ML20249A831
| ML20249A831 | |
| Person / Time | |
|---|---|
| Site: | Hope Creek  |
| Issue date: | 06/04/1998 |
| From: | Public Service Enterprise Group |
| To: | |
| Shared Package | |
| ML20249A811 | List: |
| References | |
| 1AE408, NUDOCS 9806180297 | |
| Download: ML20249A831 (100) | |
Text
l 17:26.19 PROTO-HX 3.01 by Proto-Pcw:r Ccrp:rcti:n (SN!!PHX-1009) 06/04/98 l
PSE&G - Hope Creek l
Calculation Report for i AE408 - Diesel Gen. Intercooler Heat Exchanger Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 1,000.0 Shell Flow (gpm)
Shell Flow (gpm) 880.0 Shell Temp in ('F)
Tube inlet Temp ('F) 100.0 Shell Temp Out ('F)
Constant Heat Load (BTUh) 3,118,000 Tube Flow (gpm)
Tube Temp In (*F)
Tube Temp Out (*F)
Input Fouling Factor 0 001580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall(BTUh ft2 'F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTUh ft *F) 2 Tube-Side hi(BTU /hr ft2 *F)
Heat Transferred (BTUh) 1/ Wall Resis (BTU /hr ft2 *F)
LMTD LMTD Correction Factor i
Effective Area (ft2)
Overall Fouling (hr ft2 'F/ BTU)
Property Shell Side Tube-Side Velocity (ft/s)
Shell Temp in ( F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell(*F)
Bulk Visc(Ibm /ft hr)
Shell Skin Temp ( F)
Skin Visc (Ibm /ft hr)
Tube Temp in ('F)
Density (ibm /ft')
Tube Temp Out ("F)
Cp (BTU /lbm 'F)
Tav Tube ('F)
K (BTU /hr ft *F)
Tube Skin Temp (*F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 4 619E+5 Overall Fouling (hr ft2 'F/ BTU) 0.001580 Tube Mass Flow (Ibm /hr) 5.002E+5 Shell-Side ho (BTU /hr ft2 *F) 1,182.5 Tube-Side hi(BTU /hr ft *F) 1,187.4 2
Heat Transferred (BTU /hr)
- 3. Il8E+6 1/ Wall Resis (BTU /hr ft2 'F) 5,941.6 LMTD 15.1 LMTD Correction Factor 1.0000 EfTective Area (ft2) 7370 U Overall(BTU /hr ft 'F) 280.7 2
Property Shell Side Tube-Side Velocity (ft/s) 3.04 4.17 Shell Temp In ( F) 122.0 Reynold's Number 1.604E+04 3.172E+04 Shell Temp Out ('F) 114.4 Prandtl Number 8.84 4.37 Tav Shell( F) 118.2 Bulk Visc (Ibm /ft hr) 2.75 1.59 Shell Skin Temp ('F) 114.6 2 kin Visc (Ibm /ft hr) 2.87 1.53 Tube Temp in (*F) 100 0 Density (lbm/ft')
64.56 61.95 Tube Temp Out (*F) 106.2 l
Cp (BTU /lbm *F) 0.89 1.00 Tav Tube (*F) 103.I K (BTU /hr ft 'F) 0.28 0.36 Tube Skin Temp ('F) 107.2
" Reyno!ds Number Outside Range of Equation Applicabilih
!! With Z:ro Fouling The Test Heat Load Could Not Be Achieved j
'1 9906190297 990612 I
PDR ADOCK 05000354:
P PDR
17:26 50 PROTO-HX 3.01 by Prato-Pcwcr C rporttiin (SN#PHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for 1 AE408 - Diesel Gen. Intercooler Heat Exchanger Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 900.0 Shell Flow (gpm)
Shell Flow (gpm) 880.0 Shell Temp In (*F)
Tube Inlet Temp (*F) 100.0 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 3,118,000 Tube Flow (gpm)
Tube Temp In ('F)
Tube Temp Out ('F)
Input Fouling Factor 0.001580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall (BTU /hr ft2 *F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2 *F)
Tube-Side hi (BTU /hr R2 *F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 *F)
LMTD LMTD Correction Factor Effective Area (ft )
2 Overall Fouling (hr ft2 F/ BTU)
Property Shell-Side Tube-Side Velocity (fl/s)
Shell Temp In ('F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell (*F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp ( F)
Skm Visc (Ibm /ft hr)
Tube Temp in (*F)
Density (Ibm /ft')
Tube Temp Out (*F)
Cp (BTU /lbm 'F)
Tav Tube (*F)
K (BTU /hr ft *F)
Tube Skin Temp ( F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 4.619E+5 OverallFouling(hrft2 F/ BTU) 0.001580 Tube Mass Flow (Ibm /hr) 4.502E+5 Shell Side ho (BTU /ht fl2 'F) 1,185.7 Tube-Side hi (BTU /hr ft2 *F) 1,094.1 Ileat Transferred (BTU /hr)
- 3. l l 8E+6 1/ Wall Resis (BTU /hr ft2 *F) 5,941.6 LMTD 15.4 LMTD Correction Factor 1.0000 Effective Area (ft')
737.0 U Overall (BTU /hr ft2 *F) 274.5 Property Shell-Side Tube-Side Velocity (ft/s) 3.04 3,75 Shell Temp In (*F) 122.7 Reynold's Number 1.616E+04 2.866E+04 Shell Temp Out (*F) 115.1 Prandtl Number 8.77 4.35 Tav Shell ('F)
I18.9 j
Bulk Vise (Ibm /ft ht) 2.73 1.59 Shell Skin Temp ('F) 115.3 j
' Skin Visc (lbm/ft ht) 2.84 1.52 Tube Temp In ( F) 100.0 Density (Ibm /ft')
64.54 61.95 Tube Temp Out (*F) 106.9 Cp (BTU /lbm *F) 0.89 1.00 Tav Tube (*F) 103.5 K (BTU /hr ft 'F) 0.28 0.36 Tube Skin Temp (*F) 107.9
" Reynolds Number Outside Range of Equation Applicability
!! With Zero Fouling The Test Heat Load Could Not Be Achieved r
17:27.05 PROTO-HX 3.01 by Pr:to-Pcw r C rportti:n (SN#FHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE408 - Diesel Gen. Intercooler Heat Exchanger Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 800.0 Shell Flow (gpm)
She:1 Flow (gpm) 8800 l
Shell Temp in (*F)
Tube Inlet Temp (*F) 100.0 l
ShcIl Temp Out (*F)
Constant Heat Load (BTUh) 3,118,000
)
Tube Flow (gpm)
. Tube Temp in (*F) l Tube Temp Out (*F)
Input Fouling Factor 0.001580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2 *F)
' Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr A2 'F)
Tube-Side hi(BTU /hr A2 F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 'F)
LMTD LMTD Correction Factor Effective Area (ft')
Overall Fouling (hr ft2 *F/ BTU)
Property Shell Side Tube-Side j
Velocity (ft/s)
Shell Temp In (*F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell(*F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp (*F)
Skin Visc (Ibm /ft hr)
Tube Temp in (*F) -
Density (Ibm /ft')
Tube Temp Out ('F)
Cp (BTU /lbm *F)
Tav Tube (*F)
K (BTUh ftF)
Tube Skin Temp ( F)
Extrapolation Calculation Results l
Shell Mass Flow (lbm/hr) 4.619E+5 Overall Fouling (hr ft2 *F/ BTU) 0.001580 Tube Mass Flow (Ibm /hr) 4.002E+5 Shell-Sid ~.:,(BTU /hr ft2 *F) 1,189.6 r
Tube-Side hi(BTU /hr ft2 *F) 998.7
- Heat Tramferred (BTU /hr)
- 3. ll8E+6 1/ Wall Resis (BTU /hr ft2 F) 5,941.6 LMTD 15.8 LMTD Correction Factor 1.0000 Effective Area (ft')
737.0 U Overall(BTU /hr ft 'F) 267.3 2
Property Shell-Side Tube-Side Velocity (ft/s) 3.04 3.34 Shell Temp In (*F) 123.5 Reynold's Number 1.632E+04 2.559E+04
. Shell Temp Out ('F) 115.9 Prandtl Number 8.69 4.33 Tav Shell ('F>
119.7 Bulk Visc (Ibm /ft hr) 2.71 1.58 Shell Skin Temp (*F) 116.2 Skin Visc (Ibm /ft hr) 2.82 1.50 Tube Temp In (*F) 100.0 Density (lbm/ft') -
64.53 61,94 Tube Temp Out (*F) 107.8 Cp (BTU /lbm 'F) 0.89 1.00 Tav Tube ( F) 103.9 K (BTU /ht ft 'F) 0.28 0.36 Tube Skin Temp (*F) 108.8 l
f
- Reynolds Number Outside Range of Equation Applicability I! With Zero Fouling The Test Heat Load Could Not Be Achieved L:
17:27:20 PROTO-HX 3.01 by Pr:t:-Pcw r Ccrp:rcti:n (SN#PIIX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for l AE408 - Diesel Gen. Intercooler Heat Exchanger Calculation Specifications l
Constant Heat Load / Cold inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 775.0 Shell Flow (gpm)
Shell Flow (gpm) 880.0 Shell Temp in ( F)
Tube inlet Temp (*F) 100.0 Shell Temp Out ('F)
Constant Heat Load (BTU /hr) 3.118,000 Tube Flow (gpm)
Tube Temp In (*F)
Tube Temp Out ( F)
Input Fouling Factor 0.001580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2 "F)
Tube Mass Flow (lbm/hr)
Shell-Side ho (BTU /hr ft *F) 2 Tube-Side hi(BTU /hr ft 'F) 2 lleat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft F) 2 LMTD LMTD Correction Factor Effective Area (ft')
Overall Fouling (hr ft2 *F/ BTU)
Property Shell-Side Tube-Side Velocity (R/s)
Shell Temp in ('F)
Reynold's Number Shell Temp Out ('F)
Prandtl Number Tav Shell(*F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp (*F) l Skin Visc (Ibm /ft hr)
Tube Temp In (*F)
Density (Ibm /ft')
Tube Temp Out (*F)
Cp (BTU /lbm *F)
Tav Tube ( F) l K (BTU /hr ft 'F)
Tube Skin Temp (*F)
Extrapolation Calculation Results i
Shell Mass Flow (Ibm /hr) 4.619E+5 Overall Fouling (hr ft F/ BTU) 0.001580 2
Tube Mass Flow (Ibm /hr) 3.877E+5 Shell-Side ho (BTU /hr ft2 *F) 1,190.7 Tube-Side hi(BTU /hr ft. F) 974.5 2
Heat Transferred (BTU /hr) 3.118E+6 1/ Wall Resis (BTU /hr f 2 'F) 5,941.6 LMTD 15.9 LMTD Correction Factor 1.0000 EITective Area (R2) 737.0 U Overall (BTU /hr ft2 *F) 265.4 Propeny Shell-Side Tube-Side Velocity (8/s) 3.04 3.23 Shell Temp in ("F) 123.8 Reynold's Number 1.636E+04 2.482E+04 Shell Temp Out ( F) 116.2 Prandtl Number 8.66 4.33 Tav Shell(*F) 120.0 Bulk Visc (Ibm /ft hr) 2.70 1.58 Shell Skin Terap ( F) 116.4 Skin Visc (Ibm /ft hr) 2.81 1.50 Tube Temp in (*F) 100.0 Density (Ibm /ft')
64.52 61.94 Tube Temp Out ('F) 108.1 Cp (BTU /lbm 'F) 0.89 1.00 Tav Tube (*F) 104.0 K (BTU /hr ft 'F) 0.28 0.36 Tube Skin Temp (*F) 109.0
" Reynolds Number Outside Range of Equation Applicability
!! With Zero Fouhng The Test Heat Load Could Not Be Achieved i
L
l l
17.27.37 PROTO-HX 3,01 by Pr:t>P wcr Ccrp rcti2n (SN'!PHX-1009) 06/04/98 i
PSE&G - Hope Creek Calculation Report for I AE408 - Diesel Gen. Intercooler Heat Exchanger Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 750 0 Shell Flow (gpm)
Shell Flow (gpm) 880.0 Shell Temp in ( F)
Tube inlet Temp (*F) 100.0 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 3,118,000 Tube Flow (gpm) l Tube Temp in (*F)
Tube Temp Out ( F)
Input Fouling Factor 0.001580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall (BTU /hr ft2 *F)
Tube Mass Flow (Ibm /hr)
Shell Side ho (BTU /hr ft *F) 2 Tube-Side hi(BTU /hr ft2 F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 *F)
LMTD LMTD Correction Factor Effective Area (ft')
Overall Fouling (hr ft2 F/ BTU)
Property Shell-Side Tube Side l
Velocity (ft/s)
Shell Temp In ( F)
Reynold's Number Shell Temp Out ( F)
Prandtl Number Tav Shell (*F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp ( F)
Skm Visc (lbm/ft hr)
Tube Temp In ( F)
Density (Ibm /ft')
Tube Temp Out (*F)
Cp(BTU /lbm F)
Tav Tube ( F)
K (BTU /hr ft F)
Tube Skin Temp (*F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 4.619E+5 Overall Fouling (hr ft F/ BTU) 0.001580 2
Tube Mass Flow (Ibm /hr) 3.752E+5 Shell-Side ho (BTU /hr ft2-F) 1,191.9 Tube-Side hi(BTU /hr ft *F) 950.2 2
Heat Transferred (BTU /hr)
- 3. I 18E+6 1/ Wall Resis (BTU /hr ft.*F) 5,941.6 2
LMTD 16.1 LMTD Correction Factor 1.0000 Effective Area (ft )
737.0 2
U Overail(BTU /hrft F) 263.3 2
Property Shell-Side Tube-Side Velocity (ft/s) 3.04 3.13 Shell Temp In (*F) 124.0 Reynold's Number 1.641E+04 2.40$E+04 Shell Temp Out ( F) 116.4 Prandtl Number 8.64 4.32 Tav Shell( F) 120.2 Bulk Visc(Ibm /fthr) 2.69 1.58 Shell Skin Temp ( F) 116.7 Skin Visc (Ibm /ft hr) 2.80 1.50 Tube Temp In (*F) 100.0 Density (lbm/ft')
64.52 61.94 Tube Temp Out ( F) 108.3 Cp (BTU /lbm *F) 0.89 1.00 Tav Tube (*F) 104.2 K (BTU /hrft *F) 0.28 0.36 Tube Skin Temp (*F) 109.3 g
" Reynolds Number Outside Range of Equation Applicability
!! With Zero Fouling The Test Heat Load Could Not Be Achieved
17.28:28 PROTO-HX 3.01 by Pr to-Pcwer Cerpor:tirn (SN#PHX-1009) 06/04/98 PSE&G - Hope Cre:k Calculation Report for I AE408 - Diesel Gen. Intercooler Heat Exchanger l
Calculation Specifications Constant Heat Load / Cold inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User Test Data Extrapolation Data Data Date ~
Tube Flow (gpm) 700.0 Shell Flow (gpm)
Shell Flow (gpm) 880.0 Shell Temp in (*F)
Tube Inlet Temp (*F) 100 0 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 3,118,000 Tube Flow (gpm)
Tube Temp in ( F) l Tube Temp Out ('F)
- Input Fouling Factor 0.001580 l
Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2 'F)
Tube Mass Flow (Ibm /ht)
Shell-Side ho (BTU /hr ft2 'F)
Tube-Side hi(BTU /hr f12 *F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft*#F)
LMTD LMTD Correction Factor Effective Area (ft')
Overall Fouling (hr ft2 F/ BTU)
Property Shell Side Tube-Side Velocity (ft/s)
Shell Temp in ('F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell(*F)
Bulk Visc(Ibm /A hr)
Shell Skin Temp (*F)
Skin Visc (Ibm /ft hr)
Tube Temp in (*F)
Density (Ibm /ft')
Tube Temp Out (*F)
Cp (BTU /lbm#F)
Tav Tube (*F)
K (BTU /hr ft *F)
Tube Skin Temp (*F)
Extrapolation Calculation Results ShcIl Mass Flow (Ibm /hr)
.t.619E+5 Overall Fouling (hr ft2 *F/ BTU) 0.001580 Tube Mass Flow (Ibm /hr) 3.502E+5 Shell-Side ho (BTU /hr ft2 'F) 1,194.5 Tube-Side hi (BTU /hr ft2 'F) 901.0 Heat Transferred (BTU /hr) 3.I l8E+6 1/ Wall Resis (BTU /ht ft2'F) 5,941.6 LMTD 16.3 LMTD Correction Factor 1.0000 EfTective Area (ft') -
737.0 U Overall(BTU /hr ft2'F) 258.9 Property Shell Side Tube-Side Velocity (ft/s) - _
3.04 2.92
' Shell Temp in (*F) 124.6 Reynold's Number 1.651E+04 2.252E+04 Shell Temp Out ('F) i17.0 Prandtl Number 8.58 4.30 Tav Shell('F) 120.8
. Bulk Visc (Ibm /ft hr) 2.67 1.57 Shell Skin Temp ( F) i17.3 Skin Visc (Ibm /ft hr) 2.78-1,49 Tube Temp in ('F) 100.0 Density (ibm /ft').
64.51 61.94 Tube Temp Out (*F)-
108.9 Cp (BTU /lbm'F)
'O.89 1.00 Tav Tube (*F) 104.5 K (BTU /hr ft#F).
' O.28 0.36 Tube Skin Temp ( F) 109.9
" Reynolds Number Outside Range of Equation Applicability
!! With Zero Fouling The Test Heat Load Could Not Be Achieved
17:28 45 PROTO-IIX 3.01 by Prot -Pew::r Czrportti n (SN!!PIIX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE408 - Diesel Gen. Intercooler Heat Exchanger l
Calculation Specifications Constant }{ cat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 650 0 Shell Flow (gpm)
Shell Flow (gpm) 880 0 Shell Temp in (*F)
Tube Inlet Temp ( F) 100.0 Shell Temp Out ( F)
Constant 11 eat Load (BTU /hr) 3,118,000 Tube Flow (gpm)
Tube Temp in ( F)
Tube Temp Out ('F)
Input Fouling Factor 0 001580 l
Fouling Calculation Results l
Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2 F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2-F)
Tube-Side hi(BTU /hr ft F) 2 Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft 'F) 2 LMTD LMTD Correction Factor Effective Arca(fl2)
Overall Fouling (hr ft 'F/ BTU) 2 Property ShcIl-Side Tube-Side Velocity (ft/s)
ShcIl Temp in ( F)
Rey nold's Number Shell Temp Out ( F)
Prandtl Number Tav Shell( F)
Bulk Visc (lbm/ft hr)
Shell Skin Temp ( F)
Skin Visc (Ibm /ft hr)
Tube Temp In ( F)
Density (Ibm /ft')
Tube Temp Out ('F)
Cp (BTU /lbm *F)
Tav Tube (*F)
K (BTU /hr ft 'F)
Tube Skin Temp ('F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 4 619E+5 Overall Fouling (hr ft2 *F/ BTU) 0.001580 Tube Mass Flow (lbm/hr) 3.252E+5 Shell-Side ho (BTU /hr ft2 *F) 1,197.5 Tube-Side hi(BTU /hr ft F) 851.1 2
licat Transferred (BTU /hr) 3.118E+6 1/ Wall Resis (BTU /hr ft2 *F) 5,941.6 LMTD 16.6 LMTD Correction Factor 1.0000 Effective Arca (ft')
7370 U Overall (BTU /hr ft2 *F) 254.1 Property Shell-Side Tube-Side Velocity (ft/s) 3.04 2.71 Shell Temp In ( F) 125.3 Rey nold's Number 1.664E+04 2.099E+04 Shell Temp Out ( F) 117.7 Prandtl Number 8.51 4.29 Tav Shell(*F) 121.5 Bulk Visc (Ibm /ft hr) 2.65 1.57 Shell Skin Temp ('F) 117.9 Skm Visc (Ibm /ft hr) 2.76 1.48 Tube Temp in (*F) 100 0 Density (ibm /ft')
64.50 61.93 Tube Temp Out (*F) 109 6 Cp (BTU /lbm *F) 0.89 1.00 Tav Tube (*F) 104.8 K (BTU /hr fi *F) 0.28 0.37 Tube Skin Temp ( F) 110.5
" Reynolds Number Outside Range of Equation Applicability iI With Zero Fouling The Test Heat Load Could Not Be Achieved
17:29 43 PROTO-HX 3.01 by Pr:to-Pcwsr Ccrportti:n (SNf!PHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE405 - Diesel Gen. Jacket Heat Exchanger Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 1,000.0 Shell Flow (gpm)
Shell Flow (gpm) 880.0 Shell Temp in (*F)
Tube Inlet Temp ('F) 106.1 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 5,412,000 Tube Flow (gpm)
Tube Temp In ('F)
Tube Temp Out ('F)
Input Fouling Factor 0.001580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall (BTU /hr ft *F) 2 Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr 82 *F)
Tube-Side hi(BTU /hr A2 'F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 'F)
LMTD LMTD Correction Factor Effective Area (ft )
2 Overall Fouling (hr ft2 *F/B7U)
Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp In (*F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell('F)
Bulk Visc (ibm /ft hr)
Shell Skin Temp ( F)
Skin Visc (Ibm /ft hr)
Tube Temp In (*F)
Density (Ibm /ft')
Tube Temp Out (*F)
Cp(BTU /lbm F)
Tav Tube ( F)
K (BTU /hr ft *F)
Tube Skin Temp ( F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 4.619E+5 Overall Fouling (hr A2 *F/ BTU) 0.001580 Tube Mass Flow (lbm/hr) 5.002E+5 Shell-Side ho (BTU /hr fl2-F) 977.2 Tube-Side hi (BTU /hr 82 *F) 1,262.4 lleat Transferred (BTU /hr) 5.412E+6 1/ Wall Resis (BTU /hr ft2 *F) 5,941 6 LMTD 65.6 LMTD Correction Factor 1.0000 EITective Area (ft )
304.0 2
Propeny Shell-Side Tube-Side Velocity (ft/s) 2.37 4.18 Shell Temp In ( F) 183.5 Reynold's Number 2.17f>E+04 3.457E+04 Shell Temp Out (*F) 170.7 Prandtl Number 4.93 3.98 Tav Shell(*F) 177.1 Bulk Visc (Ibm /ft hr) 1.55 1.46 Shell Skin Temp (*F) 158.9 i
Skin Vise (Ibm /ft hr) 1.82 1.25 Tube Temp in ('F) 106.1 Density (Ibm /ft )
63.35 61.84 Tube Temp Out (*F) 116.9 2
Cp (BTU /lbm 'F) 0.91 1.00 Tav Tube ( F) 1i 1.5 K (BTU /hr ft *F) 0.29 0.37 Tube Skin Temp (*F) 127.7
" Reynolds Number Outside Range of Equation Applicability
!! With Zerc Fouling The Test Heat Load Could Not Be Achieved
1 17:30:20 PROTO-HX 3.01 by Pr;to-P:wer Ccrp:rati:n (SN#PHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE405 - Diesel Gen. Jacket Heat Exchanger Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 900.0 Shell Flow (gpm)
Shell Flow (gpm) 880.0 Shell Temp in (*F)
Tube Inlet Temp (*F) 106.9 Shell Temp Out ('F)
Constant Heat Load (BTU /ht) 5,412,000 Tube Flow (gpm)
Tube Temp In (*F)
Tube Temp Out (*F)
Input Fouling Factor 0 001580 I
Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Oserall(BTU /hr ft2 *F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2 'F)
Tube-Side hi(BTU /hr ft2 F)
{
Heat Transferred (BTU /lw) 1/ Wall Resis (BTU /hr ft2 *F)
LMTD LMTD Correction Factor Effective Area (ft2)
Overall Fouling (hr ft2 *F/ BTU) i Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp In (*F)
{
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell (*F)
Bulk Visc(Ibm /ft hr)
Shell Skin Temp ( F)
Skin Visc (Ibm /ft hr)
Tube Temp In ( F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp (BTU /lbm *F)
Tav Tube ( F)
K (BTU /hr ft 'F)
Tube Skin Temp ( F)
{
l Extrapolation Calculation Results I
Shell Mass Flow (Ibm /hr) 4.619E+5 Overall Fouling (hr ft *F/ BTU) 0.001580 2
Tube Mass Flow (lbm/hr) 4.502E+5 Shell-Side ho (BTU /hr ft F) 984.4 2
Tube-Side hi(BTU /hr ft *F) 1.170.6 2
Heat Transferred (BTU /hr) 5.412E+6 1/ Wall Resis (BTU /hr ft F) 5,941.6 2
LMTD 66.7 LMTD Correction Factor 1.0000 Effective Area (ft')
304.0 U Overall(BTU /hr ft2 F) 266.9 Property Shell-Side Tube-Side Velocity (ft/s) 2.38 3.76 Shell Temp In (*F) 186.0 Reynold's Number 2.225E+04 3.155E+04 Shell Temp Out (*F) 173.2 Prandtl Number 4.82 3.92 Tav Shell (*F) 179.6 Bulk Visc (Ibm /ft hr) 1.52 1.44 Shell Skin Temp (*F) 161.5 Skin Visc (Ibm /ft hr) 1.78 1.22 Tube Temp in (*F) 106.9 Density (lbm/ft')
63.29 -
61.82 Tube Temp Out ('F) 118.9 Cp (BTU /lbm 'F) 0.91 1.00 Tav Tube (*F) 112.9 K (BTU /hr ft *F) 0.29 0 37 Tube Skin Temp (*F) 130.4
" Reynolds Number Outside Range of Equation Applicability ip
!! With Zero Fouling The Test Heat Load Could Not Be Achieved l
I
)
l
17:30 38 PROTO-IIX 3.01 by Pr:t:-P wcr Ccrpor;ti:n (SNOPIIX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE405 - Diesel Gen. Jacket Heat Exchanger Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was cd Extrapolation Was to User Specified Conditions Fouling Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 800 0 Shell Flow (gpm)
Shell Flow (gpm) 880 0 Shell Temp In (*F)
Tube Inlet Temp ( F) 107.8 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 5.412,000 Tube Flow (gpm)
Tube Temp in (*F)
Tube Temp Out (*F)
Input Fouling Factor 0 001580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2 F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2 *F)
Tube-Side hi(BTU /hr ft2 *F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 *F)
LMTD LMTD Correction Factor Effective Area (ft2)
Overall Fouling (hr ft2 *F/ BTU)
Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp In (*F)
Reynold's Number Shell Temp Out ( F)
Prandtl Number Tav Shell( F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp ( F)
Skin Visc (Ibm /ft hr)
Tube Temp In ( F)
Density (lbm/ft')
Tube Temp Out (*F)
Cp (BTU /lbm *F)
Tav Tube (*F)
K (BTU /hr ft F)
Tube Skin Temp (*F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 4.619E+5 Overall Fouling (hr ft2 F/ BTU) 0 001580 Tube Mass Flow (Ibm /hr) 4.002E+5 Shell-Side ho (BTU /hr f12 *F) 992.9 Tube-Side hi (BTU /hr ft *F) 1,076.3 2
licat Transferred (BTU /hr) 5412E46 1/ Wall Resis (BTU /hr ft *F) 5.941.6 2
LMTD 68.1 LMTD Correction Factor 1.0000 Effcetive Area (ft2) 3040 U Overall(BTU /hr ft F) 261.5 2
Property Shell-Side Tube-Side Velocity (f1/s) 2.38 3.34 Shell Temp In ( F) 189.1 Reynold's Number 2.281E +04 2.850E+04 Snell Temp Out ("F) 176 2 Prandtl Number 4.71 3 85 Tav Shell(*F) 182.7 Bulk Visc (Ibm /ft hr) 1.48 1.42 Shell Skin Temp ( F) 164.7 Skin Visc (Ibm /ft hr) 1.73 1.19 Tube Temp in (*F) 107.8 Density (Ibm /ft')
63.22 61.79 Tube Temp Out (*F) 121.3 l
Cp (BTU /lbm *F) 0.92 1.00 Tav Tube ( F) 114 6 K (BTU /hr ft *F) 0.29 0.37 Tube Skin Temp (*F) 133.6
" Reynolds Number Outside Range of Equation Applicability
!! With Zero Fouling The Test Heat Load Could Not Be Achieved
17:31:19 PROTO-HX 3.01 by Proto-Pcw:r Ccrporati a (SNI!PHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for 1 AE405 - Diesel Gen. Jacket Heat Exchanger Calculation Specifications Constant Heat Load / Cold inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 775.0 Shell Flow (gpm)
Shell Flow (gpm) 880 0 Shell Temp In (*F)
Tube Inlet Temp ('F) 108.1 Shell Temp Out (*F)
Constant licat Load (BTU /hr) 5,412,000 Tube Flow (gpm)
Tube Temp in ( F)
Tube Temp Out (*F)
Input Fouling Factor 0 001580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2#F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2dF)
Tube-Side hi(BTU /hr f12#F)
Ifcat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2dF)
LMTD LMTD Correction Factor Effective Area (f12)
Overall Fouling (hr f12 *F/ BTU)
Froperty Shell-Side Tube-Side Velocity (ft/s)
Shell Temp in ( F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell (*F)
Bulk Visc (lom/ft hr)
Shell Skin Temp ( F)
Skin Visc (Ibm /ft hr)
Tube Temp In ("F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp (BTU /lbm#F)
Tav Tube ('F)
K (BTU /hr ft#F)
Tube Skin Temp ('F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 4.619E+5 Overall Fouling (hr f12 *F/ BTU) 0.001580 Tube Mass flow (Ibm /hr) 3.877E+5 Shell Side ho (BTU /hr ft2#F) 995.4 Tube-Side hi (BTU /hr ft2#F) 1,052 6 Ileat Transferred (BTU /hr) 5,412E+6 1/ Wall Resis (BTU /hr ft *F) 5,941.6 2
LMTD 68.5 LMTD Correction Factor 1.0000 Effective Area (112) 304.0 U Overall (BTU /hr ft2#F) 260.0 Property Shell-Side Tube-Side Velocity (ft/s) 2.38 3.24 Shell Temp in ('F) 190 0 Reynold's Number 2.298E+04 2.775E+04 Shell Temp Out ('F) 177.2 Prandtl Number 4 67 3.83 Tav Shell ('F) 183 6 Bulk Visc (Ibm /fthr) 1.47 1,41 Shell Skin Temp (*F) 165.7 Skin Visc (Ibm /ft hr) 1.72 1.18 Tube Temp In (*F) 108.1 Density (lbm/ft')
63.20 61.79 Tube Temp Out (*F) 122.1 Cp (BTU /lbm#F) 0.92 1.00 Tav Tube (*F) 1151 K (BTU /hr ft F) 0.29 0.37 Tube Skin Temp (*F) 134.5
" Reynolds Number Outside Range of Equation Applicability
. !! With Zero Fouling The Test Heat Load Could Not Be Achieved
17:31:36 PROTO-HX 3.01 by Pr:to-P w r Ccrporction (SNf!PHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE405 - Diesel Gen. Jacket Heat Exchanger Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User l
Test Data Extrapolation Data Data Date Tube Flow (gpm) 750.0 Shell Flow (gpm)
Shell Flow (gpm) 880.0
' Shell Temp In (*F)
Tube Inlet Temp (*F) 108.3 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 5,412,000 Tube Flow (gpm)
Tube Temp in (*F)
Tube Temp Out (*F)
Input Fouling Factor 0.001580 i
Fouling Calculation Results I
Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2 *F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2 F)
Tube-Side hi (BTU /hr ft2 *F) lleat Transferred (BTU /hr) 1/ Wall Resis (ETU/hr ft2 *F)
LMTD LMD Correction Factor Effective Area (ft2)
Overall Fouling (hr ft2 *F/ BTU)
Property Shell-Side Tube-Side Velocity (ft/s)
ShcIl Temp in (*F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell(*F)
- Bulk Visc (Ibm /ft hr)
Shell Skin Temp (*F)
Skin Vise (ibm /ft hr)
Tube Temp in (*F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp (BTU /lbm *F)
Tav Tube (*F)
K (BTU /hr ft *F)
Tube Skin Temp (*F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 4.619E+5 Overall Fouling (hr ft 'F/ BTU) 0 001580 2
Tube Mass Flow (lbm/hr) 3.752E+5 Shell Side ho (BTU /hr fl2 *F) 997.8 Tube-Side hi (BTU /ht ft2 *F) 1,028.1 Heat Transferred (BTU /hr) 5.412E+6 1/ Wall Resis (BTU /hr ft F) 5,941.6 2
LMTD 68.9 LMTD Correction Factor 1.0000 EfTective Area (ft2) 304.0 U Overall(BTU /hr ft *F) 258.4 2
Property Shell-Side Tube Side Velocity (ft/s) 2.38 3.14 Shell Temp in ( F) 190.8 Reynold's Number 2.314E+04 2.697E+04 Shell Temp Out (*F) 178.0 Prandtl Number 4.64 3.8 i Tav Shell(*F) 184.4 Bulk Visc(Ibm /ft hr) 1.46 1.41 Shell Skin Temp (*F) 166.6 Skin Visc (Ibm /ft hr) 1.70 1.17 Tube Temp in (*F) 108.3
' Density (Ibm /ft')
63.18 61.78 Tube Temp Out ("F) 122.7 Cp (BTU /lbm *F) 0.92 1.00 Tav Tube (*F) 115.5 K (BTU /hr ft *F) 0.29 0.37 Tube Skin Temp (*F) 135.4
- Reynolds Number Outside Range of Equation Applicability t! With Zero Fouling The Test Heat Load Could Not Be Achieved
17.31 58 PROTO-HX 3.01 by Proto-P;wer Ccrporati:n (SN'lPHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE405 - Diesel Gen. Jacket Heat Exchanger l
Calculation Specifications Constant Heat Load / Cold inlet Temperature Method was Used Extrapolation Was to User Specified Conditions j
Fouling Was input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 700.0 Shell Flow (gpm)
Shell Flow (gpm) 880.0 Shell Temp In ('F)
Tube inlet Temp (*F) 108.9 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 5,412,000 Tube Flow (gpm)
Tube Temp in (~F)
Tube Temp Out ( F)
Input Fouling Factor 0 001580 l
Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall (BTU /hr ft2 'F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft 'F) 2 Tube Side hi(BTU /hr ft F) 2 Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 *F)
LMTD LMTD Correction Factor i
Effective Area (ft )
2 Overall Fouling (hr ft2 *F/ BTU)
Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp in ('F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell ('F)
Bulk Visc(Ibm /fthr)
Shell Skin Temp ( F)
Skin V,sc (Ibm /ft hr)
Tube Temp in ( F)
Density (Ibm /ft')
Tube Temp Out ('F)
Cp(BTU /lbm F)
Tav Tube ( F)
K (BTU /hr ft. F)
Tube Skin Temp ( F)
Extrapolation Calculation Results Shell Mass Flow (!bm/hr) 4.619E+5 Overall Fouling (hr ft *F/ BTU) 0 001580 2
Tube Mass Flow (Ibm /hr) 3.502E+5 Shell-Side ho (BTU /hr ft2-F) 1,003.4 Tube-Side hi(BTU /hr ft "F) 979.5 2
Heat Transferred (BTU /hr) 5.412E+6 1/ Wall Resis (BTU /hr ft F) 5.941 6 2
LMTD 69.8 LMTD Correction Factor 1.0000 Effectne Area (ft')
304.0 i
U Overall (BTU /hr ft' *F) 255.1 Property Shell-Side Tube-Side Velocity (ft/s) 2.38 2.93 Shell Temp in (*F) 192.8 Rey nold's Number 2.352E+04 2.544E+04 Shell Temp Out ( F) 180 0 Prandtl Number 4.56 3.76 Tav Shell (*F) 186.4 Bulk Visc (Ibm /ft hr) 1.44 1.39 Shell Skin Temp (*F) 168 7 Skin Visc (Ibm /ft hr) 1.67 1.15 Tube Temp in ('F) 108.9 Density (Ibm /ft')
63.13 61.76 Tube Temp Out ( F) 124.4 Cp (BTU /lbm 'F) 0.92 1.00 Tav Tube ('F) 116 6 K tBTU/hr ft *F) 0.29 0.37 Tube Sun Temp ( F) 137.5
" Reynolds Number Outside Range of Equation Applicability
?! With Zero Fouling The Test Heat Load Could Not Be Achieved
17:32:16 PROTO-HX 3.01 by Pre-to-P:wgr Ccrporttisn (SNt!PHX-1909) -
06/04/98 PSE&G - Hope Creek Calculation Report for I AE405 - Diesel Gen. Jacket Heat Exchanger l
Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 650.0 Shell Flow (gpm).
Shell Flow (gpm) 880.0 Shell Temp In (*F)
Tube Inlet Temp (*F) 109.6 Shell Temp Out ('F)
Constant Heat Load (BTU /hr) 5,412,(XX)
Tube Flow (gpm)
Tube Temp in (*F)
Tube Temp Out ('F)
Input Fouling Factor 0.001580 l
Fouling Calculation Results ShcIl Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2#F)
Tube Mass Flow (Ibm /hr)
Shell Side ho (BTU /hr ft2 *F)
Tube-Side hi(BTU /hr A2#F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2dF)
LMTD LMTD Correction Factor Effective Area (ft2)
Overall Fouling (hr ft2dF/ BTU)
Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp In ('F)
Reynold's Number Shell Temp Out ('F)
Prandtl Number Tav Shell('F)
. Bulk Visc (Ibm /ft hr)
Shell Skin Temp ( F)
Skin Visc(Ibm /ft hr)
Tube Temp in ('F)
Density (Ibm /ft')
Tube Temp Out (*F)
Cp (BTU /lbm'F)
Tav Tube (*F)
K (BTU /ht ft F)
Tube Skin Temp (*F)
Extrapolation Calculation Results ShcIl Mass Flow (Ibm /hr) 4.619E+5 Overall Fouling (hr ft2#F/ BTU) 0.001580 Tube Mass Flow (Ibm /hr) 3.252E+5 Shell-Side ho (BTU /hr fl2 *F) 1,009.7 Tube-Side hi (BTU /hr ft2#F) 930.2 Heat Transferred (BTU /ht) 5.412E+6 1/ Wall Resis (BTU /hr ft 'F) 5,941.6 2
LMTD 70.8 LMTD Correction Factor 1.0000 Effective Area (ft')
304.0 U Overall(BTU /hr ft2dF) 251.6 Property' Shell Side Tube-Side Velocity (ft/s) 2.39 2.72 Shell Temp In (*F) 195.1
. Reynold's Numbet 2.3%E+04 2.392E+04 Shell Temp Out (*F) 182.3 Prandtl Number 4.48
. 3.71 Tav Shell('F) 188.7 Bulk Visc(Ibm /fi hr) 1.41 1.37 Shell Skin Temp ('F) 171.1 Skin Visc(lbm/ft hr) 1.64 1.13 Tube Temp In (*F) 109.6 p
Density (Ibm /ft')-
63.07 61.74 Tube Temp Out ( F) 126.3 Cp(BTU /lbm#F) 0.92 1.00 Tav Tube (*F) 117,9
. K (BTU /ht ft#F) 0.29 0.37 Tube Skin Temp (*F) 140.0
" Reynolds Number Outside Range of Equation Applicability
!! With Zero Fouling The Test Heat Load Could Not Be Achieved
17.33:39 PROTO-IIX 3.01 by Proto-P w:r Ccrporrti:n (SN!!PilX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE404 - Diesel Gen. Lube Oil Cooler l
Calculation Specifications Constant Heat Load / Cold inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouhng Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 1,000.0 Shell Flow (gpm)
Shell Flow (gpm) 400.0 Shell Temp in (*F)
Tube Inlet Tcmp ( F) 116.9 ShcIl Temp Out (*F)
Constant Heat Load (BTU /hr) 1,353,000 Tube Flow (gpm)
Tube Temp in ( F)
Tube Temp Out (*F)
Input Fouling Factor 0 003580 Fouling Calculation Results Shell Mass Flow (lbm/hr)
U Overall (BTU /hr ft2 *F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft23F)
Tube Side hi(BTU /hr ft2 *F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft *F) 2 LMTD LMTD Correction Factor Effective Arca (ft2)
Overall Fouling (hr ft2 *F/ BTU)
Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp In ( F)
Reynold's Number Shell Temp Out ( F)
Prandtl Number Tav Shell (*F)
Bulk Visc (Ibm /fbhr)
Shell Skin Temp (*F)
Skin Visc (Ibm /ft hr)
Tube Temp In ( F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp (BTU /lbm "F)
Tav Tube ("F)
K (BTU /hrft#F)
Tube Skin Temp (*F)
Extrapolation Calculation Results ShcIl Mass Flow (Ibm /hr) 1.804E+5 Overall Fouling (hr ft #F/ BTU) 0.003580 2
Tube Mass Flow (Ibm /hr) 5.002E+5 Shell-Side ho (BTU /hr ft2#F) 73 i Tube-Side hi (BTU /hr ft2#F) 1,178.0 Heat Transferred (BTU /hr) 1.353E+6 1/ Wall Resis (BTU /hr ft 3F) 5,941.6 2
LMTD 33.7 LMTD Correction Factor 1.0000 EITective Area (ft')
738 0 i
Property Shell Side Tube-Side Velocity (ft/s) 1.92 3.76 ShcIl Temp In ( F) 160 2 Reynold's Number 2.721E+02 3 319E+04 Shell Temp Out ( F) 144.6 Prandtl Number 569 67 3.70 Tav Shell (*F) 152.4 Bulk Visc(Ibm /ft hr) 86.00 1.37 Shell Skin Temp ( F) 1270 Skin Visc (ibm /ft hr) 153.14 1.35 Tube Temp in (*F) 116 9 Density (Ibm /ft')
54.21 61.74 Tube Temp Out ('F)
I19.6 Cp (BTU /lbm'F) 0.48 1.00 Tav Tube (*F) 118 3 K (BTU /hr ft#F) 0 07 0.37 Tube Skin ~Icmp( F) 1201
" Rey nolds Number Outside Range of Equation Applicability f f With Zero Fouling The Test Heat Load Could Not Be Achieved
1 17.33 59 PROTO-HX 3.01 by Pr:t>P:wer Ccrporcti:n (SNCPHX-1009) 06/04/98 j
PSE&G - Hope Creek Calculation Report for I AE404 - Diesel Gen. Lube Oil Cooler Calculation Specifications l
Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User I
i I
Test Data Extrapolation Data Data Date Tube Flow (gpm) 900.0 Shell Flow (gpm)
Shell Flow (gpm) 400.0 Shell Temp In (*F)
Tube Inlet Temp (*F)
I18.9 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 1,353,000 Tube Flow (gpm)
Tube Temp In (*F)
Tube Temp Out (*F)
Input Fouling Factor 0 003580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall (BTU /hr fl2 *F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft *F) 2 Tube-Side hi (BTU /hr fl2 *F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft F) 2 LMTD LMTD Correction Factor EfTective Area (ft )
2 Overall Fouling (hr ft2 *F/ BTU)
Property Shell-Side Tube-Side l
Velocity (ft/s)
Shell Temp in (*F) l Reynold's Number Shell Temp Out ( F) l Prandtl Number Tay Shell (*F)
I Bulk Visc (Ibm /ft hr)
Shell Skin Temp (*F)
Skin Visc (Ibm /ft hr)
Tube Temp In (*F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp(BTU /lbm F)
Tav Tube (*F)
K (BTU /hr ft F)
Tube Skin Temp (*F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 1.804E+5 Overall Fouling (hr ft "F/ BTU) 0.003580 2
Tube Mass Flow (Ibm /hr) 4.502E+5 Shell-Side ho (BTU /hr ft *F) 73.8 2
Tube-Side hi (BTU /hr ft *F) 1,094.7 2
Heat Transferred (BTU /hr) 1.353E+6 1/ Wall Resis (BTU /hr ft F) 5,941.6 2
LMTD 33 6 LMTD Correction Factor 1.0000 EfTectise Area (ft )
738.0 2
U Overall(BTU /hr ft2 F) 54.5 Property Shell-Side Tube-Side Velocity (ft/s) 1.92 3.39 Shell Temp in ( F) 162.2 Reynold's Number 2.836E+02 3 049E+04 Shell Temp Out ( F) 146 6 l
Prandtl Number 547.92 3.62 Tav Shell(*F) 154 4 Bulk Visc (Ibm /fl hr) 82.49 1.34 Shell Skin Temp (*F) 129.3 Skin Visc (Ibm /ft hr) 144.72 1.32 Tube Temp In ( F) 118.9 Density (lbm/fP) 54 17 61.71 Tube Temp Out ( F) 121.9 Cp (DTU/lbm *F) 0 48 1 00 Tav Tube (*F) 120 4 K (BTU /hr fl *F) 0.07 0.37 Tube Skin Temp ( F) 122.4
" Reynolds Number Outside Range of Equation Applicability f f With Zero Fouling The Test Heat Load Could Not Be Achieved
1 17:34:18 PROTO-HX 3.01 by Pr:to-P:wcr C:rpor:ti:n (SN'lPHX-1009) 06/04/98
(
PSE&G - Hope Creek Calculation Report for l AE404 - Diesel Gen. Lube Oil Cooler Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method was Used Extrapolation Was to User Specified Conditions Fouling Was input by User Test Data Extrapolation Data l
Data Date Tube Flow (gpm) 800.0 Shell Flow (gpm)
Shell Flow (gpm) 400 0 Shell Temp in (*F)
Tube Inlet Temp ('F) 121.3 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 1,353,000 Tube Flow (gpm)
Tube Temp in ( F)
Tube Temp Out (*F)
Input Fouling Factor 0.003580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall (BTU /hr ft2 *F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft *F) 2 Tube-Side hi (BTU /hr ft2 *F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 *F)
LMTD LMTD Correction Factor Effective Area (ft')
Overall Fouling (hr ft 'F/ BTU) 2 Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp In (*F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell(*F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp ( F)
Skin Visc (lbm/ft hr)
Tube Temp In ( F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp (BTU /lbm *F)
Tav Tube ( F)
K (BTU /hr ft F)
Tube Skin Temp (*F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 1.804E+5 Overall Fouling (hr ft2 *F/ BTU) 0.003580 Tube Mass Flow (lbm/hr) 4.002E+5 Shell-Side ho (BTU /hr ft *F) 74.7 2
Tube-Side hi (BTU /hr ft2-F) 1,009.3 Heat Transferred (BTU /hr) 1.353E+6 1/ Wall Resis (BTU /hr ft2 F) 5,941 6 LMTD 33 5 LMTD Correction Factor 1.0000 EITective Arca (ft )
738.0 2
U Overall (BTU /hr ft2.cF) 54 7 i
Propert)
Shell-Side Tube-Side i
Velocity (ft/s) 1.92 3 01 Shell Temp In ( F) 164 6 Reynold's Number 2.980E+02 2.776E+04 Shell Temp Out ('F) 149.1 Prandtl Number 523.16 3 53 Tav Shell(*F) 156.9 Bulk Visc (Ibm /ft hr) 78.51 1.31 Shell Skin Temp ( F) 132.1 Skin Visc (Ibm /f) hr) 135.38 1.28 Tube Temp in ( F) 121.3 Density (Ibm /ft')
54.11 61.67 Tube Temp Out ("F) 124.7 Cp (BTU /lbm 'F) 0.48 1.00 Tav Tube (*F) 1230 K (BTU /hr ft F) 0.07 0.37 Tube Skin Temp ( F) 1251
" Reynolds Number Outside Range of Equation Applicabihty
!! With Zero Fouling The Test Heat Load Could Not Be Achieved
17:34 36 PROTO-IIX 3.01 by Prot -P;wer Ccrporcti:n (SN!!PHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE404 - Diesel Gen. Lube Oil Cooler l
Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method was Used Extrapolation Was to User Speedied Conditions Fouling Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 775.0 Shell Flow (gpm)
Shell Flow (gpru) 400 0 Shell Temp in (*F)
Tube Inlet Temp ('F) 1221 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 1,353,000 Tube Flow (gpm)
Tube Temp in ( F)
Tube Temp Out (*F)
Input Fouling Factor 0 003580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall (BTU /hr ft F) 2 Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2 *F)
Tube-Side hi (BTU /hr ft2 *F)
Heat Transferred (BTU /ht) 1/ Wall Resis (BTU /hr 82 F)
LMTD LMTD Correction Factor EfTective Area (82)
Overall Fouling (hr ft 'F/ BTU) 2 Property Shell-Side Tube-Side Velocity (ft/s)
Shell Terr.p in ( F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell( F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp ('F)
Skin Visc (IbnVft hr)
Tube Temp in (*F)
Density (Ibm /fP)
Tube Temp Out ( F)
Cp(BTU /lbm F)
Tav Tube (*F)
K (BTU /hr ft *F)
Tube Skin Temp ("F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 1.804E+5 Overall Fouling (hr 82 *F/ BTU) 0.003580 Tube Mau Flow (Ibm /ht) 3 877E+5 Shell Side ho (BTU /hr ft2 *F) 75.0 Tube-Side hi(BTU /ht ft *F) 988.2 2
lleat Transferred (BTU /hr) 1.353E+6 t/ Wall Resis (BTU /hr n23F) 5,941.6 LMTD 33.5 LMTD Correction Factor 1.0000 Effectisc Area (fl2) 7380 U Cwerall (BTU /hr ft2 *F) 54 8 Propeny Shell Side Tub -Side Velocity (ft/s) 1.92 2.92 Shell Temp in ("F) 165.4 Reynnld's Number 3.028E+02 2.711E+04 Shell Temp Out (*F) 149.9 Prandtl Number
$15.37 3.50 Tav Shell ('F) 157.7 Bulk Visc (Ibm /ft hr) 77.26 1.30 Shell Skin Temp ( F) 132.9 Skm Visc (Ibm /ft hr) 132.50 1.27 Tube Temp In (*F) 122.1 Density (Ibm /ft')
54 09 61.65 Tube Temp Out ( F) 125 6 Cp (13TU/lbm *F) 0.48 1.00 Tav Tube (*F) 123 8 K (BTU /hr ft *F) 0.07 0.37 Tube Skin Temp (*F) 1260
" Reynolds Number Outside Range of Equation Applicability l
f t With Zero Fouling The Test Heat Load Could Not Be Achieved l
I 1
17:34:52 PROTO-HX 3.01 by Prc;to-P:wer C:rpor:ti s (SN#PHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for l AE404 - Diesel Gen. Lube Oil Cooler Calculation Specifications l
Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 750 0 Shell Flow (gpm)
Shell Flow (gpm) 400 0 Shell Temp In ("F)
Tube Inlet Temp (*F) 122.7 Shell Temp Out (*F)
Constant licat Load (BTU /hr) 1,353,000 Tube Flow (gpm)
Tube Temp in ( F)
Tube Temp Out (*F)
Input Fouling Factor 0.003580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft *F) 2 Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2-F)
Tube-Side hi(BTU /hr ft2 *F) lleat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 "F)
LMTD LMTD Correction Factor F5cctive Area (ft )
2 Overall Fouling (hr ft2 *F/ BTU)
Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp in (*F)
Reynold's Number Shell Temp Out (*F)
Prandtl Number Tav Shell( F)
Bulk Visc (Ibm /ft;hr?
Shell Skin Temp (*F)
Skin Visc (Ibr.It hr)
Tube Temp in ( F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp(BTU /lbm F)
Tav Tube (*F)
K (BTU /hr ft F)
Tube Skin Temp (*F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 1.804E+5 Overall Fouling (hr ft *F/ BTU) 0 003580 2
Tube Mass Flow (lbm/hr) 3.752E+5 Shell-Side ho (BTU /hr ft F) 75.2 2
Tube-Side hi (BTU /hr ft2 *F) 965.7 Ileat Transferred (BTU /hr) 1.353E+6 1/ Wall Resis (BTU /hr ft *F) 5,941.6 2
LMTD 33 4 LMTD Correction Factor 1.0000 Effective Area (ft2) 738.0 U Overall(BTU /hr ft F) 54.8 2
Property Shell-Side Tube-Side 1
Velocity (f)/s) 1.92 2.83 Shell Temp In (*F) 166.1 l
Reynold's Number 3.066E+02 2.639E+04 Shell Temp Out (*F) 150 6 i
Prandtl Number 509.37 3.47 Tav Shell (*F) 158.3 Bulk Visc (Ibm /ft hr) 76.30 1.29 Shell Skin Temp (*F) 133.7 Skin Visc (Ibm /ft hr) 130.29 1.27 Tube Temp in (*F) 122.7 Density (Ibm /ft')
54.08 61.64 Tube Temp Out (*F) 126 3 Cp (BTU /lbm *F) 0.48 1 00 Tav Tube (*F) 124.5 K (BTU /hr ft *F) 0 07 0.37 Tube Skin Temp ( F) 126.7
" Res nolds Number Outside Range of Equation Applicabihty i
f f With Zero Fouling The Test Heat Load Could Not Be Achieved I
17.35 09 PROTO-HX 3.01 by Proto-P:wer Ccrpor:tica (SN#PHX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE404 - Diesel Gen. Lube Oil Cooler Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method was Used 1
Extrapolation Was to User Specified Conditions 1
Fouling Was input by User Test Data Extrapolation Data i
Data Date Tube Flow (gpm) 700.0 Shell Flow (gpm)
Shell Flow (gpm) 400.0 Shell Temp In ( F)
Tube Inlet Temp (*F) 124.4 Shell Temp Out (*F)
Constant Heat Load (BTU /hr) 1,353,000 Tube Flow (gpm) j Tube Temp in (*F)
Tube Temp Out (*F)
Input Fouling Factor 0 003580 Fouling Calculation Results Shell Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2 *F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr fl2 *F)
Tube-Side hi(BTU /hr A2 *F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft *F) 2 LMTD LMTD Correction Factor Effective Area (ft')
Overall Fouling (hr ft2 *F/ BTU)
Property Shell Side Tube-Side Velocity (ft/s)
Shell Temp in ('F)
Reynold's Number Shell Temp Out ('F)
Prandtl Number Tav Shell( F)
Bulk Visc(Ibm /ft hr)
Shell Skin Temp ('F)
Skin Visc (Ibm /ft hr)
Tube Temp In (*F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp (BTU /lbm *F)
Tav Tube (*F)
K (BTU /hr ft *F)
Tube Skin Temp (*F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 1.804E+5 Overall Fouling (ht ft* *F/ BTU) 0.003580 Tube Mass Flow (Ibm /hr) 3.502E+5 Shell-Side ho (BTU /hr ft2 'F) 75.8 Tube-Side hi (BTU /hr ft 'F) 922.1 2
Ileat Transferred (BTU /hr) 1.353E+6 1/ Wall Resis (BTU /hr ft2 F) 5,941.6 LMTD 33.4 LMTD Correction Factor 1.0(X)0 EfTective Area (ft2) 738.0 U Overall (BTU /hr ft *F) 55.0 2
Propeny Shell-Side Tube Side Velocity (ft/s) 1.92 2.64 Shell Temp In ('F) 167.8 Rey nold's Number 3.173E+02 2.505E+04 Shell Temp Out ("F) 152.3 Prandtl Number 493.39 3.4 i Toy Shell ("F) 160.0 Bulk Visc (Ibm /ft hi-)
73.74 1.27-Shell Skin Temp ( F) 135 6 Skin Visc (Ibm /A hr) 124.50 1.24 Tube Temp In ('F) 124.4 Density (Ibm /fl')
54.04 -
61.61 Tube Temp Out (*F) 128.3 Cp (BTU /lbm *F) 0.49 1.00 Tav Tube (*F) 126.3 K (BTU /hr ft *F) 0.07 0.37 Tube Skin Temp (*F) 128.6 1
- Rc3volds Number Outside Range of Equation Applicability
!! With Zero Fouling The Test Heat Load Could Not Be Achieved
j 17.35 29 PROTO-IIX 3.01 by Pr:to-P;wer Ccrporati:n (SNllPIIX-1009) 06/04/98 PSE&G - Hope Creek Calculation Report for I AE404 - Diesel Gen. Lube Oil Cooler Calculation Specifications Constant Heat Load / Cold Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Fouling Was Input by User Test Data Extrapolation Data Data Date Tube Flow (gpm) 650 0 ShcIl Flow (gpm)
Shell Flow (gpm) 400.0 ShcIl Temp In ("F)
Tube Inlet Temp (*F) 126.3 ShcIl Temp Out (*F)
Constant Heat Load (BTU /hr) 1,353.000 Tube Flow (gpm)
Tube Temp in ('F)
Tube Temp Out (*F)
Input Fouling Factor 0 003580 Fouling Calculation Results ShcIl Mass Flow (Ibm /hr)
U Overall(BTU /hr ft2 'F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr 82 F)
Tube-Side hi (BTU /hr ft2 'F)
Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft *F) 2 LMTD LMTD Correction Factor j
Effective Area (ft')
l Overall Fouling (hr ft2 F/ BTU) l Property Shell-Side Tube-Side j
Velocity (ft/s)
Shell Temp In (*F)
Reynold's Number Shell Temp Out ('F)
Prandtl Number Tav Shell (*F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp (*F)
Skin Visc (Ibm /ft hr)
Tube Temp In (*F)
Density (Ibm /ft')
Tube Temp Out ( F)
Cp (BTU /lbm *F)
Tav Tube ( F)
K (BTU /hr ft *F)
Tube Skin Temp (*F)
Extrapolation Calculation Results ShcIl Mass Flow (Ibm /hr) 1.804E+5 Overall Fouling (hr ft2 'F/ BTU) 0.003580 I
Tube Mass Flow (Ibm /hr) 3.252E+5 Shell-Side ho (BTU /hr ft F) 76.4 2
Tube-Side hi(BTU /hr ft F) 877.6 2
Heat Transferred (BTU /hr) 1.353E+6 1/ Wall Resis (BTU /hr-ft2 *F) 5,941.6 LMTD 33.3 LMTD Correction Factor 1.0000 EITective Arca (ft )
738.0 2
U Overall(BTU /hr ft *F) 55.1 2
Property Shell-Side Tube-Side Velocity (ft/s) 1.93 2.45 Shell Temp In ( F) 169.7 Reynold's Number 3.296E+02 2.369E+04 Shell Temp Out ( F) 154.2 l
Prandtl Number 476,27 3.34 Tav Shell (*F) 162.0 Bulk Visc(Ibm /ft hr) 71.00 1.25 Shell Skin Temp ( F) 137.7 Skin Visc (Ibm /ft hr) 118.42 1.22 Tube Temp In (*F) 126.3 Density (Ibm /ft')
53 99 61.58 Tube Temp Out (*F) 130.5 Cp (BTU /lbm *F) 0 49 1.00 Tav Tube (*F) 128.4 K (BTU /hr ft *F) 0.07 0.37 Tube Skin Temp (*F) 130.8
" Reynolds Number Outside Range of Equation Applicability
!! With Zero Fouling The Test Heat Load Could Not Be Achieved 1
3 l
)
I i
1 i
Attachment (2)
RJIR Ileat Exchanger l
i Minimum SACS Flow Rate l
t i
l l
l L_______
07 32.04 PROTO-HX 3.01 by Pr:to-Pcwer Ccrporatizs (SN#PHX-1009) 06/03/98 PSE&G - Hope Creek Calculation Report for 1 AE205 RHR Heat Exch. - Cont. Cooling Mode 2 Calculation Specifications l
Constant Inlet Temperature Method Was Used Extrapolation Was to User Specified Conditions Design Fouling Factors Were Used Test Data Extrapolation Data Data Date Tube Flow (gpm) 8,650 0 Shell Flow (gpm)
Shell Flow (gpm) 10,000 0 l
Shell Temp in ( F)
Tube Inlet Temp (*F) 100.0 l
Shell Temp Out ('F)
Shell Inlet Temp (*F) 212.0 Tube Flow (gpm)
Tube Temp In ( F)
Tube Temp Out ("F)
Fouling Calculation Results l
Shell Mass Flow (Ibm /hr)
U Overall (BTU /hr ft2-F)
Tube Mass Flow (Ibm /hr)
Shell-Side ho (BTU /hr ft2 *F)
Tube-Side hi(BTU /hr ft F) 2 Heat Transferred (BTU /hr) 1/ Wall Resis (BTU /hr ft2 *F)
LMTD LMTD Correction Factor Effective Area (ft')
Overall Fouling (hr ft F/ BTU) 2 Property Shell-Side Tube-Side Velocity (ft/s)
Shell Temp In ( F)
Reynold's Number Shell Temp Out ( F)
Prandtl Number Tav Shell( F)
Bulk Visc (Ibm /ft hr)
Shell Skin Temp (*F)
Skin Visc (Ibm /ft hr)
Tube Temp In ( F) j Density (Ibm /ft')
Tube Temp Out ( F)
Cp (BTU /lbm *F)
Tav Tube ('F)
K (BTU /hr ft F)
Tube Skin Temp ( F)
Extrapolation Calculation Results Shell Mass Flow (Ibm /hr) 5002E+6 Overall fouling (ht ft F/ BTU) 0.001054 2
Tube Mass Flow (Ibm /hr) 4.327E+6 Shell-Side ho (BTU /hr ft F) 1,748 0 2
Tube-Side hi (BTU /hr ft2 *F) 2,445.7 Heat Transferred (BTU /hr) 1.238E+8 1/ Wall Resis (BTU /hr ft2 *F) 2,187.3 LMTD 85 4 LMTD Correction Factor 0.9837 Effective Area (ft )
3,740.0 2
U Overall (BTU /hr ft F) 394.2 2
Property Shell-Side Tube-Side Velocity (ft/s) 4.54 10.19 Shell Temp In ( F) 212.0 Reynold's Number
- 1. I 16E+05 1.199E+05 Shell Temp Out ( F) 187.4 Prandtl Number 1.90 3.86 Tav Shell( F) 199.7 Bulk Visc (Ibtr./ft hr) 0.73 1.42 Shell Skin Temp ( F) 180.4 Skm Visc (Ibm /ft hr) 0 83 1.23 Tube Temp in (*F) 100 0 Density (Ibm /ft')
60.12 61.80 Tube Temp Out ( F) 128 6 Cp(BTU /lbm F) 1.01 1.00 Tav Tube ( F) 114.3 K (BTU /hr ft F) 0 39 0.37 Tube Skin Temp ( F) 129 6
" Reynolds Number Outside Range of Equation Applicability
?! With Zero Fouling The Test Heat Load Could Not Be Achieved
[
l 1
1 I
l l
l l
l l
i l
i I
i Attachment (3) i UHS Temperature Limit Evaluation l
Lineops from Previous EE l
l
PROTO-POWER CORPORAT10N 15 THAMES STREET l
PHONE: (860) 446-9725 GROTON, CT 06340 FAX: (860) 448-4860 FAX COVER SHEET l
FILE No.: Il-M l
DATE: t/24s TOTAL PAGES (INCLUDING COVER SHEET):
To:
a.4 Avpv FROM:
es&.c 4varte
- DEPT, FAX No.: i (e**) 329-tzis fax No.: _(860) 448-4860
REFERENCE:
MESSAGE:
- 4. b Hen. seu % nwM k
- s. L**/DE. r %und vou*<: M w e rsw. W s
t % :rcJ v Ws, %,a an :. qr.
- F.
To report transmittal problems or for confirmation, please call (860) 446-9725.
~..
_ - _.. _ me _,
r,.u 6/24822:15 PROTO-FLO 4.01 by Proto P wrr Cciporation - Serial #PFL-0000 ease i or 4 Public Service Electric and Gas. G9SEG\\l 1 385\\NEW UHSiSTACSUHS2 PDB - Revision 2.00 Hope Creek Generating Station _ STACS Flow Summary Report Ccnvegence-Preuurs=1.00-5 $cm Q=1 cE.2 FricMon=1 CE4 FCV=l.0E-4 PCV=1 OE3 Tctrycretws=5.0E 3 LOP /SSE
)
Flow Summary Title Diameter F10W Mmunum F!ow NPSHA NPSH (in)
(spm)
(gpm)
(ft)
Ratio IA2E201 out 19.250 10,188.11 1A1E201 out 19.250 9,706.06 I
ICP210 out 19.250 10,001.00 1 AT203 out 1.500 41.60 i
1 AP210 out 19.250 9,% 9.40 1 AE205 out 19 250 9,514.38 IDP210 cut 19.250 9,645.00 IBP210 out 19.250 9,881.35 IBlE201 out 19.250 9,573.98 IBE205 our 19.250 9,247.83 j
IB2E201 out 19.250 9,914.86 i AT205 recire 1.939 22.87 IBT205 ccuc.
2.067 24.77 1 AP2021 out 0.957 23.32 1 AP202 2 out 0.957 9.87 ICP2021 out 0 957 28.46 1CP202 2 out 0957 10.33 ICVII210 eut 3 068 125.53 IOVH21O out 3 06B t 31.05 1EVH210 out 3.058 142.80 l
1 AVH210 out 3.068 142.06 l
!? Reverse Flow Through Check Valve
&& Purnp Flow is Past End of Cune
" Flow Belew Mirtimum
$$ NPSH Available BelowNPSHRequired l
1 l-
6/2/98 22:15 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 P. 2 or 4 Public Seivfee Electric and Gas - G:P3EG.11 385\\NEW UHSiSTACSUMS2.PDB - Revision 2.00 Hope Creek Generating Station. STACS Flow Summary Report CoeverSence: Presser =1 CE-3 5.an Qal oE.2 Fnet.on=1.DE 6 FCV=1.004 PCV-l.0E-3 Tempmtur,=$.0E-3 LOP /SSE Flow Summary Title Diameter Flow Mmmunn Flow NPSHA NPSH (in)
(gpm)
(Fprn)
(ft)
Ratio 1AVH209 out 3.068 77.14 1BVH209 out 3.068 105.11 1 AVH208 out 1 939 32.13 1BVH208 out 1.939 31.65 IFVH210 out 3.068 14S.07 '
IBVH210 out 3.068 148.33 1BP202-1 out 0.957 28.46 IBP202 2 out 0.957 10.14 1DP202-1 out 0.957 25.66 1DP202 2 out 0957 9.97 1DVH210 out 3.068 144.20 1HVH210 out 3.068 144.07 1 AVH213 out 4.026 417.44 1GVH211 out 3 066 112.33 1CVH211 out 3.068 111.79 IFVH213 out 4.026 419.52 1BVH213 out 4.026 423.14 1CVH213 out 4.026 412.10
!DVH213 out 4.026 414.98 IEVH213 out 4.026 408.32 1 AK202 out 0.957 6.17
!! Reverse F ow Through Check Valve
&& P.urg Flow is Past End of Curve
" FlowBelowMinimu:n 55 NPSH Available Below NPSH Required
_ - _., _., _ _ m
.m 1
&2/98 22:15 PROTO-FLO 4.01 by Proto-P:wer Corporation - Serirl CPFL-0000 cap 2 or 4 Pabbc Service ElecMe and Gas. GAPSEO;11385\\NEW l'HS$TACSUBS2.PDB. Revision 2.00 Hope Creek Generatin8 Station - STACS Flow Summary Report l
Co*erstact. Pressm=I.05 5 Sum Q-1 DE.2 foction-l.0E4 FCV=I 034 ftv=1.003 Tctrycroture-5.0E 3 i
LOPSSE Flow Stunmary Title Diameter Flow Mamman now NPSHA NPSH l
(in)
(gpm)
(gp:n)
(ft)
Ratio 1
wuu aus u.va i 2.n l
1 AE202 out 7.931 1,173.39 18E202 out 7 981 1,153.79 1HVH211 out 3.065 112.14 1DVH211 out 3 068 111.59 1FVH211 out 3.068
!!!.44 IBVH211 out 3.068 111.56 i AVH211 out 3 068 111.27 1EVH211 out 3.068 111.24 1 AE328/1BE328 comb. out 0.546 10 94 I AE328/1BE328 out 0.546 10 94 1 AK400 out 6.065 2,089.26 1 AVE 412 out 6.065 450.72 1 EVE 412 6 065 527.56 1 EVE 412 out 6.065 528.03 1 AE408/405/404 out 7.981 1,051.12 1CVE412 car 6.065 454 45 1GVE412 out 6.065 532.40 1CE40ll'405/404 out 7.981 1,090,13 IBVE412 out 6.065 524.49 IFVE412 out 6 06$
524.49 M Reverse Row Through Check Valve
&& Purnp Dow is Past End of Curve
~. -
~~a enee ve o es sa e e w n w v.wn G2/98 22:15 PROTO-FLO 4.01 by Proto-Pow:r Corporation - Serial CPFLWJO P o r 4 of a Public Semce Electnc and Gas. G:PSEOi11-385\\NEW Ulis'STACSUHS2.PDB - Revision 2.00 11 ope Creek Generating Station - STACS Flow Summary Repon Convergence Pressure =1 oE-5 k.m Q=1.05-2 FricLn-1454 FCV=I 054 PCV-1.C5 31ernperave=$.0E 3 LOP /SSE Flow Summary Title Diameter Flow Minunurc Flow h?SHA NPSH (in)
(gym)
(spm)
(ft)
Ratio s u v s. u ow.
v.vos aiu as IHVE412 out 6.065 607.22 iBE408/405/404 out 7.981 1,075.25 1BK400 out 6.065 1,542.72 1DE408/405/404 out 7.981 1,068.88 1AK403 out 6.065 569.50 IBK403 out 6.065 580.78 RE4859B2 out 0.957 12.75 RE4559A2 out 0.957 11.78 4
!! Reverse flow Through Check Valve
&& Pump Flow is Past Er.d ofCurve
" Flow Relow Minimum
$$ NPSH Availsble Below NPSH Required
e w-w mar vw m uy i g-mwgw - ccue ------- z e :f M5-~ 6 2 92 1f 0 ~ 16263391218 F. O U 31 62/9s 22.15 PROTO FLO 4.01 by Prot:r-Pcwer Corporatiori - Serial CPFL-0000 Pase i er ze Public Service E'ectric and Gas GAPSEOil1-383\\NEW L'HSiSTACSUHS2.PDB - Revision 2 00 Hope Creek Generstmg Station. STACS Heat Exchanger Data Report Conveguce Pnusure t 0E-3 Sum Q-t.052 Fru. tion-1.0E 6 FCV-1.0E 4 PCV=1.CE 3 T...-.;.st=5.0E-3 LOP /SSE 00E129 HX Type: Fixed Heat Load HX Status: On/ Notin &w Path Mir: Baseo. Inc.
Model: ES-24/16096 Dwas: PM050-0039-3 System Fluid:
Heat Load =
$00,000.00 BTU /hr 00X107 iLX Type: Fixed Heat Load IIX Status: On / Notin Flow Path Mfr. Ameri:an Std.
Model: 06060 Dwgs: PM050-0022 5 System Fluid:
Heat Lead -
2.240.323.00BW/hr IOC150 HX Type: Ftxed Heat Load HX Status: Off Mft:
Model:
Dwgs:
System Fluid:
Heat Load -
0.00BW/hr i
10ElI10 HX Type-Fixed Heat Load HX Status: On / Not m Flow Path Mfr: Basco,In:.
Model: 8A24A08072 Dwgs: P1342287 System Fluid:
Heat Imad -
Sl5,000.00BRI!hr 10El!4 HX Type: Fixed Heat Load HX S*atus: On / Not in &w Path I
{
Mfr: Gen. Elect. Co.
Model: MDE0965400 Dwgs: PM003-G-1-7 System Fluid:
Heat Load -
42,300.00 BRJ,hr 10E129 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: Basco. Inc.
Model: ES-24/18096 Dwp: PM050-0039-3 System Fluid-Heat Load -
10,750.00 BTIW 1
- - pm ~<. ns ~ e m m v s.m u2/9522:15 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Pase 2 or 26 Public Servi:c Electric and Oas - OnPSECTIl-355 NEW UHSiSTACSUBS2.PDB - Revision 2.00 Hope Creek Oenerating Station STACS Heat Exchanger Data Report Conversece: Pressure =1 oE 5 L.n Qal OE-2 Tnctel.DC4 FCV-1.DE4 PCV=1.3E.3 Tenveenwe=$ CE 3 LOP /SSE 10K107 HX Type: Fixed Heat Load HX Status: On i Sot in Flow Path Mft: American Std.
Model: 06060 Dwgs PM050-0022-5 Systern Fluid:
Heat Lead =
!.412,000.00 BW/hr 1 A1 Ell 8 HX Type: Fixed Heat Load H X Status: Ogg Mir:DeLaval/IMO Model: MDE1328000 Dwgs: PM012 0099 System Fluid:
Heat Lead =
0.00BTular IAIE201 HX Type: Shell & Tube HX Status: On / in Flow Path Mfh Graham Mfg. Co.
Model: 92-6 504 CGN Dwgs: PM069Q-0058 Tube Fluid: Brackish Water 12 ppt ShellFluid: Fresh Water Shell Flow - 9.743.87 Shell Temperatures - 117.04*F - 99.73*F Tube Flow = 10.316.00 Tube Temperatures = 92.40*F - 108.75'F Constmetion Type; TEMA G 1 Shella, O Shell Passes. 4 Tube Passes Shell Mio Area = 6.2530 fi^2, Design Shell Velocity = 3.900 ft/s, Shell Diameter = 92.000 Battle info: Spac.ng - 62.000 in. Thickness = 0.000 in, Ares - 0.000 ft^2, K = 0.000 Tubes: Din = 0.694 in, Dout - 0 750 in, Length = 42.00 ft, K - 9.50 Tube Pitch = 0.9375 in Tube Pitch Type - Triangular 5,700 of 5.700 Tubes Active UTubes - No Effective Area - 46,295.00 ft^2 Area factor = 0.9849 Fouling = 0.0000 (inside) 0.0012 (outside)
Hoff- 0.4888 l.
LMTD = 7.80$9 LMTD Correctiam FF = 0.7705 B - 1.0000 Heat Load =
83,362,926 23 BWihr UOverall = 299.38 STU4m/ft^2/*F l
l A2 Ells HX Type: F:xed Heat Load HX Sta:us: off Mir;DeLaval/IMO Model: MDE1328000 Dwgs: PM012-0099
' SystemFluid:
Heat Load -
0 00 BTU /hr 1
l a.
e.
,,,u l
i 6/2/98 22 15 PROTO-FLO 4.01 by Proto-P:wer Corporation - Serial #PFL-0000 r.se 3 or 26 Pub 1:c Service Electric and Gas - 0:\\PSEOi11-385WEW L'HS'.STACSL'HS2.PDB - Revision 2.00 Ilope Creek Generating Station. STACS Heat Exchanger Data Report Corscrpenes P osanal4ES Sum 0-1002 Pnctenal.GE-6 FCV-1.CE 4 I'CV-l.05 3 Terryerstss=$ OE 3 LOP /S.%.
l 1A2E201 HX Type: Shell & Tube HX Status: On /in Flow Path Mfr: Graham Mfg Co.
Model: 92-6 504 CON Dwgs: PM069Q-0058 Tube Fluid: Brac'dsh Water.12 ppt Shell Fluid: Fresh Water j
Shell Flow - 10,226 83 Shell Tengeratures = 117.04'F - 100.21*F Tube Flow = 10,270.00 Tube Temperatures = 92.40'F.109.18'F l
Construenon Type: TEMA G I Shells, O Shell Passes,4 Tube Pasas Shell Min Area = 6.2530 ft^2, Design Shell Veloesty = 3 900 ft/s, Shell Diameter = 92.000 Bame Info: Specirig = 62.000 in. Thickness = 0.000 in, Area = 0 000 ft^2, K = 0.000 Tubcs: Dm = 0.694 in, Dout = 0.750 m, Length = 42.00 ft, K = 9.50 Tube Patch = 0.9375 m Tube Pitch Type = Tnangular 5,700 of 5,"00 Tubes Active IJTubes = No Effectave Area = 46,295 00 ft'2 Area Factor = 0 9849 Fouling = 0 0000 (inside) 0.0012 (outside)
Hoff = 0.4888 LMTD = 7.8351 LMTD Corrections FF = 0.7761 Fb = 1.0000 Heat Losd =
85,145,743.76 BTU /hr 1:Overall-302.46 BTU /hr/ft^2/'F lAE1109 HX Type: Fixed Heat Load HX Status: off Mfr: Basco lec.
Model; 8A43A08048 Dwgs: PI-342287 System Fhaid:
Heat Load =
0.00 BTU /hr IAE!11 HX Type: Pited Heat Load HX Status: OniNotin Flow Path Mfr: General Elect.
Model: 264A4808 Dwas: PM003-TR 18 5 System Fluit Heat lead =
515,00100 BTU /hr IAEll2 HX Type: Fixed Heat load HX Status: On / Not in Flow Path Mft; General Elect.
Model: 114DB270 D w gs: PM003 G-1-7 Sys em Flaii Heat Load a 42,300.00 BTU,tr l
- na_c_,
,,g.
n l
649s22:15
. PROTO-FLO 4.01 by Prots-Power Corporation - Serial 6PFL-0000 Pase 4 of 26 Public Service Electric and Oss Of,PSEOil1-385.NEW UH5GTACSUHS2.PDB - Revision 2.00 Hope Creek Generating Stadon - STACS Heat Exchanger Data Report l
Converg: icc: Prespe=1.0E 5 Sum Q-1.0E-2 rncaan=1SW-6 Pcv=1.0F-4 PCV=1.0E 3 Temperat:ne $ OE-3 LOP /SSE I AE115 HX Type FixedHeat Load HX Status: On / Not in Flow Path Mfr: H.K Porter Co, Model: T-140963X45 Dwss: PE005@l2-9 System Fluid:
Heat lead =
10,750 00 BW/hr l
1 AEl16 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path Mk General Elect.
Model: 155B8243P001 Dwgs: PM003-T612 Systern Flutd.
Heat Lead =
5,412,000.00 BTU /hr I AEll7 HX Type. Fixed Heat Load HX Status: Off Mk General Elcet Model: MDE0924300 Dwga: PM003-0-1-7 l
Systern Fluid:
Heat Load =
0.00 BTU /hr IAE126 HX Type: Fixed Heat Load HX Status: Off M&: AmericanStd.
Model: 5-046 17 168-3 Dwgs: N1-B31-SI-120 Systern Flutd:
Heat Load -
0.00 BTU!br IAE130 HX Type: Fixed Heat load HX Status: oft i
Mfr: Ametek/Whitlock Model: 4-WISHT 4-A CB Dwgs: PM007-0031-3 System Fluid.
Heat Load -
0.00 BTU /hr 1AE202 10( Type: Fixed Heat Load HX Status: off Mft: Alfa-LavalInc.
Model; A 20 BXS Dwgs PM071Q-0010 System Fluid; fresh Water l
Heat Load =
0.00 D'IU/hr
- e u se se m m enuwwcws cm m a ca9 s m n ;5escasizas p. is. ss
]
6/2/9s 23:15 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Page 9 of 26 Publi: Sen-ice Electric and Gas C APSEGs!!-3 B5WEW UHS \\STACSUHS2.PDB Revision 2.00 j
Hope Creek Generstmg Station STACS Heat Exchanger Data Report i
remverwec: Preswre=107 5 Sum Oal.0E-2 Friction-l.0E 6 FCV=1 CE4 PCv=1.0F-3 Terrperande=5.0E-3 LOP /SSE lAE205 HX Type: Fixed Heat Load HX Status: On / r:: Flow Path Mft: Dcita Southern Model: 21 A9227AN Dwgs: NO-E11-B001-5 l
System Fluid: Fresh Water l
Tube Flow - 9,450.78 Tube Temperatures - 99 99'F 125.22'F l
Heat Losd =
132,500,000.00 BTU /hr l
1AE214 HX Type: Fixed Host Load HX Status: On / Not in How Pa&
Mfr:CVIIce.
Model: C735-9934 Dwgs PM04SQ-0071-4 i
System Fluid:
l Heat Load -
19,500,000.00 BTU /hr l
1AE21R HX Type: 131xed Heat Load HX Status: Off Mir: CVIInc, Model: C735-9934 Dwgs: PM048Q 0071-4 Sys:cm Fluid:
Heat Load 4 0.00 BTU /hr IAE278 HX Type: Nxed Heat Load HX Status: Off Mfr: CVIInc.
Model:
Dwgs: PM048Q System Flmd:
Heat Load -
0.00 BTU /hr IAt328 HX Type: Fixed Hest Load HX Status: On / m Flow Path Mfr: Parker-!!a:uson Model: HDTC-SS-6 2 Dwgs:
System Fluid:
Shell Dow - 3.03 ShcIl Temperatures - 99.99*F - 122.00'F Heat Load =
$5,000 00 BTU /hr
s em %,v-
_. ; w r w > m w w >. w -
mg.: c4 e a c E ~ T. 15,2 5 3 0 5 4 2 A 5 F.11 31 6/2/98 22:15 PROTO-FLO 4.01 by ProtooPower Corporation - Serial #PFL-0000 Page e or 26 1
Public Service Electne and Oss OfPSEGil1 385;NEW UMS'STACSLES2.PDB -Revision 2.00 Hope Creek Generating Station STACS Heat Exchanger Data Report i
crmergence. Pressuro=t 42 5 Sam Q-1.0E 2 Frstion=1 CE 6 FCV=I.GE 4 PCV=1.oE.i Terripcetrure=5.0s.3 LOP /SSE IAE404 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mfr AmencanSt1 Model: 17072 CPT Dwgs: PM018Q System Fluid: Fresh Water Tube Flow = 1,080 45 Tube Temperatures = 115.94*F - li k 48'F Heat Load =
1,353,000.00BIU/br IAE405 HX Type: Fixed Heat Load HX Str,tus: On/ inflow Path Mfr: American Std.
Model: 19084 CPT Dwas: PM01SQ System F'uld. Fresh Water Tube Flow = 1,077.93 Tube Temperatures = 105.82'F 115.94*F Heat Load =
5.412.000.00 BTU /hr l
IAE408 HX Type: Fixed Heat Load HX Strus: On /in Flow Path Mir: American Std.
Model: 19198 Dwgs: PM018Q System fluid: Fresh Wa:er 3
Tube Flow = 1,076 60 Tube Temperatures = 99.991 105.82*F I
Heat Load =
3.116.000 00 BTU.itr 1 AKIII HX Type: Fixed Heat had HX Status: On / Not in Flow Path Mfr: Carri:t Corp.
Model 19FAS$3B5005932 Dwgs: PM623 0002 9 System Fluit Heat Load =
502,781.00 BTU /hr 1AK202 HX Type: Fited Heat Load HX Sta:us: On iin Flow Path Mfr CVllac.
Model: C'JS-9909 Dwgs: PM048Q-0044 2 System Fluii Fresh Water Tube Flow - 6.15 Tube Tempentures - 99 99'F - 116.37'F fieat Load =
50,000.00 BTUs hr l
L _ _ _ _.. _. _ _ _ _ _ _. _ _ _ _ _ _ _ _ _ _
wm ye se o w vm,vo w.wse,. m r we ces sm vv 3eeze :s u s e
=.ic3r 6/2/9s 22:15 PROTO-FLO 4.01 by Proto-Power Corporcion - SerialitPFL-0000 Pm 7 of 26 Public Servsce Electric and Gas - G3PSEGIl 385WEW WS'.STACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station-STACS Heat ExchangerData Report 0,nvcepnw: hessur==1 OC-5 Sum O=1 AE 2 Friction =1.0E-6 FCV=t Ok.-4 PCV-1 CE ) Temperstre=5 CE 3 LOP /SSE lAK400 HXType: Fixed Heat Load MX Status: On /in Flow Path Mft: Carrier Corp.
Model: 19FA455B122022 Dwgs: PM723Q System Fluid: Fresh Water Tube Flow -2,086.02 Tube Temperatures - 99.99'F - 107.26'F Heat Load -
7,530,700.00 BTU /hr lAK403 HX Type: Fixed Heat Load HX Status: On / m Flow Path Mfr: Carrier Corp.
Model: 19FA441Bil42020 Dwgs: PM723Q SystemFlutd. Freshwater Tube Flow = $66.40 Tube Temperatures - 99.99'F - 108.90*F Heat Load -.
2,515,340.00 B'IU/hr LAP 176 HX Type: Fixed Heat Load HX Status: Oo / Notin Flow Path Mfr: Camer Corp.
Model 19FA999100718 Dwgs: PM623118 System Flutd; Heat Lead =
100,000.00 BT(1/hr IAP202 1 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mfr; Grabarn Mfg. Co.
Model: 6X4C-12 Dwgs: Ni-El1-C002 51 System Fluid. Fresh Water Tube Flow - 23.15 Tube Temperatures = M.99'F - 130.43'F Hest Lead -
350,000.00 BTU /hr l
1AP202-2 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mfr: Graham Mfg. Co.
Model: 992C430BX Dwgs: NI-El1 C002-6 System Fluid. Fresh Water Tube Flow - 9.86 Tube Temperatures = 99.99'F - 102.04*F Heat Load =
10,000.00 Bmlu l
- ~ -
6/2/98 22.15 PROTO-FLO 4.01 by Prots P:wer Corporation - Saia! #PFL-0000 Pase a er 26 Pub:ie Serv:ce E!ectric and Oss - 0:\\PSEOill 385WEW UHS'STACSUHS2.PDD - Revision 2.00 Hope Creek Generating Stanon STACS Heat Exchanger Data Report Cmcrgencc. P cmrcel.0E-$ Sum Q=i.0E 2 Friction-1 CE-5 FCV=1.cE-4 PCv=1.0E-3 Ternperature*5.0E 3 LOP /SSE 1 AVE 412 HX Type: Fixed Hest Load HX Status: On / in Flow Psih Mft: Trane Co.
Model MDE1291600 Dwgs: PM731Q System Thdd: Fresh Water Tube Flow - 450.25 Tube Temperatures = 99.99'F - 104.91*F HeatLoad=
1,100.000.00 BTU /hr l
1 AVHI13 HX Typc: Fixed Hest Load HX Status: On / Not in Flow Path M&: Amer. AirFhr.
Model: H)6MPACYA Dwgs: PM611 A-0030-4 System Flund:
Heat Load =
502,781.00 BTU /br 1AVH116 HX Type: Fixed Heat Load M X S atus: On / Not in Flow Path M&: Amer. Airfl2.
Model. H36MPACYA Dwgs: PM611A-0031-4 System Fluid:
Heat Load =
$30.000.00 BTU /hr
!AVM208 HXType: Fixed Heat Load HX Status: On / in Flow Path Mfr: Amer. Air fitt.
Mode 1: MDE1572400 Dwas: PM711Q System Fluid. Fresh Water Tube Flow e 32.11 Tube Tempera *un:s = 96.88*F - 99.70'F Heat Load =
43.000.00BI1J/hr IAVH209 HX Type: Fixed Heat Load HX S*atus: On / in Flow Path Mfr: Amer. Air Fltr.
Model: MDE1571400 Dwas: PM711Q System Fluid Fresh Water Tube Flow - 77.09 Tube Tempersnares = 99.99'F - 103.00'F Heat Lom I =
115,000 00 BR'/h:
= _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ - _ _.
o m-m o m m c e r o om ao 6/2/98 22:15 PROTO FLO 4.01 by Proto-Power Corporation - Serial CPFL 0000 Pase 9 of 26 Public Service Electric and Gas - 0:TSEOu l-385WEW UHS \\STACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station. STACS l
Heat Exchanger Data Report Cr.nvergenr Preasurr=1 Uk-S bam Q-1.0G-2 incdon=1.Dd4 FCV.I.0E-4 PCv=I.0k-1 Temperara=-3hii-3 LOP /SSE 1AVH210 HX Type: Fixed Heat Load HXSus: On / m FlowPath Mfr: Amer. Air Ehr.
Model MDE1570300 Dwas: PM711Q System Fluid: Fresh Water T Ae Flow - 141.97 Tabe Ternperatures - 99.99'F - 102.97'F HesILoad-210,000.00 BTU /hr 1 AVH211 HX Type: Fixed Heat Load HX Stanis: off MA: Amer. Air Fitr.
Model: MDE1573500 Dwgs: PM711Q System Fluid: Fresh Water Heat Load =
0.00 BTUar 1 AVH213 HX Type: Fixed Heat Load HX Status: oty Mft: Amer. Air Fltr.
Model: MDE2475600 Dwgs: PM786Q System Fluid: Fresh Water Heat Load =
0.00 BTUar 1B1 Ell 8 HX Type: Fixed Heat Load HX Status: On / Not in Fkw Path Mft: DeLaval'IMO Model: MDE1328000 Dwgs: PM012-0099 System Fluid:
j Heat Load =
400,000.00 BTU /hr i
1
_- - -. ~..
.,,__._-.,_=.--._;-;-
6/2'98 22:19 PROTO-FLO 4.01 by Prmo-Power Corporation - Serial #PFL-0000 ecss 10 of 24
_ Pub!]: Service Electric ar.d Gas - 0:\\PSEGill-385\\NEW UHS'STACSUHS2.PDB - Revision 2.00 l
Hope Creek Gene:ating Station STACS l
Heat Exchanger Data Report t anvergence. Preware=1 tw$ sum Q=1.0f'-2 Frction=l.CE4 FCV=14E.4 PCV-l.0E4 Temprwure=S.0E-3 LOP /SSE IBIE201 HX fype: Shell& Tube HX Status: On / inflow Path Mir. Graham Mfg. Co.
Model. 92 6-504 CGN Dwgs: PM069Q-0058 l
Tube Fluid. Brackish Water-12 ppt Shell Fluid: Fresh Water I
Shell Flow = 9,610 60 -
Shell Temperatures = 114 24*F - 96.72*F Tube Flow - 10,106.00 Tube Temperecues - 89.21'F 105.90'F Construe:lon Type:' LEMA G 1 Shells, O Shell Passes,4 Tube Passes Shell Min Area -= 6.2$30 fr2, Design Shell Velocity - 3.900 ft/s, Shell Daarneter = 92/J00 B1ffle info: Spacmg = 62.000 in, Thickness = 0.000 in Area = 0.000 ft^2, K = 0.000 Tubes: Da = 0.694 in. Doat = 0.750 in, Length = 42.00 ft, K = 9.50 Tube Pitch = 0.9375 in Tube Pitch Type = Triangular 5,700 of 5,700 Tubes Active UTubes = No Effective Area -46.295.00 ft^2 Area Factor = 0.9849 Fouling = 0.0000 (insidel o.0012 (outside)
Hoff = 0.4888 LMTD = 7.9225 LMTD Corrections FF = 0.7698 Pb = 1.0000 Heat 1. cad =
83,389,813.35 BIU hr UOverall = 295.35 BTU /hrrfr^2/*F iB2E118 HX Type: Fixed Heat Load HX Status: On/ Not in Flow Path Mfir.DeLaval/IMO Model: MDE1328000 Dwas: PM012-0099 Systern Fluid:
Heat Lead =
400,000.00 BTUh l
l 1
I
m - v s m m m m ~- m v y. w r ~. r --- - v _ m m
,, a-- -.-. :,,;. n ---
6/2/9s 22:!$
PROTO-FLO 4.01 by Proto-Power Corporation - Scrial CPFL-0000 Page 11 of 26 p
Pabhc Semce Electnc and Gas - G:TSEG\\ll-385\\NEW UHSiSTACSUHS2 PDB - Revision 2.00 Hope Cicek Gen:radng Station - STACS l
Heat Exchanger Data Report conntsence: Pressurc=1.CE-3 Sam Q-10C-2 Frice.on=1.OE-6 FCV*l.0E a PCV=1 cH Temperara e=$ 0E-3 LOP /SSE IB2E201 HX Type: Shell & Tube HX Status: On / in Flow Path Mfr: Graham Mfg. Co.
Model: 92 6 504 CGN Dwgs: PM069Q-005B Tube Flmd Brackish Water - 12 ppt ShellFluid: Fresh Water Shell Flow - 9.952.29 Shell Temperatures = 114.24'F 96.98'F Tube Flow = 10,190.00 Tube Temperatures = 69.21'F - 106.09F Construction Type. TEMA G 1 Shells, O Shell Passes,4 Tube Passes Shell Min Area = 6.2530 ft^2, Design Shell Velocity = 3.900 Als, Shell Diameter e 92.000 Baffic Info: Spacing = 62.000 in Thielmess = 0 000 in, Area = 0 000 ft^2, K = 0.000 Tubes: Din = 0.694 in. Dout - 0.750 in, Length = 42.00 A. K - 9.50 Tube Pitch = 0.9375 in Tube Pitch Type = Triangular 5,700 of 5,700 Tubes Acuve UTubes - No EtYective Area = 46,295.00 ft*2 Area Factor = 0 9849 Fouling = 0.0000 (uiside) 0.0012 (outaide)
Hof- 0.4888 LMTD - 7.9560 LMTD Correenons FF - 0.7747 Fb - 1.0000 Heat lead -
85,083,411.22 BTU /hr UOverall = 298.ll BTU /hr/ft'2/*F IDEl100 HX Type: Fixed liest Load HX S:stus. On /Not in Flow Path Mfr: Basco inc.
Model: 8A44A08048 Dwgs: P1-342287 System Fluid:
Heat Load -
461,650.00 BTU /hr IBElII HX Type: Fixed Heat Load IIX Status: On iNotin F]cw Path Mft: Genera 1 Elect.
Model: 264A4808 Dwgs. PM003-TR-lS-5 System Fluid:
Heat Load -
9,360.000.00 BTU 1 r IBE112 HX Type: Fixed Heat Load HX Status? On / Not in Flow Path Mfr: General Elect.
Modeh 114D8270 Dwgs: PM003-G-t-7 5ystern Fluid:
Heat Load =
5,487,500.00 BTU /hr
- uu tu,s u
- a r en encrewowen r.cre zea aas s;:sz va ses:53s1z:a
- p. Iw at 6/2/9s 22:15 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Pese 12 or 26 Public Semce Electnc and Gas - G:'.PSEOill-385\\NEW UHS \\STACSL71S2.PDB - Revisice 2.00 Hope Creek Generating Stanon-STACS Heat Exchanger Data Report Cortverse ce: Pressure tS15 5 Sum Q-l.')E 2 Trcto==1SE.6 FCV-11]E 4 PCV-1.0E.3 Tempereurs+$ OEr3 LOP /SSE IBEl15 HX Type: Fixed Heat Load HX S:stus: On / h*ct in Nw Path Mft: H K. Porter Co.
Mode:: T-140963X45 Dwgs: PE005-0012 9 System Fluid:
Heat Load -
515,000.00 BTU /hr IBEl16 HX Type: Fixed Heat Load HX Status: On / Not in now Path M&: General E'.ec*
Model: !!$B8243P001 Dwgs: PM003-T6-12 System Fl:ud:
Host 1. mad -
42,500.00 BTU /hr IBE117 HX Type: Fixed Heat toad IC* Status: Oa/ Notin Flow Path Mfr. Gen: ral Elect.
Model: MDE0924300 Dwgs: P WOO 3-0-1-7 System Fluid:
Heat Load =
8,050,000.00 BTU /hr 1BE126 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path Mir: Arnetican Std.
Model: 5-0046 17-16%-3 Dwgs: N1-B31-SI 120 System Ruid:
Heat Load = -
5.530,000.00 BTU /hr IBE130 HX Type: Fixed Heat Load HX Status! On / Not in Row Path Mfr: Ametek/Whitlock Model: 4 W18HT-4-A-CB Dwga: PM007 0031-3 System Fluid:
Heatload =
42,300 00BTC/hr i
IBE202 '
HX Type: Fixed Heat Load HX Status: Off Mfr: Alfa Lava! Lnc.
Model: A-20-BXS Dwas: PM071Q-0010 Syssem Fluui: Fresh Wate:
Heat Load
- 0.00 BTU /hr i
1' l
~ *-'
.,m.
6/2/9822.15 PROTO-FLO 4.01 by Proto Power Comoration - Seri:1 #PFL-0000 p.,13 er 2e Public Service Electne and Gas - GnPSEG11-185WEW LilS'.STACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station STACS Hest Exchanger Data Report Convergence: Premrtal CE-S brn Q=1 CE-2 F coon =1 DE-6 FCY-1.0T;A PCV 1.0E4 Tenverstunr-5.0E 3 LOP /SSE IBE205 HXType: Fixed Hest Load HX Status: On / in Flow Path Mfr: Delta Southern Model: 21A9227AN Dwgs: NO Ell 8001-5 System Fluid: F esh Water Tube Flow - 9.185.94 Tube Ten:peratures - 96.88*F - 125.89'F Heat Load =
132,500,000.00 BTU /hr 1BE214 HX Type. Fixed Heat Load HX Status: On / Not in Flow Path Mir: CVIinc.
Model: C735-9934 Dwgs: PM048Q 0071-4 System Fluid:
Heat Load -
9,565.00 BTL*/hr 1BE218 HX Type: Fixed Hess Load HX Status: On/ Notin Flow Path Mfr: CVI Ir.c.
Model C735-9934 Dwas: PM048Q-00714 System Fluid:
Heat IAnd =
10,750.00 ETU'hr IBE278 liX Type: Fixed Hest Load HX S stus-On / Not m Flow Path Mfn CV1 inc.
Model.
Dwgs: PM045Q System Fluid.
Heat Load =
6,000.00 BTD/hr IBE328 MX Type: Fixed HeatImad HX Staars: On / in Flow Path Mft: Parker-Hanison Model: HDTC SS 6 2 Dwgs:
System Fluid:
Shell Flow = 5.86 Shell Temperansres = 99.99'F - 118.90*F Heat Load -
55.000.00 BTU /hr l
l l
l I
c.
6/2/9822.15 PROTO-FLO 4.01 by Proto P wer Corporation - Serial #PFL-0000 Pos. u er 26 Pub!ic Service Electric and Gas - 02SEOill-385WEW UHS'$TACSL't!S2.PDB - Revmon 2.00 Hope Creek Generstmg Stabon - STACS Heat Exchanger Data Report Cemnence Prenn=1.00-5 Sum Q-1.0E 2 Triction=1054 FCV=1 C2 4 PCV=1.0L-3 Tewpernaae=$.0E-3 LOP /SSE IBE404 HX Type. Fixed Heat Load HX Status-On !in Flow Path Mir: Amencan Std.
Model: 17072 CPT Dwp: PM01BQ Synem Fluid: Fresh Water 1
Tube Flow - 1,074.60 Tube Ten:peratures = 112.93*F - 115.45'F Heat load -
1,353,000.00 BTU /hr IDE405 H X T n w: Fixed Hea: Load HX Status: On / in Flow Path Mfr: American S d.
Model: 19054 CPT Dwgs: PM018Q 5
System Flutd: Fresh Water Tube Flow = 1,072.16 Tube Temperatures - 102.74*F 112.91*F Heat Load =
5,412,000.00 BTU /hr IBE405 HX Type: Fixed Heat Load HX Status: On / m Flow Path Mfr: American Std.
Model: 19198 Dwgs: PMOISQ SystemFluid: Freshwater Tube Flow = 1,070.87 Tabe Temperatures - 96.88'F - 102.74'F Heat load -
3,118,000.00 BTU /hr 1BKill HX Type: Fixed Hest Load HX Status: On / Notin Flow Path Mft: Carner Corp.
Model: 19FA553Bf005932 Dwgs: PM623-OOO2 9 System Fluid:
Heat Lead -
19,500,000.00 BTU /hr IBK202 HX Type: Fixed Heat Load HX Etatus: On / La FlowPath M tr. CVI Inc.
Model: C735 9909 Dwgs: PM048Q-0044-2 tutem Fluid: Fresh Weter Tube Flow - 5.92 Tube Temperatures = 96.88'F - 113.87'T
[
Host Load a 50,000.00 BTU /hr I
l t
l l
6/29823.15 PROTO FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 t'ase is or 26 Put:lic Service Electric and Gas - G:PSEG'.11-3851NEW LJH5STAC5 UHS 2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Conversnee Pressure-1.0E4 Sum Q=1.0E-2 fnetion=1 CE4 FCVal.0F-4 PCV-1.0D3 Tempr'sase=ioE.3 LOP /SSE IBK400 HX Type: Fixed Heat Load RX Status: On / m Flow Path Mft: Carrier Corp.
Model: 19FA4558122022 Dwgs; PM7230 System Fluid. Fresh Water Tube Flow = 1.839 58 Tube Ternperatures - 96.88T - 105.11*f Heat Load =
7,530,700.00 BTUh IBK403 HX Type: fixed Heat Load HX Status: On / in Flow Padt Mfr: Camer Corp.
Model: 19FA441B1142020 Dwgs: PM723Q System Fluid: Fresh Water Tube Flow - 579.73 Tube Temperatures = 96.88'F = 105 6l'F Heat Losd -
2,515.340.00 BR /br i
!BP176 HX Type: Fixed Hect Load HX Status: On / Not in Flow Path I
Mfr: Camer Corp.
Model 19FA999-1007-18 Dwgs. PM623118 System Fluid:
HearLond=
100,000.00 BTUh 1BP202 1 HX Type; Fixed Heat Lund HX Status: On / in Flow Path Mft: Graham Mfg. Co.
Model: 8X4C 12 Dwgs: N1-El1-C002-$1 System Fluid: Fresh Water Tube Flow = 28.30 Tube Temperatures - 96.88'F-121.76'F 1
Heat Load =
330,000.00 BnJ/hr l
IBP202 2 HX Type: Fixed Heat baad HX Status: On / m Flow Path Mft: Graham Mfg Co.
Model: 992C430BX Dwgs; N1-E;'-C002 6 System Fluid: Fresh Water Tube Flow - 10.14 Tube Temperatures = 96.88'F - 98.86*F Heat Load =
10,000.00 BTU /hr l
1 I
i I
6/2/9s 22:15 PROTO.FLO 4.01 by Proto-Power Cceporation - Serial #PFL-0000 Pces16 of 30 Public Service Electne and Gas - G6PSEGill.385WEW L'HS\\STACSLTIS2.PDB. Revision 2.00 Hope Creek Generating Station. STACS Heat ExchangerData Report Cense sera:Preuwl455 sam Qa1452 rrienan=1.GE4 FCWI CE-4 PCV-1 CL3 Temperature =5.0E-J LOP /SSE IBVE412 HX Type: Fixed Heat Load HX Status: On / in Nw Path M&: Trane Co.
Model. MDE1291600 Dwgs: PM731Q System Fluid: Fresh Water Tube Flow = 524.04 Tube Temperatures - 96.88'f - 101.10T j
Heat Load =
1,100,000.00BW/br 1BVH113 HX Type: Fixed Heat Load HX Status: off Mft: Amer AirFitr.
Model: H36MPACYA Dwgs: PM611 A-0030 4 Sysicm Fluid:
l Heat Load =
0.00BTt'/hr l
IBVH:16 HX Type: 71xed Heat Load HX Status: On / Not in Flow Path Mh: A:ner. Air Fiz.
Model: H36MPACYA Dwgs: PM611 A-0033 4 System fluid:
Heat Load :.
530,000.00BW/hr IBVH208 HX Type; Fixed Heat Load HX Status: On / in Flow Path Mft:Arner. Air Ficr.
Model: MDE1572400 Dwgs: PM71IQ Sysicm Fh:id. Fresh Water Tube Flow = 31.63 Tube Temperatures - 96.88'F 99.74*F Heat Loed -
45,000.00 BTL*/hr iBVH209 MX Type: Fixed Hea: Load HX Stams: On /in Flow Path Mfh Amer. Air F1tr.
Model: MDE1571400 Dwgs: PM71IQ System fluid. Fresh Water Tube Flow - 105.06 Tube Temperatees -s 99.997 102.20'F Heat Load =
115,000.00 BIUhr m______.___.. _ _ _ _. _
r sun u za uiza e--
e num m - c ;ma - - -
m-- m a s iz az 1. - : sc 5 3 y5 ai--
.aa
,1 629822:15 PROTO-FLO 4.01 by Proto-Power Coporation = Serial CPFL-0000 case 17 or 26 Public Service Electric and Gas 0:PSEG\\ll-385'NLW UHSiSTACSUHS2.PDB. Revuton 2.00 Hope Creek Generstmg Station STACS Heat Exchanger Data Report Conve gru Prraurs=1.0E-5 Sum Q-1,0E-2 Fncton=1.0E4 FCV I 96 4 WJv=14t-3 Tempe sn.re=5 DE-3 LOP /SSE IBVH210 HX Type Futed Heat Load HX Status: On / m Flow Fath Mft: Amer. Air Fitr.
Model: MDE1570300 Dwgs: PM71IQ System ficid: Fresh Water l
Tube flow = 148.25 Tobe Temperatures = 96.88'F - 99.73'F j
Heat Load =
210,000.00 BTUAr IBVH211 HX Type. Fixed Heat Load HX Status: Off Mfr: Amer. Air Fitr.
Model: MDE1573500 Dwp: PM71IQ System Fimd: Fresh Wawr Heat Load -
0.00 BTU /hr IBVH213 HX Type-Fixed Heat f.oad HX Status: off Mft: Amer. Air Fitr.
Model: MDE2478600 Dwas: PM786Q System Fluid: Fresh Water Heat Load e 0.00 BTU,hr ICIElla HX Type: Fixed Hest Load EX Status: On / Notin Flow Path Mfr. Delaval/IMO Model: MDE1328000 Dwgs: PM012-0099 System Fluid Heat Load =
400.000.00 BTU /hr IC2Elth HX Type-Fixed Heat Losd HX Status: On / Not in Flow Path Mfr: DeLaul/IMO Model: MDE1328000 Dwgs: PM012 0099 System Fluid.
Heat Lead =
400.000.00 BIL*/hr ICEl12 HX Type: Fixed Hest Load HX Status: On / Notin Flow Path Mfr General Elect.
Model: 114D8270 D w ss: PM003-G-1 7 System Fluid.
Heat Load =
5.487,500.00 BTL*/nr
6/2/98 22:15 PROTO FLO 4.01 by Pmts-Power Corporation - Serial #PFL-0000 Page 18 of 20 Pubhc Semce Ele:tne and Gas - G ;PSECt.11 385WEW UllS\\STACSUHS2 PDB - Revision 2 00 Hope Creek Gecc: arms Station - STACS Heat Exchanger Data Report Conscrgence. Pressurcal OE 5 St.m Q-t CE.: fnction=LCE 6 T'CV=1 DE-4 PCV-1.0F.-) Ternpcanse=5.0E 3 LOP /SSE ICE 130 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: Ametek/Whitlock Model. 4-W18HT-4 A CB Dwgs: PM007-0031-3 System Muid:
Heat Load -
42,300.00 B1t/hr ICE 404 HX Type: Fixed Heat Load HX Status: On /in F:ow Path Mfr Amencan Std.
Model: 17072 CPT Dwgs: PM018Q System Fluid: Fresh Water Tube Flow - 1,089.46 Tube Temperature = Il5.81'F !!8.32*F Heat Load =
1.353.000.00B1V/hr ICE 40$
HX Type. Ftxed Heat Load HX Status: On / in Flow Path Mfr: American SM.
Model: 19064 CFf Dwgs: PM018Q SystemFluid: Fresh Water Tabe Flow = 1,086 95 Tube Tempentures = 105.78'F - 115.81*F Heat Load =
5 412,000.00 BTU /br ICE 408 HX Type: Fixed Heat lead HX Status: Os /in Flow Path Mfr: American Std.
Model: 19198 D w gs: PM018Q System Fluid: Fresh Water Tube Flow = 1,085.62 Tube Tempersmres = 99 99'F-105.78'F Heat Load -
3.11S.000.00 BTU /br ICK111 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: Carrier Corp.
Model: 19FA55385005932 Dwgs: PM623-0002-9 System Fluid-Heat Load =
19,500,000.00 BTUihr l
. un u
- z c. a. : en em v.- m
.ee~
- . a.: m em i. awea 2=L=l:
F.
-:aa l
& 2/9s 22:15 PROTO-FLO 4.01 by Prots-Pow:r Corporation - Serial tiPFL-0000 p ;,i9 or 26 y
Public Scruce Electne and Oss - G:$$EG'Il-385\\NEW UH5$TACSUHS2.PDB Revisios 2 00 l
Hope Creek Generating Stadon. STACS Heal Exchanger Data Report Cueverver.ce Presswe=1 Jh.-$ Sum Q=1.Dr-2 Fnctional OE-6 FCV-1.0C.4 PCV=1 Gh-3 Tenpersmr:=.S.0E 3 LOP /SSE 1 cpl 76 HX Type: Fixed Heat Load HX Status: On / Not iri Flow Path Mfr: Carrier Corp.
E del: 19FA999100715 Dwgs: PM623-Il8 System Fluid:
Heat toad =
100,000.00 BTU'hr 1CP2021 HX Type: Fixed Heat Load liX Status: On / in Flow Path Mft: Oraham Mrg. Co.
Model: EX4C-12 Dwas: N1 El1.C002 51 System Fluid; 5 hell Flow = 2s.29 Shell T+.iares = 99.99'F-124.90'F Heat Load -
350,000.00 BTU.br 1CP202-2 HX Type: Fhed Heat Load HX Status: On / in Flow Path Mfr: Graham Mfg. Co.
Model: 992C430BX Dwgs: N! El1-C002-6 System Fluid. Fresh Water i
Tube Flow - 10 32
'Iube Temperatures - 99.99'T - 101.94*F j
Heat Losd -
10.000.00 BTU &r 1
ICVE412 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mft: Trane Co.
Model: MDE1291600 Dwgs: PM731Q System Fl. tid. Fresh Water Tube Flow = 453 99 Tube Temperamres - 99.99'F - 104. 87'F Heat Load =
1,100,000.00 BTU.tr ICVH113 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr Amer. Air Fitr.
Model: H36MPACYA Dwgs: PM611A.0030-4 System Fluid-Heat Load -
502,7s1.00 BTUtr I
l l
_____m.
- ~~, -
- - use - u
<~as v2/98 22.15 PROTO-FLO 4.01 by Proto-Power Corporati:n Serial f;PFL-0000 Pass 20 of 26 Public Semce Elect:ic and Gas - G:PSEG\\11-385\\NEW UHSWTACSOHS2.PDB. Revision 2.00 Hope Creek Generating Stanon - STACS Heat Exchanger Data Report cw...seu.e: mouwe-a ac-5 son Q-1.0E-2 Fricuoerd OE.6 FC%1.ck-4 PCV=I oE-3 Tempets.*wS.0E 3 LOP /SSE 1CVH210 HX Type: Fixed Heatlead HX Status-On /in Flow Path Mft: Amer. Air Fltr.
Model: MDE1570300 Dwgs: PM71IQ Systern Fluid: Fresh Water Tube Flow = 125 44 Tube Temperatures - 99.09'F 103.20*F Hest Load -
200,000.00BWhr ICVH211 HX Type: Fixed Heat Load MX Status: off Mft: Amer. Air Fitr.
Model: MDE1573500 Dwgs: PM71IQ System Flu 2d: Fresh Water Heat lead -
0.0(TBTU,hr l
ICVH213 HX Type: Fixed Heat Load HX Status: off 1
Mfr-Arner. Air Fitr.
MWel: MDE2478600 Dwys: PM786Q SystemFlmd: Fresh Water Heat Load -
0.00Bmhr IDEll2 HX Type: Fixed Heat Land HX Status: On! Not in Flow Path Mfr: General Elect.
Model: 114D8270 Dwas: PM003-G-1-7 System Fluid.
1 Heat Load =
5,487,500.00 BTU /hr l
1DE404 HX Type: fixed Heat Load HX Status: On / in Flow Path Mfr: Arncncan Std.
Model: 17072 CPT Dwgs: PM018Q SystemFluid: Fresh Water Tube Flow - 1,%8 23 Tube Temperatures - 113.00*F.115.56*F 1
l Heat Load =
1.353,000.00 BTU /hr
)
i t
I l
l.
e l~
l L_-_-__------_---_
.w u u - u m - m
.- - m-wc. -- --- --- - c u a- --- ym-, g-, u.- n y 2, e --- -------- - m -, t 3-y 1-- --- -
(
6'2/98 32:13 PROTO-FLO 4.01 by Proto-Power Corporadon - Scrial CPFL-0000 case 2 or :6 i
Public Service Electne and Gas - GAPSEG\\11 385'NEW UHS \\STAC51JHS2.PDB - Revision 2.00 t
l Hope Cicek Generaeng Station - STACS l
Heat Exchanger Data Report I
Cone sence: Pronure='.0E 3 Surr.Q=1.0E-2 Frieta-LDE 6 FCV-1 CE-4 PCv=t.0E-3 Ten:perature-!.0E 3 LOP /SSE
]
l IDfA05 HX Type: Fned Heat Load HX Status: On / in Flow Path Mfr: American Std.
Model: 19054 CPT Dwgs: PM018Q SystemFluit Fresh Water Tube Flow - 1,065.79 Tube Temperatures - 102.77'F - l 13.00*F l
Heat Load -
5.412,000.00 BTU /lir i
IDE406 HX Type. Fixed Heat Load HX Status: On / in Flow Path Mfr: Amencan Std.-
Model: 19198 Dwgs: PM018Q System Fluid. Fresh Water Tube Flow = 1,064.30 Tube Temperatures - 96.88'F - 102.77'F Heat Lead -
3,118,000.00 BTUhr 1DK111 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path Mfr: Carrier Corp.
Model: 19FA553B5005932 Dw5s: PM623-0002-9 System Fluid:
Heat Load -
19.500,000.00 BTU /hr 1DP176 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: Carner Corp.
Model: 19FA999-1007-18 Dwss: PM623-118 Syst:m Flmd.
Heat Load -
100,000.00 BTUrbr 1 D'e202-1 HX Type: Faed Heat Load HX Status: On / m Flow Path Mft: Oraham Mfg. Co.
Model: 8X4C 12 Dsgs: N1.El t-C002-51 l
SystemFluid: Fresh Water Tube Flow - 25.50 Tube Temperatures - 96.88'F.124,49*F Heat Lead -
350,000.00 BTUtr i
l 1
~. _.
6/2/9s 22:15 PROTOELO 4.01 by Proto-Power Corporation - Seri:14PFL-0000 Pcai 22 << 2e Pubhc Service Electric and Gas - G:'.PSEGill.385\\NEW UH5iSTACSUMS2.PDB - Revision 2.00 Hope Creek Geocrating Station STACS Heat Exchanger Data Report Comergence. Preuurc=1.OE-5 Sum Q=1.0E-2 Fricuon-1 CE 6 FCV-1.00-4 PCval.0E 3 T:'riperar.rc=J.0E 3 LOP /SSE IDP202 2 HX Type: Fixed Heat Load HX Status-. On hn Flow Path Mfir: Graham Mfg. Co.
Model: 992C430BX Dwgs: N1-Ell-C002-6 System Fluid: Fresh Water Tube Flow = 9.97 Tube Temperatures = 96.88'T 98.90'F Heat Load =
10,000.00B'IU/hr 1
i IDVE412 HX Type: Fixed Heat Load HX Sta'us: On / in Flow Path Mft: Trane Co.
Model: MDE1291600 Dwgs: PM731Q Syaiem Fluid: fresh Water Tube Flow - $20.08 Tube Temperatures = 96.88'F - 101.13 F HeatLoad=
1,100,000.00 B1U.'hr iDVH113 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path 1
Mh: Amer. Air Fitr.
Model: H36MPACYA Dwas PM611A-0004-7 System Fluid:
Heat Load =
502.781.00 BTU /hr
!DVH210 HX Type: Fixed Hcat Load HX Status: On /in Flow Path Mfr: Amer. Air F1tr.
Model MDE1570300 Dwgs: PM71IQ System Fluid: Fresh Water Tube Flow = 14411 Tube Temperatures = 96.88'F - 99.67T j
Heat Load -
200,000.00 BTU <br IDVH211 HX Type: Fixed Heat Load HX Status: off Mfir: Amer. Air Fitt.
Model: MDE1573500 Dwas: PM7110 SystemFluid: Fresh Water Heat Lead =
0.00BTUsht i
l 4
4 1
l
J ur4 ez'ee al:40 Fc F a o 7 0 -F C tJEF.CRs 10[ 4J6 5292 TC 160330$1119 F. 16e si 6/r90 23:15 PROTO-FLO 4.01 by Proto-Powcr Corporation - Serial #PFL-0000 Page 23 of 20 Pub!:c Service Electric and Gas G:\\PSEG\\11-385\\NEW UNS'STACSUMS2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Ccewegence: Presu,rc=1 OF-5 Sum Q=10E-2 frn: tion-l.0E-6 FCV-1.0E-4 PCV=10F-1 Terripersture='.0E-3 LOP /SSE IDVH213 HX Type: Fhed Heat Load HX Status: Off Mfr Arrer. Att Fitr.
Model: MDE2478600 Dwgs: PM786Q SystemFlu:d; Fresh Water Heat Load -
0.00 BTU /hr IEVE412 IlX Type: Fked Heat Load HX Status: On /in Flow Path Mft: Trane Co.
Model: MDE1291600 Dwgs: PM73IQ g
System Fhtid: Fresh Water Tube Flow = $27.50 Tube Temperatures = 99.99'F - 104.19'F Heat Load -
1,100,000.00 BTU.hr IEVH113 HX Type: Fixed Heas Load HX Status: On / Notin Flow Path Mir; Arner. Air F1tr.
Model: H36MPACYA Dwgs: PM6L1A 0004 7 System Fluid.
Heat Lead -
502,781.00 BTU /hr IEVH210 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mfr:Arner. Air Fitt.
Model; MDE1570300 Dwgs: PM71IQ System Fluid Fresh Water Tube Flow = 142.7i Tube Temperatures - 99.99'F - 102.96 F Heat Lotd =
210,000.00 BTU.hr IEVH211 HX Type: Fixed Heat Lead HX Status: Orr Mfr: Amer. A:r FItr.
Moden: MDE1573500 Dwgs: PM71IQ SystemFluid; Fresh Water Heat Lead,
0.00 BTU /hr 1EVH213 HX Type: Fixed Heat Load HX Status: Ofr Mfr Amer. Att Fitr.
Model: MDE2478600 Dwgs: PM786Q System Fluid. Fresh Water Heat Load =
0.00 BTU /br
~_ -
C2,98 22:15 PROTO-FLO 4.01 by Proto-Power Corporati:n = Seri:1 #PFL.0000 Pap 24 or a Public Scrvice Electric and Gas - GnPSEG' 11 385WEW UIIS\\STACSUHS2 PDB. Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Convegrce-Prww1.0E 3 Sum Qal.0E 2 Fricacrial CE 6 FCv=1.0E 4 PCV*l CE 3 Teeperatum=.4.0E.3 LOP /SSE l
IFVE412 HX Type: Fixed Heat Load HX Status-On /in FlowPath l
Mft: Trane Co.
Model: MDE1291600 Dwas: PM731Q l
Systern Fluid: Fresh Water Tube Flow " 524.04 Tube Temperaintes - 96.88'F - 101.10*F Heat Load =
1,100.000.00 BTU /hr 1FVH113 HX Type-Fned Heat Load HX Status: On / Not sn Flow Path Mfr: Amer. Air Fitr.
Wdel: H36MPACYA Dwgs: PM61:A-0004-7 System Fluid:
Heat Load =
502,781.00 BTU /hr 1FVH210 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mfh Amer. Air Flcr.
Model: MDEl570300 Dwas: PM711Q System Fluid: Fresh Water Tube Flow - 147.99 Tube Temperatures - 96.88'F. 99.73'F Heat Loed -
210,000.00 BTU /hr IFVH211 HX Type: Fixed Heat Load HX Star.is: Off Mfh Amer. Air Fitr.
Model: MDE1573$00 Dwgs: PM711Q System Ficid: Fresh Water Heat Load -
0.00 BTU /hr IFVH213 HX Type: Fixed Heat Load HX Swtus; off Mfr:Artwr. Air Fitt, Model: MDE2478600 Dwas: PM786Q System Fluid: Fresh Water Heat Load =
0.00 BTU /br
W2 98 22:15 PROTO-FLO 4.01 by Proto-Power Corporatisrt - Seria! CPFL-0000 ecseas or a Public Service Electric and Oas - 0:\\PSEO\\11-385\\NEW UHS \\STACSUHS2.PDB - Revision 2.00 Hope Creek Ger.erarms Station - STACS Heat Exchanger Data Report Cornergence Pressar&1.0E 3 Sum Q :.0E-2 Fncem=1 ot!4 FCv=1.cE4 P('v=1 OE 3 Ternpera:ure=5.0E.3 LOP /SSE IGVE412 HX Type: Fhed Heat Load HX Status: On / in Flow Path Mh: Trane Co.
Model: MDE1291600 Dwgs: PM731Q System Fluid. Fresh Water Tube Flow a $31.94 Tube Tcrnperaturcs - 99.99'F - 104.16'F Heat Load =
1.100,000 00 BTU %
IGVH210 HX Type: Thed Heat Load HX Status: On / in Flow Path 1
Mft: Amer. Airfltr.
Model: MDE1570300 Dwgs: PM71IQ l
System Fluid: Fresh Water Tube Flow = 130.96 Tube Temperatures = 99.99'F 103.07'F
]
Heat Load -
200,000 00 BTU /hr 1GVH211 HX Type: Fhed Heat Load HX Status: Off Mft: Amer, air Fitt.
Model: MDE1573500 Dwgs; PM71IQ Syuen Flaid: Fret,hWater Heat Load -
0.00 BTU /hr lHVE412 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mfr. Trane Co.
Model. MDE1291600 Dw5s: PM731Q System Fluid Fresh Water Tube Flow - 606.78 Tube Temperatures - 96 88*F - 100.53'F Heat Load -
1.100,000.00 BTU /hr i
l IHVH210 HX Type: Fhed Hem Lad HX Status: On / in Flow Path Mft: Amer. Air Fitr.
Model: MDE1576300 Dwgs: PM71IQ System Fluid: Fresh Water Tube Flow = 143.99 Tube Temperatures - 96.88'F - 99 67*F Heat Load =
200,000.00 BTU &
{
6/2S 8 22:15-PROTO-FLO 4.01 by Proto. Pawer Ctrpor: tion - Serial cPFL-0000 P25c 26 of 26 Pubhc Service Elecme and Oss - G:\\PSEG\\11-385iNEW UHS'STACSUHS2.PDB - Roision 2.00 Hope Creek Generanng Stanon-STACS Heat Exchanger Data Report Corwergenec:Pnuureel.0F.$ Sum Q-1.0E-2 Fncta=2.0E4 rCVal.0F4 PCV=1.024 Teactatses oe-3 LOP /SSE lHVH211 HX Type: Fixed Heat Load HX Stanas: off Mfr:A ner. Air Fhr.
Model: MDE1573500 Dwss: PM7110 Systemmid: FrestiWater 2
Heat Losd =
0 00 BTU /hr 1
l i
l
- TOTAL : AGE.031
1 l
PROTO-POWER CORPORATION g
15 THAMES STREET PHONE: (860) 446-9725 GROTON, CT 06340 FAX: (860) 448-4860 l
l fax COVER SHEET Fn s N o.: #1-ssr 1
DATE: 4 /A/98 l
TOTA 1. PAGES (INCLUDING COVER SHEET): SI.
To:
8,b 3.u:,w FROM:
Ar.c Ast:~
DEPT.
FAX No.: i < es) 33 * - <ais fax No.:
(860_) 448-4860
REFERENCE:
MESSAGE:
1, b, Hn n u.
%e. rss str s An-L., e/p s g
- n w S e e %%ea.. -fL s. rw:&
n t) d5 r u,ee.J o e :s 9 4.s " F.
I %.
g.,.c J.:...e 4 -Air A m.. - 2::4.4 cm kagr&t~s essd WeA ssws cla s e.% % t at sews cc
+, x-ut es.4
%.a.
A u.s: c; :J rk s -.I s s > w, e.
To report transmittal problems or for confirmation, please cal! (860) 446-9725.
i r.
v2
=c
- . v u e n: - --v a-vas,em vm w
n = :: = ;v a n =va.:
..e.
6/2/98 20:35 PROTO-FLO 4.01 b) Proto-Power Corporation - Serial CPFL-0000 Paae 1 of 4 Public Service Elcetric and Gas - G '.PSEG' Il-385WEW UILTSTACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station STACS Flow Summary Report Cemcrger.c Prossure*! 0E.5 SLrn Q=1.CE 2 Pncgion=1 GE 6 FCV-105-4 PCN=1.0F 3 Tec'.pe ati.rs=5 02 3 LOP,5SE - EOB Failure Flow Summary Title Diameter Flow Mmimum Flow NPSHA NPSH (m)
(gpm)
(gpm)
(fi)
Ratio 1 A2E201 out 19.250 10,168.22 i A!E20I out i9.250 9,705.93 1CP210 out 19.250 10,000.99 1AT203 out 1J00 41.60 1 AP210 out 19.250 9,969.40 1 AE205 out 19.250 9,514.39 1DP210 out 19.250 9,645.20 IBP210 out 19.250 9,881.56 1B1E201 out 19.250 9,574 05 iBE205 out 19.250 9.249.01 1B2E201 out 19.250 9,915.20 1 AT205 recire, 1.939 22.87 IBT205 recfrc.
2.067 24.78 1 AP2021 out 0.957 23.32 1 AP202-2 out 0.957 9.87 ICF2021 out 0.957 28.46 1CP202 2 out 0.957 10.33 1CVH2:0 out 3.068 125 53 1GVH2to out 3.06 E 131.05 j
1EVH210 out 3.068 142.50 1 AVH210 out 3.068 142.06
!! Reverse Flow Through Check Valve
&& Pump Flowis Past End of Curve
" Flow BelowMmunum
$5 NPSH Avadable BelowbTSHRequired
, mc. n ; 3. v.
v r
-gu 2 r.L e.
- cap 5 a.-
'ei difE "O
I M Nild 5 "D
)
i 6/2/98 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 race : ot 4 Public Service Electnc and Gas - G:7SEGilI 385 SEW UHS'STACSUllS2.PDB - Reviswa 2 00 Hope Creek Generaung Station - STACS Flow Summary Report Cour swe : Pmsun=1.00 3 Sum Q=1.052 Fn, hon =1.CE-s FCV-1.0E.4 PCV=9.0E 3 Tape mase=3 OE 3 i
i LOP /SSE. EOB Failure I
Flow Summary Title Diameter Flow Mimmum Flow NPSHA NPSH (in)
(gpt.1)
(trprn)
(ft)
Rabo 1 AVH209 out 3 068 77 14 IBVH209 out 3.063 105.11 1 AVII208 out 1.939 32.13 IBVH208 out 1.939 31.65 1FVH210 out 3.068 148.08 IBVH2 to out 3.068 148.34 1BP2021 out 0.957 2547 1BP202 2 out 0.957 10.15 IDP202-1 out 0.957 25.6B IDP202 2 out 0.957 9.97 1Dvil210 out 3.063 144.21 1HVH210 out 3.068 144.0t l AVH213 out 4.026 417 44 IGVH211 out 3.068 112.33 1CVH211 out 3.068 111.79 IFVH213 cut 4.026 419.56 IBVH213 out 4.026 423.17 1CVH213 out 4.026 412.10 1DVH213 out 4.026 415.01 1EVH213 out 4.026 405.32 1AK202 out 0.957 6.17
!! Revene Flow Through Chek Valve
&& Pattp Flow is Past End of Curve Flow Below Mmunum SS NPSH Available Below NPSH Requued
r m.
on u ; c.; o -.. v wem cm zou u & m ro asc53 n n.5
.c.
l 6/2/cs 20 35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000
\\
Pse3or4 Public Service Electric and Gas - GAPSEGil-385'hTW UHS'STACSL71S2.PDB Revision 2.00 Hope Creek Generating Station. STACS FlowSummary Report Convergen.:e Preuuto=1.OE-5 Sum Q-1.0L 2 tnemonal.GE 6 FCV-1.0E-4 PCV=1.0E.3 Temperinne=5 0E J LOPiSSE. E0B Failure Flow Summary Title Diameter Flow Mmimum Flow NPSHA NPSH (in)
(gym)
(spm)
(ft)
Ratic ldh.LUL Uul U.7) i
?.' M J
1 AE202 out 7.981 1.178.39 1BE202 out 7.981 1,153.86 IHVH2II out 3.068 112.15 IDVH211 out 3.068 111.60 1FVH211 out 3.068 111.45 iBVH211 out 3.06S 111.57 1 AVH211 out 3.068 111.27 IEVH211 out 3.068 111.24 1 AE328/lBE328 comb. out 0.546 10.94 1AE328/lBE328 out 0.546 10.94 1AK400 out G.065 2,089.26 1 AVE 412 out 6.065 450.72 1 EVE 412 6.065 527.56 1 EVE 412 out 6.065 528.03 1 AFA08/400/404 out 7.961 1,081.12 1CVE412 out 6.065 454.45 IOVE412 out 6.065 532.41 1CE408/405/434 out 7.981 1.090.13 IBVE412 out 6.065 524.52 1FVE412 out 6.065 524.52
!! Reverse Flow nrough Check Valve
&& Pump Flow is Past End of Curve
" Flow Delow Minunum
$$ NPSH Available Below NPSH Reqwred
~ ~ ---
n, - n
~~u eece,, o -eco e n c e
,wn l
6/2/98 20:35 PROTO-FLO 4.01 by Proto-P wer Corporation - Sedal CPFL-0000 rese 4 or 4 Publ:c Semce Electne and Gas - OnPSEG11 385\\NEW (JH5%STACSUHS2 PDB - Revision 2.00 hpe Creek Gescratmg Station - STACS Flow SummaryReport Cor:ve genec:Pesssurnt.C2 $ Sum Qal.CE 2 Frimon=1.004 fCV-1.004 PCVal.CE 3 Ternpraturc=5.0E 3 LOP /$$E - EOB Failure l
F!ow Summary Title Diameter Flow Mmimum Flow NPSHA NPSH I
On)
(spm)
(gpm)
(n)
Ratio w v c,a ow a.voa uv.ao 1HVE412 out 6.065 607.27 l
1BE408/405/404 out 7.981 1.075.35 1BK400 out 6 065 1,842.96 1DE408/405/404 out 7.981 1,068.99 1AKdO3 out 6.065 569.50 IBK403 out 6.065
$$0.84 RE4859B2 out 0.957 12.75 RE4859A2 out 0.957 11.78 I
J l
?! Reverse Flow Through Check Valve AA Pump Flow is Past End of Curve
r
- .az'se 2.: n re cac~J-F;t.JEF ORF 202 445 629c. TO 160930312;5 F.06 31 6/2/98 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Page or 26 Public Servia Electnc and Gas. G:',PSEG Il-385WEW UHS'STACSUHS2.PDB. Revision 2.00 Hope Creek Generstmg Station STACS l
Heat Exchanger Data Report Cceve sern Prusre=t OF 5 som Q=1.0E-2 friction =1.CE-6 FCV=1,0E-4 PCV=1.0E 3 Tempercure=$ OE-J LOP'SSE-EOB Failure 00E129 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: Basco,Inc.
Model: ES-24/18096 Dwgs: PM050-0039 3 System Flaid.
Heat Load =
500,000.00 BTU /hr 00K107 HX Type. Fixed Heat Load HX Stanas: On / Notin Flow Path M&:American Std.
Model: 06060 Dwgs: PM050-0022 5 System Fluid:
Heat Load =
2,240,323.00 BTU /br 10C150 HX Type: Fixed Heat Load HX Status: Off Mft:
Model:
Dwgs:
System Flmd:
(
Heat Load -
0.00 BTU /tr 1
10 Ell 10 HX Type: Fixed Heat Load HX Status: Oni Notin Flow Path I
Mfr. Basco, lac.
Model: 8A24AC8072 Dwgs: P1-342287 System F1md:
Heat Load -
515,000.00 BTU /hr 10El14 HX Type: Fixed Heat Load HX Status: On / Not n Flow Path j
Mft: Gen. E:ect. Co.
Model. MDEO965400 Dwas: PM003.G-l.7 Sy stem Fluid:
Heat Load =
42.300 00 BTU /hr 10E129 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: Basco, Inc.
Model: ES 24/18096 Dwgs: PM050 0039-3 System Fluid:
Heat Load =
10,750.00 BTU /hr i
l l
l
6/2/9s 20.35-PROTO-FLO 4.01 by Proto. Power Corporation - Serial #PFL-0000 rase a of 26 Public Service Electnc and Gas - OAPSEGill 3 A5\\NEW UHSTSTACSUHS2.PDB - Revision 2.00 Hope Creek Generstag Stanon-STACS Heat Excharign Data Report Convergence Pressaval.0R 3 Sum Q=1.062 Frierte1.0E4 KN*I.Cc 4 PCv=1 OL3 Ter::pera ire =5.0E.3 LOP /SSE - EOB Failure 10K107 HX Type: Fixed Heatload HX Stanis: On / Notin Flow Path M&: American Std.
Model; 06060 Dwgs: PM050-0022 5 System Fluid:
Hrat Load-5,412.000.00 BTU /br IA1 Ells HX Type: Fixed Heat Load HX Status: Off M&: DeLaval/IMO Model: MDE!328000 Dwgs: PM012-0099 System Fluid:
Heat Load =
0.00 BTU /hr IA!E201 HX Type: Shell & Tube HX Status: On / in Flow Path Mfr: Oraham Mfg. Co.
Model: 92-6-504 CGN Dwgs: PM069Q-0058 Tube Fluid: Brackish Water - 12 ppt ShellFluid: Fresh Water Shell Flow - 9.743.90 ShellTemperatures = 117.06*F-99.68'F Tube Flow - 7,363.00 Tt:be Temperatures - $7.96*F 110.96*F Constructica Type: TEMA-O 1 Shells, O Shell Passes,4 Tube Passes Shell Min Area = 6.2530 ft*2, Design Shell Ve'.ocity - 3.900 ft s, Shell Diameter - 92.000
/
Baffle Info: Spacing - 62.000 in, Thickness - 0.000 in. Arca = 0.000 ft^2, K - 0.000 Tubes; Din = 0.694 in, Dout - 0.75o in, Iangth = 42.00 ft, K - 9.50 Tube Pitch - 0.9375 in Tube Pitch Type e Triangular 5,700 of 5,700 Tubes Active tJrubes - No Effective Area - 46,295.00 A^2 Area Factor - 0.9849 Fouling = 0.0000 (inside) 0.0012 (outside)
HofT= 0.4888 LMTD r 8.6049 LMTD Corrections FF = 0.7487 Fb = 1.0000 Heat Load -
83,768,336.04 BTU /hr UOverall-280.88 BIU<hr/ft^2/*F IA2 Ells HX Type: Fixed Hect Load HX Sta:us: Off Mfr: DeLaval/IMO Model; MDE1328000 Dwgs: PM012-0099
. System Fluid-Heat Lead =
0.00BIU/hr
i Jun u 3a.:1g; Fr nutc-PCUE: C ;M '
200 hG 6;91 TC 16C5323121&
F.08<31 6/2/98 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Scrial #PFL-0000 Pase 3 or 26 Pubiic Semce Elecmc and Gas - Gr PSEG\\11 385\\NEW UHSGTACSI;HS2.PDB - Revision 2.00 Hope Creek Generating Station - STAC3 Heat Exchanger Data Report Cor.ve*3 cess-Prwsm=1.oE 5 Som Q=1.0E.2 fricdon=1.0E-6 FCV-1.0G4 PCV=1 CE.) Tergerarw3.0E.3 1
LOPiSSE - EOB Failure IA2E201 HX Type: Shell & Tube HX Status: On / in flow Padi Mft: Graham Mfg. Co.
Model: 92-6-504 CGN Dwas: PM069Q458 Tube Fiuid: Brackuh Water - 12 ppt Shell Fluid: Fresh Water Shell Flow - 10,226 85 Shell Temperatures - 117.06'F - 100.27$F i
]
Tube Flew = 7,332.00 Tube Temperatures = 37.96'F Ill.38'F i
Construction Type. TEMA-O I Shells. 0 Shell Passes. 4 Tube Fasses Shell Min Area = 6.2530 tY2, Design Shell Velocity = 3.900 ft/s, Shell Diameter = 92.000 Faffic Infe: Spacing = 62.000 in, Rickne s = 0.000 in, Ana = 0.000 fP2, K = 0.000 Tubes: Din = 0.694 in, Dout = 0.750 in. Length - 42.00 ft, K = 9.50 Tube Pitch = 0.9375 in Tube Pitch Type - Tnangular 5,700 ef 5,700 Tubes Active UTubes = No Uffecthe A:ea - 46,29100.Y2 Area Factor-0.9849 Fouling = 0.0000 (inside) 0.0012 (outside)
Hoff- 0.4888 LMID = 8.5714 LMD Corrections FF = 0.7548 Fb-1.0000 Heat Load =
84,933,112.89B1thr Loverall-283.58 BTIJ/hr/ft^2/*F 1 AEl109 HX Type: Fixed Heat Load 11XStatus; oft Mft:Basco lne.
Model: f3A43A08048 Dwgs: P! 342287 System Fluut Heat Load -
0.00 BWihr
Model: 264A4808 Dwgs: PM003.TR 18-5 System Fluid:
Heat Load -
515.000 00 BTUthe
!AE112 HX Type: Fixed Hear Load HX Status: Oc / Not in Flow Path Mft: General Elect.
Model: 114D8270 Dwgs: PM003 G-17 System Fluid:
Heat Load =
42,300.00 BW/hr
~-
- m.,
- ~~ sees
.s me eeem m e, s e. _1 6/2/98 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Seriil (!PFL-0000 P:ge 4 or 26 Public Service E!cetne and Gas G APSEGill-385'NEW UHS \\STACSUHS2.PDB - Revision 2 00 Hope Creek Ocaerating Station - STACS Heat Exchanger Data Repon
' onvergenec: Pressure-1.02 3 sum G=1.0E.2 trienarel.0E 6 FCV=1.::R4 PC'Wl.0E 3 Temperature-5.0E-3 l
LOP /SSE E0B Faihre I
l 1 AEl15 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: H.K. Portes Co Model: T-140963X45 Dwgs: PE005-0012 9 System hid:
Heat Load -
10,750 00 BTU /hr IAEl16 HX Type. Fixed HeatLoad HX Status: On / Not in Flow Path l
Mft:Geocral Elect.
Model: 155B8243P001 Dwgs: PM003-T61-2 System Fluid:
Heat Load -
5,412,000.00 BTU /hr 1 AE!17 HX Type: Fixed Heat Load HX Status: Off Mfr: Geners! Elect.
Modch MDE0924300 Dwgs: PM003-G-1-7 i
System FMd:
Heat Load =
0.00 BTU /hr
{
1AE126 HX Typr Fixed Heat Load EX Status: oft Mfh Amencas Std.
Modch 5 046-17168 3 Dwgs: N1 B31-SI 120 System FMd:
Heat load =
0.00 BTU /hr l
1AE130 RX Type: Fixed Heat Load RX Status: Ofr Mfr: Ametek/Whitlock Model: 4-W15HT-4-A CB Dwgs: PM007-0031-3 System mid:
Heat Load =
0.00 BTU /hr 1
1AE202 HX Type: Fixed Heat Lead HX Status: og Mfr: Alfa LavalInc.
Model: A-20-BXS D w as: PM071Q-0010 System Fluid: Fresh Water Heat Load -
0.00 BTU /hr 1
l l
)
Jun 02 ss zi:e2 rF F40TC-PCWER OCRs 200 446 6292 TO 16C90291218 A.10/31
~
6/2/93 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Pases or 26 Public Servi:e Electne and Gas - G:\\PSEGil1 385WEW UHS \\STACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station STACS Heat Exchanger Data Report rnavergen:e: Preswre=1 GE.5 Sum Q 1.oE4 rnctional OE-6 FCV=l.0E4 PCV-l.0E.3 Temperse m.8.004 LOPiSSE EOB Failure iAE205 MX rype: Fixed Heat I.ead HX Status: On / m Flow Path Mfr: Delta Southern Model: 21 A9227AN Dwgt: NO-E11-B001-5 l
System Fluid: Fresh Water Tube Flow - 9.450 78 Tube Tc:aperstmes - 100.01'F 125.23*F Heat Load =
132,500,000.00 BTU /hr 1AE214 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mh: CVI inc.
Model: C735-9934 Dwgs: PM048Q 00714 System Fluid:
IIcat Losd -
19.500,000.00 BTU /hr 1 AE218 HX Type: Fixed Heat Load HX Status: Off Mfr: CVIInc, Model: C735-9934 Dwgs: PM048Q-00714 System Fluid:
j Heat Load =
0.00BTUehr
! AE278 HX Type: Fixed Heat Load HX Status: Ott 1
Mft; CVI inc.
Model:
Dwgs: PM04BQ l
hstem Flaii Heat Load =
0.00 BTU /hr IAE328 HX Type: Fixed Heat Load HX Status: On !m Flow Path Mft: Parker Hanisoc Model: HDTC-SS-6-2 Dwgs:
System Fluid:
Shell Flow - 5 03 Shell Temperettres = 100.0l'F - 122 Ol'F Heat Load =
55,000.00 BTU.hr l
l
- - - ~~---
~~ ~
l l
tv2.H 20:35 PROTO FLO 4.01 by Proto-Power Corpor: tion - Serial CPFL-0000 P:se 6 or 26 Public Service Electr.e ar.d Gas - G.\\PSEG\\11-385\\NEW UHS'STACSL'HS2.PDB. Revision 2.00 Hope Creek Generstmg Stanon - STACS Heat Exenanger Data Report
'onverscace Presure=1.0E.5 5;m Q 1.CE 2 Mcdon=1.0E4 FCV=1.0E-4 PCV=LCE 3 Terrvraturc=5 OE-3 LOP /SSE. E0B Failare IAE404 HX Type: Fised Heat und EX Status: On / in Flow Path Mfr: Amentan Std.
Model: 17072 CPT Dwgs: PM018Q System Fh:id. Fresh Water Tube Flow - 1.080.45 Tube Temperatures = 115.%'F - 1I8.49'F Heat Load-1,353,000.00 BTU!hr IAE405 MX T)pe: Faed Heat Load HX Status: Oc /in riow Path Mfr: Amencan 5td.
Model: 19084 CPT Dw8s: PM018Q Sys:cm Fluid: Fresh Water Tube Flow ' 1,077.93 Tube Temperatures - 105.84*P. I15 96*F Heat Load a 5,412.000 00B11.i.1:r IAE40s HX Type: Fned Heat Load HX Stana: On /in Flow Pat Mft:Amencan Std.
Model: 19198 Dwgs: PM018Q System Flufd: Fresh Water Tube Flow = 1,076.60 Tube Temperatum = 100 Ol'F - 105 34*F Hess Load -
3,118,000.00 BITJ/hr 1AK111 HX Type: Fixed Heat Load HX Status: Oc / Not m Flow Path l
MIr: Camer Corp.
Model: 19FA553B5005932 Dwss. PM623-0002 9 System Fluid:
Heat Load -
502,781.00D7U/hr 1AK202 RX Type: Fixed Heat Lead HX Status! On! m Flow Path Mft: CVIInc.
Model: C735-9909 Dvss: PMG46Q-0044 2 System Fluid. Fresh Water Tube Flow - 6.15 Tube Teciperatures = 100.01'F - 11638*F liest Lead =
50,000.00 BTUlr l
l I
sun wn.:.1:a z o a -: 5 eiez n. sesaalit e c.
2 3:
6/2/9820:35 PROTO-FLO 4.01 by Proto-Power Cogoration - Serial #PFL-0000 Page 7 d 26 Public Service Eleetnc arid Gas - G:\\PSEGil 1 385GEW UHS'STACSUHS2 PDB - Revision 2 00 Hope Creek Genera *2ng Station - STACS Heat Exchanger Data Report cornersence. Preswrc-1.0E 5 5em Q-1.0F. 2 fnewn-LDE4 Ft.Y= t.0E 4 PCV-1.06-3 Temperarce=3 DE-:
LOP /SSE. EOB Failure l
1AK400 HX Type: Fixed Heat Load EX Stams: On / m Flow Path Mfr: Cam:r Corp.
Model: 19FA455B122022 Dwgs: PM723Q 3
System Fluid Fres!' Water j
Tube Flow - 2,080.02 Tube Temperarses = 100 01'F - 107.28'T Heat Load =
7,530,700.00 BTU /hr I
1AK403 HX Type: Fixed Heat Load HX Statur On / mFlow Path Mft Camer Corp Model: 19FA441B1142020 Dwgs: PM723Q System Fluid: Fresh Water Tube Flow - 568.40 Tube Temperatures = 100.01'F - 108.92*F Heat Lead -
2,515,340.00 BTU /hr 1APl76 HX T>Te: Fixed Heat Load HX Status: On /Notin Flow Path Mfr:Camer Corp Modeh 19FA999-1007-18 Dwgs: PM623-118 System Fluid:
Heat Load -
100,000.00 BTr/hr IAP202-1 HX Type: Ftxed Heat Load HX Status: On / in Flow Path M&: Graham Mfg. Co.
Model: 5X4C-12 Dwgs. N1. Ell-C002-51 SystemFlad: Fresh Water Iube Flow - 23.15 Tube Temperstwes = 100.01'F - 130 44'F Heat Load -
350,000.00 BTUtr I AP202 2 MX Type: Fixed Heat Load HX Status: On / m Flow Path Mfr: Oraham Mfg.Co.
Model 992C430BX Dwgs: h1.El1 C002.b S> stem Fluid: Fresh Water Tube Flow - 9.86 Tube Temperatures = 100 01'F - 102.05'E Ileat Load -
10,000.00 BIU'hr
w n ot.sg. 217c2 c; - carc-pgen c;FA 200 445 EI92 Tc 16033331112 F.,13 31 vv9s 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial APFLJJ000 Page s or 26 Pubbe Semce Ele:me and Gas - G:'.PSEC.! 1 385WEW UHS $TACSLTIS2.PDB - Revision 2.00 Hope Crcck Generating Station - STACS Heat Exchanger Data Repert Convenence P:tutte-l.02-5 sum Q-1 OD:Incenn=1.CE 6 FCV=1.0E 4 PCV-1.0E-3 Tex.i. :...-S.CE-3 LOP /SSE - ECB Failure IAVE412 HX Type: Fixed Heat Lead HX Status: On / in Flow Path Mft: Trane Co.
Model: MDE1291600 Dwas: PM731Q System Fluid Fresh Water Tube Flow a 450.25 Tube Temperatures - 100.01'F - 104.93*F Hest Load 1,100,000.00B1U/hr I AVH113 HX Type: Fixed He.at trad HX Status: On / Not in Flow Path Mft: Amer. Air Fitr.
Model: H36MPACYA Dwgs: PM611 A-0030 4 System Fluid:
Heat Load =
502,781.00BIr/br i AVH116 HX Type: Fixed Heat Load HX Status: On /Notin Flow Path Mft: Amer. Air Fitt.
Model: H36MFACYA Dwgs: PM611 A 0033 4 System Fleid:
Heat Load =
330,000.00 BTU /hr l
lAVH208 HX Type: !"med Heat Load HX Status: On /in Flow Path Mi Amer. Air Fltr.
Model: MDE1572400 Dwas. PM711Q SysternFluid: Freshwater Tube Flow - 3211 Tube Temperatures = 99.03'F - 101.57'F Heat Lond =
45.000.00BTUtr 1AVH209 HX Type: Fixed Heat Load HX Status: Os /in Flow Path Mft: Amer. Air Flir.
Model: MDE1571400 Dwgs: PM711Q System Fluid. Fresh Water Tube Flow - 77 09 Tube Temperatures = 100.01'F 103.01'F Heat Load =
115,000.00 BTU /hr m______._____
--, f.
u
--n z m t-e -,.; -;,- s a,e e m
_O
- n e25i rv 1609326: 2 2
~.;1 s; v2ns 20:35 PROTO-FLO 4.01 by Proto-Powsr Corporation - Serial rtPFL-0000 P.,9 er 2 6 Public Service Eleetne arid Gas - O?.PSEG 11 285'NEW UHS'.STACSUHS2 PDB - Rension 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Ccrwgme Preswe=1.0E-5 sum Q=LDE 2 Frictan=1 CE4 FCVal 0E 41Cr'*1 DE-3 Temis!.ww-5 063 LOP /SSE - EOB Failure 1AVH210 HX Type: Fixed Heat Load HX Stams-On / m Flow Padi Mft; Amer An Titr.
Mcdel. MDI:1570300 Dwgs PM711Q System Flmd. Tresh Water Tbbe Flow - 141.97 Tube Temperatures = 100.01'F - 102 99'F Heat Load =
210,00000 BTU /hr I AVH211 HX Type: Fixed Heat Load HX Stams. Otr Mfh Amer. Air F tr.
Model: MDE1573500 Dwgs: PM71IQ System Fluid: Frcah W ter Heat Load :
0.00 BTU /hr 1AVH213 HX Type: fixed Heat Lead HX Status: Off Mfir: Anner. Air Fitr.
Model: MDE2478600 D* gs: PM786Q SystemFluid: Fresh Water Heat Load -
0 00 BTU /hr iBIElIS RX Type: Fixed Heat Load HX S'atus: On / Not in Flow Path Mft: DeLa.alSf0 Model: MDE1326000 Dwgs: PM012 0099 Sys:em Fluid:
Heat Load =
400.000.00 BUJ/hr i
)
m.,
- av ocec <
rw.w,ve eee
-e m es... omaeeasooe r.4# so 6/3/98 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 rage ;o of as Public Semc: Electric act Or.s - 0:\\PSEG\\ll-3EFFEW IJfS'5TACSURS2.PDD - Reviston 2.00 Hope Creek Generating Station - STACS Heat Enhanger Data Report Convergence Prmve=1.0ES Sum Q=1.0E-2 Trw:wn=I DE-6 PCV=l.C1M MV=l.CE 3 Terr.pera::4rc=5.GG3 LOP /SSE - E0B Failure l
1B1E201 HX Type; Shell& Tube HX Status-On / in Flow Path Mfr: Graham Mfg. Co.
Model: 92-6 504 CGN Dwgs: PM069Q-0055 1
Tube Fluid. Breckisl: Water - 12 ppt ShellFluid: Fresh Water Shell F cw - 9,611.57 Shell Tereperatures = 116.42*F - 98.88*P Tube F'ow - 7,679 00 Tube Temperatures
- 87.96*F.109.92*F Construccon Type: TEMA G 1 Shells, O Shell Passes,4 Tube Passes Shell Min Arca - 6.2530 A*2, Design $ bel! Velocity = 3.900 ft's, Shell Diameter - 92.000 Baffle Info: Specing - 62.000 m, Thickness = 0.000 in, Area = 0.090.Y2, K = 0.000 Tubes: Dic = 0.694 in, Doat = 0.750 in, Length = 42.00 S, K - 9.50 Tube Pitch -- 0.9375 in Tube Pitch Type -Triangular 5,700 of 5,700 Tubes Active L Tubes - No Effective Area = 46,295.00 A*2 Area Frctor = 0.9849 Foulmg = 0.0000 (inside) 0.0012 (octside)
HoK-3.4888 LMTD - 8.5194 LMTD Corrections FF = 0.7498 Fb - 1.0000 Heat Load =
83,403,430 97 BTU /hr UOverall-252.03 BTU /hr/a^2/'F 1B2El18 ILX Twe: Fned Heat Load HX Sts:as' On / Not in Flow Path Mft: DeLavaFIMO Model. MDE1325000 Dwgs: PM012-0099 Spiem Fluid:
Heat Loed -
400,000.00 BIV/hr
1 e/2/98 2025 PROTO-FLO 4.01 by Proto-Power Corporation - Serial tlPFL-0000 Pc;c !I of 26 Pubbe Service Electnc acd Gas - G5PSEG'.ll-385WEW UHS'STACSUHS2.PDB - Revision 2.00 Hope Creek Generstmg Station - STACS Heat Exchanger Data Report Umcreence l'ressww=1.0ti-s um Q-1.CE 2 Frienan=1 oF4 FCV-l.CC4 n. =1.CE 3 Terr:pe:srce=LOE-3 N
l l
LOP /SSE EOBFailure 1B2E201 HX Type: Shell & Tube HX Status: On / in Flow Path Mfr: Graham Mfg. Co, Model: 924 504 CGN Dwgs: PM069Q-00$S Tube Flaid: Brs:kish Water - 12 prt ShellFluid: Fresh Water Shell Flo= = 9,953.43 Shell Temperatures = 116.42'F - 99.19'F Tube flow - 7,741.00 Tube Temperatures = 87.96*F - 110.12'F Const:uction Type: TDLA G 1 She!!s, o Shell Passes,4 Tube Passes Shell Min Area = 6.25.10 ft'2, Design Shell Velocity = 3.900 A/s, Shell Diarr.eter = 92.000 Baffle Info: Spacir.g = 62.000 in Thickness = 0.000 in, Area = 0.000 n'2, K - 0.000 1ubes: Din = 0 694 in. Dout = 0.750 in, Length = 42.00 it, K = 9.50 Tube Pitch a- 0.9375 in Tube P.tch Type = Triangular 5,700 of 5,700 Ts.bes Actise UTubes - No Effective Area r 46.295.00 ft^2 Area Factor = 0.9849 fo'aling = 0 0000 (inside) 0.0012 (outside)
Hoff'e 0.4888 LMTD = B.5293 LM7D Corrections FF = 0.7549 Eb - 1,0000 Heat Load -
84,839,003.35 Bit'/br L~Overall-284.62 BTU /hr/ft^2/'F IBE1109 HX Type. Fixed Heat Load HX Status: On / Not in Flow Path Mfr: Basco inc.
Model: BA44A08048 Dwgs: Pl.342287 S) stem Fluid:
Heat Load =
481,650.00 BTU /hr IBEl11 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: General Elect.
Model: 264A4808 Dwgs. PM003-TR-18-5 System Fluid:
Heat Load =
9,360,000.00 BTUh l
IBE112 HX Type: Fixed Heat Load HX S atus-On /Not in Flow Path i
Mh: General Elect.
Model; 114Df270 Dwgs: PM003 G-1-7 System Fluid:
Heat Load =
5,487,500.00 BTUtbr
/64 Ol# R 21: 04
.T E F 0 0 T i. - P C W E G.CR0 200 445 E292 T ', 16053091216 F.17 21
^
I I
6/2/9830:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 rap 12 er 26 Public Sernce Electric and Gas. G:,PSEGil1 385'.NEW UHS \\STACSL'HS2.PDB. Revision 2.00
}fope Creek Generating Station - STACS Heat Exchanger Data Report Cocterpece: Pmere=1.0E-5 Som Q=1.0E-2 Fnction=1.0E4 KV=1.0E4 PCV=1.0E-3 Tcmp.vatvm=102 3 LOP /SSE. E0B Failure IBEl15 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: H.K. Porter Co.
Model: T.140963X45 Dwgs; PE00$-0012-9 bystem Fird:
Heat Load =
515,000.00 BTU /hr IBEll6 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path Mfr: General E!cct.
Model: 1$$B8243P001 Dwgs: PM003-T6-1 2 System Fluil Heat Load =
42.500.00 BTU /hr IBEl17 HX Type: Fixed Heat Load HX Status: Ou / Not in Flow Path M&: General Elect.
Model: MDE0924300 Dwgn: PM003-0-1-7 System Eid.
Heat Load =
6,0$0,000.00 BTU /hr iBE126 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: Ainer.can Std.
Model; 5 0046-17-168 3 Dwgs: N1-B31-S!-120 System fluid.
Heat Load =
5.630,000.00 BTU,hr IBE130 HX Type: Fixed Heat Load HX Status: on / Notin Flow Patn Mft: Artietek/Whitlock Model. 4.W1811T.4.A.CB Dwgs: PM007 0031 3 System Fluid.
Ilent Load -
42,300.00 BTUhr IBE202 HX Type: Fixed Heat LoaJ HX Stams. off Mft: Alfa Lavelin:.
Model A-20-BXS Dwgs: PM0710 0010 System F!uid Fresh Water Heat Load =
0.00 DTU/hr
~... _
- n. --
n
~~e nn,~ o msa w n w e.s.
as I
v2/98 20.35 PROTO-FLO 4.01 by Proto-Power Corporation - Seri11 #PFT 0000
' ra.13 or :.5 Pub! : Service Electne and Oas G:\\PSEOill 365'.NEW LHSWTACSLHS2.PDB Revision 2.00 Hope Creek Generatng Station - STACS Heat Exchanger Data Report Comergerce P esswe=1.0E 3 Sun Q=1.9E 2 Fr.ction=14E4 FcV=1 CE 4 KN=1.0F-l Terspentarc=$.0E 3 LOP /SSE - E0B Failare 1BE205 HX Type: Fix.ed Heat Load HX Status: On / in Flow Path Mfr: Delta Southem Model; 2!A9227AN Dwgs: No-E 1 B0015 System Fluid: Fresh Water Tube Flow = 0,185.76 Tube Temperatures = 99.05'F - 128.0S'F Heat Load =
132.500,000.00 BTU /hr 1BE214 HX Type: Fixed Heat Load HX Status [ On / Not in Flow Path Mir: CVIInc.
Model: C735-9934 D=gs: PM048Q-0071-4 Systern Fluid:
Heat Load -
9,565.00 BT1*/hr 1BE218 HX Type: Fixed Heat Load HX Status; On / Not in Flow Path Mfr: CVJ Inc.
Model: C735-9934 Dwgs. FM048Q-00'l 4 System fluid:
Heat Load :-
10,750.00 BTU /hr IBE178 HX Type: Fixed Heat Load HX Smtus: On /Not m Flow Path Mft: CVI Inc.
Model:
Dwgs: PM048Q System Fitiid:
Heat Load =
6.000.00 BTU /hr IBE328 HX Type: Faxed Heatload HX Status: On /in Flow Path Mft: Parker Hamson Model: HDTC-SS-6 2 Dwgs:
Sys:em F;uid.
Shell Flow -5.56 Shell Temperatures - 100 Ol'F - 115.91'F 11 eat Load -
55,000.00B'IUhr
- u u n 4
- sse m mu1o+0 e coup asa ~as szsa va ;5csaystzse p. i s :3 3 1
l l!-
6/2/9s 20 35 PROTO-FLO 4.01 by Proto-Pow;r Corporation - Serial #PFL-0000 Pase 14 of 26 Publi: Service E!ectric and Gas - 0:'PSEG\\l1-333WEW UHS \\STACSUHS2.PDB - Revision 2.00 Hope Creek Generstmg Station - STACS Heat Exchanger Data Report Convergence: hehnme-! OC-3 Sum O=: CE 2 Fnewn=1.CE-6 FCV=1.0f 4 PCVal OE-3 Terope:::ture=! OE-3 LOP /SSE EOB Failure 1BE404 HX Type: Fixed Heat Load HX Status: Os / m Flow Path Mfr: Arnetican Std Model: 17072 CYT Dwgs: PM01 BQ Systern Flu;d: Fresh Water Tube Flow = 1,074.69 Tube Temperatures - 115.09'F - I l 7.63'F Heat load -
1.353,000.00 BW/hr l
1BE405 RX Type: Fixed Heat Load HX Status: On /in Flow Path l
Mft:Amencan Std.
Mmlet. 19084 CPT Dwgs: PM018Q System Fluid. Fic3E Water Tabe Flow = 1,072.19 Tube Tem,cratures - 104.91F - 115.09'F Heat Load -
5,412.000 00 BW.hr iBE408 HX Type: Fixed Heat Load HX Stants: Ou /in Flow Path Mfr: Amencan Std.
Model: 19198 Dw5s: PM018Q System Fluid. fresh Wat:r Tube Flow - 1,070.87 Tabe Teraperatures - 99 05'F - 104.91'F Heat Load -
),11B,000 00 BW/hr 1
IBK111 HX Type: Fixed Heat Load HX Status: On / Not m flow Path Vfr:Camer Corp Model: 19FA553B5005932 Dwgs: PM623-0002-9 System Fluid:
Heat Load -
19.500,000.00 BTU /hr
)
1DK202 HX Type: Fixed Heat Load HX Staans: Os /in Flow Path Mfr CVIinc.
Model C735-9909 Dwgs: PMD4SQ.004A2 System rinid: Fresh Ware Tube Flow = $.92 Tube Temperatures = 99.05'F - 116 06:F Heat Losd -
50,000.00 B7U'hr J
6'2/9s 20:35 PROTO FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 page is or :s Pchhc Serv:ce Electric and Gas G:\\PSEU l1385\\NEW UHS'STACSUHS2 PDB Reviston 2.00 Hope Creek Generstms Station-STACS Heat Exchartger Data Report Conve pm Prunurval.0P 5 51m Q=1.oE.2 Ficeon=1 Oti4 FCV=LOEJ PCv=1 CE-) Tempernsre=5 OE-3 LOP /SSE-E0B Failure IBK400 HX Type: Fixed Heat Lmd HX status: On /in now Path Mf'r; Carrier Corp.
Model 19FA455B122022 Dwas: PM723Q System Fit:id: Fresh Water Tube Flow = 1,839.73 Tube Temperature 2 = 99.057 - 107.29'F Heat Load a 7,530.700 00BTUrtr 1BK403 HX Type: Fixed HeatLoad HX Status: Oc / in Flow Path Mft: Camer Cog.
Model; 19FA441B1142070 Dwgs: PM723Q System Fhaid: Fresh Water Tube Flow = 579.76 Tube Tercperatures - 99.05'F - 107.78'F Heat Load =
2,515,340.00 BTU /hr 1DPl?6 HX Type: Fixed Heat Load HX Stams: On /Notin Flow Path Mfr: Carrier Corp.
Modeh 19FA999-1007-18 Dwgs: PM623-118 System Fluid:
Heat Land =
100,000.00 BTU,hr 1 BP202-1 HX Type: Fixed Heat Load HX Status:. On /in Flow Path Mfr: Graha n Mfg. Cu Model 8X4C-12 Dwgs: NI ElI.C002-31 System Fluid: Fresh Water Tube Flow = 23 30 Tube Ternperatures = 99.05'F - 123.947 Heat load =
350.000 00 BTU tr IBP202-2 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mfr: Graham Mfg Co.
Model. 992C430BX D wss: NI Ell-C0024 SystemFlubi Fresh Water Tube Flow = 10.14 Tube Temperatures = 99.05'F - 101.0 T j
Heat Lcad =
10,000.00 BTU /hr l
1 l
l
- ur, cz'si 21
- c5 eF F;c c-m E.: ccR-400 b u E292 rc isrcastile F.21 ;;
6/2,9s 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Senal #PFL-0000 P ge !6 of 26 Public Service Elecmc and Gas - G.\\PSEG\\11365WEW UHSGTACSUNS2.PDB - Revision 2.00 Hope Creek Cenerating Station - STACS Heat Exchanger Data Report Cor*.e3ense. Irrssunr=L'.E 5 Sum O*!.0E 2.' fictional 056 FCV='.CE-4 PCV-l.CL3 lemperaturc=5 OT 3 LOP /SSE - EOD Faihre 1BVE412 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mir. Trace Co.
Model: MDE1291600 Dwgs: PM731Q System Fidd-Finh Water Tube Flow - $24.06 Tabe Temperstates - 99.05'F 103.28*T Heat Load -
1.t00,000.00BnJ/la IBVH113 HX Type: Fixed Heat Load HX Status: OtY Mft: Amer. Air Fitr.
Modeh HMMPACYA Dwgs: PM611A 0030-4 Spiem Fluid-Heat Load -
0.00BR!!hr IBVHI16 MX Type: Fixed HeatLoad HX S*.atus: On/Not in Flow Path Mft: Amer. Air Fitr.
Modeh H36MPACYA Dwgs: PM611A4)033-4 System riuki.
Heatload -
530,000 00 BTU /hr 1BVH208 HX Typ e Fixed Heat Load HX Status: Cm /in Flow Path Mfr: Amer. Air Fitr.
.\\1odeh MDE!$72400 Dw35: PM71IQ System Fluid: Fresh Water Ttbe Flow - 31.63 Tube Ternperatures = 99 OS*F - 101.92*F Heat Load -
45,000.00 BTI,Wr IB W1209 HX Type: Ftxed Heat Load HX St:tus: On /ic Flow Path Mft: Arner. Air Fitr.
Model: MDE1571400 Dwgs: PM711Q System FImd; Frnh Water Tube Flow - 105 06 rube Tarnperatures = 100.0!*F.102 21'F Heat Load -
115,000.00 BTU /hr T
m_____
O./9820:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Page 17 or 2e Public Service E!ectnc and Oas - OnPSEG11-385'.NEW UH56TACSUHS2.PDB - Revision 2.00 Hope Creek Ger:erating Station. STACS Heal Exchanger Data Repott Ccevergcrce P ossure=1.oE-5 Sum Q=1 JE-2 Fnedcww=I OE-6 FCV-LoE4 PCVal OE.3 Tempencev=1CE-3 LOP /SSE - EOS Failure 1BVH210 HX Type: Fixed Hear Load M X Status: On / d Flow Path Mfn Amer. Air Fltr.
Modch MDE1570300 Dwgs: PM711Q System Fluid. Fresh Watet Tube Flow = 148 25 Tube Temperatures - 99.05'F 101.90*F Heat Load -
210,000 00 BTU /hr 1BV11211 HX Type. Fixed Heat Load HX Status: oft l
Mf!r: Amer. Air Fitr.
Model: MDE1573500 Dwgs: PM71lQ System Fluid: Fresh Water Hoat Lead =
0.00 BTU /hr 1BVH213 HX Type: Fixed Heat Load HX Status: Off 1
Mft: Amer. Atr Fltr.
Model: MDE2478600 Dwgs: PM786Q i
System Fluid: Fresh Water Heat Load =
0.00 BTU /hr 1ClEl!8 HX Type: Fixed Heat Load HX Status. On I Not m Flow Path Mft: DeLaval'IMO Model: MDE1328000 Dwgs: PM012 0099 System Fluid-Hest Load =
400,000.00 BTU /hr iC2E1i8 HX Type: Fixed Heat Load HX Status: On /Notin Flow Path Mfr: DeLavaLIMO Model: MDE1328000 Dwas: PM012-0099 Systern Fluit Heat Land =
400,000.00 BTU /hr ICEl!2 MX Type: Fned Heat Load HX Sta'us: On / Not in Flow Path Mtv: General Elect.
Model. 114D8270 Dwge: FM003 G-1-7 System Fhud:
Heat Load =
5,487,500.00 ETU,br I
l l
l
77w g d: c.s W F,0TV-M WER C. P :'
20; W EE51 TC LM C SLEls 5.21 3:
s I
6/2/9s 30 35 PROTO-FLO 4.01 by Proto-Power Corporadon - Serial #PFL-0000 Pa;;e 18 of 26 Pubbe Service Ecctnc and Gas - 0:PSEG',11 385WEW UH5'STACSUHS2.PDB - Revishn 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report rnevcepence Prwsweal.0F.-$ Sum Qal.0E-2 Fnctional.0E-6 FCY=1.0E4 FCV=1 OE-3 Temperatw5_CE.)
LOP /SSE-EOB Failure l
l 1CE130 HX Type. Fixed Heat Load HX Status: On / Not in Flow Path Mir: AmereldWhat!ock Model: 4-WI 8HT-4.A G Dwgs: PM007-00313 System Fluid:
)
HestLead=
/.2,300.00 BTU /hr
{
ICE 404 HX Type: Fixed Heat Load HX Status: On /In Flow Path l
Mfr:Arnoncan Std.
Model: 17072 CPT Dwga: PM01SQ l
System Fluid Fresh Water l
Tube Flow = 1.089.47 Tbbe Temperatures = 115.83'F Il8.34'F Host Load =
1,353.000.00 BTU /hr ICE 403 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mfr: Amencac Sti Model: 19084 CPT Dwgs: PM018Q System Fluii Fresh Water Tube Flow = 1,086 95 Tube Temperatures = 105.79'F-115.83'T Hest Load -
5,412,000.00 BTU /hr
!CE401 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mfr:Arnencan Std.
Model: 19198 Dwgs. PM018Q Syriem Fluid: Fresh Wate:
Tube Flow = 1,085.62 Tbbe Temperatures = 100.01'F.105.79'F Heat Load =
3,118,000.00 BTU /hr i
!CK111 HX Tge Fixed Heat Load HX Status. On / Not in Flow Path Mfr: Canier Corp.
Model: 19FA553B5005932 Dwgs' PM623-0002-9 System Fluid:
HeatLoad=
19,500,000.00 BTU /hr i
]
l i
i
~ - ---
, -. -e n n
e-
~~c neeo.. n eue m a
<.. -..; s 6/2/98 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial OPFL-0000 P e.19 or 26 Public 5=va:e Electnc and Gas - G APSEGil1 365iNEW UHS'.'TACSUHS2 PDB - Reviston 2.00 Hope Creek Generstag Station-STACS Heat Exchanger Data Report Comergenes. Preuure-1 CE-S $um Q-10E 2 Triction=1.0E4 FCV=1.05 4 POV=1 CF,-J Ts.wesre5 DE-3 LOP /SSE - E03 Failure ICPl?6 HX Type' Fixed Heat Lead HX Status: On / Not in Flow Pat Mir: Carr:er Corp.
Model. 19FA999-1007-18 Dwgs: FM623-11E System Fluid.
Heat Lead -
100,000 00BRJ/hr ICP2021 HX Type: Fuad Heat Lad HX Status: On /in FlowFach Mfr: Graham Mfg. Co.
Model: 8X4C-12 Dwgs: N1-E11 C002 51 System Fluid-Shell Flow = 28.29 Shell Temperatures - 100.01 *F - 124.91'F Heat Load -
350.000.00 BTU /hr ICP202-2 HX Type: Fixed Heat Load HX Status: On / in Flow Path i
Mft:GrahamMfg Co Model: 992C430BX Dwgs: N1-E11.C002 6 System Fluid: Fresh Water Tube Flow = 10.32 Tube Temperatures - 100.01*F - 101.96*F Heat Load =
10,000.00BnJ/hr ICVE412 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mft: Trane Co.
Model: MDE1291600 Dwgs PM731Q l
System fluid: Fresh Water Tube flow - 453.99 Tube Teinperatures - 100.01*F - 104.89 F Heat Lead -
1,100,000.00BRl/hr 1CVH113 HX Type: Fixed Heat bad HX Status: On / Not in Flow Path
.\\lfr: Amer. AirFitr.
Model: H36MPACYA Dwgs: PMbil A-0030-4 System Fluid:
Heat Lead -
502.781.00 BTU /hr i
I i
l i
i
- u,- yzx 33-- z mg-ww nnyc ycyggw,7.y- -- mur-ug-- g g3g-- r; ; 3 a 2 mg 3 5 - ---- --
c e/2ss 20:33 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Pm zo et 2s Public Service Electric and Gas. G:TSEG\\11-3856EW UHS'STACSUHS2.PDB Revision 2.00 Hope Creek Generstmg Station. STACS Heat Exchanger Data Report Converpau: Preuurc=l OE 5 Sum Q-1.0E 2 Tnctiu '<.0E G FCV-1.06.-4 PCval.0E-31erepc'se5 0E-3 LOP.3SE - EOB Fadure ICVH210 HX Type: Fixed Heat Lead HX Status: on / in Plew Path Mfr: Amer. Air Fitr.
Model' VDE1570300 Dwgs: PM711Q SysternFluid: Fresh Water Tube Flow - 125.44 Tube Te nperatures - 100.Ol*F 103.22'F Heat Load =
200,000.00BW&r 1CVH211 HX Type: Fixed Heat Load HX Status: Off Mfr: Amer. AirFly.
Model: MDE1573500 Dwgs: PM71 tQ SystemFluid: Fresh Water Heat lead -
0.00 BTU /hr iCVH213 HX Type: Fixed Heat Load HX Status: off Mfr: Amer. Air Fitr.
Model: MDE2476600 Dwgs. PM786Q System Fkid: Fresh Water Heat load -
0.00 BTU /hr 1DE112 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: General Elect.
Model: !!408270 Dwgs: PM003-O-1 7 System Fluid:
HeaiLead=
5,487,500.00 BTU /hr 1DE404 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mft: American Std Mode!. 17072 CPT Dwgs: PM018Q System Fluid: FreA Water Tube flow - 1,066.33 Tube Temperatures = Il5.19*F - 117.74*F j
Heat Load =
1,353,000.'JO BTU 4r l
i l
l l
[_
J
av., e.:. u a m w % ;-m ws u wv--
w; wJ5 Ezsz T; :ree s m ill s F. 2U 31 6/2/98 20:35 PROTO FLO 4.01 by Proto-Pcwer Corporation - Serial #PFL-0000 P=se 21 or M Pubhc Service Electne and Oas - G:'PSEG'11 385WEW UHSiSTACSUHS2.PDB - Revision 2.00 Hope Creek Generatics Staten - STACS Heat Exchanger Data Report Convergmx tw.ure=1.oH-3 %m Q 1.0E 2 Frictirr=10G4 FCV=1.0F-4 MN=1.0Ed Temperstn=EE-3 LOP /SSE ECB Failure IDE405 HX Type. Fixed Heat Load HX S:ana: On / :n Flow Path Mfr: Arnerican Std.
Model: 19084 CFT Dwas: PM016Q SystemEuid Fresh Water Tube Flow = 1.065.53 Tube Temperatures = 104.95'F 115.18*F Heat Load =
5.412,000 00B7U/hr IDE408 hX Type: Fixed Heat LoaJ HX Star
- On / in Flow Path Mfr: American Std Model: 19198 Dwgs: PM018Q System Fluid: Frnh Water -
Tube Flow = 1,064.51 Tube Temperatures - 99.05'F - 104.95'F Heat Load -
3.118.000.00 BTU /hr IDK!1I HX T)pe: Fixed Heat Load HX Status On / Notin flow Path Mir. Camer Co.p.
Modei 19FA553B5005932 Dwas: PM623-0002-9 System Fleid-Heat Load =
19,500,000 00 BTU /tr 1DPl76 HX Type. Ftxed Heat Load HX Status: On /Not in Flow Path J
Mir: Camer Ccrp.
Model: 19fA999-1007-18 Dwgs: PM623-118 l
System Fluid:
f Heat Load -
100,000.00 BTU /hr I
I I
IDP702-1 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mir: Graham Mfg. Co.
Model: EX4C-12 Dwgs: NI-Ell <002 51 Syr, tem Fhud: Fresh Water Tube Flow - 25.51 Tube T mperatures = 99.05'T.126 66*F Mest Load -
350,000.00 BTUtr
--m
.... - em um-
-e esee o-
.2eam o s w r.:,..: 4 6/2'98 20:35-
- PROTO-FLO 4.01 by Proto-Power Corporadon - Serial #PFL4000 P4 c22 of 26 Public Service Electric and Gas - G4PSEGIl 385WEW UHS'sTACSUUS2 PDB - Resision 2.00 Hope Creek Gercrating Station - STA CS Heat ExchangerData Report Conserrmer Preme=1 CE 5 Sum Q=1 OE 2 fdeuar.=1.07 6 FCV*t CE-4 PCV-1 OE.1 Terr +e ::tse-5.CE-3 LOP /SSE. EOB Fail:ne IDP202-2 HX Type: Fhed Heat toad HX Status' Os /in flow Path Mh.GraEam Mfg. Co.
Model: 992C430BX Dwss: h*l-El l-C002-f-System Fluid Fresh Water Tabe Flcw a 9 97 Tube Temperatures
- 99.05'T - 101.07'E Hest Load -
10,000.00 BTU /hr IDVFA 12 HX Type. Fixed Heat Load HX Stetus: On /13 Plow Path M&: Trane Co Modeh MDE1291600 Dwgs: PM731Q Syswm Fluid. Fresh Water Tube Flow = 520.10 Ti.be Temperattees - 90.05'F - 103.31'F Heatload =
1,100,000.00 DTUehr IDVH!!3 HX Type: Fixed Heat toad HX Status: On / Not m Flow Path Mft: Amer. Air Fitr.
Model: H36MPACYA Dwgs. PM611A-0004 7 System Fluil HeatLoad-502.78L00 BTU /hr iDVH210 KX'tWe: Fixed Heat Load HX Stard On / in Flow Path Mfr: Amer. Air Fitr, Model: MDE1570300 Dwgs: PM711Q System fluid: Fresh Water Tube Flow - 144.12 Tube Tempc:n ures - 99.0S*F - 101.55*F Heat Load -
200,000.00 BTU /hr IDVH211 HX Type: Fixed Heat Loart HX Stsoss-OtY Mfr. Amer Air F'tr.
Model MDE1573503 Dwgs: PM71IQ System Fluid: Fresh Water Heat load -
0.00 BTU /hr
y - y,_ a y_
, m gy _g y----------;g7-g - g 3 y-3;g.3g3;;)-
6'2/9s 20:35 PROTO-FLO 4.01 by Proto-Power Corporation - Serial $PFL-0000 Piec 23 cr 26 t
{
Public Semce Electric and Gu - OnPSEG,I1-385NEW L'HS'.STACSURS2.PDB - Revision 2.00 t
Hope Creek Generateg 9:ati0n - STACS Heat Exchanger Data Report Convergenes Preswe=1.0E.5 Sum Qal 05 2 Frwtion-l.0E-6 FCVal.0E4 PCv=.4E3 Tc*npen.ture=5 013 LOP /SSE EOBFailure IDVH213 HX Type: Fhed Heat Load HX Status: OIT M&: Ainer. A:r Fit.
Model: MDE2478600 Dwgs: PM786Q System F;uid: Firsh Wates Heat Load =
0 00 BTU,hr 1 EVE 412 IIX Type: Fited Heat load HX S'atus: On /in Flow Path Mir:Tratie Co. -
Model: MDE1291600 Dwgs: PM731Q System Fluid: Fresh Water Tube Flow - 527,50 Tube Temperatures = 100.01'F 104.21*F Heat Load =
1,100,000.00 BTL*/hr lEVHil3 HX T pe: Fixed Heat Load HX Statt.s: On / Lt in Flow Path 3
Mfh Amer. Air Fitr.
Model: H36MPACYA Dwas PM61IA 0004 7 System F!uld; i
i Heat load a 502,781.00DTUhr IEVH210 HX Type: Fixed Heat Load liX Status: Oc /in Flow Path Mf', Amer Air Fitr Model: MDE1570300 Dwgs: PM711Q r
System F1md: Fresh Water 1
Tube Flow = 142.7)
Tube Tennperatures = 100.01'F - 102 97'F HeatIcad-210,000.00 BTU /hr IEVH211 HX Type: Fixed Heat Load HX Status' OtY Mfr* Amer. Ate Fitt.
Model: MDE1573500 Dw58: PM71IO SystemFled Fresh Water heat Lead -
0.00 BTUtr IEVH213 HX Typer fixed Hear Load HX Status: off Mft: Amer. Air F1tr.
Mode!: MDE247S600 Dwp: PM786Q System Flui: Freth Water Heat Load =
0.00 Bnh
Jur. 02*5: II:c~ 50 S E o - F ^ L:EF.~, O R F 223 445 6251 TC 1 E 0'3 3 312. 3 F. 23. J.
6/2/96 20 35 PROTO-FLO 4.01 by Proto-Power Corporation - Scrial #PFL-0000 Page 24 of 26 Pubhe Service Electric and Gs - GAPSEOil13ES.NEW UHSWTACSUES2.PLB - Revision 2.00 Hope Creek Generattrig Station STACS HeatExchanger Data Report Cor,vergerse, tren.rs=1.CE $ 3.m Q-1 OE 2 fnchm=L0E 6 FCV*l.0E4 PCWLOE 3 Tercersane=5 OE-J LOP /SSE - EOS Failure IFVE412 HX Type: Flxed Heat Load HX Str.tus: On / m Flow Path Mft; Trace Co.
Model MDE1291600 Dwgs: PM731Q Systern fluit Fresh Water Tube Flow - $24.06 Tube Temperatwes - 99.05'F - 103.28*F Heat Iead -
1,100,000.00DTU,br IFVH113 HX Type: Faed Heat Load HX Status; On / Not m Flow Path Mfr: Amer. Air Fitr.
Model: H36MPACYA Dwss: PM611 A-0004-7
$ystem Thud-Heat Load -
502.781.00 BTU /br IFVH210 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mir: Amer. AirFitr.
Model: MDE1570300 Dwgs: PM71!Q System Fluid: Fresh Water Tube Flow = 147.99 Tube Temperatures - 99.05'P - 101.91'F Heat lead =
210,000 00 BTU /hr 1FVH211 HX Type: Fixed Heat Load HX Status: ogr Mft: Amer. Air Fitr.
Model: MDE1573500 Dwgs; PM711Q Sys*.em Fluid: Fresh Water Heat Load =
0.00 BTC/hr 1FVH213 HX Type: Fixed HeatImad HX Status, og Mft: Amer. Air Fitt.
Model MDE2478600 Dugs: PM786Q S3 stem Fhid: Fresh Water Heat Load -
0.00 BTU /hr i
L__________--____.
J Jr. 02
- Es 21. C - - FP R C - 's - F ~% E R CCRP 203 4 ;6 $252 Tv 1E093.;512:5 F.GJ<31 6/2/9s 20.35 PROTO-FLO 4.01 by Proto-Power Corporati:n - Se:ial #PFL-0000 page 25 or :e Pcblic Service Elect-ic and Gas GnPSEG11 385WEW (~HSiSTACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Heal Exchanger Data Report Cenergence. Prenurs': CE-5 Sum Q-1.061 fncunn=l.0E-6 FCV=1 DE4 PCV'l.UfA Ts.was-10E-3 LOP /SSE. EOB Failure IGVE412 HX Type: Fixed HeatLoad HX Status: On / m flow Path Mti Trace Co.
Model: MDE1291600 Dwgs. FM731Q System Fluid: Fruh Water Tube Flow = $31.94 Tube Temperatures - 100.017 104.177 l
Heat Load =
1,100,000.00Bn'h l
IGVH2I0 HX Type: Fixed Hea: Load HX St:tus: On / m Flow Path Mfh Amer. Alr Fitr.
Model MDE1570300 Dwgs: PM711Q System Fluid: Frnh Water Tube riow - 130.96 Tube Temperatures = 100.01T - 103.08T Heat Load -
200,000 00 BTU /br IGVH21:
HX Type: Fixed Heat Load HX Status: Orr Mfh Amer, air Etr.
Model: MDE1573500 Dwgs: PM71IQ System Fluli Fresh water j
Heat Load -
0.00 BTU /hr lHVral2 HX Type: Fixed Hear Load EX Status: On /in Flow Path Mfh Trane Co.
Model; MDE1291600 Dwgs. PM731Q System Flutd: Fresh Water Tube Flow - 606.81 Tube Temperatures = 99.057 102.707 Heat Load a 1,100,000.00 BTU 4ir
)
I t
IHVH210 MX Type: Fixed Heat Laad HX Status: On /in flow Path Mft: Amer. Air Fitr.
Model: MDE1570300 Dwgs: PM711Q System Eu.d Fresh Water Tube Flow = 144 00 Tube Temperrures = 99.0$T - 101.65T IIcat Lead =
200,000 00 BTU /hr
<e.,
m.
-mme
-~mme-
.w-r see we.
was....opsa c n
.s.
o, 6/2/9s 20:35 PROTO FLO 4.01 by Proto-Power Corporation = Serial #PFL-0000 race 26 or :6 Public Service Electne and Gaz Of PSEOil 1 382 EW IJHS4TACSUHS2.PDB - Revision 2.00 Hope C:eek Generating Station. STACS Heat ExchangerData Repon Coctogence Premn=i CE-5 Sn Q-1.0E-: fncuan=1.0E4 FCVal.02-4 PCv=1.05.1 Temperanst=5 CE J IOP/SSE - EOB Failare iHVH211 HX Type: Fixed Hest Load HX Status: off Mfr: Arner. Air Fitr.
Modci: MDE1573500 Dwas: PM711Q System Fimd: Fresh Water Heat Lead -
0.00 BTU /hr j
1 I
i l
l l
- -_ ~ __
~..
,,e,._
t PROTo POWER CORPORATION 15 THAMES STREET PHONE: (860) 446-9725 GRoToN, CT 06340 FAX: (860) 448-4860 FAX COVF.R SHEET i
FILE No.: H -s#'
DATE: #4 hA l
TOTAL PAGES (INCLUDING COVER SHEET); sa l
To:
8-b DWMr FROM:
Me Ash j
DEPT.
fax No.:
( m ) ins-izi<
FAX No.: _(860) 448-4860 l
REFERENCE:
MESSAGE: It. k
% ac a es s.(c > Gr-
- s.
2.*rh>v -:+ -u _sep n d A L_4 _ w h,j.,
- u Lr. J. YLs 6os s -.-. - ta
_ _ %1rla. vha.,.
ra alt zs -4 v;s
.w en:~1st,e zzo-s
% J J 5-eat ut~ :, sc-rs e. <k ma d Vds %sse.nu :, n. e
- F.
feu
- - Lhd u m c %
I vbe.-
t a.r,.ci-
~;% % G OC w, M ac w rris du s.
To report transmittal problems or for confirmation, please call (860) 446-9725.
~ -.
+-u mm a.e v. es. a w 6/?/98 09.55 PROTO-FLO 4.01 by Prots Power Corporation - Senal #PFL-0000 p.ge i of 3 Pubhc Service Electne and Gas G.\\PSEGil1-385\\NEW UHSGTACSUHS2.PDB Revision 2.00 Hope Creek Ger.erating Station - STACS Flow Summary Report Conwgene huwe=1.0E ! Sum Q=1.05-2 Menan=1.08-6 FCV=1.0E 4 PCV=1.05 3 Tempers.ec=545-3 LOPiSSE B Loop - 2 EDGs X-Ted - No SFP EDG Rm Clrs Throttled - Red Rm Clis Iso Flow Summary Title Diameter Flow Mmhnum Flow NPSHA NPSH (m)
(gpm)
Igpm)
(ft)
Ratio IDP210 out 19.250 9,828.36 1BP210 out 19.250 10,072.84 iB1E201 out 19.250 9,757.52 iBE205 out 19.250 9.132.09 1B2E201 out 19.250 10,106.09 1BT205 recire.
2.067 24.62 1 AP2021 out 0.957 22.57 1AP202 2 out 0957 9.55 ICP202-1 out 0.957 27.32 iCP202 2 out 0.957 9.92 1CVH210 out 3 068 121.71 1 AVH210 out 3 068 139.50 1 AVH209 out 3.068 77.23 1 AVH206 out 1.930 31.85 1BVH210 out 3 068 146.04 iBP2021 out 0.957 28.09 IBP202 2 out 0.957 10.01 1DP2021 out D 95
25.51 1DP202-2 out 0957 9.91 IDVH210 out 3.068 146.55 l
IFVH213 out 4.026 422.16 i
!! Revene flow Through Check Valve
&& Pump Flow is Past End ofCurve l
" Flow BelowMininu:m
$5 NPSH Available Below NPSH Required l
z
__mm
~y, i
ese98 09:55 PROTO-FLO 4.01 by Proto-P:wer Corporation - Serial #PFL-0000 P p 2 or 3 Public Servici Ele:tnc and Gas G:'PSEG\\11-385 NEW UHSiSTACSUH32.PDB - Revision 2.00 Hope Creek Generating Station STACS i
Flow Summary Report Ccase3cocc: Pycus't=1 DR-3 km Qal OE-2 Fnc m=1.CG4 FCVal.0EA PCV=l.0E 3 Temperausrs=5.0E-3 LOP /SSE - B Loop 2 EDGs X-Tied No SFi - EDO Rm Cirs Throttled Red Rm Clrs Iso Flow Summary Title Diameter Flow Mmunum Flow NPSHA NPSH (in)
(spm)
(gpm)
(8)
Ratio j
1BVH213 out 4.026 425.79 ICVH213 out 4 026 394.75 IDVH213 out 4.026 417.57 IBK202 out 0957 5.98 IDVH211 out 3.068 114.52 l
l IBVH211 out 3.068 114.68 1 AE328/lBE328 comb. out 0.546 12.20 1AE328/1BE328 out 0.546 12.20 1 AVE 412 out 6 065 235.64 IEVE412 6.055 235.16 IEVE412 out 6.065 235.64 1 AE408/405/404 out 7.981 1,074.33 ICVE412 out 6.065 233.53 IGVE412 out 6.065 233.53 1CE408/405/404 out 7.981 l.064.76 1BVE412 out 6.065 232.74 iFVE412 out 6.065 232.74 1DVE412 out 6.065 232.20 INVE412 out 6.065 232.19 1BE408/405/404 out 7.981 1,061.10 IBK400 out 6.065 1.597.89
'! Reverse Flow Through Check Valve
&& Pump Flowis Past End of Curve
- Flow Below Muumum
$$ NPSH Asailable BelowNPSH Required l
6/3/98 09:55 PROTO-FLO 4.01 by Proto-Pswer Corporation - Serial CPFL-0000 Pase 3 of 3 Pub!ic Service Electric and Gas. CdPSEG11-385\\NEW UHSsSTACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Flow Summary Repon Cor.verscnce Pressure =1.0E-5 Sum Q=1.0E-2 Friction =l OE-6 PCV-1.0E-4 PCV=1 SE-3 Temperature =5 DE-3
)
LOP /SSE. B Loop. 2 EDGs X Tied - No SFP - EDO Rm Clrs Throtded Red Rm Chs Iso Flow Summary Title Diameter Flow Minimum Row NPSHA NPSH (m)
(sp:n)
(gpm)
(ft)
Ratio ILJE4U5<GU3/894 Oul
/.751 4,UJ5./4 1BK403 out 6.065 407.97 RE465982 out 0.957 12.99 i
!! Revesse Flow Through Check Valve
&& Pump Flow is Past End of Curve
" Flow Briow M' imum
$$ NPSH Available Below NPSH Requhed m
1
j Jun 03'sa :a: 13 F4 FCOTC-PCWER CCPP 200 445 5292 TC 16052391218 F.25 30 6/3/98 09.55 PROTO-FLO 4.01 by Proto-Power Corporation - Senal #PFL-0000 Page3 cr14 Pub!1c Service E!ec:nc and Gas. G APSEGill.315iNEW UHS \\STACSUHS2.PDB. Revision 2 00 Hope Qock Generstmg Stanon STACS Manual Valve Line.Up Report Conergener Pressre=1.CE-5 Sum Q=1. Chi-2 fri:non=1.0TM FCVel OE-4 POV-t OE4 Temperarre=5.CE 3 LOP /SSE - B Loop. 2 EDGs X.Ticd. No SFP. EDG Rm Clrs "Dirottled. Red Rm Cirs Iso Tag Valve Type Position Actual "
V.V4Da USAl
& W UU7e V.0105 Ba11 100.00 %
V-0106 Ball 100.00 %
V.0107 Ball 100.00 %
V 0108 Ball 100.00 %
V-0109 Ball 100.00 %
V-0112 Plug 65.00 %
V-0116 P;ug 70.00 %
V-0120 Plag 70.00 %
l V-0124 Plug 6100%
V-0128 Plug 70.00 %
V-0132 Plug 65.00 %
V-0138 Butterfly 0 00 %
V-0139 Butterfly 100.00 %
V.0140 Butterfly 100.00 %
V-0141 Butterfly 0.00 %
V-0142 Ball 0.00 %
v 0143 Ball 100.00 %
V-0144 Rall 100.00%
V-0145 Sall 100.00%
V-0146 Ball 100.00%
V-0147 Ball 0.00 %
V.0148 Ball 100 00 %
V 0149 Ball 0 00 %
V.0222 Plug 40.00 %
V-0223 Plug 40.00%
V-0224 Plug 40.00 %
V 0225 Plug 40.00 %
V.0225 Plug 40.00 %
V-0227 Plug 40.00 %
V.022B Plus 4000%
V-0229 Plug 40.00 %
V-0230 Plug 25.00 %
V 0231 Butterfly 100.00%
- Actual Position for Panially Open Check Valves
on - ce noa.-,, va, -. e n n we
~~e nn
,n oweseee m e c. ew a 6/3/9s 09:55 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 rase 4 er14 Public Sen' ice Electric and Gas - G \\PSEO\\l1385\\NEW UHS \\STACSUBS2 PDB Revision 2.00 Hope C:eck Generstmg Station-STACS l
Manual Valve Line-Up Report j
Convergence Frnsercat OK $ Ntm Q=1 DE-2 Fric' son =1.0E4 FCV-1.0E4 PCVal.0E.3 Tergerswe=5.0E4 LOP /S SE - B Loop. 2 EDGs X. Tied - No SFP - EDG Rm Clts Throttled - Red Rrn Cirs Iro Tag Valve Type Position Actual "
v -v4 a.s atsucruy 4 vv.vv7e V.0235 Butterfly 100.00%
V.0237 Buttarfly 100.00%
V-0238 Ball 100.00%
V-0241 Ball 100.00%
V-0242 Plug 25.00 %
V-0244 Ball 100.00 %
V-0245 Plug 25.00 %
V-0247 Ball 100.00 %
V.0248 Plug 25.00 %
V-0250 Ball 100.00 %
V-0251 Plug 25.00 %
V.0253 Ball 100.00%
V-0254 Plug 25.00 %
V.0256 Ball 100.00 %
V.0257 Plug 25.00 %
V.0259 Ball 100.00 %
V.0260 Plug 25.00 %
V.0270 But:erfly 71.56 %
V-027i Butterfly 100.00 %
V-0272 Butterfly 100.00 %
V-0273 Butterfly 42.48 %
V.0275 Butterfly 57.55 %
V 0277 Butterdy
$7.57%
V.0278 Gate 100.00 %
V.0279 Gate 100.00%
V.0280 Gate 100.00%
V.0281 Plug 51.95 %
V.0282 Gate 100.00 %
V-0283 Gate 100.00%
V.0284 Plug 5 t.63%
V 0285 Gate 100.00%
V-0286 Oste 0.00%
V.0287 Plug 51.28 %
- Actual Poinzon for Partutlly Open Check Vahes t
J ut4 03'93 10:13 FF C00TO-PCWER CCRo 203 445 6292 TO 16C93091219 c.07 30 6/3/98 09:55 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 P.. i of 24 Public Service Ele:me and Gas - 0:\\PSEO\\11 385\\NEW UHS 4TACSUHS2.PDB - Revision 2.00 Hope Crect Generstmg Statmn - STACS Heat Exchanger Data Report Con.ergrnte Prewr=1tLS Sum Q=1.CE 2 fricour.=1.01!4 rCV= LDE-4 PCV=1.or.-3 Temperatst=3 DE 3 LOP /SSE - B Loop - 2 EDGs X-Tied No SFP - EDO Rm Cirs Throttled - Red Rm Clrs Iso 00E129 HX Type: Fixed Heat Lead HX Status: On / Not in Flow P1A Mft: Basco lac.
Model. ES-24/18096 Dws:: PM050-0039 3 System Fiu:d.
Heat Load =
500,000.00 BTU &
00K107 HX TYPE: Fixed Heat Load HX Status: On / Not in flow Path Mfr: American Std.
Model. 06060 Dwgs: PM050 0022 5 System Fluid:
Heat Load -
2,240.323.00 BTUN 10C150 HX Type: Fixed Heat Load HX Status: Off Mft:
Model Dwas:
System Fluid:
Heat Load =
0.00 BTU /br 10E1110 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: Basco, Inc.
Model BA24A08072 Dwgs: PI 342287 System Fluid:
Heat Load =
$15,000.00 BTU /br 10E114 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: Gen. Elest. Co.
Model: MDE0965400 Dwgs: PM00M.1-7 System Fluid:
Heat Load =
42.300.00 BTU /hr 10E129 HX Type: Faed Hest Load HX Status' On / Not in Flow Path Mir: Basco, Inc Model. ES 24/18096 Dwgs: PMD50 0039 3 System Fluid:
Heat Lead =
10,750.00 BTU /br
i
-- ~
- m. o,
<sv.m<v-wem we
~~e sees uv m u-v e.se m l
6/35809:55 PROTO.FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 page2 or 24 Public Service Electric and Gas - GsP5EGil1385WEW UHS'.STACSUHS2.PDB - Revision 2.00 i
Hope Crack Generating Station - STACS i
Heat Exchanger Data Report Cc necrpunce Messurcat 0F.4 Scm 0-1.0E-2 fric*non=1.0E 6 FCV=1.0E.4 PCV-1.0E-3 Tenperates.0E-3 LOP /SSE. B Loop 2 EDGs X Tied. No SFP. EDG Rm Clrs Throt. led - Red R:n Cirs Iso 10K107 HX Type: Fixed Heatload HX Status: On /.Not in flow Path Mfr: Amencan Std.
Model: 06060 Dwas: PM050@22-5 System Fluid' Heat imd =
5,412.000.00 BTU /br I AIElls HX Type: Fixed Heat Load HX Status: Otr Mh: DcLava:/IMO Model: MDEt328000 Dwas: PM012-0099 System Flud.
Heat Lead -
0.00BTuhr IA1E201 HX Type: Shell & Tbbe HX Status: On / Not in Flow Path Mfr: Graham Mf);. Co Model: 92-6-$fM CON Dwgs: PM069Q 0058 Tube Fluid: Buckiah Water.12 ppt ShcIlFluul: Freshwater Constmetion Type: TEMA-G 1 Shells, O ShcIl Passes,4 Tube Passes She!! Mm Area - 6.2530 ft^2, Dcsign ShcIl Vclocity - 3.900 Its, She!! Diameter - 92.000 T
D 06 4 0.7 n
- 42.
ft,
= 9.5 Tube Pitch - 0.9375 in Tube Pi*ch Type - Tnangular l
5,700 of 5,700 Tubes Active UTubes - No i
Effcenvc Arca = 46.295 00 ft*2 Area Fa: tor - 0.9849 l
Foutmg = 0.0000 (mside) 0 0012 (outside)
Hoff = 0 4568 LMTD = 0.0000 LMID Correccons FF = 0.0000 Fb = 0.0000 Heat Load -
0.00 BTU /hr UOverall- 0.00 BlU/hr/ft^2/'F 1A2El18 HX Type: Fixed Heat Load HX Status: Off Mft: DeLavaL1MO Model: MDE1328000 Dwgs: PM012-0099 System Fluid-Host Load -
0.00 BTU /hr
J.m 03 's s t o : Z a s:R FDCTC-DOWER C04F 203 416 329 ~ T2 16C9339121E F. 0 3,12 93/98 0935 PROTO-FLO 4.01 by Proto-P:wer Corporation - Scrial #PFL-0000 rase 3 of 24 Pubhe Servi:e Electric ami Gas - G:7SEG\\11-385iNEW UllS'STACSUHS2.PDB - Revision 2.00 Hope Creek Generatin5 tation STACS S
Heat Exchanger Data Report Cun,erp*sc !*ressure=1.CEd Sum Q=1.0E 2 Frt:tonel oE-6 FCVM.05-4 PCVM.CE4 Temperats -5.004 LOP /SSE - B Loop - 2 EDGs X-Tied - No SFP EDO Rm Clrs Throttled Red Rm Clrs Iso 1A2E201 HX Type: Shell& Tube HX Status: On/ Notin Flow Path Mfr: Graham Mfg. Co Model: 92 6-504 CGN Dwgs: PM069Q&58 Tube Fluid: Braciash Water 12 ppt ShellFluid: Fresh Water Construction Type: TEMA-G 1 Shells, O Shell Pssses,4 Tube Passes Shell Min Area = 6 2530 ft^2, Design Stell Velocity = 3.900 ft/s, Shell Diameter = 92.000 Bame info: Spacing = 62.000 in, Thickness = 0.000 in, Area = 0.000 fr2, K = 0.000 Tubes: Dm = 0.694 in, Dout = 0.750 m Iength = 42.00 ft, K = 9.50 Tube Pitch = 0.9375 in Tube Pitch T>pe = Tnangular 5,700 of 5,700 Tubes Active UTubes - No E#ective Area = 46.295.00 fP2 Area Factor = 0.9849 Fouling = 0.0000 (Inside) 0.0012 (outside)
Hoff= 0.4888 LMTD = 0.0000 LMTD Corrections FF = 0.0000 Fb = 0.0000 Erat Load =
0.00 BTU /hr UOyetall = 0.00 BTUzhrift^2/*F 1AEl109 HX Type: Fixed Heat Load HX Status: off Mfr: Basco inc.
Model: BA43A05048 Dwgs: P1342287 Sys:cm Fluid:
Heat Load =
0 00 BTU /hr I AEl11 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mir: Geceral Elect.
Model 264A4EOS Dwgs: PM003 TR 18 5
)
System Fluid:
Hea: Load -
515,000.00 BTUihr 1 AE112 HX Type: F xed Heat Load HX Status: On / Not in Flow Path Mfr: General Elect.
Model: ll4DB270 Dwgs: PM003-G 17 System Fluid:
Heat Load =
42,300.00 BTU /hr
______2____
~-n
__w c. m. n 6!3/98 09.95 PROTO-FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 Pas.c or 24 Public Service Electne and Oas - G:\\PSEGill-385\\NEW UHS'STACSUHS2 PDB - Revision 2.00 Hope Creek Generatesg Sation-STACS Heat Exchanger Data Report C mverg:nce Prcasu cal.0F.-$ Sum Q=LCB 2 Fnctien=l.004 PCV=l.064 PCV-1.0E-3 Tempersaae-5.0E 3 LOP /$5E - B Loop 2 EDGs X-Tied - No SFP - EDG Rze Clrs Throttled Red Rm Clrs Iso 1AE115 HX Type: Tixed Host Load HX Status: On / Not m flow Path Mir. H.K. Poner Co, Model: T-140963X45 Dwgs: PE005-0012-9 System Fluid.
Heat Load =
10.750.00 BTU /hr IAE116 HX Type: fixed Heat Load HX Status: On / Not in Flow Path M&: General Elect.
Model: 155B8243P001 Dwgs: PM003-76-1 2 System Fluid:
Heat Load =
5,412.000.00 BTU /hr IAE117 HX Type Tixed Heat Load HX Status: orr Mfr: General Elect.
Model: MDE0924300 Dwgs: PM003-G-1-7 System Fluid:
Heat Lead-0.00 BTU &
IAE126 HX Type: Fixed Heat Load HX Staras: og Mfr: Amencan Std Model: 5-046-17-168-3 Dwgs: N1 B31-S1-120 System Fluid:
Heat Load =
0.00B7U/hr i
IAEl30 MX Type: Fixed Heat Load HX Status-Off Mfr: Ametek!Whitlock Model: 4-W16HI-4-A-CB Dwgs: PM007-00313
)
System Fluid:
Heat Load -
0.00B7U/hr j
IAE202 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path l
Mfri Alfa Lavalloc.
Model: A 20 BXS Dwgs: PM071Q-0010 System Fluid:
I Heat Lead =
16,100.000.00 BTU /hr
=
l
--~,mm m
.s eme - me u..
,mu u t a a e.12 m
6/3/98 09:55 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 P.rg,e 5 cf 24 Public Service Electnc and Gas - GnPSEG511 3855NEW UHSWTACSURS2 PDB - Revision 2.00 l
Hope Creek Generating Station - STACS Heat Exchanger Data Report Converg::1ce: Freuvre=1 OE 3 Sn1 Q-l.0E-2 Pnenem-l 0E-6 PCV-;.0Ee PCV-1.0F 3 T:rrwro=5.0E 3 LOP /SSE B Loop.2 EDGs X-Tied - No SFP EDG Rm Cln Throttled - Red Rm Clis Iso l-IAE205 HX Type. Fixed Heat Lead HX S: ants: On / Notin Flow Path l
l Mft: Delta Southern Model: 21 A9227AN Dwgs: NO-Ell-B0015 1
Systern Fluid-Heat Load =
132.500,000 00 BTU /hr 1AE214 HX Type: Fixed Heat Load HX Status: On / Not in Flow Pa'h Mfr CVIInc.
Model C735 9934 Dwgs: PM04tQ-00714 System Fluil Heat Load -
19,500,000.00 BTU /hr l AE218 EX Type: Fixed Heat Load HX Status: off Mft: CVI Lt.
M.xlel. C735-9934 D w gs: PM048Q-0071-4 System Fluid-Heat Load =
0 00 BTU /hr 1AE275 HX Type: Ftxed Heat Load HX Status: Off Mfr: CVI!nc.
Model:
Dwgs: PM048Q j
System Fluid-I Heat Load -
000 BTU /hr i
1AE328 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mft: Parker Hamson Model: HDTC-SS 6 2 Dwgs.
System Flutd.
Shell Flow - 5.61 Shell Temperatures = 100.00'F - 119.73'F Hcat Losd =
55,000 00B71)/hr l
l 1AE404 HX Type: Fixed Heat Load HX Status; Onlin Flow Path I
Mft: American Std.
Model: 17072 CPT D w as: PMOISQ Systern Fluid. Fresh Wates Tube Flow r 1.073M Tube Te:nperatures = 116.06'F - 11S.00*F Heat Load -
1.353,000.00 BTC&
l
JUN O ') ' 9 9 13:2. F4 FGOTO-PCWER CCRD 200 445 E292 TO 1609329:219 c.;2 20 6/3/98 09:55 PROTO.FLO 4.01 by Proto-Power Corporation. Serial #PFL-0000 Pase 6 nr 24 Public Semce Electne and Gas. OnPSEG',11 365'NEW URS\\STACSL~HS2.PDB. Revision 2.00 Hope Creek Genersting Station - STACS Heat Exchar!ger Data Report Conscrpence Preuvre=1.0E-5 Sum Qal.0E-2 Frictim1.0E 6 FCV=1.CE-4 PCV=1.DE.3 Teraperatre=5 OE-3 LOP /SSE. B Loop - 2 EDOs X-Tied - No SFP - EDG Rm Cirs Thronled - Red Rm Clrs Iso IAE405 HX Type: Fixed Heat Load HX Stana: On/in Flow Path Mft: ArneticanSul.
Model: 19084 CM Dwgs: PM01BQ System Fluid: Fresh Water Tube Flow - 1.071.14 Tube Temperatures = 105.87'F - 116.06'F Heat Load =
5,412,000 00 BTU!hr IAE408 HX Type: Fixed Heatlead HX Status: On /in Flow Path Mfr. American Std.
Mcd:l: 19198 Dwgs: PM018Q System Fluid. Fredi Water Tube Flow = 1.0C9.81 Tube Temperatures = 100.00'F.105.87'F Heat Load =
3,118,000.00 BTU /hr 1 AK111 HX Type: Fixed Heat Load HX Statua: On / Not in Flow Path Mft: Camer Corp.
Model. 19FA553B5005932 Dwgs: PM623 0002 9 System Fluid:
Heat Load =
502.781.00 BTU /hr 1
1AK202 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft; CV1 Inc.
Model: C735 9909 Dwgs: PM04 SQ-0(M4-2 System Fluid:
Heat Load =
$4,000.00 BTUh 1 AK400 H X Type: Facd Heat Load HX Status
- On / Not in Flow Path l
Mfr: Carner Corp.
Model: 19FA455B122022 Dwgs: PM723Q System Fluid:
Hest Load =
7,530,700.00 B'IU/hr 1AK403 HX Type: Fixed Heat Lead HX Status: On / Not in Flaw Path Mfc Carrier Corp.
Model 19FA441B1142020 Dwas: PM723Q System Fluid:
Heat Load -
2.515,340 00BIU/hr I
[
f t.; N 03'99 10:Z; FP S WC TC -PCWEP CCRS EOC 445 6292 TC 16033291215 F.13'30 6/3/98 09.55
- PROTO-FLO 4.01 by Proto-Power Corporation - Scrial #PFL-0000 Pase 7 or 24 Pubhc Servtee Electne and Gas G"PSEG\\11 385WEW UHSiSTACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Comergerce Nsu tv-1.0E-5 Som Q=l.0E-2 Fnctional OE-6 FCV=I.0E4 PCV=1 LE-3 Temperomrc=5 CE 3 LOP /55 E - B Loop 2 EDCs X-Tied - No S!? - EDO Rm C!rs Throttled - Red Rm Cirs Iso 1AP176 HX Type: Fixed Heat Load HX 5tatus. On / Notin Flow Path Mft: Carrier Corp.
Model 19FA9991007-18 Dwgs: PM623-118 System Fluid:
Heat Load =
100,000.00 BTU /hr IAP202-1 HX Type: Fixed Heat Load HXStatus: On /in Floa Path Mfr: Graham Mfg. Co.
Model 8X4C-12 Dwgs: N1-El1-C002-51 System Fluid. Fsce. Water Tube Flow - 22 40 Tube Temperatures - 100.00*F - 131.46'F Heat Load -
350.000_00 BTU 4 r 1AP202-2 HX Type: Fixed Heat Lead HX Status: On /In Flow Path Mfr. Graham Mfg. Co.
Model: 992C430BX Dwas: N1-El1-C002-6 System Fluid: Fresh Water Tube Flow = 9 55 Tube Temperatures - 100.00'F - 102.1 l'F Heat Load =
10,000.00 B'IU/hr 1 AVE 412 HX Type: Fixed Heat Loed HX Status: On / in Flow Path Mft: Trane Co.
Model. MDE1291600 Dwgs: FM7310 System Fluid; Fresh Water Tube Flow = 235.16 Tube Temperatures - 100.00*F - 109.42'F Heat Load -
1.100,000.00 BTU /hr
! AVH113 HX Type: Fixed Heat Load HX 5tatus: Oc / Not m Flow Path j
Mft: Amer. Air Fitr.
Model: H36MPACYA Dwgs. PM611A-0030-4 l
Sistem Fluid-HeatLoad=
502.781.00 BTC/hr l
l' l
l
JUN OT i5 iati' FR P30TC-FCWEF C Cf# 2 102 446 6292 TC 16C32091219 F. lo 20
~
639809:55 PROTO-FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 Pase of24 Public Servre Electric and Gas - G.\\PSEO\\11 385\\NEW URS\\STACSUHS2.PDB - Revisica 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Conscrgence Pressurral CE-s Surr:Q=1.0E 2 Fmuon-l.0E4 FCV=1.DFA PCV=1.0E-3 Tcapramre=S.0E-3 LOPfSSE - B Loop 2 EDGs X Tied - No SFP - EDG Rm Cirs Broeded - Red Rm Cirs Iso IAVH116 HX Type: Fixed Heat Lead HX Status: On / Not in Flow Pa'.h Mft: Arner. Air Fltr.
Mudet: H36MPACYA Dwgs: PM611 A-0033-4 System Fluid.
Heat Load =
$30,000 00B'IU/hr IAVH208 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mfr: Amer. Air Fitr.
Model: MDE1572400 Dwgs: PM71IQ System Fluid. Fre*h Water Tube Flow = 31.82 Tube Temperatures = 100 007 - 105.70'F Heat Load =
90,000.00 BTL*/hr 1AVH2O)
HX Type: Fixed Heatlead HX Status: On / in Flow Path Mft: Amer. AirFltr.
Model: MDE1571400 Dwgs: PM711Q System Fluid: Fieah Water Tube Flow = 77.13 Tube Temperatures = 100.00 7 - 106.01 7 Heat Load -
230,000.00 BTU /hr i
IAVH210 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mft: Amer. Air Fitr.
Model: MDE1570300 Dwgs PM711Q System Fluid Fresh Water Tube Flow - 139.33 Tube Temperatures = 100.00T - 106 077 Heat Load =
420,000.00 BTU /hr IAVH211 HX Type: Fixed Heat Load HX Status: Off l
Mft: Amer. Air Fler.
Model: MDE1573500 Dwgs: PM71IQ l
System Fluid:
Heat Lead =
0 00BIU/hr l
l l
l L
i i
.. _ c.,_, m c,, m o m, 6/3/98 09:55 PROTO-FLO 4.01 by Proto-Pewer Corporation - Serial #PFL-0000 ease 9 or 2a Public Service Electric and Gas GAPSEGill 385iNEW UHS \\STACSL'HS2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger DataReport Converpnec INsut*LcE 3 f am Qal CE 2 Fnction=1 CE-6 FCV=106 4 PCV-1.0E-3 Temperatur-DE 3 LOP /SSE B Loop - 2 EDGs X-Tied - No SFP - EDG Rm Clrs Throttled - Red Rm Clrs Iso 1AVH213 HX Type: Fixed Hest Lead HX States: Off Mfr: Amer. Air Fltr.
Modeh MDE2478600 Dwgs: PM786Q System Fluid:
Heat Load -
0.00Bru/hr 181E118 HX Type: Fixed Heat Load HX Status: On /Notin Flow Path Mft: DeLaval/IMO Model: MDE1328000 Dwgs: PM012-0099 System fluid.
' Heat Load =
400,000.00 BTU /hr 1BIE201 HX Type Shell& Tube HX Status: On /in Nw Path Mir: Graham Mfg Co.
Model: 92 6 504 CGN D w as: PM069Q-0058 Tube Fluid: Brackish Water - 12 ppt Shell Fluid. Fresh Water Shell mw - 9.501.78 Shell Temperatures = 119.69'F - 99 847 Tubeflow = 10,106.00 Tube Temperatures - 91.10'F - 110.36T Constructier. Type: TEMA-G 1 Shells, O ShcIl Passes. 4 Tube Passes Shell Min Area - 6.2530 ft'2, Design She!! Velocity - 3.900 ft/s, Shell Diameter = 92.000 Baffle Info Spacing - 62.000 in, Thickness - 0.000 in Area - 0.000 fia2, K = 0.000 Tuber Din - 0 694 in, Dout - 0.750 in, Length - 42.00 ft. K - 9.50 Tube Pitch = 0.9375 m Tube Pitch Type -Triangular 5,700 of 5.700 Tubes A::ive UTubes -No Ef1' ct2Ve Area - 46,295 00 ft^2 Ansa Factor = 0.9849 e
Fouling = 0.0000 (msidel 0.0012 (outside)
Huff = 0.4888 LMTD = 9.0295 LMTD Corrections FF = 0.7691 Fb = 10000 Heat Load =
96,201,D1.38 BTU /hr UOverall = 299.23 BTU /hrift^2FF 1B2El18 HX Type: Fixed Heat Load HX Status: On / Not m Flow Path Mfr: DeLas al/1MO Model: MDE1325000 Dwgs: PM012-0099 System Fluid; Heat Load =
400,000.00 BTU /hr l
l
... ~ -- ~_.-,,..-,_ --
- - ms ~<
,_mm e.wa 6,3 S 8 09:55 PROTO-FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 pcs 10 of 34 Public Service E!ectric and Gas - 0:\\PSEGill-385\\NEW UHS'STACSUHS2.PDB - Revision 2.00 Hope Creek Generatins Station - STACS Heat Exchanger Data Report Convergence Presural CE-3 Srn O=1.0E-2 Fncicavl Of 6 FCV4CE4 PCV=1.3E-3 TerrperanrredOE 3 LOP /SSE - B Loop - 2 EDGs X-Tied - No SFP EDG Rm C1rs Throttled - Red Rrn Cirs Iso IB2E201 HX Type Shell& Tube HX Status: On / in Flow Path Mfh Graharn Mfg. Co, Model: 92 6-504 CGN Dwas: PM069Q4358 Tube Fluid: Brackish Water 12 ppt ShellFluid: Fresh Waser Shell Flow = 10,15131 Shell Temperatures = 119.69'F - 10013*F Tube Flow = 10,190.00 Tube Temperamires = 9L10*F 110.58'F Construeno:t Type: TEMA-G 1
1 Shells, O Shell Pasus,4 Tube Passes Shell Mm Area = 6.2530 ft*2, Design Shell Velocity = 3.900 ft/s, Shell Diameter - 92.000 Baffle Info: Spacmg - 62.000 in. Thickness - 0.000 in Arca = 0.000 f.^2, K - 0.000 j
Tubes: Din = 0.694 in. Dout - 0.750 in, Length = 42.00 ft, K - 9.50 Tube Pitch r 0.9375 in Tube Pitch Type = Triangular 5.700 of 5,700 Tubes Acrive UTubes-No l
Effective Area-46,295.00 ft^2 Area Factor = 0.9849 Fouling = 0.0000 (inside) 0.0012 (outside)
Hoff- 0.4888 LM'ID - 9.0683 LMID Corrections FF = 0.7740 Fb = 1.0000 Heat Lo6d =
98,139,000.95 BTU /hr UOverall - 302.01 BTU /hrift^2/"F IBE1109 HX Type: Fhed Heat Load HX S:atus: On / Not in Flow Path Mir: Bases inc, Model: 8A44A08048 Dwgs: PI-142287 System Fluid; l
Heat Load =
431,650.00 BTU /hr 1 bel 11 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path Mir: General Elect.
Model: 264A4808 Dwgs: PM003 TR 18.5 System Fluid:
Heat Load -
0,360,000 00 BTU &r IDEl12 HX Type: Thed Heat Load HX Status: On / Not in Flow Path Mfr: Gener:1 Elect.
Modcl; 114D8270 Dwas: PM003-0-1 7 System Fhud-Heat Load =
5,487,500.00 BTU /hr J
i-
o w, wc ce n~~
r,,,,-
.c ecc
-v eses ;s, es se m _ a
- 6/3ss 09:55 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 esseit or34 Pubh: Setske Etocanc and Gas - O 'FSEO'.11-385WEW UHS $TACSUHS2 PDB - Revision 2.00 Hope Creek Generntmg Station. STACS Heal Exchanger Data Repert
('owegnce. henwre-1 oE4 hm O=1.cE-2 Hicton=1.0E4 FCV=1.0E 4 PCV-1 DE.3 Ternrwrsare=$.CE-3 LOP'SSE - 0 Loop 2 EDGs X-Tied - No SFP - EDG Rm Cirs Throttled. Red Rm C'rs Iso IDE115 HX Type: Faed Heat Emd HX Starus: On/ Net in Flow Path Mft: H.K. Porter Co Model: T-140963X45 Dwgs PE005-0012-9 System Fluid.
Heat Load -
5:5.000.00 BTU /hr IBEl16 HXType: Fixed Hea: Load HX Status: On/ Not in Flow Path
(-
Mft: General E!ect Model: 155D8243P001 D w gs: PM003-T6-1-2 SystemFluid:
Heat Load -
42.500.00 BTU /br 18E117 HX Type. Fixed Heat Load HX Satus: On /Netin Flow Path Mft: General Elect.
Model: MDE0924300 Dwgs: PM003 O-1-7 System Fluid.
Heat Lead -
8,0S0,000.00 BTU 4 r IBE126 HX Type: Fixed Heat Lead HX Status: 02 / Notin Flow Path Mft:Amencan Std.
Model: 5-0046-17-168-3 Dwgs: N1 B31-Si-120 System Emd.
Heat Load -
5,630,000.00 BTU /hr IBE130 HX Type. Fixed Heat Load HX Status: On / Not m Row Path Mft: Amerek/Whidock Model: 4 Wl8HT-4-A-CD Dwgs: PM007 00313 System Maid:
Heat Load =
42.300.00 BTU,'hr 1BE202 HX Type: Fixed Heat Load HX Status: On / Not in Mow Path Mfr: Alfa-LasalInc.
Model: A-20-BXS Dwas: PM071Q-0010 System Emd:
Heat Load '
8,200,000 00 BTU /in j
J tJh 0]'93 10:Z2 cA P ro T O -P O L4EF CC RP 203 546 G292 TC 16033391I10 F.19 30 1
6/3/98 09:55 PROTO-FLO 4.01 by P otooPower Corporation - Seriot CPFL-0000 Page 12 of 24 Public Scmcc Electri: and Oss OnPSEGil1-395'NEW UHS.STACSUHS2.PDB. Revision 2.00 Hope Creek Generating Station STACS Heat Exchanger Data Repott Comergence Mssurs=1w-5 km Q-10E.2 fnct.onal EPA FCY=lE! 4 PCV-l.0E 3 Tonyctawe=5.0E-3 LOPiSSE B Loop 2 EDGs X Tied No SFP - EDO Rm Clas Throttled Red Rm Clrs Iso IBE205 HX Type. Fixed Heat Load HX Status: On /in Flow Path Mfr: Delta Southern Model. 21A9227AN Dwgs: NO-Ell B001-5 System Fluid: Fatsh waser Tube flow - 9,06812 Tube Teroperatures - 100.00*F - 129.42*F Heat 12>ad -
132,500,000.00 BTU /hr 1
1BE214 11Y 'Jype: Fixed Heat Load HX Status: on / Not in Flow Path 1
I M&: CVI Inc.
Model: C735 9934 Dwas: PM048Q-00714 Synem Fluid:
Heat Load -
9.565 00 BTU /hr IBE218 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: CVI Inc.
ModeI; C735 9934 Dwas: PM048Q 00714 System Fluid:
Heat Load -
10,750.00 BTU /hr IBE278 HX Type: Fixed Heat Load HX Status-On / Not in Flow Path M&: CVIinc.
Model:
Dwgs: PM045Q System Fidd.
Heat Load =
6,000.00 BTU /hr l
1BE326 HX Type Fued Heat Load HX Status: On / in Flow Path Mft: Parker-Ha:nson Model: HDTC SS 6 2 Dwgs:
System Fluid:
l Shell Flow = 6.$4 Shell Te:nperatures - 100.00*F 116.94'F l
Heat Load =
55,000.00 BTU /h:
l I
t l
I'
J Ur4 @3'39 t @ s 2 3 F09 F 0~0-PCuER CCDF 203 445 323I TO.505~35121E F.19 30 93/98 09:55 PROTO-FLO 4.01 by Pr:to-Power Corporation - Serial f!PFL-0000 P.c.13 or 24 Pubh: Sernce Electric ar.d Gas - 0:sPSEGil 1-385NEW UH5'STACSt 1132JDB - Revision 2.00 Hope Creek Generating Station ST ACS Heal Exchanger Data Report i
Con.opene: Pressure =:.0E-3 San Q-l.CD2 F9: con =l.0E 4 FCV=1.064 PCv=1.0E4 Tenersture=5.063 LOP /SSE - D Loop 2 EDGs X-Tied - No SFP - EDO Rm Cln Thrott'ed. Red Rrn Cirs Iso 1BE404 HX Type: Fixed Hett Load HX Status: On / m FlowPath Mth Amencan Std.
Model: 17072 CPT Dwgs: PM018Q j
System Fluid. Fresh Water 1bbe Flow = 1.060.43 Tube Temperatures = 116.26'F - 118 83'F l
Heat Load -
1,353,000.00 DTU/hr l
1BE405 HX Type: Fixed Heat Load HX Status: On / m Flow Path Mfr: Amerkan S:d.
Model: 19084 CPT Dwgs: PM01SQ Systern Fluid: Fresh Water Tube Flow = 1,057.90 Tube Temperatures = 105.947 - 116.26*F Heat Load -
5,412,000.00 BTU /hr 1BE408 HX Type: Fixed Heat Load HX Status: On /in flow Pash Mfr. Amencan Std.
Model: 19198 Dwgs: PM018Q System Fluid: Fresh Water Tube Flow - 1.056 57 Tube Temperatures = 100.00T - 105.94'F Heat Load -
3,118,000.00 BTL'/hr 1BK111 HX Type-Fhed Heat Load HX Status: On / Not hi t0ow Path Mir: Camer Corp.
Model 19FA553B5005932 Dwgs: PM623-0002-9 System Fluid:
Heat Load -
19,.(00,000.00 BTilihr iBK202 HX Type: Fhed Meet Load HX Status: On /in Flow Path Mfr: CVIInc.
Model; C735-9909 Dwgs: PM043Q-0044 2 System Fluid Fresh Water Tube Flow = 5.95 Tabe Temperatures = 100.00T-116.91*F Heat Load =
50,000 00 BTUtr
(-
.r u N t.rrTIr'YTr7VM F % T G-FCUER CCRP ZU3 4 55 ' E292 YC 16033251219 0.20 30 I
l 6/3/9s 09:55 PROTO-FLO 4.01 by Proto-Powcr Corporation - Serial #PFL-0000 Page 14 of 34 Pubhc Service Electne and Gas - 0:\\PSEG'.11 385WEW UHS'STACSCHS2.PDB - Revision 2.00 Hope Creek Generstmg Station STACS Heat Exchanger Data Report Ceme genes: PresswI oF 5 Eurn Q=1 oE 2 Frienon=1ht 6 FCV=10C4 PCY=13E.17emperann=$ OF4 LOP /SSE B Loop - 2 EDGs X-Tied - No SFP - EDG Rrn Cirs Throttled - Red R:n Cirs Iso IBK400 HX Type Fixed Heat Load HX Sta:us: On / in Flow Path Mfr. Carrier Corp.
W iel: 10FA45?'t.22022 Dwas: PM723Q System Fluid: Fresh Water Tube Flow = 1,584 61 Tube Temperatures = 100.00*F 109.57'F Heat Load =
7.530,700.00 BTU 41r IBK403 HX Type: F2xed Heat Lead HX Status: On / in Flow Path Mir: Camer Ccrp.
Model: 19FA441B1142020 Dwgs: PM723Q SystemFluid: Frest Water Tube Flow 2 406.66 Tube Temperatures = 100.00'P - 112.45*F l
Heat Load =
2.515,340.00 BTU /br l
1BP176 HX Type. Fixed Heat Load HX Status: On / Not in Flow Path Mir; Carrier Corp Mod =1.
19FA9991007-18 Dwas: PM623118 System Fluid:
Heat Load =
100,000.00BW/hr IBP2021 HX Type; Fixed Heat Load HX Status: On iin F!ow Path Mft: Graham Mfg Co.
Model: 8X4C-12 Dwgs: N! Ett C002 51 SysternFluid Fresh Water Tube Flow - 27.92 Tube Ternperaturea = 100.00'F - 125.24*F Heat Load =
350,000.00 BTU /hr 1DP202-2 HX Type: Fixed Heat Load MX Status: On /in Flow Path Mfr: Oraham Mfg Co.
Model 992C430BX Dwss: N1-Ell-C002 6 System Fluid: Fresh Water Tube Flow = 10.00 Tube Temperatures = 100 00*F - 102.02'F Heat Load =
10,000.00 DW/hr i
I 1
j
- e wr u 7 a:a n wwurc-rowgw-ccwV- -
m G5E152TG1M31M1269 F.21 30 6/3/9s 09.55 PROTO-FLO 4.01 by Proto-Power Corporation - Scrial CPFL-0000 P.se Is or to Pubile Service Electric and Gas. G.'PSEG'11-385WEW UHS'STACSUHS2.PDB - Revision 2.00 Hope Creek Generstmg Station. STACS Heat Exchanger Data Report Con erge.ws: Prcurc=1 DE ! Sum Q-1 CE-21riction-1 OE4 FCV-1 CE 4 PCV-l.0E-3 Tcrnperanac=ME-J LOP.SSE B Loop - 2 EDCs X-Tied - No SFP - EDO Rm Clrs Throttled - Red Rm Chs Iso 1BVE412 HX Type: Fixed Heat Load HX Status: On /in Flow Puh Mfr. Trane Co.
Modsl. MDE1291600 Dwgs: PM731Q Syrtem Fluid: Fresh Water Tube Flow a 232.26 Tube Temperatures = 100.00*F.109.54'F Heat Load =
Model: H36MPACYA Dwgs: PM611A-00304 Systern Flid:
Heat Lead -
0.00 BTU /hr i
1BVH116 HX Type: Fixed Heat Load HX Status: On / No? in Flow Path Mfr: Amer. As Fitr.
Model: H36MPACYA Dwas: PM611 A-0033-4 System Fluid.
Heat Load =
530,000.00 BTU /hr IBVH208 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: Amer. Air Fl:r.
Model. MDE1572400 Dwgs: PM71IQ System Fluid:
Heat Load -
45,000.00 BTU /hr 1BV!f209 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfh Amer. Air Fitr.
Model: MDE!571400 Dwgs: PM711Q j
System Fluid:
Heat Load =
115,000.00 BTU,hr IBVH210 HXType: Fixed Heat Load HX Status: on / in mw Path Mft: Arner. Air fits.
Wdel MDE1570300 Dwgs: PM711Q System Fluid Fresh Water Tube %w - 145.86 Tube Temperatures = 100.00'F.105.80'F Heat Load =
420,000.00 BTU /hr
_., _ _ _ ~ <. ~
,m..,-
-~so es.
uv m m.,.sw
.u a
6/3/98 09:55 PROTO-FLO 4.01 by Proto-Power Corporation - Serid #PFL-0000 P.se 16 er 24 Pubhc Service Elecmc and Gas G;7SEO;11 385'.NEW IJHS'STACSUHS2.PDB - Revision 2.00 Hope Creek Generstmg Station - STACS Heat Exchanger Data Report Cornergence rns.ure-4 05 5 Sum Q=1.oE 2 rnction=1.0E 6 FCV-1.CE4 PCV=l.oE-3 Temperature =$.0E-3 LOP /SSE - B Loop 2 EDGs X Tied - No SFP - EDG Rm Clrs 1hrottled - Red Rm Clrs Iso IBVH211 ItX Type: Fned Heat Load HX Status: oft.
Mir; Amer. Air Fitr.
Model: MDE1573500 Dwas: PM711Q System Fluid: Fresh %'ater Heat Load -
0.00 BTU /hr IBVH213 HX Type: Fir.ed Heat Load HX Status: Off Mfr; Arr.er. Air Fitr.
Model: MDE2478600 Dwas: PM786Q g
System Fluid: Fresh Weter Heat Load =
0.00B1U/hr ICIE118 HX Type: Fixed Heat Lead HX Status: Ou / Not m Flow Path Mft: DeLaval,TMO Mode?: MDE1328000 Dwgs: PM012-0099 System Fluid:
Heat Load =
400,000.00 BTUlhr j
1C2El18 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path l
Mft: Del.aval/IMO Model: MDE1328000 Dwas; PM012 0099 System Fluid:
Heat Load -
400 000.00 BTU /hr 1CEI12 EX Typt: Fixed Heat Load HX Status: On / Not in Flow Path Mft: Ger.eral Elect.
Modeh 114DR270 D*gi: PM003-0-1-7 System Fluid:
Heat Lead =
5,487.300.00 BTU /hr ICE 130 RX Type: Fixed Heat lead HX Status: On / Not in Flow Path Mfr. Ame:ek/%%t!ock Model: 4-Wl8HT-4 A CB Dwas: PM007 0031-3 System Fluid:
Heat Load =
12,300 00 BTU /hr
.. - - _.,,,., - w -
ew
-e ws vu mum m w
- e. w.m L
6'3/98 09.55 PROTO-FLO 4.01 by Proto-Power Corporation - Serial c:PFL-0000 Pcae i7 er 24 Fabhc Service Electric and Gas - G:\\PSEG\\11-385\\NEW UHS'STACSUH52.PDB - Revision 2.00 Hope Creek Ge:2erstm.g Station - STACS Heat Exchanger Data Report Cemvergen;s. I*ressure=1.of-$ Sun Q=14E-2 rnct;on=1.0E4 FCV=1.0E-4 PCY=l.0E.-3 Ternperteure=5 OE-3 LOP /SSE - B Loop - 2 EDGs X Tied - No SFP EDG Rm Clrs Throttled - Red Rm Clis Iso l
1CE404 HX Type: Fixed Heat Load HX Status: On /in Flow Path l
Mft: Ameneen Std.
Model: 17072 CPT Dwgs: PM018Q I
System Fluid; Fresh Water Tube Flow ' 1,064.09 Tube 1 temperatures = L16.20'F - 118.77'T Heat Load =
1,353,000.00 BTU!hr ICE 405 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mfr Ameri:an Std.
Model: 19084 CPT Dwgs: PM018Q System Fluid: Fresh Water l
Tube flow - 1,061.56 Tube Temperature = 105.92*F II6.20'F Heat Load =
5.412,000.00 BTU /hr l
1CE408 HX Type: Fixed Heat Load HX Stams: On / ir: Flow Path Mfr:American Std.
Model: 19198 Dwgs: PM018Q System Fluid: Fresh Water Tube Flow = 1.06023 Tube Temperatures = 100.00*F 105.92*F Heat Load =
3.118.000.00BTUrhr 1CK111 HX Type: Fixed Heat Load HX S:atus: On / Not in Flow Path Mfr: Carrier Corp-Model: 19FA553D5005932 Dwas: PM623-0002 9 System Fluid.
Heat Load -
19,500,000.00 BTU /hr 1 cpl 76 HX Type: Fixed Heat lead MX Status: On I Not in Flow Path Mft: Camer Corp.
Model: 19FA999-1007-18 Dwgs: PM623118 System Fluid:
Heat Load -
100,000.00 BTU /hr l
p-l l
N td 03'53-10:24 FR FGC*0-PCWER CCU 233 485 829E TO 15c9~391215 P,04 30 O/98 09:$$
PROTO-FLO 4.01 by Proto Power Corporation - Serial CPFL-0000 e.g. is or 24 Public S: vice Electric and Gas GAPSEG'.11-)S5WEW UHS \\STACSCHS2.PDB - Revision 2.00 Hope Creek Generating Station - ST ACS Heat Exchanger Data Report Conyctgass. P* cum =1 OC.S Sun Q-1 UE 2 Frect.onal E4 FCVal.0E 4 PCV-l.CS-3 Temperssre40E-3 LOP /SSE. B Loop - 2 EDCn.LTied. No SFP. EDG Rm C!rs Brottled - Red Rm Clrs Iso ICP202 1 HX Type. Fixed Heat Load HX Status: On /in Flow Path Mfr: Utahaan Mfg. Co.
Model: 8X4C-12 Dwgs: N1.E11.C002 51 System Fluid.
Shell Flow - 27,15 Shell Teenperatures = 100.00*F - 125.95'F Heat Load -
350,000.00 BTUshr ICP202 2 HX Type: Fixed Heat Load HX Staats: On / in Flow Path Mft: Graham Mfg Co Model 992C430BX Dwgd: N1. Ell-C002-6 Syswm fluid: Frnh Water Tube Flow = 9.91 Tube Temperatures = 100.00'F 102.03'F Heat load =
10,000.00 BTU /h:
1CvF.412
!!X Type: Fixed Heat Load HX Status: On /in Flow Path M&: Trane Cc.
Model MDE1291600 Dwas: PM731Q System Fli.d. Fresh Water Tube Flew - 233.05 Tube Temperatures - 100.00*F - 109.50*F Heat Load =
1,100,000 00 BTU /hr ICvH113 HX Type: Fined Heat Load HX Status: On / Not in Flow Path Mft: Amer. Air F1tr.
Model: H36MPACYA Dwgs: PM611 A 0030-4 System Fluid-j Heat Load =
502,731.00 BTIJ&
ICVH210
!!X T>pe: Fixed Heat Load HX Status: On /in Flow Path Mfr: Arner. Air Fitr.
Model. MDE1570300 Dwas: PM71IQ I
Sptem Fluid. Fresh Water i
Tube Flow - 121.54 Tube Ternperatwes - 100.00*F.106.63*F HentLoad=
400,000.00 B lt'/hr I
l i
L---
~
J tJN @J'39 10iE4 FR F4979-FCWEP CCR3 200 445 6252 TC 1 6C 3;30 $ ;2 1 3 F.25 20 6/3/98 09:59 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Pase 19 cf 34 Public Service Electnc and Ges. GVSEO!l 385WEW UHS'STACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Converarsce: henm=1.0F 3 Sum Q-1.0E.2 Fnztice=1056 FCV=1 CE4 PCV=I 4E-2 Ternpm'.sr=$.C&3 LOP!SSE - B Loop - 2 EDGs X-Tied. No SFP EDO Rrn Cirs Throttled - Red Rm Chs ho 1CVH211 HX Type: Fixed Heat Load HX Stams: off Mfr: Amer. Air Fit,
Model: MDE1573500 Dwgs: PM7110 System fluid:
Heat lead =
0.00 BTV/hr 1CVH213 HX Typ : rixed Heat Load HX Status: off j
Mfr: Amer. AirFitr.
Model: MDE2478600 Dwgs: PM786Q System Flund: Fresh Water Hea: Load-0.00 BTU /hr IDE112 HX Type: Fixed Heat Load HX Status: on / hot in Flow Path Mfr: General Elect.
Model: 114DB270 Dwas: PM003-G I-7 System Fluid:
Heat Load =
5,487,500.00 BTU /hr IDE404 HX Type: Fixed Heatload HX S*.stus: Ou / in Flow Path Mfr:Arocr2can Std.
Model: 17072 CM Dwas: PM015Q Systern Fluid. Fresh Water Tube Flow - 1.058.07 Tube Temperatures - 116.29 F - 118.88'F Heat Load =
1,353,00(LO0 BTutr 1
IDE405 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mft: American Std.
Model: 19084 CPI Dwgs: PMOISQ Sysectn Fluid. Fresb Water Tube Flow = 1.055.54 Tube Temperatures = 105 967 - 116.29'F Heat Losd =
5,412,000.00 BTutr I
i
(
.~ _
c. _. -,
6/3/98 09:55 PROTO-FLO 4.01 by Prols-P:wer Corporation - Serial #PFL-0000 Pase 20 of 24 Public Service Electic and Gas 04PSEGil1 385'NEW UHS'STACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Coevsrgewe. msastr=1.0E 5 5am O=1 CE 2 Frictional oE 6 FCv=1.ok 4 KV 1.0E 3 7ernpermare=5.oE-3 t.OP/SSE B Loop 2 EDGs X Tied-No SFP EDG Rm Chs Throttled Red Rm CirsIso IDE408 HX Type: Fixed Heat Load HX Stat's On / in Flow Path Mfr; Ameri:an Std.
Model: 19198 Dwgs: PM018Q '
System Fluid. Fre_h Water Tube Flow - 1,054 21 Tube Temperamres = 100.00*F - 105.96'F Host Load =
~,,118,000.00 BTutt 1DK111 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path l
Mfr: Carrier Cap.
Model. 19FA553B5005932 Dwgs: PM623-0002-9 l
System F;u:d:
Heat Load -
19,500,000.00 BTUb IDPl?6 HX Type: fixed Heat Loed HX Status: On / Not in &w Path Mft: Camer Corp.
Model: 19FA999100718 Dwgs: PM623115 System Fluid:
Heat Load -
100,000.00 B1L'/hr IDP202-1 HX Type: FixedIIcat Load HX Status: On / in Flow Path Mft: Oraharn Mig. Co.
Model: EX4C-12 Dwgs: N1-Ell-C002 51 System Fland: Fresh Water Tube Flow = 25 34 Tube Tensperatures = 100.00'F 327.80*F Heat Load -
350.000.00 BTU /hr IDP202 2 HX Type. Fixed Heat Load HX Status: Oniin Flow Psi Mfr: Graham Mfg. Co.
Model 992C430BX Dwgs: h*l-Ell-C002 6 SystemFluid. Fresh Watet Tube Flow a 9 90 Tube Temperatures - 100.00'F - 102.04'F l
Heat Imad -
10,000.00 BTL't
~~m
_,, _ ee _ m r,com 6<3/9s 09.55 PPOTO FLO d.01 by Proto Power Corporation - Seritt #PFL-0000 P gr 21 or 24 Publi-Senice Electric and Gas G:WSEG11-365WEW IJHS'STACSL*HS2.PDB. Revision 2.00 Hope Creek Generstmg Station - STACS Heat Exchanger Data Report Com erwece: Picnurs=in$ Sum Qal.0E-2 Fncton=1.0E 6 FCV-l.0E-4 PCv=1.00-3 Tempersa.rea5.0E-)
LOP!SSE B Loop 2 EDGs X Tied.No SFP - EDG Rm Cirs Throttled. Red Rm Cirs Iso -
' 1DVE412 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mfr: Trane Co.
Model. MDE1291600 Dwgs: PM731Q System Fluid: Fresh Water i
Tube Flow - 231.72 Tube Temperatures = 100.00"F - 109.56*F Hast Load =.
1.100,000.00 BTU /hr IDVH113 HX Type: Fixed Heat Lead HX Status: On / Not in Flow Path Mfr: Amer. Air Fltr.
Model: H36MPACYA Dwgs: PM611A-0004 7 Systern Fluid:
Heat Load =
502,781.00 BTU'br IDVH210 HX Type-Fixed Heat Load IIX Status: On / in Flow Path l
Mft: Amer. Air Fitr.
Modci MDE1570300 Dwgs: PM71IQ System Fluid: Fresh Water Tube Flow = 146.38 Tube Temperatures = 100 00*F.105.50*F Heat Load -
400,000 00 BIL*/br IDVH211 HX Type. Fixed Heat load MX Status: Off Mir: Amer. Air Fitt.
Model: MDE1573500 Dwgs: PM711Q System Fluid: Fresh Water Heat Load a 0.00 BTU <hr 1DVH213 HX Type: Fixed Hest Load HX Status: off Mfr. Amer. Air Fltr.
Model: MDE2478600 Dwgs: PM786Q System Fluid: Fresh Water Heat Load =
0 00BTC/hr l
1
J U ti 03'33.Js25 FR c :E O T 's -? C W E F CORS 200 445 EI92 T0 16050291215 F.26-20 6/3/98 09 55 PROTO-FLO 4.01 by Proto Power Corporation - Scrial #PFL-0000 Pro.22 or 24 Publie :",crvice Electric and Oss - G APSECil1 385'iNEW UHS'STACSL'HS2.PDB - Revision 2.00 Hope Creek Generanns Station - STACS Heat Exchanger Data Report l
Cor.vergen;c: ?rcisrc=1.CE 3 Sum @l CE J Frtctica=1.0E4 FCV=102 4 PCVel.0E-) Temps sa.sc=5.oE-3 l
LOP /SSE B loop - 2 EDGs X Tied - No SFP - EDG Rm Clrs Tbmttled Red Rm Cirs Iso 1
1 i
lEVE412 HX Type: Fixed Heat Load HX Status: On/ in Flow Path 1
Mfin Tranc Co.
Mc, del: MDE1291600 Dwgs: PM731Q l
System Fluid. Fresh Wate Ibbe Flow - 235.16 "Iube Toprures = 100.00*F - 109 42*F Heat Load -
1,100,000.00 BTU /hr iEVHI13 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mh: Amer. A'r Fltr.
Model: H36MPACYA Dsgs: PM611 A-0004-7 System Flaid.
Heat lead s 502,781.00 BIUthr 1EVH210 HX Type: Fixed Heat Load HX Status: Ou / Not in Flow Path M&: Amer. Air Fitr.
Model MDE1570300 Dwgs: PM711Q System Fhad:
Heat Load =
210,000.00 BTU /hr 1EVH211 HX Type: Fixed Heat Load HX Status: otr Mft: Amer. Air fitr.
Model: MDE1573500 Dwgs: PM711Q System Fluid:
Heat Load -
0.00 BTU /hr IEVH213 HX Type Fixed Heat Load HX Status: Ofr Mfr: Amer. Air Fiv.
Model: MDE2478600 Dwgs: PM786Q Sys:cm Fluid:
Heat load =
0.00 BTU /hr 1FVE412 HX Type: Fixed Heat Load HX Stasts: On / in Flow Path Mir:Trane Co.
Model: MDE1291600 Dwas: PM731Q System Fluid: Fresh Water Tube Flow - 232.26 Tabc Temperatures - 100.00'F - 109.54'F l
Heat Load =
1,100,000.00 BTUlr i
l
n-
- n
.w._
~
.v,,
<~ --
~~e eses av mueemsm
<.a.m J
6/3/98 09:55 PROTO-FLO 4.01 by Proto P wcr Corporation - Setial(lPFL-0000 Pne 23 or 2:
Pubhc Service Electne and Gas O \\PSEOil1-385;NEW UHS \\STACSUHS2 PDB - Revision 2.00 l
Hope Creek Generating Station - STACS Heat Exchanger Data Report Cor. vergence Prnsunt-1.CE 3 Sum Q=l CE-2 fncuen-l.oF4 FCV=1 CE4 PCV=LCns 3 Ternpernase=5.0E4 LOP /SSE B Loop 2 EDGs X Tied - No SFP - EDG Rm C!rs lbott'ed Red Rm Cirs Iso IFVH113 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mir. Amer. AirFitr.
Mode 1: H36MPACYA Dvgs: PM611 A-0004-7 System Fluid.
Heat Load =
502,"81.00 BTWhr IFVH210 HX Type: Fixed Heat Load HX Status: On / S*otin Flow Path Mft: Amer. Air F1tr.
Model: MDE1570300 Dwgs: PM71IQ System Fluid-Heat Load-210,000.00 BTU,tr IFVH211 HX Type: Fixed Heat Load HX Status: off Mft: Amer. Au Fitr.
Model: MDE1573500 Dwgs: PM71IQ System Fluid:
Heat Load =
0.00 BTU /hr IFVH213 HX Type: Fixed Heat Load HX Status: off M&: Amer. Air Fitr.
Model: MDE2478600 Dwas: PM786Q Systern Fhaii Fresh Water Heat Lead =
0.00 BTU /hr IGVE412 HX Type: Fhed Heat Load HX Status: On /in Flow Path Mfr: Trane Co.
Model: MDE1291600 Dwgs: PM731Q System Fluid Fresh Water Tube Flow = 233.05 Tube Tempemtures = 100.00*F 109.5l'F Heat Load =
1,100,000.00 BTUhr 1GVH210 HX Type: Fixed Heat Load HX Stams: On /Not in Flow Path l
Mft: Amer. Ais Fitr.
Model. MDE1570300 Dwgs: PM711Q Sptem Fluid Heat Load =
200,000.00 BTU /hr I
F t
m _ ____________. _ _ _ _
,--~_._r
,,c, ses,,
_ee.-m
<. a s. ae v3 98 09:55 PROTO-FLO 4.01 by ProtE-Power Corporation - Serial CPFL-0000 Pase 24 er 34 Public Service Electric and Gas - G;\\PSEGsl1 385sNEW l'HS'STACSUHS2.PDB - Revtsion 2.00 Hope Creek Generatuig Station STACS Heat Exchanger Data Repon Cc,r,vergerce Pnmansa1.0F 5 KurnQ=;@:Fnct:en=10E4 TCV-1 DE-d PCV=LCE4 TempeveamscE4 LOP /SSE - B Loop. 2 EDGs X-Tied - W S5P - F.DO Rin Clrs Brottled-Red Rm Clts Iso I
1GVH211 HX Type: Thed HeatLoad HX Status: On / Not in Flow Path Mft: Amer. au F1tr.
Model: MDEI573500 Dwgs: PM711Q System F1md Heat Land =
135,000 00 BTUt iHVF412 HX Type: Fixed Heas Lnad HX Status: On / in Flow Path Mfh Tranc Co.
Model: MDE1291600 Dwgs: PM731Q System F1md. Fresh Water Tube Flow = 231.71 Tube Temperatures - 100.00"F - 109.56*F l
Heat Load =
1,100,000.00 BTUk IIW H210 HX Type: Fhed Heat Load HX Status: On / Not in Flow Path Mfh Amer. Air Fitt.
Modeh MDE1570300 Dwgs: PM71IQ System Flut Heat Lcad -
200.000.00 BTU /lu 1HVH211 IDC Type: Fixed Hea: Load HX Santus: Off Mfr: Amer, Air Fltr.
Model: MDE1573500 Dwgs: PM711Q System Fimd:
Heat Load =
0.00 BW/hr i
i I
l l-L.
l.
1 l
i l
>+ TOTAL :A3E.030
==
__w
,.m,a PROTo-POWER CORPORADON h
15 THAMES STREET PHONE: (860) 446-9725 GROTON, CT 06340 FAX: (860) 448-4860 FAX COVER SHEET FILE No.: 11-78f DATE' //#/W I
TOTAL PAGES (INCLUDING COVER SHEET):
2.7 4
To:
AA o.Mu
- FROM.
A h 4 t*~
i DEPT.
FAX No.:
u,,) ng - e ur fax No.: _(860)448-4860 REFERENCE' MESSAGE: A* b, decs se n.
r s salts the-nord opseeZim w,'Yk %,
lee p s. -r ks. r~uu:ra. at udJ E n ssv a ves is GN.1 1 Tks. s e.s-J SAct Ip s a mm Osl e
- 91. 5 of.
W 1
To report transmittal problems or for confirmation, please call (860) 448-9725.
m,v, v m e-see eee e m vu mssu s8285 P.@2 2@
0 4/9s 12:22 PROTO-FLO 4 01 by Proto-Power Corporation - Serial #PFL-0000 rase 2 d 3 Public Service Electric and Gas - G9SEO\\1 I-365WEW UHS'STACSUHS2 PDB - R Hope Crock Generating Station - STACS Flow Summmy Report Convergence: Premura=1 GE.$ Swn Qal.0E-7 Fricton=10E4 FCV=LE4 PCv=1.0E-3 Tetrpermarc=5.0E 3 Nonnal Operation. Two Loops Flow Summary Title Diameter Flow Minimum Flow NPSHA NPSH (in)
(gpm)
(gpm)
(ft)
Ratio IAEll2 out 6.065 546.81 1BE)12 out 6.065 502.93
- 1CE112 out 6.065 502.93 1 del 12 out 6.065 535.51 1 AVH113 out 4.026 204.61 IBVH113 out 4.026 204.55 IEVH113 out 4.026 204.75 1DVH113 out 4.026 198.29 1AVH116 out 4.026 214.95 1CIElIs out 3.068 154.39 ID1E118 out 3.068 144.58 I A! Ell 8 out 3.068 137.90 1BE126 out 7.981 1,230.18 1 AE126 out 7 961 1,224.14 1DKilI out 13.250 3,500.31 1 AK111 out 13.250 3,500.30 IDK11.1 out 13.250 3,500.22 10C150 out 3.068 14.69 10K107 out 1.939 162.68 ICE 130 out 0.957 18.00 1 AE130 out 0.957 16.70
!! Reverse Flow Through Check Valve
&& Pump Flowis Past End of Curyc
_______________u
o-
~~e eems vu umwaawiana v. 42' M 6ty9813:33 PROTO-FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 rise 3 or 3 Public Semcc Electric and Gas G:PSEGil1485\\NEW UHSiSTACSUHS2.PDB -Revis Hope Creek Generateg Station - STACS Flow Summary Report Convergence Presspe=LOF-5 SumQ 1.CD2 Fnctier.-l.0E-6 FCV=1 OE 4 PCV=1.0E-3 Ternpersture=5.0E 3 Normal Operation - Two Loops Flow Summary Title Diameter Flow Minimum Flow NPSHA NPSH (tn)
(gym)
(gpm)
(ft)
Ratio
& Dr.4 JU UUI U.yJ /
4 0.VU 1 AT216/lBT216 out 1.939 S1.14 IBK403 out 6.065 408 01 RE4859B2 out 0.957 9.59 l
i l
It Revene FlowThrough Check Valve
&& Pump Flow is Past End of Curve
" Flow Below Minimum
$$ NPSH Available Below NPS!4 Required
~~w nn u,
o mene s m e. ae as 6/49812:22 PROTO FLO 4.01 by Pr:to-Power Corporation - Serial CPFL-0000 P:se 1 or 23 Public Service E!ectric and Gas - OnPSEG\\11-385WEW UHS \\STACSUHS2.PDB - Re Hope Creek Generating Station. STACS Heat Exchanger Data Report
(.cnverpexe: Preaure-l.0E.3 Sum Q=LUE-2 Fnctwn=t.0Edi FCV=1.054 PCV-1.043 Tarpretate-S 0E.3 Normal Operation -Two Loops 90E129 HX Type: Fixed Heat Load HX Status: On / Not m Flow Path M&: Dasco,3ne.
Model: E3-24/18096 Dwgs: PM0$0-0039 3 System Fluid:
Heat Load '
$74,700.00 BTU /hr 00K107 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path M&: American Std.
Model: 06060 Dwss: PM0504022-5 System Fluid.
t Hest Load =
392,415.00 BTU /hr 10C150 HX Type: Fixed Heat Load HX Status: On / in Flow Path j
Mfir:
Model:
Dwgs:
System Fluid. Fresh Water Tube Flow = 14.42 Tube Temperatures = 95.00T - 164.72*F Heat Load,
500,000.00 BTU /hr IOE1110 HX Type: Fixed Heat Load MX Status: On / Notin Flow Path Mft: Basco, Inc.
Model: 8A24A08072 Dwgs; P1342287 Sysum Fluid:
Heat Load -
9,360,000.00 BTU /hr 10El14 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mh: Gen. Ele:t. Co.
ModeI: MDE0965400 Dwgs: PM0034-1-7 System Fluid: Fresh Water i
Tube Flow - 203.62 Tube Ternperatures = 95.00*F - 98.87'F Heat load -
392,000,00 BTU /hr 103129 HX Type: Fixed heat load HX Status: Off Mir: Basco, Inc.
Model: ES-24/18096 Dwgs: PM050-0039 3 System Fluid; Heat Load -
0.00 BIU/hr u_____-____---_----
~~a
== av m - e6eo*
P 02' G 6 4/98 12:22 PROTO-FLO 4.01 by Proto-Power Corporation - Serial L'PFL-0000 ttsi2 er 23
{
Public Service Electne and Gas. 0:TSEOill-38MNEW UMSiSTACSL'HS2.PDB - Revision 2.00 f
Hope Creek Generating Statacc. STACS Ffest Exchanger Data Report Cunversenec Prcuwl.0u.5 %rnQ=1 CE 2 Frkuon=LoE4 FCV=1.0G4 PCV-1.0E-3 Tempersare=5.0E-3 Normal Operation - Two Loops 10K107 HX Type: Fixed Heatlead HX Status: On /in Flow Prth j
Mfn American Std.
Model: 06060 Dwas: PM050-0022 5 Systern Fluid: Fresh Water Tube Flow = 161.66 Tube Ternperatures - 95.00T - 122.861 Heat Load =
2,240,000.00 BTU /hr 1A1El18 HX Type: Fixed Heat Load WA Sta:us: On /in Flow Path Mir:DeLaval/lMO Model: MDE1328000 Dwgs: PM012-0099 System Fluid: Fresh Water Tube Flow = 137.74 Tube Temperatures = 95.007 - 100.84Y Heat Load =
400,000.00 BTU /hr i
IA1E201 HX Type: Shell& Tube HX Status: On / in Flow Path Mft: Graham Mfg. Co.
Modet 92-6 504 CGN Dwgs: PM069Q-0058 Tube Fluid: Bracidsh Water-12 ppt Shell Fluid: Fresh Water Shell Flow - 10,304.47 Shell Teroperatures = 106.907 94.86"F Tube Flow = 12,620.00 Tube Temperatures = 90.47T - 100.339 I
Construction Type: TEMA O 1 Sh:lls,0 Shc!1 Passes. 4 Tube Passes
)
- Shell Min Area = 6.2530 ft*2, Design Shell Velocity = 3.900 ft/s, Shell Diameter - 92.000 Baffle Info: Spacir.g - 62 000 in. Thickness = 0.000 in, Area = 0.000 ft^2, K = 0.000 Tubes: Dm = 0 694 in. Dout = 0.750 in, Len8th = 42 00 ft, K = 9.50 s
Tube Pitch = 0 9375 in Tube Pitch 'lype = Triangular 5,700 of 5,700 Tubes Active UTubes = No EtTective Area = 46,295.00 f:^2 Area Factor = 0.9849 Fouling
- 0.0000 (maide) 0.0012 (outside)
Hoff = 0.4888 LMTD = 5 4025 LMTD corrections FF = 0.7981 Fb = 1.0000 Heat Load a 61.546,146.41 BTUtr UOverall-308.31 BTU /hr/ft^2/T l
L i
L____________
- - ~._
~~e
-se se m w.eo
=e 6/4/98 12:22 PROTO-FLO 4.01 by Proto-Power Corporation = Serh1 CPFL-0000 Pase 3 of 23 Public Service E!cetric and Gas GnPSEG\\l1335NEW L'HESTACSLES2.PDB - Revision Hope Creek Generstmg Station-STACS Heat Exchanger Data Report Ccr.vergen6. Preswre=14E 3 km Q-1 CZ 2 Fricoana 11E-6 FCY=1 CE-4 PCVal.3E.3 Ternpratef 05 3 Normal Operation Two Loops l A2E118 HX Type: Fned Heat Load HX Status: On / Not in Flow Path Mfr. DeLaval'IMO Model MDE1328000 Dwgs: PM012 0099 Systern fluid:
Heat Load =
502,781.00 BTU /hr 1A2E20I HX Type: Sliell& Tube HX Status: On /in Flow Path Mfr; Graham Mrg. Co.
Model: 92-6-504 CGN Dwgs: PM069Q-0058 Tube Fluid: Brackish Water - 12 ppt ShellFluid: Fresh Water Shell Flow = 10.810.80 Shell Temperatures - 106.90T - 95.15T Tube Flow = 12.562.00 Tube Temperatures - 90.47T - 100.62*F ConstrucsonType TEMA-G 1 Shells, O Shell Passes,4 Tube Passes Shell Mm Area = 6 2530 ft*2, Design Shell Velocity - 3 900 fds, Shell Diameter = 92.000 Bame info: Spacmg = 62.000 in. Thickness = 0.000 in Area = 0.000 ft^2, K = 0.000 Tubes: Dm - 0 694 i:t. Dout - 0.750 in, Length = 42.00 ft. K = 9.50 Tube Pitch = 0.9375 in Tube Pitch Type - Triangular 5,700 of 5,700 Tubes Aenve Urubes - No Effective Area = 46,295.00 ft^2 Area Factor = 0.9849 Fouling =. 0.0000 0nside) 0.00!2 (outside)
Hoff = 0.4888 l
LMTD = 5.4412 LMTD Conect2ons FF = 0.8031 Fb=1.0000 Heat Load -
63.008,246.26 BTL'/hr Loverall = 311.48 BTU /hr/ft^2/T 1 AE1109 HX Type: Futed Heat Load HX Sta*us: off Mfr. Basco Inc.
Model: BA43A08048 Dwgr PI-342287 System Fluid.
Heat Load =
0.00BTUbr I AEl11 HX Typc: Fixed Beat Load HX Status-On /in Flow Path l
Mfr: General Etxt.
Model: 264A4808 Dwgs: PM003-TR 15-5 System Fluid: Fresh Water l
Tube Flow = 1.721.29 Tube Temperatures = 95.007 - 105.93*F l
Heat load =
9.360,000.00 BTU /hr i
i
)
j
~. -
n-
- ~, e e n u+
o mum e =
w. a t 2s 6 mss 12:22 PROTO FLO 4.01 by Proto-Power Corporation = Serial f PFL-0000 P:sc 4 or 23 Public Service E!ectric and Gas - G.'.PSEG\\11 385WEW UHS'SI ACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Curve gence Mnu cal 05 5 Sum Q-1.CC-2 Ametien=1.0E4 FCV-1 OE 4 /CV=1.oE-3 Temperature =5 DE-3 Normal Operation. Two Loops 1AEl12 HX Type: Fixed Heat Load HX Status: On /in Flow Pai Mfr: General Elect.
Model: 114D6270 Dwas: PM003-G 17 System Flaid: Fresh water Tube Flow = 544 41 Tube Temperatures = 95.00*F - Il5.26'F Heat Load -
5,487,500.00 BTU /hr 1 AEl15 HX Type: Fixed Heat Load WX Status: On /in Flow Path Mfh H.K. Porter Co.
Modeh T-140963X45 Dwas: PE005-0012 9 System Flaid: Fresh Water Tbbe Flow - 66.05 Tube Temperatures - 95.007 - 110.67'F Heat Load -
$15,000.00 BTU /hr 1 AEll6 HX Type Fixed Heat Lund HX Status: On /in Flow Path M&: General Elect.
Model: 155B5243P001 Dwgs: PM003-T6-1-2 System Fluid: Fresh Water i
Tube Flow = 10.00 Tabe Temperatures - 95.00'F - 103.64'F
{
Heat Imd -
43,000.00 BTU /hr i
1AEll7 HX Type: Fixed Heat Load HX Status: On /in Flow Path I
Mfr: General Elect.
Model: MDE0924300 Dwgs: PM003-0-1-7 System Fluid: Fresh Water Tube Flow = 1.157.54 Tube Temperatures - 95.00'F - 108.98'F Heat Load -
8,050,000.00 BTUSar l
J 1AE126 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mft: American Std.
Model: 5-046 17-168 3 Dwgs: N1.B31-St-120 System Fluid: Fresh Water Tube Flow - 1,221.83 Tabe Temperatu es - 95.00*F - 104.26'F i
Heat Load =
5,630,000.00 DTU/hr 1
m._
<~e.--w-ww-s w ees scwe vu eeS N CE
^ 82'Ea 6/4/981302 PROTO FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Pcge 5 of 33 Public Semce Electric and Gas - 0;PSEGill 385\\NEW UHSiSTACsCHS2.PDB - Revision 2.00 Hope Creek Generscng Station - STACS Heat Exchanger Data Report Cur.vwgence Pr:ssu:v=1.0E-mm Q=1.0E 2 Friction =1.0F-6 FCVul CE4 PCv=1.CE-) Temperature.4 OE-3 No: mal Operation -Two Loaps l
i 1AE130 HX Type: Fixed Heat Load MX Status: On /in Nw Path Mir:Ametek/Whi: lock Model: 4-W18HT-4-A-CB Dwgs: PM007-0031 3 1
4 Systens Fluid: Fresh Water Tube mw = 16 68 Tube Temperatures = 93.00*F 100.06*F Heat Load-42,000.00B1U/hr IAE202 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mh: Alfa.LasalInc.
Modeh A.20-BXS Dwas: PM071Q-0010 System hid. Fresh Water Tube Nw = 1,310.80 Tube Temperatures = 91.19'F - 103.53*F Hest Load =
8,050,000.00 BTU /hr 1AE205 HX Type: Fixed Heat Load EX Status: On / Not in Flow Path Mfr Delta Southern Modeh 21A9227AN Dwas: NO-Ell-B001-5 System Wid:
Heat Load =
400,000 00 RTU/hr IAE214 HX Type: Fixed Heat Load HX Status: On / Notin Nw Path Mfr: CVIInc.
Meh C735 9934 Dwgs: PM048Q 00714 System Fluid; i
Heat Load =
5,412,000.00 BTU /br i
1 AE218 HX Type: Fixed Heat Load HX Status: Off Mft: CVI!nc.
Modeh C735-9934 Dwgs: PM048Q-00714 System Fluid:
Heat Load -
0 00 BTU /hr I
1AE218 liX ~Iype: Fixed Heatlead HX Status: Off Mfr:Cyline.
Model:
Dwas: PM048Q System mid.
Heat Load =
0.00 BTU /hr I
1 l
- _ cee n e cem 6/4/98 12:22 PROTO FLO 4.01 by Proto-Pewer Corporation - Scrial CPFL-0000 pcse 6 or 23 Public Service Electric and Gas. OrPSEGil1-385iNEW UHS'.STACSUllS2 PDB - Revision l
Ilope Creek Generating Station STACS Heat Exchanger Data Repon convergence Picuore=14E.5 Surn Q=I.oE.2 rneton=1.oE4 FCVsI oE4 KY=1.0F-3 Tecueronsrc-5.cn.3 Normal Operation -Two Loops IAE328 hX Type: Fixed Heat Load HX Status: On/ Not in Flow Path Mfr: Parker Haceu Model. HDTC-SS4-2 Dwgs:
System Flusi j
Heat Load =
1,353,000.00 BTU /hr 1AE404 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path Mfr: Amencan Std.
Model: 17072 CPT Dwgs: PM018Q System Fluid:
Heat Load =
100,000.00 BTU /hr IAE405 HX Type; Fixed Heat Load liX Status: On / Not in Flow Path Mfr:American Std Model: 19064 CPT Dwgs: PM018Q System Fhtid.
Heat Load -
502,781.00 BTU /hr t
IAE408 HX Type: Faxed Heat load HX Stams: Off Mft: American Std.
Model; 19198 Dwgs: PM01SQ System Fluid:
Heat Load =
0.00 BTU /br 1AK111 HX Type: Fixed HeatLoad HX Stan:s: On /in Flow Path Mft; Carner Corp.
Vodel: 19FA553B5005932 Dwgs: PMti23-0002 9 System Fluid: Fresh Water TV,be Flow = 3,492.21 Tube Temperamtes = 95.00'F - 106.22'F Heat Load =
19,500,000.00 BTU /hr 1AK202 HX Type: Fixed Heat Load HX Stams: On / Not in Flow Path Mfr: CVIinc.
Model: C735-9909 Dwgs: PM04SQ-0044-2 System Fluid.
Heat Load =
50,000.00 BTU /hr i
- .m gr.f " OJ 12 W3 FR PRO *C-PCAER CCRP 203 446 9292 TO 15033391215-P,10 26 0 4,98 12.22 PROTO>FLO 4.01 by Pr
- to-Powcr Corporation - Serial #PFL-0000
- pa,e 7 of 23 Public Ser vic e Elcetrie and Oss - OnPSECill.385NEW UHS'STAC$tJHS2 PDB - Reviamn 2 00 Hope Cicek Generating Stanoc STACS Heat Exchanger Data Report
('oevupece Presswl DE-S hm Q 1 w-2 Fnctel.0E4 FCV=l.0F4 PCV-l.0E-3 lenperstwo-5.061 Normal Operahon - Two Loops 1AK400 HX Iype: Fixed Heat Load HX S*stus: Ou / Not in Flow Path Mft: Cartier Corp.
Model: 19FA455B122022 Dwgs: PM723Q System Fluid:
Heat Lond m 7,530,000 00 B1UAr
!AK403 HX Type: Fixed Heat Lead HX Statw On / Not in Flow Path Mfr. Cames Corp.
Model: 19FA441B1142020 Dwgs: PM723Q System Fluid; llent Load 's 2.520,000 00 BTtMr 1APl?6 UX Type; Flaed Heat Load HX Status: On / Not in Flow Path Mft: Carrier Corp.
Model: 19FA999100718 Dwas: PM623118 Sysum Fluid; Heat load =
100,000 00 BTU 4r i AP202-1 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: Graham Mfg. Co.
Model. SX4C-12 Dwgs: N1.El1-C002-51 System Fluid:
Heat Load -
90,000.00 BTU,b 1 AP202 2 HX Type: Fixed Heat Load HX Status: On / Not m Flow Path Mfr: Oraham Mfg Co.
Model: 992C430HX Dwgs NI Ell-C002 6 System Fluid-Heat Load -
10,000.00Blub IAVE412 HX Type: Fixed Heat Lead HX Statn On / Not in Flow Path Mft: Trane Co.
Model: MDE1291600 Dwgs: PM731Q Syitem Fluid Heat Load -
880.000.00 Pr'tr 1
_.- ~ - -.
~.
~~n esws us sw u m eaze v.: g se 6/4/98 12:22 PROTO-FLO 4.01 by Proto-Pewer Corporation - Seriel CPFL-0000 Page 3 of 23 Public Service Elecmc and Oss - G:'P5EGill-385\\NEW t.HS$TACSLHS2.PDB - Rev1aio\\
Hope Creek Generating Station - STACS Heat Exchanger Data Report Convergence:Prescursal.00 5 Surn Q=1 CE.2 fnenen=1.0E4 FCV-lhEJ PCV-l.0ll-3 Terryerarm-5 cP-3 Norn:a1 Operation-Two Loops 1
1 AVH113 HX Type: Fixed Heat Load HX Status: On /in Flow Path M6 Amer. Air F!tr.
Model: H36MPACYA Dwgs: FM611A-0030-4 System F12sd: Fresh Water Tube Flow - 204.41 '
Tube Temperatures - 93.00*f - 99.95'F i
He4t Load =
503.000.00 BTTJ/hr 1 AvH116 HX Type: Fixed Heat Load HX Status: On /in Flow Path i
Mft: Amer. Air Etr.
Model: H36MPACYA Dwgs: PM611 A-0033 4 Syste:n Fluid: Fresh Water Tubc Flow - 214.75 Tube Tempetstures = 95.00'F - 99.71*F Heat Load =
503,000 00 BTUihr 4
1AVH208 HX Type: Fixed Heat Load HX Status: off Mfr: Amer. Air Fl*r.
Model: MDE1572400 Dwgs: PM71IQ System Fluid:
Heat Load -
0.00 BTU,hr IAVH209 HX Type: Fixed Heat Load HXStatus: On / Notin Flow Path Mfr: Amer. Air Flti.
Model: MDE1571400 Dwgs: PM71IQ System Fluid:
Heat Load =
107,139 00 DTU/hr 1 AVH210 1DC Type Fixed Heat Load HX Status: 0: / Not m Flow Path Mft: Amer. Air fitt.
Mode!: MDE1570300 Dwgs: PM711Q System Fluit Heat Load -
211,655.00 BTU /hr i AVH211 HX Type: Fixed Heat Lead HX Status: On / Notin How Path Mh: Amer. Air Etr.
Model: MDE1573500 Dwgs: PM71IQ System Flaid:
Heat Load =
13B,696.00BTtMr I
l i
._ _ _ _ _ - m. v m aw v-su "* sm $4 i omm P.12/26 t
6/4/98 12:22 PROTO-FLO 4.01 by Proto-Power Corporation - Serial CPFL.0000 p s.9 or 23 Public Service Elecific and Gas. G:'PSEGill-385\\NEW UHS \\STACSUHS2.PDB Res Hope Creek Generatirig Station. STACS Heat Exchanger Data Report Cumerpnce Preuse= t 05 5 Sum Q-1.0f' 2 Fncnon=1 OE4 FCV 1 OE 4 PCY=1 OP-3 Terrsmaanre=.505 3 Normal Operation.Two Loops I AVH213 HX Type: Fixed Heat Load HX Staras: On / Not in Flow Path
~ Mfr Amer. Air Flu Model: MDE2478600 Dwgs PM786Q System Fluid:
Heat Load =
1,092,643.00 B1Uitt 1BIE118 HX Type Fixed Heat Load HX Status: On / in Flow PaJi Mft: DeLaval'IMO Model: MDE1328000 Dwgs: PM012 0099 System Fluid: Fresh Water l
Tube Flow = 144.42 Tube Temperatures - 95.00*F.100.57'r Heat Lead -
400,000,00 BTU,hr 191E201 IDC Type: Shell& Tube HX Status: On/ m FlowPath Mfr: Graham Mfg. Co.
ModcI: 92-6-$04 CGN Dw5s: PM069Q-0058 Tube Fluid: Drackish Water.12 ppt ShellFluid: Presh Water Shell Flow 7,162.11 ShellTemperatures -94.80'F 91.18'F Tube Flow = 12.352.00 Tube Temperanites - 90.47'F 92.58'F Cocatrucuon Type: TEMA-O 1 Shells, O Shell Passes,4 Tilbe Passes
{
Shell Min Area - 6.2530 h^2. Design Shell Velocity - 3.900 A/s, Shell Diameter - 92.000 f
j Deffle lufo: Spacing 5 02.000 in, Thicknees = 0 000 in. Arca - 0.000 ft*2, K = 0.000 Tubes: Din = 0.694 in. Dout = 0.750 in, Length - 42.00 A K = 9.30 Tiibe Pitch = 0.9375 m Tube Pitch Type
- Triangular 5,700 of 5,700 Tubes Acuve UTubes = No Effecrise Area = 46,295.00 ha2 Area Factor = 0.9849 Fouhng = 0.0000 (inside) 0.0012 (outside)
HoII= 0.4888 LMTI) = 13231 LMTD Corrections FF - 0.7582 Fb - 10000 Heat Load =
12,896,523 00DTL'/hr UOverall = 277.68 BTI.Wr/A^2/'F IB2E118 HX Type: Fixod Heat Load HX Status: On / Not irl Flow Path Mir: DeLaval'IMO Model: MDE1328000 Dwgs: Pmol 2-0099 Sy temFluid:
i
' Heat Load =
400,000 00BTUrt 1
i-l i
~~w en v e mmma
- 7. WN G4/9812:22 PROTO-FLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 Paan to of 23 Public Service Electric and Gas - G:\\PSEG\\11 355'.NEW UHS;.STACSCHS2.PDB. Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report
)
i Converseix Pressuro=1 OE 5 Sum Q-1.0E-2 Friction-1 OE4 FCN=1.0E 4 PCV-1.53 Ternpermane=5.0E4 NormalOperation -Two Loops IB2E201-HX Type: Shellds Tube HX Status: On /in Flow Path Mfr Graham Mfg. Co.
Model: 92-6-504 CGN -
Dwgs: PM069Q-0058 l
Tube Fluid Brackish Water.12 ppe Shell Fluid: Fresh Water ShellFlow = 7,413.13 Shell Tenpratures = 94.80*F - 91.21'F Tube Flow = 12,458.00 Tube Temperatures = 90.47'F - 92.62'F Construction Type: TEMA-G 1 Shella, O Shell Passes,4 Tube Passes Shell Min Area - 6.2530 R^2, Design Shell Velocity = 3.900 fvs, Shell Daarneter = 92.000 BafTJe info: Spacmg = 62.000 in, Thickness 0.000 in, Area = 0.000 A'2, K = 0.000 Tubes: Din = 0.694 in. Doint - 0.750 in. Length = 42.00 !!, K = 9.50 Tube Pitch = 0.9375 in Tube Pitch Type = Triangular 5,700 of 5,700 Tubes Active UTubes -No Effective Ares = 46,295.00 ft^2 Area Factor = 0.9849 Foulag = 0.0000 (inside) 0.0012 (outside)
Ho# = 0.4888 LMTV = 1.3346 LMTD Correcisons FF = 0.7634 Fb = 1.0000 HeatLoad='
13,228,817.9s BTU /hr UOverall = 280.48 B1U/hr/fta2/*F 1 bel 109 HX Type: Fined Heat I.osd HX Status: On / Not in Flow Path Mfh Danco inc.
Model: 8A44A08048 Dwgs. Pl.342287 System Fluid-Heat Load =
481,650.00B1Uhr 1 bel 11 HX Type: Fixed Heat Load HX Status: On / Not m Flow Path Mft: General Elect.
Model: 264A4808 Dwgs: PM003-TR-18-5 System Fluid:
Heat Load =
9.360,000.00 BTU /hr
\\
iBEl12 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mfn General Elect.
Model: 114D8270 Dwas: PM003-G-1-7 l
System Fluid: Fresh Water
- Tube Flow = 500.51 Tube Tenprstures = 95.001 - 117.04'F Heat Load =
5,487,500.00 BTU /hr w_____-___---_----------
- - - =
m..
~~m e m e,e ve meeemew r,3 e a 6/4/98 12:22 PROTO-FLO 4.01 by Proto-P wcr Corpor tion - Serial #PFL-0000 l
1 rap it d u Public Service Electric and Ca4 O \\PSEOil1385WEW LHSsSTACSUHS2 PDB Revision 2.00 Hope Creek Generating Station STACS Heat Exchanger Data Report
(:rmvergc9se. Preewre=1.0E-S Sum Qal OE 2 Tmton=1,oE4 PCV-l.004 PCV=10F,-J 7ensnrsture=5SE 3 Normal Operation -Two Loops IBE115 HX Type: Fixed Heat Load HX Status: OniNot in Flow Path Mft: H.K. Porter Co.
Model: T 140963X45 Dwas: PE005 0012-9 System Fluid:
Heat Load -
$15,000.00 BTU /hr IBE116 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfb General Elect.
Model: 15588243P001 Dwas: PM003 TG.1-2 l
System Fluid:
Heat Load a 42,500.00 BTU /hr IBEl17 HX Type: Fixed HeatLoad HX Status: On / in Flow Path Mfh General Elect.
Model: MDE0924300 Dwgs: PM003-O-1-7 System Flald. Fresh Water Tube Flow ' t,157.63 Tube Temperatures - 95.00'F - 108.98T Heat load -
8,050,000.00 BTU /hr IBE126 HX 'lype; Fixed Heat Load HX Status: On / in Flow Path Mfr: American Std.
Model: 5 0046-17 168 3 Dwas: N1-B31 SI 120 System Flmd: Fresh Water Tube Flow - 1,227.87 Tube Toruperatures - 95.00*F - 104.22*F Heat Load -
5,630,000.00 BTV/hr IBE130
- HX Type: Fixed Heat Load HX Stams: Ou / in Flow Path Mft:Ametek/Whitlock Model: 4 W18HT-4-A-CB Dwgs: PM007-0031-3 Syr.emFluid. Freshwater Tube Flow = 17.9S Tube Temperatures - 95.00*F 99.69'F Heat Load -
42,000.00 BTU /hr I
l
6/4/98 12 23 PROTO-FLO 4.01 by Proto-Power Corporation - Scrial #PFL-0000 Pese la e 23 Public Service Electric and Gas G:\\PSEGil1-385WEW UHSiSTACSUHS2 PDB -Revision 2.00 Hope Creek Ocaerating Stanon - STACS Heat Exchanger Data Repon Convugence. Prenorc=1.0E-5 3en Qal.3E-2 Pricdon=1.00 6 FCv=1.0F4 PCV=1 SE4 Tecpermarc=5.0E4 Normal Operation - Two Loops IBE202 HX hpe: Fixed Heat Load HX Status: On /in Flow Path Mfr: Alfa Laval In:.
Model: A-20 BXS Dwgs: PM071Q-0010 System Flutd: Fresh Water Tube &w = 1,347,45 Tube Temperatures - 91.19'F - 103.197 Heat Load -
8,050,000.00 BTU /hr 1BE205 11X Type: Fixed 11eatload HX Status: Off Mft; Delta Southem Model: 21A9227AN Dwgs: No.El1-B0015 System Fluid: Fresh Water Heat Load.
0.00 BTU /hr IBE214 HX Type: Fixed Heat Load HX Status: Or./ Not in Flow Path Mft: CVIinc.
Model: C735 9934 Dwas: PM046Q-0071-4 System Fluid:
Heat Load =
9,565.00 BTU /hr 1BE218 HX Type: Fixed Heat Load HX Status: On/ Notin Flow Path Mfr: CVIinc.
Model: C735 9934 Dwgs: PM048Q-0071-4 System mid:
Heat Load -
10,750 00 BTU /hr 1
IBE275 HX Type: Fixed Heat Load HX Status! On / Not in Flow Path Mh: CVIInc.
Model:
Dwgs: PM048Q System Fluid:
Hemt Load -
6,000.00 BTL*/hr IBE328 HX Type: Fixed Heat Load HX Status: On / Notin FlowPath Mfh Parker-Hanison Model: HDTC-SS-6 2 Dwgs:
System Fluid:
Heat Losd =
55,000.00BTC/hr
.m_
<- < w,v re e ww ma =ee esas uv 2 %Sm 2 3 9 P 16' M 6/4/95 12:22 PROTO-FLO 4.01 by Proto Pzwer Corporation - Serial #PFL-0000 rage is or 23 Public Service Electne and Oas G?PSEGIl 385'.NEW L'HS\\STACSCHS2.PDB - Revision 2.00 Hope Creele Generating Station STACS Heat Exchanger Data Report Cmwergence Ptessure=1.0li 5 Sum Q.1 ok.2 Fnct,cm=1 DE 6 FCV-1.0E4 PCv=1%) Temperatw5.CE-3 Normal Operation - Two Loopa 1BE404 HX Type: Fixed Heat Load MX S:stus: On / Not in Flow Path Mfr: American Std.
Model: 17072 CPT D w as: PM018Q System Fluid:
Heat Load =
1.353,000.00 BTU!br IBE405 HX Type Idixed Heat Load HX Status: On /Not m Flow Path Mfr: American Std.
Model: 19084 CPT Dwgs: PM018Q System mid:
Heat Load =
$,412,000.00 BTU /br IBE40g HX Type: Fhed Heat Load HX Status: On / Not m Flow Path Mfr:American Std.
Model: 19198 Dwgs: PM018Q System Fluid:
Heat Load =
3,118,000.00 BTU /hr IBK111 HX Type: Fixed Heat Load HX S:stus: On /in Flow Path Mft; Carrier Corp.
Model 19fA553B5005932 Dwgs: PM623 0002 9 SystemFluid: Fresh Water Tube Flow - 3,492.21 Tube Temperatures = 95.00'P - 106.22'F Heat Load -
19,500,000.00 BTU &r IBK202 HX Type: Fixed Heat Load HX Status: On / in Flow Path Mft: CV! Inc.
Model. C735 9909 Dwgs: PM048Q4044-2 System fluid: Fresh Water Tt.be Flow = 7.42 Tt:te Teraperatures = 91.19'F - 104.73'F licatLoad-50,000.00 BTU %r I
I i
l i
L_____________
~ _____
6/4/98 12-22 PROTO-FLO 4.01 by Proto-Power Corporation - Serir.1 #PFL-0000 e e u or 23 n
Pubhc Semce Electnc and Gas. G APSEOs11 385tNEW UHStSTACSLTIS2.PDB Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Converysmco Pressur.*l.0G4 Sum Q-l 0E-2 Fnchs-1.0f 4 FCV-1 CE 4 PCV-LOF!.4 Tempemuse=5 OE 3 Norrnal Operanon-Two Loups IBK400 HX Type: Fixed!!est Load HX Status: On / in Flow Path Mfr: Carnet Corp.
Model: 19FA455B122022 Dwgs: PM723Q System Fluid: Fresh Water Tube Flow = 1,585.14 Tube Temperatures n 91.19'F - 100.74'F Heat Load =
7,530.000.00 BTU /hr IBK403 HX T>pe: Fixed Heat Load tiX Status: On /in Flow Path Mfr CarrierCorp.
Model: 19FA441B1142020 Dwas: PM723Q System Fluid: Fresh Water Tube Flow w 407.01 Tube Temperatures - 91.19"F - 103.63'F Heat Load -
2,520,000.00 BTU /hr 1BP!76 HX Type: Fixed Heat Load HX Status: On / Not m Flow Path Mft: Carner Corp.
Model: 19FA999-100718 Dwgs: PM623118 System Fluid:
Heat Load =
100,000.00 BTU /hr IBP202 1 liX Type: Fixed Heat Load HX Status: off Mfr: Graham Mfg. Co.
Model. $X4C-12 Dwgs: N1-ElI.C002-51 System Fluid-Heat Load =
0.00 BTU.'hr 1BP202 2 HX Type: Fised Heat Load HX Status-orr Mft: Orsham Mfg. Co.
Model: 992C430BX Dwgs: N1-El1 C002-6 System Fhud:
Heat Load -
0.00 B11*/hr IBVE412 IIX Type: Fixed Heat load HX Status: OE Mfr: Trane Co.
Model: MDE1291600 Dwas: PM731Q System Fluid.
Heat Lead =
0 00BTLlhr I
i
m~
em eo.am
<~v,e re-s-
. vxr sea ces ecss vv noesaasizas P.le S@
6!4/98 12:22 PROTO-FLO 4.01 by Proto-Pcwer Corporation - Serial CPFL-0000 pass is or 23 Pubhc Service Elcetrie and Gas - Cr.PSEG\\ll-385;NEW UHS'5fACSUIS2.PDB. Revision 2 00 Hope Creek Generstmg Station STACS Heat Exchanger Data Report Comergence Press.se=1.tsF.-3 Swn Q-1.0k. 2 Fncien*l.0ti-6 FCWI.054 PCV=l.05) 'fernp;ta 2e*S OF.-J Norma 10peration-Two Loops IBVHn3 HX Type: Fixed Heat Load HX Status: On /in FlowPath Mft: Amer. Atr Fitr.
Model: H36MPACYA Dwgs: PM611 A-0030-4 System Fluid: Fresh Water Tube Flow - 204.35
'hbe Temperatures - 95.00*F - 99.95'F Heat Load -
503,000.00BTUh 1BVHI16 HX Type: Fixed Heat Load HX Status On / Notin FlowPath Mft: Amer. Air Fitt.
Model: H36MPACYA Dwss: PM611A-0033-4 System Fluid:
Heat Load =
530,000.00 BTU /hr IBVH208 HX Type: Fixed Heat Load HX Status: Orr Mfr: Amer. Air Fitr.
Model: MDE1572400 Dwgs: PM711Q System Fluid-Heat Load -
0.00 BTUh 1BVH209 HX Type: Fixed Heat Load HX Status: On/ Notin Flow Path Mfr: Amer. Air Fitt.
Model: MDEtS71400 Dwas: PM711Q System Fluid:
Heat Losd -
107,139.00 BTU /hr IBVH210 HX Type: Fixed Heat Load HX Status: off l
Mft: Amer. AirFitr.
Model: MDE1570300 Dwgs: PM71IQ System Fluid.
Heat Load =
0.00BTuhr l
ISVH211 HX We: Frxed Heat Imd HX Status: off Mir: A:ncr. AirFitr.
Model: MDE1573500 Dwgs: PM711Q System Fluid;
)
l Heat Load -
0.00 BTU /br
m.
Omu
~~a eee uv e eue e s a w P
I5' 6/4/98 12:23 PROTO-FLO 4.01 by Proto-Power Corporation - Serial #PFL-0000 Pese 16 or 23 Pubil:: Service Electric and Gas - 0:'.PSEG\\11 3851NEW UHSGTACSUHS2.PDB - Revision 2.00 Hope Creek Generating Station. STACS Heat Exchanger Data Report Convergence eciaure=1.cF.-S Sam Q-14C-2 fneter=10F 0 FCV-14"s PCY=l.05.1 Terrsera:Tc=$ DE-J Normal Opera: ion - Two Loops IBVH213 HX Type; Haed Heat Load HX Status: Off Mfr: Amer. Air Fit:.
Model: MDE2475600 Dwgs: PM786Q System Fluid:
Heat Load =
0.00 BTU /hr ICIE!18 HX Type: Fixed Heat Load HX Status: On /fa Flow Path Mft: DeLaval/IMO Model: MDE1328000 Dwgs: PM012 0099 System Fluid: Fresh Water Tube Flow = 154.23 Tube Temperatures = 95.00*F 100.21*F Heat Load -
400,000.00 BTU /br IC2El18 HX Type; Fixed Heat Load HX Status: On / Not in Flow Path M&:DeLaval/LMO Model: MDE1328000 Dwgs: PM012-0099 System Fluid:
Heat Load -
400,000.00 BTU /hr ICEl12 HX Type: Fixed Heat Load HX Status: On /in Flow Path Mth General Elect.
Model: 114DR270 Dw;s: PM003-G-1 7 System Fluid. Fresh Wate:
Tube Flow - 500.51 Tube Temperances - 95.00*F - 117.04'F Heat Load -
5,487,500.00 BTU,tr ICE 130 HX Typc: Fixed Heat Load 11X Status: On /in Flow Path Mft:Ametek/Wir.tlock Model: 4-W18HT-4-A-CB Dwgs: PM007 0031-3 Sprem Fluid; Fresh Water Tube Flow = 17.98 Tube Temperatures 95.00*F - 99 69'F Heat Load
- 42,000.00 B'IV,tr
- ~ ~
~~vv
~~~m n a ':%
6/4/98 12:22 PROTOoFLO 4.01 by Proto-Power Corporation - Serial CPFL-0000 case i7 or 23 Public Service Electri: and Gas - G.'PSEG\\11-385'NEW UHS'5TACSUH$2.PDB - Revision 2.00 Hope Creek Generstmg Station - STACS Heat Exchanger Data Report
(;cmcrgence. Pressure =1 CE 3 $n Q=1 CE4 Frictual.0[-6 FCY=1.0E-4 PCV-1 DE-31ernpers-n-5 0G-3 Normal Operation. Two Loops ICE 404 HX Type: Fixed Heat Load HX Status:- On / Not in Flow Path Mft:American Std.
Model: 17072 CFF Dwas: PM018Q System Fluid:
Heat Load -
1,353,000 00BIU/hr ICE 405 MX Type: Fned Heat Load HX Status: On /Notin Flow Path Mft: American Std.
Model: 19084 CPT Dwgs: PM018Q System Fluid:
Heat Load -
5,412,000 00 BTU /hr
!CE408 HX Type: Fued Heat Load HX Status: On / Not in flow Path 3
Mft:American Std.
Model. 19198 Dwgs: PM018Q System Fluid:
Heat Load -
3,118,000.00 BTU /hr i
ICK111 HX Type: Fned Heat Load HX Stams: On / Not in Flow Pa:h Mft. Camer Corp Model. 19FA553B5005932 Dwgs: PM623-0002 9 System Fluid.
Heat Load =
19,500,000.00 BTU /hr ICPl76 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mir: Carrier Corp.
Model: 19FA999-1007-15 Dwgs: PM623-118 System Fluid:
)
Heat Load -
100,000.00 BTU
ora meron 1. ora rev-1.or-1 Pcv=1.0e-3 Ternpsraare=5 Ch-J k
Normal Operation-Two Loops
!CP202-2 HX Type: Thed Heat Load HX Status: Os / Not m Flow Path Mft: Graham Mfg. Co.
Model: 992C430BX Dwp: N1-E11-C002 6 System fluid:
Heat Load 4 10,000.00 BTU,hr ICVE412 HX Type: Fixed Heat Load HX Statas: On / Notin Flow Path Mft: Trane Co.
Model MDE1291600 Dwgs: PM731Q System Fluid.
Heat Load -
880,000.00 BTU /hr ICVH113 HX Type: Fixed Heat Load HX Status: Oc / Not in Flow Path Mft: Amer. AtrFitr.
Model: H36MPACYA Dwss: PM611A-00304 Sys:cm Fluid:
Heat Load =
502,781.00 BTL*!hr ICVH210 HX Type: Fixed Heat Load HX S:atus: On /Notin Flow Path i
Mfr: Amer. Atr Flcr.
Model: MDE1570300 Dwgs: PM711Q System Fluid:
Heat Load -
200,957.00 BTUhr 1CVH211 HX Type: Fixed Heat T.oad HX Staans: On / Notin Flow Path j
I Mft: Amer. Air Fl:r.
Model MDE1573500 Dwgs: PM71IQ i
System Fluid:
Heat Load =
138,696.00B1U/hr ICVH213 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: Amer. Air Fitr.
Model: MDE2478600 Dwgs: PM786Q System Fluid.
Heat Lead -
1,092,643.00 DTU,tr
JUN 04'5B ;2i57 FR FROTO-FCWEF CCRP 103 446 13292 TC 16093091219 F.22 26 6/4/98 12:23 PROTO-FLO 4.01 by Proto Power Corporation - Seria] #PFL-0000 e.ge 19 or 23 Public Semce Electne and Gas - 0;\\PSEGill-383\\NEW UHSTSTACSUHS2.PDB Revision 2.00 Hope Creelc Generating Station - STACS Heat Exchanger Data Report Convergence: Presswc-1 DC-$ $sn Q=1.CE 2 Fncten=1.CE4 FCV=LUF-4 PCVal DE-3 Temperst.re=5.0F.3 Normal Operation - Two Loops IDE112 HX Type: Fixed Heat Load HX Sta:us: On / in Flow Path Mft: General E'ect.
Model: 114DB270 Dwgs: PM003-G-1-7 System Fluid. Fresh Water Tube Flow - 533.11 Tube Temperatures - 95.00'F - 115.69T Hear Load =
5,487,500.00 BTU /hr IDE404 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mh: American Std.
Model. 17072 CPT Dwgs: PM0!8Q System Fluid.
Heat Load -
1,353,000.00 BTU /hr IDE405 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path hifr Am:ncan Std.
Model: 19084 CPT Dwgs: PM01BQ System Fluid:
Heat Load-5.412.000.00 BTU /hr IDE408 HX Type: Fixed Heat Load HX Status: On /Notin Ficw Path Mfr: Amencan Std.
Model: 19198 Dwgs: PM018Q System Fluid:
Heat Load =
3.118,000.00 B'IUhr IDK111 HX Type: Faed Heat Load HX Status: On / m Flow Path Mfr: Carner Corp.
Modci: 19FA553B5005932 Dwgs: PM623-0002 9 System Fluid Fresh Water Tube Flow = 3,492.13 Tube Temperatures - 95.00T 106.22*F Heat Load -
19,500.000.00 D'It'/hr iDPl76 HX Type: Fixed Heat Load HX Status: On / Notin Flow Path Mfr Canier Corp.
Model: 19FA999-1007-18 Dwgs: PM623-118 System Fhid:
Heat Load -
100,000.00 BTU /h.-
I
~~e esee ~ oeeweewecie
- . w is
&4/98 12:22 PROTO-FLO 4.01 by Proto-Power Corporation - Seria! CPFL-0000 Pase ao or 23 Public Service Electric cad Gas G9SEGill-385%EW UHS \\STACSUHS2.PDB. Revision 2.00 Hope Creek Generating Stadon-STACS Heat Exchanger Data Report Canverpa:c. Pn:uurv-1.CE.5 San Q-1 OE-2 Frictiel.0E 6 FCV-1 CE-4 PCV=1 AE-3 Termperaturc=S.0E-3 NormalOperation TwoLoops
!DP202-1 HX Type: Fixed Heat Load HX Status: off Mh: Graham Mfg. Co.
Model: 8X4C-12 Dwgs: El-El1 C002 5i System Fluid:
Heat Load -
0.00 BTU!hr 1DP202 2 HX Type: Fhed Heat Load HX Stata: off Mfr: Grahaan Mfg. Co.
Model. 992C430BX Dwgs: N1.E11-C002-6 System Fluid:
Heat Lead -
0.00 BTU /hr IDVE412 HX Type: Fhed Heat Losd HX Status: og Mfr: Trane Co.
Model: MDE1291600 Dwgs: PM731Q System Fluid:
Heat Load -
0.00 BTU /hr IDVH113 11X Type: Fmt Meat Load HX Star.* On /in Nw Path Mfr: Amer. Air Fitt.
Model. H36MPACYA Dwgs: PM611A-0004 7 System Fluid Fresh Water Tube Flow = 198 09 Tube Tc:nperatures = 95.00'F - 100.10*F Heat Load -
503.000.00 BTU /hr IDV11210 HX Type: fhed Heat Load HX Status: off Mfr: Amer. Air Fjtr.
Model: MDE1570300 Dwgs: PM71IQ System Flmd:
Hear Load -
0.00 BTU /hr IDVH211 HX Type: Fixed Heat Load HX Status: og Mfr: Amer. Air Fltr.
ModcI: MDE1573500 Dwgs: PM711Q System Fluid:
Heat Load -
0.00 BTUthe
~..
~-m
_.__w g. e., c,
6/4/98 12:22 PROTO FLO 4.01 by Proto Power Corporation - S rial #PFL-0000 Pzgg 23 cf 23-Pubhc Smice Electric and Oas - OMSEOill.385'.NEW UHS'STACSLES2 PDB - Revision 2.00 Hope Creek Generating Station - STACS Heat Exchanger Data Report Convergence Presswe=1.0E.5 Surn Q=1 CF-2 Pncoces t.0E-6 FCV=1.CEJ PCV=l C E-) Ternparatur:=54E.3 Normal Operaton - Two Loops
!DVH213 HX Type: fixed Heat Load HX Status: Off Mft: Amer, Air F1tr.
Model MDE2478600 Dwgs: PV7860 System Fluid:
Heat Load -
0.00BTUN 1 EVE 412 HX Type: FixedHea Lead HX Status: On / Notin Flow Path Mft: Trane Co.
Model: MDE1291600 Dwgs: PM731Q Sys:ern Fluid:
Heat Load =
880,000.00BTUh IEVHil3 HX Type: Fixed Heat Load HXS:atus: On / m Flow Path Mfr: Amer, Air Fitr.
Model: H36MPACYA Dwgs: PM611A 0004-7 System Fluid: Fresh Water Tube Flow - 204.55 Tube Temperamret - 95.00'F - 99.94*F Heat Load -
503,000.00 BTUh IEvH210 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mft: Amer. AirFitr.
Model: MDE1570300 Dwgs: PM71IQ Syste:n Fluid:
Heat Load -
2tl,655.00BTUh iEVH211 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mir: Amer. Air F'tr.
Model: MDE1573300 Dwgs: PM711Q System Fluid.
Heat Load =
138,696.00BTUh IEVH213 HX Type: Fixed Heat Load HX Status: On / Not in Flow Path Mfr: Amer. Air Fitr.
Model. MDE2478600 Dwgs: PM786Q System Fluid:
Heat Load -
1,092,643.00 BTU /hr m__._______--_._.___m_
m._
~~a
==uv
==="
" # d8 j
6/4/98 12:22 PROTO-FLO 4.01 by Proto-P wer Corporation - Serial f:PFL-0000 rage 22 of 23 Public Semce Electri: and Gas - G?.PSEGill 383 WEW UHSisTACSUllS2.PDB - Revis Hope Creek Generating Station - STACS Heat Exchanger Data Report Convergence: !%aureal.0P. J Surn Qa: CE-2 Fncto1=1.0E-6 FCV40h-4 PCV-1.0E 3 Terrperat.n=5 0F
Model: MDE1291600 Dwgs: PM731Q I
System Fluid:
Heat Load =
0.00 BTUb IFVH113 HX Type: FixedHeat Load HX Status: On / Not in Flow Path Mh: Amer. Air Fitr.
Model: H36MPACYA Dwgs: PM611A-0004 7 Syr. era Fluid.
H::st Load --
502,781.00 BTU /hr IFVH210 HX Type: Fixed Heat Load HX Status: Off Mfn Amer. Airliltr.
Mode}. MDE1570300 Dwgs: PM71IQ System Fluid:
Hent Lead =
0.00 BTU /hr lFVH21i flX Type: Fixed Heat Load HX Stams: Off Mft: Amer. Atr F!tr.
Model: MDE1573500 Dwgs: PM711Q System Fluid-Heat Load -
0.00 BTU /hr IFVH213 HX Type: Fixed Heat Load HX Status: Off Mft: Amer. AirFitr.
Model MDE2478600 Dwgs: PM786Q System Fluid; Heat Load =
0.00 BTU /hr IOVE412 HX Type: Fixed Her.T.oad HX Status: On / Not in Flow Path Mfr: Trane Co.
Modcl: MDE1291600 Dwgs: PM731Q System Fluid:
Heat Load =
580,000.00 BTU /br l
_ ~._
-o eses
,s ammmm v. a ae 64/98 12:22 PROTO FLO 4.0I by Proto-Power Corporation - Scrini CPFL-0000 P2se 23 or 23 Public Ser+ ice E:ectri: and Gas - GAI'SEO\\11-385WEW IJHS'STACSCHS2.PDB Hope Creek Generating Station - STACS Heat Exchanger Data Report Cornergence: Presswrs=1 CF 3 Sum Q-1DE 2 Fnction=1.0D6 FCV=l.3E4 PCv=1.003 Temperature =5 0F.
Normal Operation. Two Loops 1OVM210 HX Type: Fixed Heat Load HX Status: Ort / Not in Flow Path Mfr. Amer. Air Fltr.
Model: MDIl570300 Dwgs: PM711Q System Fluid:
Heat Load -
200,957.00 BTU /hr lOVH211 HX Type: Fixed Heat Load HX Status; On / Not in Flow Path Mfn Amer, au Fitr.
Model: MDE1573500 Dwgs: PM711Q System Flaid.
Heat load =
138,696 00 BTU /hr 1HVE412 HX Type: fixed Heat Loud HX Status: OIT Mft: Trane Co.
Model: MDE1291600 Dwgs: PM731Q System Fluid:
Heat Lead -
0.00BTUhr lHVH210 IlX Type: Fixed Heat Load HX Status: Off Mir: Amer. AirFits.
Model MDE1570300 Dwgs: PM711Q System Fluid-Heat Load -
0.00BIU/hr llW H211 HX Type: Fixed heat Load EX Status: Off Mft: Amer. Air F'tr.
Model: MDE1573500 Dwgs: PM71IQ Syuem Fluid.
j
{
Heat Load =
0.00 B"IUAv 1
TOTAL PA3E.026 **
==
t l
l l
Attachment (4)
UllS Temperature Limit Evaluation Lineups (Microsoft Excel Spreadsheet) 1 i
I l
l l
l 1
i
n n more esaw UHS ?cmperrtare Lmd E<aivition VHS/SSWS/ SACS Limmng Confgyratons LOC /VUA a
a e
e a
e 2
s a c e
o a
a a
e a
s s
o o
1 2
1 2
s s
s s
a c
e o
a e
a a
e s
s a
s e
a s
s s
a t
t i
2 1
2 e
e a
a a
a a
s s
s w
w w
w e
e a
e s
s s
s a
s s
a c
c c
c a
a a
a a
s s
s s
e e
c
- *
- w w
s s
s s
a a
a e
s s
s s
e c
c c
a e
e o
o e
e e
e w *
- w s
s s
s t
e s
a s
e a
8 P
8 8
8 9
E E
8 P
E E
E E
e I
t W
W a
s e
0 m
6 t
M a
=
m s
s 0
0 m
m m
a M
M w
D D
0 0
e e
a e
s a
w e
a p
y v
e e
e e
e e
e 5
e o
e e
e G
o o
G e
9 5
e
%e f ewee 2N 2 222 2 N
326 0
" 277 0
" 235 0
' t332 0 48 2e 44 23l "s?_ e at
- 22 2 222 2 71
- C 22
'4262 0 00
- P80 0 "es3 0 4F 24 54 4al Ca 2_ e ps, i
cossewee 222 2 222 2 N
22 l Ge*0 0 8376 0 0999 0 8643 0 64 94 09 39 0'ste_e pm, a 22 2 222 2 fin C
E 22 l "tes 0 00 9347 0 9826 0 44 M 84 35 04s'e_e on, BSWS P#N 8 wee t
'22 2l 222 2l me l lRl l l l l lCl l l l l l l l l I l l l l l l l l l 22 l
'20S7 0l 0 0l "864 0l 92002 0] l 44 44l 88 72j a qu2 e go SSW9 as 8ewee 9U 2l 222 2l F2 a l j l l l l l lEl l l l l l l l l l l l l l l l l l l22l
'4262 0l 0 0l 19 780 0l * *883 0l l 47 24l 48 64l 04:2_e pe, FOG Fewee
2 9 N22 Se e C
C C
N 12
'7057 0 OG H 096 0
- 2002 0 65 82 98 72
'6 2 e pw 2121 222 2 te s C
C A
12 64a4 0 4410 0 Httt 0 197'2 0 67 64 88 5'
- sey e so utg 222 2 Se e C
C C
C E
92 920$7 0 00
" 898 0
'7002 0 75 02 88 72
- Ss2_e pt 2H +
222 2 te s C
C C
A 92 4444 0 8850 0 "6HO "7'70 7018l as s' t es?_e pa, sac s as, sewee 2'22 222 2 30 g E
22 H320 0 91277 0 H MS O 99332 0 99 92 84 21 0%2_e pm, U22 222 2 1c e C
E 22 94282 0 00 19740 0 HM3 0 SS 26 to 64 04 2 e pn, SACS um paeree 229 2 222 2 F2 n X
22 99326 0 91277 0 91235 0 91132 0
'8 92 44 23 09:2_e pa, 924 2 222 2 F2 n C
X 22
'8252 0 00 H 700 0
" 443 0 49 'e es 64 04 2_e sa, 2" 2 222 2 oua C
a 22 11326 0
" 277 0
" 23S 0
" 132 0
'S 79 to 23 09:2._e an, ttt 2 222 2 wa C
C R
22 94282 0 00 H700 0
843 0 79 SS 84 64 Des?_t pa, AOf sacs Leap 8mesei 202 2 222 3 72 n a
a 23
" 320 0 91277 0 99nSO 1*132 0 0 00 8799 0'a2_e pa, 102 2 222 3 F2 n C
a a
23 00 947t2 0 11783 0 Hee 8 0 0 00 88 03 OSt2_e sa, 22 222 3 T1a C
C a
a 23 00 00 92497 0
'298F 0 0 00 e4 52 t is2_e gn, l
202 2 222 3 72 n a
a a
23 4410 0 0370 0 4901 0 4083 0 0 00 84 42 0'ete e on, I
407 Sswa Leeli Peeren 22 2 222 3 F2 A a
a C
C 23 00 00 92410 0 12520 0 0 00 48 48 SSs?_e on.
22 2 III 3 72 m a
a 23 00 00
'2497 0
'25670 0 00 as 52 u 2_e on, t
s 22 2 222 3 72 A a
a C
C a
21 00 00 H205 0
" 102 0 0 00 67 Se SSvio_e pe, not one sacs www p temp 292 21 292 21 r2 n l l l l l l l l l l l l l l lal lal 1 l l l l l l l l 22l n12s 0l "2n 0l unS ol "332 01 l se s2l se e'l 04 2_e p,
not. ca ssws ow, p. to p
'22 2 522 2 72 n a
a C
C
' 22 12927 0 00 00 129s1 0 e5 99 45 83 S?m2_e pn, 922 7 222 2 r2n a
a C
22
'2638 0 00 994t 0 92t 7 0 65 60 84 09
- Ss2_c on,
??? 2 222 2 72 m a
a 22 3990 0 8473 0 6522 0 8997 0 OS #9 8S 79 34:2 e pa, l
1 l
H-0-EG-MEE-1236, Rev. 0 l
weout uncertant/
Page 2 of 5
____-__---~v w u muuim ever unS Temperatur2 trut Eo.,aten UHS /SSWS/ SACS Lirmting Configuratens LOP /SSE a
a o
e a
e 2
s a
e e
o a
a a
e a
e s
o o
i 2
2 s
s s
s a
e e
o a
e a
a e
e s
s s
u a
s s
s s
t :
e 1
9 e
a a
a a
s s
s s
e e
a e
s s
s a
s s
s e
e e
e a
a a
a e
s s
s e
o e
c
, w e
- e u
s s
s s
a a
a e
a e
a s
c e
c e
a e
a o
e o
e g
a p * * *
- e e
a s
3 s
t s
8 8
8 a
p p
e a
e a
t r
s s
P 8
P P
g g
g g
e a
a a
t u
w 9
a o
e e
e a
e
=
w a
=
s s
o o
m m
w w
w w
o o
D o
e e
6 w
=
f y
p p
p y
r v
s e
e e
e e
a p
p p
e o
e e
r3 0
o o
p 9
9 s
anosovee 777 ;
222 2 l
??
' M2 0 9 9054 0l
'04'O O
- 963 01 to 17 et 44 Os 7 J pm, 972 2 222 2 F2 m C
l 22
'2042 0 0 01
'2435 0
'7S44 01 66 2' 89 '6 34123 pi, 500 Feves 7?? 71 222 7 l
I 22 7964 0 793' 0 6759 0 8288 0 64 35 se se O's'e_p pa.
- 22 2l 222 2 f2n 4
C 1
72 50279 0 00 9549 0 9632 0 82 48 64 F4 04 rig J g 59as % seve.
'n 21 777 71 300 ! ist i I I I ICI l l l 1 l 1 I I I I I I i i I I I 1 221 n93' 01 0 01 "u2 01 m43 01 i eS iel as ul
'ea_, e.,
ssan -n sewe,
'n ri 2n 2i rta l I I I I I I Isl l I I I I I I I I I I I I I i i i lui 'rur 01 0 01
'249 01 rS44 cl I sa 2?l 49,el
- 4a_, a eaoe au H29 722 7 94 e C
C C
I 12 9'991 0 00 M642 0
" P43 0 64 77 40 64
- e:23 p.,
l'2 '
n22
'4 e C
C A
92 90019 0 9971 0 9911 0 9904 0 89 'S 67 '3
+4s23 asu 9"'
222 2
'd e C
C C
C I
92 1'951 0 00
" 642 0 "f43 0 80 69 48 64 ten 2_p pau 21' 9 222 2 14 s C
C C
N
- 2 90011 0 997' 0 9911 0 9944 0 77 2e et ')
v es;J,,y SACS Pwg Femros 292 7 222 7 30 $
I 22 19102 0 19054 0 10870 0
943 0 89 58 64 44 0'#7> saw 187 2 222 2 30 4 C
R 22 92047 0 00 97431 0
- ?S44 0 82 92 t9 's 04:2 J usu lac 8 wm passes 72, 2 272 y F2 h N
72 M '07 0 HOS4 0 108 PO O
- M30
'5 24 se 44 01s2J pa,
'l' 2 222 2 F2 #
C I
22 92842 0 00 92431 0
'2944 0 79 25 89 16 04m2 3 ses 2'92
??2 2 N/a C
N 22 99102 0 1'064 0 10470 0 99983 0 78 30 as de 09:2_p pas m2 221 3
- ita C
C R
22 92442 0 00
'7431 0 42544 0 e* 06 89 18 Ger2J ane aof SACS Leap Fease i _
202 2 772 3 F2 h a
a 73 19102 0 91054 0 1ceP0 0
" 983 0 0 00 07 to 01:23 ses 901 2 722 1 F2 h C
a a
23 00 17794 0 92418 0 92549 0 0 00 se c?
09:2J gaa 22 272 3 F2 h C
C a
a 23 00 00 14127 0 14200 0 0 00 39 $F M s2J ga.
2g2 2 272 3 Y2 m a
a a
21 8007 0 0064 0 83SS 0 44 ?S 0 0 00 84 22 09n10J paw 407 83ws Leap 8eesee 72 7 227 3 77 n a
a C
C 23 00 00 t'952 0 97059 0 0 00 80 29
$5:23 pe; 22 2 222 3 F7 m a
a 23 00 00
'4'27 0 14200 0 0 00 89 $7
' 1:23 os, 22 2 222 3 72 m a
a C
[j a
23 00 00 500tS 0
$0704 0 0 00 47*s S$s e j se, s
40f One eaC5 Pwg Per Law 2'2 71 r*2 2l r2 n l l I I I I I I I I I I I I lal lal i I I I I I I i 1221 m0201 nOS4 01
+0er0 01 usc3 01 i es tel es sel v.2 3,.,
aOT One SSW4 Pwg per Leap
'27 7
' 72 2 72 n a
a C
C 22
- 2Ses o 00 00
- 24270 es te 89 75 sh23 pe, t22 2 722 2 F2 #
A a
C 22 10429 0 00 90900 0 1094e 0 42 't 47 33 45:2J an.
222 2 222 2 F2 4 a
a 22 4829 0 3903 0 84S8 0 eS2e 0 09 4S AS 77 3de2_p pm, I
l I
l H-0-EG-MEE-1206, Rev. O witnout uncertainty A
achment 2 Page 3 of 5 i
i i
l C.___-______________.-___--.
m m m owe w v.
4-UHS Temperature Lmt E ciustien UMS/SSWS/ SACS Limeg Configurations. LOctuuA - TO CTB a
a e
e a
a e
2 7
a C
S 0
e a
e e
a e
s 0
0 t
2 9
2 S
9 S
a C
8 0
a 8
a a
S 8
e e
a s
s s
a s
s 8
8 L
s 1
2
+
2 s
e a
a a
a 3
3 3
3 w
w w
W e
a g
5 S
S S
8 s
a C
C C
C a
a a
a g
3 3
3 e
o C
e v
S S
S n
n a
8 8
8 9
5 C
C C
C a
C 3
0 m
o e
g g
e p
W W W W e
a S
3 8
4 s
F s
s a
e p
p p
p p
E E
D D
F F
'g g
g g
o e
e i
6 y
y f
o, a}O e
m e
I M
M
=
M 3
g C
0
- M O
O O
e e
e e
9 a
m a
v v
e e
e e
e e
e e
o e
.fc o o a
p
=
s t
s
~e, eve.
nr71 in 21 I I I I I I I I I I I I I I I I I I I I I I I i i i Inl mn 01 iiv0 el *voo 01
'nor 01 I ee n) u sal v 0_, %
ss*s en ewe.
.n 21 rn e@ ist i l l I ICI I I I I I I I I I I I I I I I I I Inl
'424s ol 0 01 4+s3 0!
0 584 01 i or n! e$ul s.0_e en, ssws -a swee in r1 nr 71 '7* l i I I I I I l'l I I I I I I I I I I I I I I I I i 1721
'u* 01 0 01 M*e' 01 Osarol I sa eol e,sil wC;,
s-A s e.we.
497 5 277 7 id e C
C C
8 52 94248 0 00 Oss) 0
'Mee 0 47 38 49 Se a sse e pe, rar i 777 7
- e e C
C a
e7 9957 0 1995 0 3349 0 13444 0 49 37 e9 %s eseo_e am tt**
772 7 e4 (
C C
C C
a t7
+47e4 0 00 04430 Oste 0 40 4' 99 to
'6a0_c p%
7ei e 772 7
- e g r
C C
a 17 9997 0 99 % 0
- 1464 0 03410 78 49 89 94 54a0 e n%
sacs on *wes 7< 7 21 7n 71 10 e l i I I I I I I I I I i l i I lal iI I I I I I I I 1 221 mee 01 m$001 Dies 01 m07 01 I se ul e,5cl v 0;,,
SACSmnSeesee 77t 2l ??2 7 72 n N
22 13389 0 3110 0
- 1909 0 43070 00 09 69 50 Cese_e p%
795 71 222 7
- ,a C
a 22 93369 0 93310 0 01000 030F 0 Pe 44 69 50 0' E0_c an, AOY lac 9 teep Feese l
707 7 772 3 77 m I
a a
73 13300 0 03900 93188 0 13307 0 0 00 84 97 09 s0_t pe,
'02 2 722 3 F2
- C a
a 23 00
- 0343 0 04430
- MG30 0 00 et t2 0%e0_e ca.
77 772 3 72 n C
C a
a 23 00 00 917M 0 08000 0 00 es 7F t is0_t pas _
aOT - SSwa toep Feesee 77 7 722 3 72 a l a a
C C
23 00 00 Mete 0 93499 0 0 00 49 291 95:0_c pa, 72 2 722 3 van I a
a n
00 00 OOs 0 Oas0 0 0 00 se 2ri s i.0_e p.,
aOY One 9aC3 #wse periery 7'7 71 tia ri r2n l 1 I i 1 1 1 I I 1 1 I I I lal lal l I I I I I I i 1271 mae 01 m*0 01 Oies 01
+330701 I s0 es) se nal O'n0; on, aOf - One SSW8 #wayper toep j
922 7 t22 7 72 m a
a C
C 72 9640A 0 00 00 98a43 0 47 47 e7 40 52v0; une t72 2 272 2 f2*
a a
C 77 SeM10 00 90340 0 90479 0 S' 32 SF e4
- Sv03 et, 772 7 772 2 P2 m a
a 22 19284 0
- 0240 0 90247 0 80110 0 88 17 67 M 34sn3 on, l
I i
1 i
l H-0-EG-MEE-1206, Rev. O l
Weout Uncertainty l
Page 4 of 5 4
i ik_________
1
___.---~v
- w m pq ave a *, y UHS Temperature Lima Evstaten UHS /3SWS, SACS Limeg Con 6gurdens LOP /SSE. cTB a
a e
a A
e
+
2 2
s a
C e
o a
a e
e a
e s
0 0
2 2
s s
s s
a C
s o
a e
a a
e o
e i
s s
s e
e a
s-a s
s t
L s
1 2
e 2
e e
a a
a a
s s
s s
e a
w w
e e
a e
s s
s a
s s
e a
C C
C C
a a
a a
e a
e s
s e
e c'
a
- a w e
u s
s s
a a
n a
e s
s a
s C
C C
C a
C e
o e
o e
g
, *
- w w e
e s
s s
s 6
e a
a s
l e
e a
e s
s s
s s
s e
u 2
F
=
e e
m e
a e
m
=
M M
s 0
0 M
a w
M D
D D
0 e
e o
e e
M M
4 o,
.e y
a e
e s
s o
e e
o a
o o s
s n
. r oes e
m 2l In 21 I I I I I I I I I I I I I I I I I I I I I I I I I i 1 221
'32'0 01 ' v 01
'N'2 01
- 2,es 01 I eessi usil ve; o=
ss*s % e we.
'n 21 2n 21 we l isi l I I I ICI I I I I I I I I I I I I I I I I I lui
'1Fs 01 0 01
'vss el
'un ci I sF ni ess41
's 0, o=
is*s -s s e
in 21 2n 21 72
- l I I I I I I lui i l i I I I I I I I I l l l 1 I I Inl
's004 01 0 01
'a 2e2 01 talse 01 i se 2sl 30 0el naso; pa, EDG8 ewes s t2 '
222 2
$4 e C
C C
12
' 3 FS4 0 00
'3's$ 0 132F' O 95 07 99 14
'es0; en, I'29 222 2
'd e C
C I
12 t *014 0
'176s 0 9 9634 G 19 F27 0 90 36 se s) w ascy pe
's t i 222 2 ta d C
C C
C z
12 11Fs4 0 00 43955 0 13279 0 83 09 ev id
' 4 0_, pa, 7tt '
222 2 se e C
C C
N 12 954'4 0 9'745 0 1'814 0 19727 0 80 $P A4 63
'es0J ok sacs %
- ewe.
242 21 m il ic e l i I I I I I I I I I l l 1 I ini i I I I I I i i i 1 721 miO DI ' 3+ s* 01 ' 2s F2 01 *nes 01 1 90 71 es e'l v 0; on, sacs== sewee 229 2l 222 2 F2 a l
N 22
'1210 0 93951 0 92872 0 92948 0 79 441 89 4' S's0J on, 194 2) 222 2 49a i
C E
22 93290 0 13'91 0 12872 0
'2908 0 09 9! 094' 0's0 3 sa, AOT - sacs Leap Fewee 202 2 222 3 F2 m a
a 21
'3210 0 13'91 0
'2872 0
'2905 0 0 00 84 90 05 s0_p pm, 902 2 222 3 72 h C
a a
23 00 18964 0 9426$ 0 14397 0 0 00 49 Se ess03 an, 72 222 3 F2 h C
C a
a 23 00 00 t5F03 0 994S3 0 0 00 90 24 9
- so; an, Aof. Sews Leen. Fonsge 22 2 n23 72 h a
a C
C 21 00 00 93279 0
'3198 0 0 00 et t3 siso_ gas 22 2 2M }
F2 h a
a 23 00 00 99701 0 tSGS10 0 in to fa e5:03 on, AOF One sacs 8wg pef Lee, 212 2) 252 2] F2n l l I l l I I I I l l l l l lal Ial I l l l l l l l l 221 13290 0!
13599 01 12872 0) 12948 01 l 90 741 90 82}
O's0J an, act.one news a, av Lees w
922 2 122 2 72 n a
a C
C l
22 149F2 0 00 00 939F3 0 6F 40 47 82 52WJ sa, in z m2 72
- a a
C 22
$ 20s3 0 00 ii4Fs 0
..sn D es 1 se s2
.s.0_,,,,
l m2 m2 Fr a a
a i
22 100e0 0 sesF 0 sFoe 0 usi 0 sF 2e sF 02 us0m i
1 i
1 1
l l
l I
1 H-0-EG-MEE-1206, Rev. O Wdhout Uncertainty Page 5 of 5
1 l
FORM NC.DE-AP.ZZ-0010-1 Page 2 of 4 CERTIFICATION FOR DESIGN VERIFICATION Reference No.
H-1-EG-MEE-1301
SUMMARY
STATEMENT A line-by-line check was performed per paragraph 3.1.3 of NC.DE-AP.ZZ-0010.
The Verification Checklist was consulted in detail.
The approach taken, of exhaustively examining each possible approach
{
to the problem of raising the permissible river water temperature, and then exhaustively examining each system and alignment cooled by-the SACS system, is appropriate.
The assumptions and inputs for the evaluation are correct.
.The conclusion specifically addresses the purpose of the evaluation.
I note the irony that while most of the systems proved capable of dealing with a SACS temperature of 100F, one particular lineup of the SACS system forces the continued use of 95F water.
1 i
The undersigned hereby certifies (in the right column) that the l
design verification for the subject document has been completed, the questions from the generic checklist have been reviewed and addressed as appropriate, and all comments have been adequately incorporated.
hN
.$~elva sr Design Verifier Assigned By Sig (signature of Manager / Supervisor)phturd of Design Verifier / Date 1
I Design Verifier Assigned By Sig (signature of Manager / Supervisor)pature of Design Verifier / Date Design Verifier Assigned By Sig (signature of Manager / Supervisor)pature of Design Verifier / Date Design Verifier Assigned By Sig I
(signature' of Manager / Supervisor)pature of Design Verifier / Date i
l If the Manager / Supervisor acts as the Des 1 a verifier, the signature of the next 9
higher level of technical management is required.
I Page
_1._ of l
Nuclear-Conunon Rev. 3 i
u
FORM NC DE-AP.ZZ-0010-1 P;ga 4 Of 4 1
CERTIFICATION FOR DESIGN VERIFICATION REFERENCE DOCUMENT NO. /REV.
H-1-EG-MEE-1301 l
COMMENTS RESOLUTION The intent of the 3rd Reworked and paragraph of section 6.7 is incorporated, ffp((
unclear:
)
- which coolers isolate?
- which EDG room coolers get cross-tied?
- does the proposed 25%
throttling apply to all EDG room coolers or only redundant coolers?
Request you review this section.
The final paragraph of Concur.
Incorporated, j$g4/(
section 6.16 is the heart of the conclusion.
Recommend it be moved to section 7 i
In section 6.4, the GE UHS Concur.
Incorporated as j4hp$f work requires a reference.
reference 5.6.33 In section 6.3, the design Incorporated j$(4Ff room temperature for the pipe chase requires a reference.
Recommend DITS 7.5 i
Note typos, punctuation Corrected jgy,r1 f J -Ir Acceptance AWli rJ~ fr
&AJLhGd c,/rIn at i
SUBMITTED BY DATE RESOLVE 6~BY DATE Resolution l
h-Page 1 of
-Nuclear. Common Rev.-3 l
L-____:_-.._---
L.
-_2.
--