Separator Drain Drain Tank 32A to Tank 32A to Heater Heater EC-F-20233 EC-F-20233 MSD-O1.9A TK MSD-01.9A TK 32A 32A toto HD HD TK TK Drain Tank Drain Tank Sh. 11 Sh. Z-type Z-type 19 19 0.167 1.000 0.167 1.000 Moist Sep Moist Sep Dr:
Dr: Moist Moist Separator Separator Drain Drain Tank Tank 32B 32B toto Heater Heater EC-F-20233 .
MSD-O1.9B TK MSD-01.9B TK 32B 32B toto HD HD TK TK Drain Tank Drain Tank Sh. 2 Sh.2 Z-type Z-type 19 19 0.167 1.000 0.167 1.000 EC-F-20223 EC-F-20223 PD-01.1 PRESEP 11B PD-01.1 PRESEP DR to B DR to HDR HDR Presep Dr:
Presep Dr: Moisture Preseparator 11B Moisture Preseparator Drain to B Drain to Header Header Sh.1 Sh.1 Z-type Z-type 19 19 0.250 0.250 1.000 1.000 EC-F-20223 EC-F-20223 PD-01.3 PRESEP PD-01.3 PRESEP 1A 1A DRDR to to HDR HDR Presep Dr:
Presep Dr: Moisture Moisture Preseparator Preseparator 1A 1A Drain Drain to to Header Header Sh.1 Sh.1 Z-type Z-type 19 19 0.250 1.000 0.250 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, Appendix A, Revision 00 A, Revision Page 30 Page of 44 30 of 44
.- .- . .""I Ch 'ECHNOLOGIES, INC.
C~. II ECHNOLOGIES, /NC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Uprate Anillysis Analysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle Diagram No. Souree L OC. No. Factor Factor EC-F-20223 EC-F-20223 PD-01.5 PRESEP PD-01.5 PRESEP 2B DR to 28 DR to HDR HDR Presep Dr:
Presep Moisture Preseparator Dr: Moisture Preseparator2B2B Drain Drain to to Header Header Sh. 1 Sh.1 Z-type Z-type 19 19 0.250 1.000 0.250 1.000 EC-F-20223 EC-F-20223 PD-01.7 PRESEP PD-01.7 PRESEP 2A 2A DR DR toto HDR HDR Presep Dr:
Presep Dr: Moisture Moisture Preseparator Preseparator 2A 2A Drain Drain to to Header Header Sh. 1 Sh.1 Z-type Z-type 19 19 0.250 1.000 0.250 1.000 Presep Dr:Moisture Presep Dr: Moisture Preseparators Preseparators Drain Drain Header Header Between Between EC-F-20223 EC-F-20223 PD-02.2 PRESEP HDR PD-02.2 PRESEP HDR to to HD HD TK TK 1A Connection 1A Connection andand 2B 2B Connection Connection Sh. 1 Sh.1 Z-type Z-type 19 19 0.500 1.000 0.500 1.000 Dr: Moisture Presep Dr:
Presep Moisture Preseparators Preseparators Drain Drain Header Header Between Between EC-F-20223 EC-F-20223 PD-02.3 PRESEP PD-02.3 PRESEP HDR HDR to to HD HD TK TK 2B Connection 2B Connection and 2A Connection and 2A Connection Sh. 1 Sh.1 Z-type Z-type 19 19 0.750 1.000 0.750 1.000 Presep Dr:
Presep Dr: Moisture Moisture Preseparators Preseparators Drain Drain Header Header to to Heater Heater EC-F-20223 EC-F-20223 PD-02.4 PRESEP PD-02.4 PRESEP HDR HDR to to HD HD TK TK Drain Tank Drain Tank Sh. 1 Sh.1 Z-type Z-type 19 19 1.000 1.000 1.000 1.000 Reheater Dr:
Reheater Dr: Reheater Reheater 33A 33A Drain Drain to to Reheater Reheater Drain Drain Tank Tank EC-F-20233 EC-F-20233 RHD-O1.10A 11 RH RHD-01.10A RH 33A 33A toto TK TK 33A 33A 33A 33A Sh. I Sh.1 HBD HBD 20 20 0.167 1.000 0.167 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater Drain Drain Tank Tank 33A 33A to to Reheater Reheater Drain Drain EC-F-20233 EC-F-20233 RHD-O1.10A 22 TK RHD-01.10A TK 33A 33A toto A A HDR HDR Tank "A-Train" Tank "A-Train" Header Header Sh. 1 Sh.1 HBD HBD 20 20 0.167 . 1.000 0.167 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater 33B 33B Drain Drain to to Reheater Reheater Drain Drain Tank Tank EC-F-20233 EC-F-20233 RHD-O1.10B 11 RH RHD-01.10B RH 33B 33B toto TK TK 33B 33B 338 33B Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr:
Reheater Dr: Reheater Reheater Drain Drain Tank Tank 33B 33B to to Reheater Reheater Drain Drain EC-F-20233 EC-F-20233 RHD-01 . I O B 22 TK RHD-01.10B TK 33B 33B to to B HDR B HDR Tank "B-Train" Tank "B-Train" Header Header Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr:
Reheater Dr: Reheater Reheater 31A 31A Drain Drain to to Reheater Reheater Drain Drain Tank Tank EC-F-20233 EC-F-20233 RHD-O1.1A 11 RH31AtoTK31A RHD-01.1A RH 31A to TK 31A 31A 31A Sh. 1 Sh.1 HBD HBD 20 20 0.167 1.000 0.167 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater Drain Drain Tank Tank 31A 31A to to Reheater Reheater Drain Drain EC-F-20233 EC-F-20233 .
RHD-01 .lA 22 TK RHD-01.1A TK 31A 31A to to AA HDR HDR Tank "A-Train" Tank "A-Train" Header Header Sh. 11 Sh. HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr: Reheater Reheater Dr: Reheater 31 31B Drain to B Drain to Reheater Reheater Drain Drain Tank Tank EC-F-20233 EC-F-20233 RHD-O1.1B 11 RH RHD-01.1B RH 31B 318 to tOTK31B TK 31B 318 31B Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr: Reheater Reheater Dr: Reheater Drain Drain Tank Tank 31 31B to Reheater B to Reheater Drain Drain EC-F-20233 EC-F-20233 RHD-01.1B 22 TK RHD-01.1B TK 31B 31B to to B HDR B HDR Tank "B-Train" Tank "B-Train" Header Header Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater 32A 32A Drain Drain to to Reheater Reheater Drain Drain Tank Tank EC-F-20233 EC-F-20233 RHD-O1.3A 11 RH RHD-01.3A RH 32A 32A to to TK TK 32A 32A 32A 32A Sh. 1 Sh.1 HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr:
Reheater Dr: Reheater Reheater Drain Drain Tank Tank 32A 32A to to Reheater Reheater Drain Drain EC-F-20233 EC-F-20233 RHD-O1.3A 22 TK RHD-01.3A TK 32A 32A to to AA HDR HDR Tank "A-Train" Tank "A-Train" Header Header Sh. 1 Sh.1 HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr:
Reheater Reheater 32B Dr: Reheater 32B Drain Drain to to Reheater Reheater Drain Drain Tank Tank EC-F-20233 EC-F-20233 RHD-01.38 11 RH RHD-01.3B RH 32B 328 to to TK TK 32B 32B 32B 32B Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, Appendix A, Revision 00 A, Revision Page 31 Page 31 of 44 of 44
/-- .--. r '4, cb, t'ECHNOLOGIES, INC.
c~. {ECHNOLOGIES, /NC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Uprate Ahdlysis Airdiysis Op Steam Flow Flow Duty CHECWORKS Line Name Line Description . Cond Cycle DIagram No. S L N Factor Factor ource OC. o.
Reheater Dr:
Reheater Reheater Drain Dr: Reheater Drain Tank Tank 32B 328 to to Reheater Reheater Drain Drain EC-F-20233 EC-F-20233 3HD-01.38 2 TK 32B RHD-01.3B 32B to to B B HDR Tank "B-Train" Tank "B-Train" Header Header Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater Drain Drain Tanks Tanks Outlet Outlet "A-Train" "A-Train" Header Between Header Between FW FW Heater Heater 36C 36C Takeoff Takeoff and and FW FW Heater Heater EC-F-20233 EC-F-20233 RHD-02.10A TK RHD-02.10A TK AA HDR HDR toto FWH FWH 36 36 36B 368 Takeoff Takeoff Sh. 2 Sh.2 HBD HBD 20 20 0.333 1.000 0.333 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater Drain Drain Tank Tank "B-Train" "B-Train" Header to FW Header to FW EC-F-20233 EC-F-20233 RHD-02.10B B RHD-02.10B B HDR HDR to to FWH FWH 36A 36A Heater 36A Heater 36A Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr:
Reheater Dr: Reheater Reheater Drain Drain Tank Tank "A-Train" "A-Train" Header Header to to FW FW EC-F-20233 EC-F-20233 RHD-02.11A A HDR RHD-02.11AA HDR to to FWH FWH 36A 36A Heater 36A Heater 36A Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr: Reheater Reheater Dr: Reheater Drain Drain Tank Tank "B-Train" "B-Train" Header Header to to FW FW EC-F-20233 EC-F-20233 RHD-02.12B B RHD-02.12B HDR to B HDR to FWH FWH 36B 36B Heater 36B Heater 368 Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater Drain Drain Tank Tank "A-Train" "A-Train" Header Header to to FW FW EC-F-20233 EC-F-20233 RHD-02.13AA RHD-02.13A A HDR HDR to to FWH FWH 36B 36B Heater 36B Heater 36B Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater Drain Drain Tank Tank "B-Train" "B-Train" Header Header to to FW FW EC-F-20233 EC-F-20233 RHD-02.14B B RHD-02.14B B HDR HDR to to FWH FWH 36C 36C Heater 36C Heater 36C Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Dr:Reheater Reheater Dr:
Reheater Reheater Drain Drain Tank Tank "A-Train" "A-Train" Header Header to to FW FW EC-F-20233 EC-F-20233 RHD-02.15A A RHD-02.15A A HDR HDR to to FWH FWH 36C 36C Heater 36C Heater 36C Sh. 2 Sh.2 HBD HBD 20 20 0.167 1.000 0.167 1.000 Reheater Dr:
Reheater Reheater Drain Dr:Reheater Drain Tanks Tanks Outlet Outlet "B-Train" "B-Train" Header Between Header Between Tank Tank 33B 33B Connection Connectionandand Tank Tank 32B 326 EC-F-20233 EC-F-20233 RHD-02.7B TK B RHD-02.7B B HDR to FWH FWH 36 Connection Sh. 2 Sh.2 HBD HBD 20 20 1.000 0.333 . 1.000 0.333 Reheater Dr:
Reheater Reheater Drain Dr: Reheater Drain Tanks Tanks Outlet Outlet "A-Train" "A-Train" Header Between Header Between Tank Tank 33A 33A Connection Connection and and Tank Tank 31A 31A EC-F-20233 EC-F-20233 RHD-02.8A TK A HDR RHD-02.8A HDR toto FWH FWH 36 36 Connection Connection Sh. 11 Sh. HBD HBD 20 20 0.333 1.000 0.333 1.000 Reheater Dr:Reheater Reheater Dr: Reheater Drain Drain Tanks Tanks Outlet Outlet "B-Train" "B-Train" Header Between Header Between Tank Tank 32B 32B Connection Connection and and FW FW Heater Heater EC-F-20233 EC-F-20233 RHD-02.8B TK RHD-02.8B TK BB HDR HDR toto FWH FWH 36 36 36C Takeoff Sh. 2 Sh.2 HBD HBD 20 20 0.500 1.000 0.500 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater Drain Drain Tanks Tanks Outlet Outlet "A-Train" "A-Train" Header Between Header Between Tank Tank 31A 31A Connection Connection and and FW FW Heater Heater EC-F-20233 EC-F-20233 RHD-02.9A TK RHD-02.9A TK AA HDR HDR toto FWH FWH 36 36 36C Takeoff 36C Takeoff Sh. 1 Sh.1 HBD HBD 20 20 0.500 1.000 0.500 1.000 Dr: Reheater Reheater Dr:
Reheater Reheater Drain Drain Tanks Tanks Outlet Outlet "B-Train" "B-Train" Header Between Header Between FW FW Heater Heater 36C 36C Takeoff Takeoff and and FW FW Heater Heater EC-F-20233 EC-F-20233 RHD-02.9B TK B RHD-02.9B FWH 36 B HDR to FWH 368 36B Takeoff Sh. 2 Sh.2 HBD HBD 20 20 0.333 1.000 0.333 1.000 Calculation No.
Calculation 040711-01, Appendix No. 040711-01, Appendix A, A, Revision Revision 00 Page 32 Page 32 of of 44 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES,INC. INC. IP3 CHECWORKSPower IP3 CHECWORKS Power Uprate Uprate Analysis Analysis
(
Appendix B Appendix B Component Level Component Level Wear Wear RateRate Changes Changes due due to SPU to SPU
(
Calculation No. 040711-03, Calculation No. Appendix B, 040711-03, Appendix Revision 00 B, Revision Page Page 33 of 44 33 of 44
IP3 CHECWORKSPower IP3CHECWORKS PowerUprntc UprateAnalysis CSI CSITECHNOLOGIES, TECHNOLOGIES, INC. INC. Analysis
(
0.476 16.5% 196.5 206.9 10.4 35.67 26.66 -25.3% 1 rate.
EX-05.1A-OlN ES: LPTO 32 HEATERS 0.408 Typical of 6 inlet nonfes in this Wear Rate Analysis run with the highest wear 0.408 0.476 16.5% 1s.5 206.9 10.4 23.87 17.89 -25.1% 2 rate.
EX-05.1A-04N ES: LPTO32 HEATERS Typical of 3 90 deg elbows (wlin 1 pipe diameter of upstream fitting) in this 0(-05.2A-02E ES: LPTO 32 HEATERS 0.408 0.476 16.5% 196.5 206.9 10.4 22.38 17.01 -24.0% 3 Wear Rate Analysis run with the highest w a r rate.
Typical of 6 45 deg elbows (whn 1 pipe diameter of upstream fitting) in this 0(-05.1A-03E ES: LPTO 32 HEATERS 0.408 0.476 16.5% 196.5 206.9 10.4 20.33 15.45 -24.0% 4 Wear Rate Analysis run with the highest w a r rate.
,Typical of 3 45 deg elbows in this Wear Rate Analysis run with the highest wear, EX-05.2A-05E ES: LPTO32 HEATERS 0.408 0.4761 16.5%1 i96.5l 206.91 10.41 19.171 14.571 -24.0%1 5 I Irate.
EX-04.21-02P ES: LPTO33 HEATERS 0.476 0.473 -0.7% 246.1 254.8 8.7 4.10 11.91 192.1% 1 EX44.647T ES: LPTO33 HEATERS 0.476 0.473 -0.7% 246.1 254.8 8.7 4.10 11.98 192.1% 2 EX-04.602P ES: LPTO 33 HEATERS 0.476 0.473 -0.7% 246.1 254.8 8.7 4.10 11.97 192.0% 3 Typical of 2 type-15 tees in this Wear Rate Analysis run with the highest EX-04.13-07T ES: LPTO33 HEATERS I 0.4761 0.4731 -0.7%1 246.11 254.81 8.71 4.111 11.981 191.8%1 I 4 lchangeinwearrate.
(
Calculation No. 040711-01. Appendix B, Revision 0 Page34 Page of44 34of 44
CS/
CSI TECHNOLOGIES, TECHNOLOGIES, INC.
INC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Uprate Analysis Analysis
(
Appendix Appendix C C Steam Steam Cycle Level Wear Cycle Level Wear Rate Rate Changes Changes duedue to to SPU SPU
(
(
Calculation No.
Calculation 040711-03, Appendix No.040711-03, Appendix C, Revision 00 C,Revision Page 35 Page of 44 35of44 II--
CSI CSI TECHNOLOGIES, TECHNOLOGIES, INC. INC. 1p3 CHECWORKS Power IP3 CHECWORKS Power UpnteUprate AAnalysis nabu Location Wear Rate Change' Temperature 3 Steam QuaJJty' Flow Rate
( Steanl No of Avg Change Max Change Min Change Avg Absolute Avg SPU Wear Rate SPU Temp SPU QU.lllty SPU Flow Change ,n Notes Cycle Sjstern Stearn Cycle LocatiO)' Cornps Change Temp Change Quality Changl; Rate FI'Nv Rate
(%) (%) (%) Imlls yr) loc No Analyzed (mlls/vr) (dell F) (deq F) I I I 1 IMlb/hr) 101
~~~~~~---
~~-..~~~--- 1 33 , CD CD .ConnecbonfromHDPtoBFP Connection from HOP to BFP 57 57 33.5%
5% 55.3%
3% 33.3%'
3% 00.11 22.8 8 3753 375.3 66.44, 00: 0O! 1384 13.84 83%
6.3%
FWH FWH 5 to C 5 to o n n w nf Connection from rom 44 CD CD ,HDP HOP 37 37 22%,
2.2% 0%
44.0% 22.1%
1% 00.11 33.3 3 3773 377.3 57 57' 01 01 01 01 990, 9.90 55%
5.5%
55 CD CD FWH4toFWH5 FWH 4to FWH 5 46 46 55.5%
5%' 77.4%
4% 55.4%;
4% 00.22 44.7 7 2983, 298.3 44.7' 7, 0:
0 00:: 990' 9.90 55%
5.5%
66 CD CD 1FWH3toFWH4 FWH 3toFWH4 39 39 56%,
5.6% 77.3%;
3%' 55.5%
5% 00.2 2 33.9 9 2452 245.2 11.4.
4, 00:; 0O* 990 9.90 55.5%
5%
77 CD CD FWH2toFWH3 FWH 2 to FWH 3 146 146 10 10.0%0% 11 11.4%4% 92%'
9.2% 00.33 33.0 0 1980 198.0 66.22, 0, 0 0:
0' 990 9.90 55%
5.5%
88 CD CD FWHltoFWH2 FWH 1 to FWH 2 39 39 55.2%
2%: 55.2%
2%' 552%
2%' 00.22 33.7 7 1569 156.9. 11.2 2' 00 : 01 0: 990 9.90 55%
5.5%
HDP HOP Outlet OuUet toto CD CD System System ,
99 , HD HD ,Conne&on Connection 46 46 O%,
88.0% 0%
99.0% 0%
880% 00.44 55.33 3703 370.3' a9B9! 001, 001 394 3.94 76%
7.6%
10 10 ' HD HD ,HDTanktoHDP
'HD Tank to HOP 17 17 9 0%
9.0% 9 1%'
9.1% 9 0%
9.0% 00.22 22.55 3895 369.5 4-4.6:
6: 0O*, 01 0, 394' 3.94 76%
7.6%
11 11 HD HD 'FWH6toHDTank FWH 6 to HD Tank 37 37 -1
- 11%'1% -0
- 07% 7% -4
-4.9%9% 00.00 22.55 3942, 394.2 77.5' 5: Oi 0, 01 01 172 1.72 147%
14.7%
12 12 iI HD HD .FWH5toHDTank FWH 5 to HD Tank 48 48 66.3%
3% 66.3%
3% 66.3%
3% 00.11 1 1.88 3798 379.8 55.7' 7 0O[ 01 01 102 1.02 101%
10.1%
Decrease Decrease in in post-SPU post-SPU average average wear wear rate rate due due toto chemistry chemistry (hydrazine (hydrazine concconc.
decrease), which outweghs decrease). which outweighs temperature temperature increase increase toward toward peak and flow peak and flow rate rate 13 13 HD HD FWH4toFWH3 FWH 4to FWH 3 92 92 -270%
-27.0% -24
-246% 6% -38
-381% 1% -0
-07 7 1 1.99 2530 253.0 3 30 0, 00 , 0, 0 00.55 55, 9 1% increase 9.1% increase.
Decrease Decrease in in post-SPU post-SPU average average wear wear rate rate due due toto chemistry chemistry (hydrazine (hydrazine concconc.
( decrease),
decrease), which which outweighs outweighs temperature temperature increase toward increase toward peak and flow peak and flow rate rate 14 14 HD HD ,FWH3toFWH2 FWH 3to FWH 2 148 148 -58
-58.2% 2% -57
-572% 2% -62
-62.9% 9% -2
-20 0 15 1.5 2041 204.1 7 7.22 00 0O. 1 02 1.02 44%
4.4% increase increase.
Decrease Decrease in in postSPU post-SPU average average wear wear rate rate due to due to chemistry chemistry (hydrazme (hydrazine concconc.
decrease),
decrease), which which outweighs outweighs temperature temperature increase toward toward peak peak and and flow rate flow rate increase 15 15 HD HD FWH2toFWHI1 FWH2toFWH 42 42 -67 8%
-67.8% -67 5%
-675% -70 8%
-708% -1 9
-19 09 0.9 1657 165.7 32 3.2 0, 0 0, 0, 1 50 1.50 8 0% increase.
8.0% increase Locabon consists Location consists of only 88 FAC-susceptible of only FAC-suscepbblc i
components (2 components (2 nozzles nozzles & 866 valves) valves). AllAll other components other components havehave been been replaced replaced with with 17 17 , EX EX H PExtraction HP E M o n t otoFFWH WH6 6 8 8 -43 9%
-43.9% -438%
-438% -440%
-440% -4 8
-48 62 6.2 4418, 441.8 127 12.7 937 93.7 21 2.1: 0 85 0.85 20 7% FAC-resistant 20.7% FAC-resistant material.
matenal 18 18 ' EX EX ,PresepExtractiontoFWH5 Presep Extraction to FWH 5 83 83 71 7%
71.7% 78 8%
78.8% 31 3%
313% 33 33 78 7.8 3852 385.2 96 96 939' 93.9 -15
-1.5 098 0.98 60%
6.0%
, Represents conditions Represents condltrons in in both Moisture both Moisture PD 8 Moist PD& Moist Separator Separator & Pre-8Pre- Separator and Separator and MOisture Moisture Preseparator Preseparator 19 19 MSD ,Separator MSO Drains to Separator Drains HD Tank to HO Tank 227 227 29 8%
29.8% 663%
66.3% -332%
-332% 01 0.1 11 1.1 3648 384.8 43
-4.3 00 0 0 1 10 1.10 -9 8% Drains.
-98% Drains 20 20 Reheater Drain RHD , Reheater RHO Drain to FWH 66 to FWH 517 517 9 6%,
9.6% 9 7%
97% 6 7%
6.7% 03 03 34 3.4 4898 489.8 4 2
-4.2 39 3.9 19 1.9 087 0.87 93%
9.3%
Locatton contains Location contains superheated superheated steamsteam after after SPU (previously SPU (previously had had been been wetwet steam).
steam)
, Greatest percent percent change change decrease decrease in in wear wear Greatest 21 21 Ex EX LPExtractlontoFWH4 LP Extraction to FWH 4 119 119 -100 0%
-100.0% -100 0%
-1000% 100 0%
-1000% 33
-3.3 0033 0.0 71 337.1 391 391 100 100 02, 0.2; 0 55 0.55 9 1% rate 9.1% (post-SPU) rata (post-SPU).
Greatest percent Greatest percent change change increase increase in in wear wear 22 22 EX EX LPExtmbontoFWH3 LP Extraction to FWH 3 158 158 1650%
165.0% 1921%.
192.1% 83 9%
83.9% 82 82 130 13.0 2548 254.8 87 8.7 905 90.5 -51
-5.1 0 47, 0.47 -0.7% rate (post-SPU).
-0 7% rate (post-SPU) 23 23 EX EX LPExtracbontoFWH2 LP Extraction to FWH 2 30 30 -21 1 %
-21.1% 102%
10.2% -25 3%
-253% -5 4
-54 172 17.2 2069 206.9 104 10.4 751 75.1 87' 8.7 048 0.48 185%
16.5%
24 24 I W EX , L ~non
,LI' P m Oon to to fWH FWH 11 54 30 4%
30.4% 32 8%
32.8% 2 3%
2.3% 23 23 95 9.5 1683 168.3 57 5.7 ni n.l 44 4.4' 079:
0.79 185%
18.5%
Calculation No.
Calculation No.040711-01, 010711-01, Appendix Appendix C, Revision 00 C, Revision Pagel' of 44 Page 36 of44
CSI TECHNOLOGIES, CSI TECHNOLOGIES,INC. INC. CHECWORKS Power Lp3 CHECWORKS lP3 Uprate Analyrb Power Uprnte Allalysis LocatlQI' Wear Rate Change' Temperature' Steam Qua!ltyl Flow Rate'
( Stc 3n) No of Avg Change Max Change Min Change Avg Absolute A'9 SPU Wear Rate SPU Temp SPU Quadlty SPU Flow Change In <<<Oles Cycle Sy:stt'nl Stedrn Cycle Location Cornps Change II1Hls yrl Temp Change Quality Change Rate FIG'll! Rate C'/o) (%) (%j Lac No Analyzed (mllslyr) (dell F) (dell F) \ I ,,) (Mlblhr) (nl 16 HD FWH 1 ID Condenser o - -, - - - 918 1051 o, o, 229 11 4% 'v,HECWORKS model No Components from this location in the 25 MS ,Steam Gen ID HP Turbine 0 - - - - - 497,9 -11,8 99.s 1 -o.3! 12.89 5.5% CHECWORKS model.
No Components from this location in the 26 : MS Steam Gen ID Reheater Shell 0 - -, - - - 507.3 -7.9' 99.a! -o.19i 0.87 7.8% CHECWORKS model.
No Components from this Iocalion in the 27 MS HP Turbine ID Moist SeparatDr 0 - - - - - 387.3 0.9 90.3' -0,7' 12.04 4.7% CHECWORKS model.
location does not contain piping 28 MS Moist Separator ID Reheater 0 - - - - - - - - -! - - components.
No Components from thi$ location in the 29 MS Reheater ID LP Extraction 0 - - - - - 482.6 51 100' 0 9.78 6.2% CHECWORKS model.
No Components from this location in the 30 SG Steam Gen Blowdown 0 - - -. - - 512.4 -2 a Oi 0 0.06 -42.2% r.HECWORKS model.
i No Components
~: Components from from this locatmn in thi$ location in the the CHECWORKS ECWORKS model. model Temperature Temperature and and allty show no change as they were not Boiler Feed Pump Turbine shown on the p!l!Hlprate HSD so were 31 MS Drain 0 - - - - - 101.7 0 87.4! 0 0.16 37,9% assumed ID be equallD the SPU condition.
Total Components Total Analyzed=
Components Analyzed: 2312 2312 (All CHECWORKS (All CHECWORKS modeled mcdeledcomponents components except except those those containing wnbning Chromium)
Chromium)
( See Appendix (1) See (1) Appendix A A for a cross-reference for a between the cross-reference between the Steam Steam Cycle Locabon and Cycle Location and the the CHECWORKS CHECWORKS lines lines in in these locaWns these locations.
Values in (2) Values (2) in GREEN GREEN showshow where where FAC FAC has has decreased decreased while while values values in in RED RED show show where FAC has where FAC has increased.
increased In In the the wear rate change wear rate columns negative change columns negabve values are GREEN values are GREEN andand pooitIve positive values values are RED are RED.
In the (3) In (3) the temperature temperature change change field, field, values values that move toward that move toward the the FAC FAC peak (at -275 peak (at -275 deg deg FF for for 1-phase I-phase andand 300 deg deg F F for 2-phase) are for 2-phase) RED while are RED those that while those move away that move from the away from the peak peak are GREEN are GREEN.
(4)In (4) In the the quality quality change change field, values thai field. values that move toward the move toward the FAC FAC peak (at -50%)
peak (at -50%) areare RED RED while those that while those that move move _y away from from the peak are the peak are GREEN.
GREEN (5) Values Values in GREEN show in GREEN show where rate has where flow rate has decreased decreased while values in while values in RED RED show show where rate has where flow rate has increased.
increased FAC rates increase FAC rates increase wth increasing flow with looreasing rates and flow rates and decrease decrease With with decreasing decreasing Rowflow rates rates.
I
(
Cakulntion No.
Calculation No.Il407I1-01, Appendix C, 040711-01, Appendix C , Revision Revision II 0 Page 37 of 44 Pagel70f44 i
CSI TECHNOLOGIES, INC.
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CSI CSI TECHNOLOGIES, TECHNOLOGIES, INC.INC. IP3 CHECWORKS IP3 CHECWORKS Power Power Uprate Up rate Analysis Analysis
(
Attachment Attachment A A
Referenced Referenced Correspondence Correspondence andand Communications Communications
(
CalculationNo.
Calculation No. 040711-01, AttachmentA, 040711-01, Attachment Revision00 A,Revision Page39 Page 39 of of 44 44
CSI CSI TECHNOLOGIES, TECHNOLOGIES, /NC. INC. IP3 CHECWORKS IP3 CHECWORKSPower UprateAnalysis PowerUprate Analysis Reference Reference 7.3.1 7.3.1
(
i Email Email from from Harry Harry Hartjen Hartjen (IP3)
(IP3) to Daniel R.
to Daniel R. Poe Poe (CSI (CSI Technologies),
Technologies), dated dated 10/12/2004, 10/12/2004, regarding regarding SPUSPU implementation implementation dates, dates, CSI CSI Doc.
Doc. No.
No. 040711 11.
04071111.
Dan:
Dan:
Following Following are input to are input the DDIR:
to the DDIR:
No. 8A SPU No. 8A SPU operations operations are expected to are expected to be be implemented implemented on on 11/22/2004 11/2212004 at at IP2.
IP2.
No. 9A SPU No.9A SPU operations operations are expected to are expected to be implemented on be implemented on 04/08/2005 at IP3.
04/0812005 at IP3.
Harry Harry Hartjen Hartjen (91 4) 736-8356 (914) 736-8356
(
CalculationNo.
Calculation No.040711-01, 040711-01,Attachment AttachmentA, Revision00 A,Revision Page40 Page 40of of44 44
CSI TECHNOLOGIES, CSI TECHNOLOGIES, INc.
INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis Analysis Reference 7.3.2 Reference 7.3.2
(
Email from Email from Harry Harry Hartjen Hartjen (IP3) (IP3) to to Daniel Daniel R. R. Poe Poe (CSI (CSI Technologies),
Technologies), dated dated 10/18/2004, 10/18/2004, regarding operational regarding operational and and configuration configuration changes changes due due to SPU,CSI to SPU, CSI Doc.
Doc. No. 04071113.
No. 04071113.
Dan:
Dan:
Attached is Attached is the the response responsefrom from our our engineer, engineer, the the Shaw Shaw Group Group toto your your request request for for aa listing listing of of all all operational operational and/or configuration and/or configurationchanges changes due due to to the the SPU.
SPU.
Note that Note that there there areare no no operational operational and/or and/or configuration configurationchanges changes to to IP2JIP3 IPUIP3 duedue to to the the SPU.
SPU.
This information This informationwas was required required for for DDIR DDlR NO.6No. 6 andand 7.7.
Per your Per your request, request, aa hard hard copy copy set set of of IP3 IP3 FAC FAC isometric isometric drawings drawings will will be be mailed mailed today today to to your your attention.
attention.
Note that Note that drawing drawing EC-H-50077 EC-H-50077 is is not not yet yet revised revised in in this this mailing.
mailing. ForFor correct correct piping piping configuration, configuration, see see the the information II sent information sent you you for for the the 3R12 3R12 Checworks Checworks update. update.
Included in Included in this this mailing mailing is:is:
1.
- 1. Flow Accelerated Flow Accelerated CorrosionCorrosion Program Program Checworks Checworks Analysis Analysis Enhancement, Enhancement, Technical Technical Report No.
Report No. 00130-TR-001 00130-TR-001 Revision Revision 00 VolumeVolume 11 of of 1.
- 1. December, December, 2000. 2000. This This report report serves serves asas the the Unit Unit 22 Checworks Checworks Model Model documentation.
documentation. In In addition addition to to the the Checworks Checworks Wear Wear Rate Rate Analysis Analysis RunRun Definitions Definitions listed in listed in Table Table 1.0, 1.O, there there are are the the following following two two additions:
additions:
a.
- a. X-under w/exp X-under wlexp joints joints b.
- b. CND FWH CND FWH 22 22 to to FWH FWH 23; 23; this this was was added added due due to to the the SPU.
SPU.
This information This information was was required required for for DDIR DDlR NO.4No. 4 Harry Hartjen Harry Hartjen
(
From: Cunningham, From: Cunningham, Glenn Glenn [1]
Sent: Thursday, Sent: Thursday, October October 07,20042:45 07, 2004 2:45 PM PM To: Hartjen, To: Hartjen, Harry Harry Cc: Scanlon, Cc: Scanlon, Michael;Michael; Chakrabarti, Chakrabarti, Syamal Syamal
Subject:
RE:
Subject:
RE: RAIRAI FAC-1 FAC-1 Harry, There There are are nono operational operational changes changes for for Steam Steam PlantPlant Systems, Systems, suchsuch as as use use of of additional additional trains trains or or use use ofof bypass bypass lines lines notnot currently currently in in operation, operation, associated associated with uprate of with uprate of IP2 IP2 // IP3.
IP3. Changes Changes due due toto the the uprate uprate which which affect affect FACFAC are are primarily primarily changes changes in in system system flowrates f10wrates andand temperatures, temperatures, which which areare documented documented in in the the Heat Heat Balance Balance calculations.
calculations. Impact Impact of of these these changes changes on on piping piping velocities velocities and and temperatures temperatures is is addressed addressed in in the the applicable applicable sections sections of of the BOP Uprate the BOP Uprate Engineering Reports, forwarded Engineering Reports, forwarded to to Entergy Entergy for for review.
review.
Modifications Modifications associated associated withwith thethe uprate uprate of IP2 // IP3 of IP2 IP3 include:
include: (1)
(1) MSR MSR internal internal moisture moisture separation separation system system replacement, replacement, (2) HP Turbine (2) HP Turbine rotor rotor replacement, replacement, (3) (3) HP HP turbine turbine interstage interstage drain drain piping piping modification, modification, and and (4)
(4)
Relocation of Relocation of HPHP turbine turbine 1 1"stage st stage pressure pressure taps.taps.
Regards, Regards, Glenn Glenn C. C.
From:
From: Hartjen, Hartjen, Harry Harry [3]
Sent:
Sent: Wednesday, Wednesday, OctoberOctober 06,200406, 2004 1 1:30
- 30 PMPM Calculation Calculation No. 040711-01, Attachment No. 040711-01, Attachment A, A, Revision Revision 00 Page Page 4141 of of 44 44
CS/TECHNOLOGIES, CSI TECHNOLOGIES, INC. /NC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis Analysis To: Cunningham, To: Cunningham,Glenn Glenn
(
Subject:
RE:
Subject:
RAI FFAC-1 RE:RAI AC-1 Glen:
Glen:
This is This to confirm is to confirm thatthat the the wear wear rate rate comparison comparison will will be be completed completed by by 12131/2004.
12/31/2004.
A s II mentioned As mentioned to to you you wewe are are having having aa contractor contractor perform perform the the update update to to our our Checworks Checworks models.
models. One One of of inputs II have the inputs the have to to provide provide to to them them is:is:
The listing The listing of of all Unit 22 and all Unit Unit 33 operational and Unit operational and/or and/or configuration configuration changes changes due due to to the the power power uprate uprate (Le.,
(i.e.,
additional trains additional trains inin operation, operation, bypass bypass lines lines operated operated at at full full power, power,etc.)etc.)
Do you Do you have have this this information information or or can can you you direct direct mymy question question to to someone someone who who has has this this information.
information.
Thanks, Thanks, Harry Hartjen Harry Hartjen (914) 736-8356 (914) 736-8356 From: Cunningham, From: Cunningham, Glenn Glenn [5]
Sent: Wednesday, Sent: Wednesday, October October 06,200412:50 06,2004 1250 PM PM To: Hartjen, To: Hartjen, Harry Harry
Subject:
FW:
Subject:
FW: RAI FAC-1 RAI FAC-1 From: Cunningham, From: Cunningham, Glenn Glenn (t, Sent:
Sent: Wednesday, Wednesday, October October 06,2004 12:41 PM 06, 2004 12:41 PM To:
To: 'hartje@entergy.com'
'hartje@entergy.com'
Subject:
Subject:
RAI FAC-1 RAI FAC-1 Harry, Harry, Ass II indicated, A indicated, II made made a a few few edits edits in in your your input.
input. Please Please confirm confirm that that thethe wear wear rate rate comparison comparison discussed discussed in in the the last last sentence sentence will will be be completed completed by by the the end end of of 2004.
2004.
Thanks, Thanks, Glenn C.
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it.
The The Shaw Shaw Group Group Inc.Inc.
(, http://www.shawgrp.com http://www.shawgrp.com Calculation No.
Calculation No. 040711-01, 040711-01, Attachment Attachment A, A. Revision Revision 00 Page 42 of Page 42 44 of44
CSI TECHNOLOGIES, CSI TECHNOLOGIES,INC. INC. IP3 CHECWORKS Power IP3 CHECWORKS Power Uprate Uprate Analysis Analysis Q
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you are If you If are not not the the addressee addressee indicated indicated inin this this message message (or(or responsible responsible for delivery for delivery of of the the message message to to such such person),
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email. Please Please advise advise immediately immediately ifif you you or your or your employer employer do do not not consent consent to to Internet Internet email email for for messages messages of of this this kind. Opinions, kind. Opinions,conclusions conclusions and and other other information information inin this this message message thatthat do not do not relate relate to to the the official official business business of of The The Shaw Shaw Group Group Inc.Inc.or its or its subsidiaries shall subsidiaries shall be be understood understoodas as neither neither given given nor nor endorsed endorsed by by it.
it.
The Shaw The Shaw Group Group Inc.
Inc.
http://www.shawgrp.com http://www.shawgrp.com
(
(
Calculation No. 040711-01, Calculation No. 040711-01, Attachment Attachment A, A, Revision Revision 00 Page Page 43 43 of of 44 44
CS/TECHNOLOGIES, CSI TECHNOLOGIES, /NC.
INC. IP3 CHECWORKS IP3 CHECWORKSPower Power Uprate Uprate Analysis Analysis Reference 7.3.3 Reference 7.3.3
(
Email from Email from RonRon Macina Macina (IP3) (IP3)to to Brian Brian Trudeau Trudeau (CSI (CSITechnologies),
Technologies), dated dated 1110/2005, 1/10/2005, regarding addition regarding addition al a1 Heat Heat Balance Balance Diagrams Diagrams and and uprate uprate start start dates, CSI Doc.
dates, CSI Doc. No No 04071140.
04071140.
CSI Doc. No. 04071140 CSIDoc.No.04071140 Brian, Brian, Please find Please find below below thethe requested requested HeatHeat Balances/Information.
Balances/lnformation.
IP3 Pre
- 1) IP3
- 1) Pre and and Post Post Appendix Appendix K K Heat Heat Balances Balances ccIP3TuningR4 Pre
<<IP3TuningR4 Pre Appendix Appendix K K (3037 (3037 NSS Pwr).pdf>> <<IP3TuningR4 NSS Pwr).pdf>> 4P3TuningR4 Post Post Apendix K.pdf>>
Apendix K.pdf>>
- 2) IP2
- 2) IP2 Pre Pre Appendix Appendix K K Heat Heat Balance Balance ccIP2-TuningR4 Pre
<<IP2-TuningR4 Pre Appendix Appendix K NSS Pwr).pdf>>
(3090 NSS K (3090 Pwr).pdf=
Start Date
- 3) Start
- 3) Date for for IP3 Appendix K IP3 Appendix K uprate uprate waswas 12122102 12/22/02
- 4) Start
- 4) Start Date Date for for IP2 IP2 Appendix Appendix K K uprate uprate waswas 5/23/03 5/23/03 Thanks, Thanks, Ron Macina Ron Macina 914-736-8363 914-736-8363
Original Message-----
Original Message-----
From: Brian From: Brian Trudeau Trudeau [7]
Sent: Tuesday, Sent: Tuesday, December December 28, 28,2004 352 PM 2004 3:52 PM To:
To: Macina, Ron Macina, Ron
Subject:
Subject:
Request for Request for Additional HBDs Additional HBDs (i
CSI Doc. No. 04071 137 CSIDoc.No.04071137 Ron, Ron, Based on Based on our our discussion discussion earlier today, itit appears earlier today, appears that that we have some we have some additional work additional work toto do do onon this this end.
end. We We plan plan onon modeling modeling allall three three power power levels (100% -- the levels (100% the Original Original power power level, -1 01.4% -- the level, -101.4% the Appendix Appendix K K power power level, and level, 105% -- the and 105% the SPU SPU power power level) level) for each unit.
for each unit. In In doing doing this, this, we we will will capture capture plant plant conditions conditions at at each each point point in in history.
history.
To To complete complete this this task, task, wewe will will need need the the following following input:
input:
(1) Unit (1) Unit 3 PEPSE or 3 PEPSE or HBD HBD at at -101.4%
-101.4% power power (the (the Appendix Appendix K K power power uprate) uprate)
(2)
(2) Unit Unit 2 Original PEPSE 2 Original PEPSE or or HBD HBD at 100% power at 100% power (pre-Appendix (pre-Appendix K) K)
(3) Unit (3) Unit 33 Start Start date date for for the the Appendix Appendix K K Uprate Uprate (4)
(4) Unit Unit 22 Start Start date date for for the Appendix K the Appendix K Uprate Uprate Please Please letlet me know ifif you me know you have have any any questions.
questions. We We will will be be contacting contacting Harry Harry to to inform inform him him of of this this plan.
plan.
Thank Thank you,you, Brian Brian Trudeau Trudeau CSI CSI Technologies, Technologies, Inc. Inc.
(847)
(847) 836-3000 836-3000 ext.ext. 71 717 7 f( www.csitechnologies.com www.csitechnologies.com Calculation No. 040711-01, Calculation No. Attachment A, 040711-01, Attachment A, Revision Revision 00 Page 44 of Page 44 of 44 44
CsS1I TECHNOLOGIES. INC.
TECHNOLOGIES, INC.
<;Co0 iIJJ ,ii :f
. II l:' nn<:g ii iIii i'i' :'"
IIt1 ii fl/I g t' ,
- -I i CALCULATION CALCULATION APPROVAL APPROVAL COVER COVER SHEET SHEET Document Document
Title:
Title: Indian Indian Point Point Unit Unit 3 3
CHECWORKS CHECWORKS Power Power Uprate Uprate Analysis Analysis Document Document No.:
No.: 04071 1-01 040711-01 Client:
Client: Entergy Entergy Nuclear Nuclear Northeast Northeast Project No.:
Project No.: 04071 0407111 This This calculation calculation has has been been prepared prepared inin accordance accordance with with Section Section 4.3 4.3 of the CSI of the CSI QualityQuality System System Manual, Manual, Revision Revision 2.
2.
Revision:
Revision: 00 (For-Use)
(For-Use) 47 47 pages pages Prepared:
Prepared: ~L~ Date: a1slo~
7J~rudea:ll k t I Verified:
Verified:
MD P. Aplington (CSI) ro~ Date:
Date: 3/2.3/0 5
(
Approved:
Approved: --1 Poe (CSI)
R. Poe Daniel R.
Daniel t &c-(CSI)
Date:
Oate: 3/23/o~-
Approved:
Approved: Date:
Date:
\i
(S I TECHNOLOGIES. INC.
C () II .i IJ II i il g F n gill t' e ;- s
(
Revision Control Revision Control Sheet Sheet Project Number:
Project Number: 040711 040711 Project Name:
Project Name: Indian Point Indian Point Units Units 2 2&8 33 CHECWORKS Power CHECWORKS Power Uprate Uprate Analysis Analysis Client:
Client: Entergy Nuclear Entergy Nuclear Northeast Northeast Document Document
Title:
Title: Indian Point Indian Point Unit Unit 3 3 CHECWORKS CHECWORKS PowerPower Uprate Uprate Analysis Analysis Document Document Number:
Number: 04071 1-01 040711-01 Rev.
Rev. Date Date Description of Description of Changes Changes CSI CSI Client Client Approval A-.1!I!roval Approval 00 3/23/05 3/23/05 Initial Issue Initial Issue -- For Use Use 4 tD# 9 M
(
i