Bundle ID 60-762-3.2
Iteration 0:
Outlet Temp: 294.26
Tube Side Exit Temp: 322.03
Tube Side
| Temperature | Density | Viscosity | Therm Cond |
|---|---|---|---|
| 323.15 | 987.99 | 5.46E-04 | 0.64059 |
| 324.82 | 987.18339 | 0.00053264 | 0.64232346 |
| 333.15 | 983.16 | 4.66E-04 | 0.65097 |
| Tin | Density | h in | T out | h out |
|---|---|---|---|---|
| 353.15 | 971.76 | 335.050 | 293.15 | 83.956 |
| 355.372222 | 970.322222366 | 344.389999066 | 294.26 | 88.598464 |
| 363.15 | 965.29 | 377.080 | 303.15 | 125.780 |
Shell Side
Outlet Temp: 355.37
Shell Side Exit Temp: 326.68
| Temperature | Density | Viscosity | Therm Cond |
|---|---|---|---|
| 323.15 | 987.99 | 5.46E-04 | 0.64059 |
| 324.82 | 987.18339 | 0.00053264 | 0.64232346 |
| 333.15 | 983.16 | 4.66E-04 | 0.65097 |
| Tin | Density | h in | T out | h out |
|---|---|---|---|---|
| 293.15 | 998.16 | 83.956 | 353.15 | 335.050 |
| 294.26111088889 | 997.87555561244 | 88.603110181689 | 355.37 | 344.38066 |
| 303.15 | 995.60 | 125.780 | 363.15 | 377.080 |
============================================================================================================
TubeID = 0.002539
TubeFlowVelocity = 1.5289349639583
TubeSideRe = 7194.7511092977
TubeSidePr = 3.4708679172553
NuLamH = 4.363
TSLamh = 1103.7641811658
NuTurbh = 42.411778529288
TSTurbh = 10729.452670219
TSTransh = 12314.252507243
TubeSideh = 10729.452670219
ShellXA = 0.0015556046285163
SequivD = 0.0034283857990767
SSReLong = 5154.0238312143
SSPr = 3.4708674410068
SSLongTurbNu = 47.777865593964
SSLongTurbh = 8951.3974617426
SSLongLamh = 1873.5448623459
SSMassVelocity = 1667.3689743189
SSReTran = 9938.9765948154
SSTranhL10000 = 16098.312710073
SSTranhG10000 = 21464.416946764
SSTranh = 16098.312710073
ShellSideh = 12524.855085908
ShellSidehcomp = 12524.855085908
CS U = 5091.9380775505
CS A = 1.1888479098525
TubeHeatCapacity = 5124.670785943
ShellHeatCapacity = 5270.1905493894
MinHeatCapacity = 5124.670785943
MaxHeatCapacity = 5270.1905493894
CS NU = 1.1812544051023
ReducedHeatCapacity = 0.97238814003354
Effectivness (Counter) = 0.54560528862794
Effectiveness (Parallel) = 0.45766537706086
Effectiveness = 0.545605289
CS Q = 170869.56842313
Tube side exit temp = 322.03
Shell side exit temp = 326.68
RLD = 287.99330445057
SGMA = 0.2899672039886
DP = 1153.8407382956
TDP Trans = 12963.751313316
TDP Laminar = 4930.330684138
TDP Turb = 12691.138259422
TDP = 12691.138259422
SDP = 49694.539081767
Transverse Area = 0.00070505955
Lognitudinal Area = 0.00077780231425815
Avg. Trans. Velc. = 1.7896417401906
Avg. Long. Velc. = 1.6222682510317
Velocity Estimate = 1.7059549956112
THotIn = 355.372222
TColdIn = 294.26111088889
THotOut = 322.03
TColdOut = 326.68
Log Mean Temp. Diff. = 28.22803876593
Tube Hold Up Volume = 0.00060345929265122
Shell Hold Up Volume = 0.0011374814384405
============================================================================================================
Bundle ID 60-762-3.2
Iteration 1:
Outlet Temp: 322.03
Tube Side Exit Temp: 321.76
Tube Side
| Temperature | Density | Viscosity | Therm Cond |
|---|---|---|---|
| 333.15 | 983.16 | 4.66E-04 | 0.65097 |
| 338.7 | 980.14635 | 0.000431035 | 0.6558318 |
| 343.15 | 977.73 | 4.03E-04 | 0.65973 |
| Tin | Density | h in | T out | h out |
|---|---|---|---|---|
| 353.15 | 971.76 | 335.050 | 313.15 | 167.570 |
| 355.372222 | 970.322222366 | 344.389999066 | 322.03 | 204.69728 |
| 363.15 | 965.29 | 377.080 | 323.15 | 209.380 |
Shell Side
Outlet Temp: 326.68
Shell Side Exit Temp: 327.01
| Temperature | Density | Viscosity | Therm Cond |
|---|---|---|---|
| 303.15 | 995.60 | 7.97E-04 | 0.61435 |
| 310.47 | 993.08924 | 0.000691592 | 0.6246712 |
| 313.15 | 992.17 | 6.53E-04 | 0.62845 |
| Tin | Density | h in | T out | h out |
|---|---|---|---|---|
| 293.15 | 998.16 | 83.956 | 323.15 | 209.380 |
| 294.26111088889 | 997.87555561244 | 88.603110181689 | 326.68 | 224.14952 |
| 303.15 | 995.60 | 125.780 | 333.15 | 251.220 |
============================================================================================================
TubeID = 0.002539
TubeFlowVelocity = 1.5289349639583
TubeSideRe = 8827.34506879
TubeSidePr = 2.7535901365627
NuLamH = 4.363
TSLamh = 1126.9768189839
NuTurbh = 46.240765836682
TSTurbh = 11944.137334403
TSTransh = 15736.137959119
TubeSideh = 11944.137334403
ShellXA = 0.0015556046285163
SequivD = 0.0034283857990767
SSReLong = 3993.1964479648
SSPr = 4.6290126482458
SSLongTurbNu = 44.089765974043
SSLongTurbh = 8033.403657821
SSLongLamh = 1822.0563163231
SSMassVelocity = 1667.3689743189
SSReTran = 7654.6525891891
SSTranhL10000 = 14733.699071873
SSTranhG10000 = 19644.93209583
SSTranh = 14733.699071873
ShellSideh = 11383.551364847
ShellSidehcomp = 11383.551364847
CS U = 5193.6957628662
CS A = 1.1888479098525
TubeHeatCapacity = 5129.6426257618
ShellHeatCapacity = 5264.5126552009
MinHeatCapacity = 5129.6426257618
MaxHeatCapacity = 5264.5126552009
CS NU = 1.2036928890688
ReducedHeatCapacity = 0.97438128877783
Effectivness (Counter) = 0.55004496914281
Effectiveness (Parallel) = 0.45944998447449
Effectiveness = 0.550044969
CS Q = 172427.08509894
Tube side exit temp = 321.76
Shell side exit temp = 327.01
RLD = 287.99330445057
SGMA = 0.2899672039886
DP = 1145.6156977294
TDP Trans = 12867.378704858
TDP Laminar = 4364.4792530278
TDP Turb = 12018.217879773
TDP = 12018.217879773
SDP = 53285.069962212
Transverse Area = 0.00070505955
Lognitudinal Area = 0.00077780231425815
Avg. Trans. Velc. = 1.7896417401906
Avg. Long. Velc. = 1.6222682510317
Velocity Estimate = 1.7059549956112
THotIn = 355.372222
TColdIn = 294.26111088889
THotOut = 321.76
TColdOut = 327.01
Log Mean Temp. Diff. = 27.928331613762
Tube Hold Up Volume = 0.00060345929265122
Shell Hold Up Volume = 0.0011374814384405
============================================================================================================
Bundle ID 60-762-3.2
Iteration 2:
Outlet Temp: 321.76
Tube Side Exit Temp: 321.76
Tube Side
| Temperature | Density | Viscosity | Therm Cond |
|---|---|---|---|
| 333.15 | 983.16 | 4.66E-04 | 0.65097 |
| 338.57 | 980.21694 | 0.000431854 | 0.65571792 |
| 343.15 | 977.73 | 4.03E-04 | 0.65973 |
| Tin | Density | h in | T out | h out |
|---|---|---|---|---|
| 353.15 | 971.76 | 335.050 | 313.15 | 167.570 |
| 355.372222 | 970.322222366 | 344.389999066 | 321.76 | 203.56841 |
| 363.15 | 965.29 | 377.080 | 323.15 | 209.380 |
Shell Side
Outlet Temp: 327.01
Shell Side Exit Temp: 327.01
| Temperature | Density | Viscosity | Therm Cond |
|---|---|---|---|
| 303.15 | 995.60 | 7.97E-04 | 0.61435 |
| 310.64 | 993.03093 | 0.000689144 | 0.6249109 |
| 313.15 | 992.17 | 6.53E-04 | 0.62845 |
| Tin | Density | h in | T out | h out |
|---|---|---|---|---|
| 293.15 | 998.16 | 83.956 | 323.15 | 209.380 |
| 294.26111088889 | 997.87555561244 | 88.603110181689 | 327.01 | 225.53024 |
| 303.15 | 995.60 | 125.780 | 333.15 | 251.220 |
============================================================================================================
TubeID = 0.002539
TubeFlowVelocity = 1.5289349639583
TubeSideRe = 8811.2387744398
TubeSidePr = 2.7592554649669
NuLamH = 4.363
TSLamh = 1126.7811283813
NuTurbh = 46.204901566367
TSTurbh = 11932.801082672
TSTransh = 15702.955813714
TubeSideh = 11932.801082672
ShellXA = 0.0015556046285163
SequivD = 0.0034283857990767
SSReLong = 4007.1459153475
SSPr = 4.6108905309741
SSLongTurbNu = 44.138426751371
SSLongTurbh = 8045.3559203318
SSLongLamh = 1822.7554791771
SSMassVelocity = 1667.3689743189
SSReTran = 7681.8436980696
SSTranhL10000 = 14751.444467521
SSTranhG10000 = 19668.592623362
SSTranh = 14751.444467521
ShellSideh = 11398.400193927
ShellSidehcomp = 11398.400193927
CS U = 5194.099789899
CS A = 1.1888479098525
TubeHeatCapacity = 5129.5574118091
ShellHeatCapacity = 5264.5495309513
MinHeatCapacity = 5129.5574118091
MaxHeatCapacity = 5264.5495309513
CS NU = 1.2038065242376
ReducedHeatCapacity = 0.97435827731347
Effectivness (Counter) = 0.55007214052649
Effectiveness (Parallel) = 0.4594645889863
Effectiveness = 0.550072141
CS Q = 172432.738223
Tube side exit temp = 321.76
Shell side exit temp = 327.01
RLD = 287.99330445057
SGMA = 0.2899672039886
DP = 1145.6982048081
TDP Trans = 12868.339904938
TDP Laminar = 4369.0674234259
TDP Turb = 12024.154567889
TDP = 12024.154567889
SDP = 53235.510052662
Transverse Area = 0.00070505955
Lognitudinal Area = 0.00077780231425815
Avg. Trans. Velc. = 1.7896417401906
Avg. Long. Velc. = 1.6222682510317
Velocity Estimate = 1.7059549956112
THotIn = 355.372222
TColdIn = 294.26111088889
THotOut = 321.76
TColdOut = 327.01
Log Mean Temp. Diff. = 27.928331613762
Tube Hold Up Volume = 0.00060345929265122
Shell Hold Up Volume = 0.0011374814384405
============================================================================================================
| Performance Calculations - 60-762-3.2 | |||||||
|---|---|---|---|---|---|---|---|
| Date: | 2026-04-08 14:02:18 | ||||||
| Customer: | Item No: | #### | |||||
| Model No: | 01182-14 | Rev: | #### | ||||
| Flow Direction: | |||||||
| Material of Construction: | SS316L | Heat Transfer Area: | 12.8 ft² / 1.19 m² | ||||
| Performance of One Unit (SI) | |||||||
| Fluid Allocation | Shell Side | Tube Side | |||||
| Fluid Name | Water | Water | |||||
| Flow Rate | lpm | 75.71 | 75.71 | ||||
| kg/h | 4532.84 | 4407.68 | |||||
| Inlet Pressure | barg | 1.03 | 1.03 | ||||
| Temperature (In/Out) | °C | 21.11 | 53.86 | 82.22 | 48.61 | ||
| Velocity | m/s | #### | #### | ||||
| Pressure Drop | bar | 0.53236 | 0.12024 | ||||
| Hold-up Volume | cm³ | 1137.48 | 603.46 | ||||
| Fouling Resist. (min) | m²-K/W | ||||||
| Heat Exchanged | 172.43 | kW | LMTD | 27.93°C | |||
| Transfer Coefficient | 5194.1 | W/(m²-K) | Effectiveness | 0.55 | |||
| Performance of One Unit (ENG) | |||||||
| Fluid Allocation | Shell Side | Tube Side | |||||
| Fluid Name | Water | Water | |||||
| Flow Rate | gpm | 20 | 20 | ||||
| lb/h | 9993.2 | 9717.27 | |||||
| Inlet Pressure | psig | 15 | 15 | ||||
| Temperature (In/Out) | °F | 70 | 128.95 | 180 | 119.5 | ||
| Velocity | ft/s | #### | #### | ||||
| Pressure Drop | psi | 7.72 | 1.74 | ||||
| Hold-up Volume | in³ | 69.41 | 36.83 | ||||
| Fouling Resist. (min) | ft²-h-F/BTU | ||||||
| Heat Exchanged | 588364.93 | BTU/hr | LMTD | 50.27 °F | |||
| Transfer Coefficient | 5194.1 | BTU/(hr-ft²-F) | Effectiveness | 0.55 | |||
| Remarks: | ̇See sales drawing for more details about the Selected heat exchanger model | ||||||
| ̈Solid model available upon request | |||||||
| Errors and warnings | |||||||
| Proprietary and Confidential: | The information contained in this document is the sole property of Exergy, LLC. Any reproduction, disclosur us, in part or as a whole, without the written permission of Exergy, LLC is prohibited. | ||||||