02 heat exchangers

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Chapter 2: Heat Exchangers Rules of Thumb for Chemical Engineers, 5th Edition by Stephen Hall Units: This Excel workbook includes Visual Basic for Application function subroutines. Macros must be enabled for them to work. Guide to Using this Workbook 4. Calculate the inside film coefficient on the Tubes htc worksheet 6. Calculate the outside film coefficient on the Shell htc worksheet 7. Determine the pressure drop on the shell side on the Shell Pressure Drop worksheet 9. Complete a TEMA datasheet on the Shell-and-Tube worksheet ChemEng Software sells an Excel template called TANKJKT The primary purpose of this workbook is to demonstrate the use of the Bell-Delaware method fo shell-and-tube heat exchangers. The method is applicable to exchangers with NO PHASE change. worksheets follow the text in the stepwise evaluation of a heat transfer problem that is defi the hot and cold fluid properties. Input cells have RED text. Cells with black text are formu 1. Define the components in the hot and cold streams on the Process Fluids worksheet. Store t properties for new (previously unknown) components on the Fluid Data worksheet. worksheet 3. Use the Tubes Pressure Drop worksheet to determine the tube diameter, length and number of passes in the exchanger, based on a pressure drop criteria Geometry worksheet. 8. Compute the overall heat transfer coefficient, clean and fouled, on the Overall U workshee iterate until the assumed overall U in Step 3 agrees with the calculated U-clean 10. The Conversions worksheet is used for data, including the status of radio buttons and che and must not be deleted! www.chemengsoftware.com Customary US SI

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Page 1: 02 Heat Exchangers

Chapter 2: Heat ExchangersRules of Thumb for Chemical Engineers, 5th Edition

by Stephen Hall

Units:

This Excel workbook includes Visual Basic for Application function subroutines.Macros must be enabled for them to work.

Guide to Using this Workbook

2. Define the mass fraction of the components, flow rates, and temperatures on the Process Data worksheet

4. Calculate the inside film coefficient on the Tubes htc worksheet

5. Determine the shell diameter and enter information about the tube bundle and baffles on the Shell Geometry worksheet.

6. Calculate the outside film coefficient on the Shell htc worksheet

7. Determine the pressure drop on the shell side on the Shell Pressure Drop worksheet

9. Complete a TEMA datasheet on the Shell-and-Tube worksheet

ChemEng Software sells an Excel template called TANKJKT

The primary purpose of this workbook is to demonstrate the use of the Bell-Delaware method for rating shell-and-tube heat exchangers. The method is applicable to exchangers with NO PHASE change. The worksheets follow the text in the stepwise evaluation of a heat transfer problem that is defined by the hot and cold fluid properties. Input cells have RED text. Cells with black text are formulas.

1. Define the components in the hot and cold streams on the Process Fluids worksheet. Store the properties for new (previously unknown) components on the Fluid Data worksheet.

3. Use the Tubes Pressure Drop worksheet to determine the tube diameter, length and number of tube passes in the exchanger, based on a pressure drop criteria

8. Compute the overall heat transfer coefficient, clean and fouled, on the Overall U worksheet; iterate until the assumed overall U in Step 3 agrees with the calculated U-clean

10. The Conversions worksheet is used for data, including the status of radio buttons and checkboxes, and must not be deleted!

www.chemengsoftware.com

Customary US SI

Page 2: 02 Heat Exchangers

TANKJKT models heat transfer in vessels with jackets and/or internal coils. It includes a database of properties for glass-lined reactors, heat transfer fluids, and insulation materials. Order on-line or by telephone, 24-h/d; credit cards accepted.

Page 3: 02 Heat Exchangers
Page 4: 02 Heat Exchangers

Use this worksheet to define the components present in the hot and cold streams for a heat transfer problem.Multiple components from the Fluid Data properties table can be specified, and their properties will be averaged.Averging properties for non-ideal solutions, such as polar mixtures (with water), gives poor results.A better approach is to define the properties for the mixtures at several temperatures and add them to the database.

Use the dropdown list to view the Fluid Data content: Methyl Alcohol

To add new materials to the Fluid Data, go to the Fluid Data worksheet tab

Hot Fluid ComponentsName in Data Table? Description

1 Water YES City water 2 Methyl Alcohol YES pure component 3 4 5 6 7 8 9

Cold Fluid ComponentsName in Data Table? Description

1 Water YES City water 2 3 4 5 6 7 8 9

The composition (i.e., mass fraction of each component) is specifed on the next worksheet.

Problem Statement:Define components for the hot and cold streams

Page 5: 02 Heat Exchangers

Use this worksheet to define the components present in the hot and cold streams for a heat transfer problem.Multiple components from the Fluid Data properties table can be specified, and their properties will be averaged.Averging properties for non-ideal solutions, such as polar mixtures (with water), gives poor results.A better approach is to define the properties for the mixtures at several temperatures and add them to the database.

Page 6: 02 Heat Exchangers

InputsHot Side

Fluid name Distilled WaterFlow Total lb/h 396,000 Temperature, in °F 90 Temperature, out °F 77 Pressure, in psig 29 Press Drop Allowed psig 2 Fouling Resistance ft²-h-°F/Btu 0.0005

Cold SideFluid name Raw WaterFlow Total lb/h 1,188,000 Temperature, in °F 68 Temperature, out °F 72 Pressure, in psig 60 Press Drop Allowed psig 10 Fouling Resistance ft²-h-°F/Btu 0.0005

mass fracComponent Density

Hot Side Fluid Components mass fraction mole fracti lb/ft31 Water 1 61.91 2 Methyl Alcohol 0 - 3 4 5 6 7 8 9

OK 61.91

Cold Side Fluid Components1 Water 1 62.25 2 3 4 5 6 7 8 9

OK 62.25

Problem Statement:Specify process conditions for a liquid-liquid heat exchange problem, and perform a heat balance

Hot Side Flow

Hot Side Temperature In

Hot Side Temperature Out

Cold Side Flow

Cold Side Temperature In

Cold Side Temperature Out

Page 7: 02 Heat Exchangers

Shell Side Tube SideParameter Units In Out InFluid Name Distilled Water Raw WaterFlow Total lb/h 396000 1188000

Vapor lb/hLiquid lb/hSteam lb/hWater lb/hNoncondensable lb/h

Evap/Cond lb/hTemperature (In/Out) °F 89.6 68Density lb/ft3Viscosity cPMolecular Weight, vaporMolecular Weight, noncondensiblesSpecific Heat Btu/lb-°FThermal Conductivity Btu/h-ft-°FLatent Heat Btu/lbInlet Pressure psig 29.00754 60Velocity ft/sPress Drop Allowed psig 1.5 10Fouling Resistance ft²-h-°F/Btu 0.0004996871 0.000499687

Page 8: 02 Heat Exchangers

Temp, CTemp, C

Heat Transferred 5,002,748 Btu/h

Temp, CTemp, C

mass fracViscosity Sp Heat Therm Cond H Vap Density Viscosity Sp Heat

cP MW Btu/lb-°F Btu/h-ft-°F Btu/lb lb/ft3 cP MW Btu/lb-°F0.774094394 18.02 1.00 0.35 971.63 62.11 0.902497 18.02 1.00 0.515864406 32.04 - - 472.91 - 0.562399 32.04 -

0.774094394 1.00 0.35 62.11 0.902497 1.00

1.02 18.02 1.00 0.34 971.63 62.19 0.96 18.02 1.00

1.02 1.00 0.34 62.19 0.96 1.00

Page 9: 02 Heat Exchangers

Tube SideOut

Raw Water1188000

Page 10: 02 Heat Exchangers

32.00 25.00 Heat (5,002,748) Btu/h (1,466,306) Watts

20.00 22.33 Heat 5,002,748 Btu/h 1,466,306 Watts

(0)

Therm Cond Antoine Coefficients VP VP Partial P Viscosity using Eq 27-3Btu/h-ft-°F A B C mm Hg psig psig Wi ln(visc) 0.35 8.03 1,706.13 231.49 35.69 (14.01) 1 -0.256061 - 7.97 1,515.29 232.99 180.57 (11.20) 0 0 0.35 -0.256061

0.34 8.03 1,706.13 231.49 35.69 (14.01) 1 0.015857 0.34 0.015857

Page 11: 02 Heat Exchangers

Viscosity Based on the Wall TemperaturesViscosity using Eq 27-3 If Shell Side If Tube Side

cP ln(cP) cP ln(cP)-0.10259 0.94347 -0.058191 0.92645 -0.076395

0 0.576321 0 0.570588 0

-0.10259 0.94347 -0.058191 0.92645 -0.076395

-0.040408 0.94 -0.058191 0.93 -0.076395

-0.040408 0.94347 -0.058191 0.92645 -0.076395

Page 12: 02 Heat Exchangers

InputsFluid flowing in tubes Raw WaterAssumed overall U Btu/h-ft²-°F 520 Safety factor for fouling 20%Tube OD in 0.750 Tube wall thickness BWG 14 Tube length ft 15 Tube Passes 1 Shell Passes 1

Data (from the Process Data and F Factor worksheets)Flow rate lb/h 1,188,000 Heat transferred Btu/h 5,002,748 Temp diff correction factor 1.000 Average viscosity cP 0.99 Average density lb/ft3 62.22 Pressure at inlet psig 60 Pressure drop allowed psig 10 Tube roughness ft 0.0000067

CalculationsTube inside diameter in 0.584 Flow area per tube ft² 0.00186 Tube area available ft²/ft 0.1963 Log-mean temp diff °F 12.74 Mean temperature difference °F 12.74 Adjusted duty Btu/h 6,003,298 Tube area required ft² 906 Total tube length req ft 4,615 Number of tubes 308 Tubes per pass 308 Actual area ft² 907

Flow rate per tube lb/h 3,857 Velocity in tube ft/s 9.26 Reynolds Number #VALUE!Friction Factor #VALUE!Pressure Drop, tubes psig #VALUE!

Pressure drop, enter/exit ft fluid neglectEnter/exit tubes ft fluid 2.00 End losses in bonnets/channels ft fluid - Subtotal, extra losses tube side ft fluid 2.00

psig 0.86

Problem Statement:Calculate the tube side pressure drop based on process data and heat load, using rule-of-thumb heat transfer rate and safety factor

Result

Standard tube lengths in the US are 4, 8, 12, 15, and 20 ft

Minimum = number of shell passes, or may be a multiple of 2 times the shell passes. This is the total number of tube passes, example: 3 shells, 2 tube passes in each shell = 6 tube passes

Typical value is0.5 to 2.5 m/s or2 to 8 ft/s

After stepping through all of the worksheets to "Overall U", come back here and iterate this assumption until it agrees with the calculated (clean) U

D8
After stepping through all of the worksheets to "Overall U", come back here and iterate this assumption until it agrees with the calculated (clean) U
D12
Standard tube lengths in the US are 4, 8, 12, 15, and 20 ft
D13
Minimum = number of shell passes, or may be a multiple of 2 times the shell passes. This is the total number of tube passes, example: 3 shells, 2 tube passes in each shell = 6 tube passes
D40
Typical value is 0.5 to 2.5 m/s or 2 to 8 ft/s
Page 13: 02 Heat Exchangers

Total pressure drop, tube side psig #VALUE! #VALUE!

Page 14: 02 Heat Exchangers

Minimum = number of shell passes, or may be a multiple of 2 times the shell passes. This is the total number of tube passes, example: 3 shells, 2 tube passes in each shell = 6 tube passes

After stepping through all of the worksheets to "Overall U", come back here and iterate this assumption until it agrees with the calculated (clean) U

Page 15: 02 Heat Exchangers

Inputs (copied from the Process Data and Tubes worksheets)Hot Side

Fluid name Distilled WaterTemperature, in °F 89.60 Temperature, out °F 77.00

Cold SideFluid name Raw WaterTemperature, in °F 68.00 Temperature, out °F 72.20

Tube passes 1 Shell passes N 1

CalculationsIntermediate value R 2.999 Intermediate value P 0.195 Intermediate value S 1.581 Intermediate value W 0.517 Intermediate value W' 0.805

General CaseNumerator (1.042)Denomenator (1.107)

General Case Answer F 0.942

R=1 CaseNumerator 0.341 Denomenator 0.345

R=1 Answer F 0.990

Choose which one F 0.942

Problem Statement:Calculate the LMTD configuration correction factor

Result

Page 16: 02 Heat Exchangers

Inputs Fluid flowing in tubes Raw WaterAssumed inside heat transfer coef Btu/h-ft²-°F 1,057

Data (from the Process Data and Tubes Pressure Drop worksheets)Assumed overall U Btu/h-ft²-°F 520.0 Outside surface area ft² 907.1 Tube outside diameter in 0.750 Tube inside diameter in 0.584

ft 0.049 Tube length (one path) ft 4,620.00 Bulk viscosity cP 0.99 Viscosity at tube wall cP 0.93 Bulk heat capacity Btu/lb-°F 1.00 Bulk thermal conductivity Btu/h-ft-°F 0.34 Reynolds Number #VALUE!

CalculationsInside surface area ft² 706.36 Overall U based on inside area Btu/h-ft²-°F 667.81 Average temperature, shell side °F 70.10 Average temperature, tube side °F 83.30 Mean wall temperature, inside °F 74.96

Temp, C 23.87 Sieder-Tate term (visc ratio^0.14) 1.01 Prandl Number 6.98

Laminar flow calculationInside heat transfer coefficient Btu/h-ft²-°F #VALUE!

Turbulent flow calculationInside heat transfer coefficient Btu/h-ft²-°F #VALUE!

Transition flow calculationInside heat transfer coefficient Btu/h-ft²-°F #VALUE!

Choose which oneInside heat transfer coefficient Btu/h-ft²-°F #VALUE!

Problem Statement:Calculate the tube side heat transfer coefficient

Result

Page 17: 02 Heat Exchangers

InputsNumber of shells 1 Shell inside diameter in 21.25 <-- Minimum diameter is 23.3 inOuter tube limit (diameter) in 19.00 Baffle cut fraction 0.25 Baffle spacing in 10.00 Baffle diameter in 21.00 Number of sealing strips per side 2 Tube pitch layout 90 Tube pitch ratio 1.330

Data (from Tubes Pressure Drop worksheet)Number of tubes in the exchanger N 308Outside diameter of tubes in 0.75Tube length ft 15Tube passes 1

CalculationsTube pitch in 1.00 Longitudinal Tube Pitch in 1.00 Cross section for 1 tube equivalent in2 1.00 Cross section for all tubes in2 306 Area corrected for tube passes in2 306 Minimum calculated shell diameter in 21.25 Standard diameter from table in 23.25 Approximate max unsupported tube span in 59.64 Number of effective crossflow rows in each window 4.26 Number of baffles 16

Problem Statement:Calculate the shell side geometrical parameters

Minimum baffle spacing is generally one-fifth of the shell diameter and not less than 2 inches. Maximum spacing is limited by the maximum unsupported tube span (in inches, equals 74 d^.75), divided by 2, reduced by 12% for Al, Cu, and their alloys.

Optimum baffle spacing is between 0.4 and 0.6 of the shell diameter

Typically, the outer tube limit is (shell diameter - 26) mm for shells 635 mm (25 in) and larger; (shell diameter - 22 mm) for shells that are 254 to 610 mm (10 to 24 in) and slightly less for smaller shells

D9
Typically, the outer tube limit is (shell diameter - 26) mm for shells 635 mm (25 in) and larger; (shell diameter - 22 mm) for shells that are 254 to 610 mm (10 to 24 in) and slightly less for smaller shells
D11
Minimum baffle spacing is generally one-fifth of the shell diameter and not less than 2 inches. Maximum spacing is limited by the maximum unsupported tube span (in inches, equals 74 d^.75), divided by 2, reduced by 12% for Al, Cu, and their alloys. Optimum baffle spacing is between 0.4 and 0.6 of the shell diameter
Page 18: 02 Heat Exchangers

<-- Minimum diameter is 23.3 in

Minimum baffle spacing is generally one-fifth of the shell diameter and not less than 2 inches. Maximum spacing is limited by the maximum unsupported tube span (in inches, equals 74 d^.75), divided by 2, reduced by 12% for Al, Cu, and their alloys.

Optimum baffle spacing is between 0.4 and 0.6 of the shell diameter

Typically, the outer tube limit is (shell diameter - 26) mm for shells 635 mm (25 in) and larger; (shell diameter - 22 mm) for shells that are 254 to 610 mm (10 to 24 in) and slightly less for smaller shells

Page 19: 02 Heat Exchangers

Inputs Fluid flowing in shell Distilled WaterAssumed outside heat transfer coef Btu/h-ft²-°F 704 Baffle hole clearance 0.03

DataFlow rate lb/h 396,000

lb/s 110.00 Assumed overall U Btu/h-ft²-°F 520.0 Outside surface area ft² 907.1 Tube outside diameter in 0.750

ft 0.063 Number of tubes in the exchanger N 308 Viscosity at tube wall cP 0.93 Bulk viscosity, shell cP 0.84

lb/ft-s 0.00056 Wall viscosity, shell cP 0.94 Bulk heat capacity, shell Btu/lb-°F 1.00 Bulk thermal conductivity, shell Btu/h-ft-°F 0.35

Btu/s-ft-F 0.000097 Shell inside diameter in 21.25 Tube bundle outside diameter in 19.00 Baffle cut fraction 0.25 Baffle spacing in 10.00 Pitch layout 90 Pitch Ratio 1.33 Tube Pitch in 1.00 Tube Pitch, normal to flow in 1.00 Tube Pitch, parallel to flow in 1.00 Number of sealing strip pairs per side 2

CalculationsAverage temperature, shell side °F 70.10 Average temperature, tube side °F 83.30 Mean wall temperature, outside °F 73.56

Temp, C 23.09

Crossflow area between baffles, As ft² 0.4707 Reynolds Number 25,929 j-ideal factor coefficients a1 0.370

a2 (0.395)a3 1.187 a4 0.370 a 0.169

j-ideal factor 0.007 Sieder-Tate term (visc ratio^0.14) 0.98

Problem Statement:Calculate the shell side film coefficient using the Bell-Delaware method

Page 20: 02 Heat Exchangers

Ideal heat transfer coefficient Btu/h-ft²-°F 1,708.59

Correction Factor for Baffle Cut and SpacingBaffle cut, lc in 5.31 Intermediate 0.56 Fraction of tubes in crossflow Fc 0.67 Baffle cut correction factor Jc 1.03

Correction Factor for Baffle Leakage EffectsAngle to edge of baffle Theta-1 1.05 2.09440 Shell-to-baffle spacing sb 0.25 Shell-to-baffle leakage area Asb 5.56 Shell-to-outer tube limit distance C1 2.25 18.25Angle to edge of tubes and baffle Theta-3 1.95 1.90 Fraction of tubes in one window Fw 0.16 0.15 Baffle hole to tube OD spacing tb 0.03 Tube-to-baffle leakage area Atb 4.74 Angle to window Theta-2 2.04 2.0943951Tubes in baffle window Ntw 50.00 46.67 Area occupied by tubes in window Awt 22.09 20.62 Gross window area Awg 64.87 69.34 Free area for fluid flow in one window Aw 42.78 48.72 Intermediate ra 0.54 Intermediate rb 0.24 Baffle Leakage Effects factor Jl 0.78

Correction Factor for Bundle and Partition Bypass EffectsFormula coefficient C 1.25 Number of bypass divider lanes Np - Width of bypass divider lanes wp 1.50 Area of bypass divider lanes, Abp ft² 0.16 Ratio, bypass to crossflow area rc 0.33 Tube crossings Ncc 10.65 Ratio of sealing strips to tubes 0.19 Bundle Bypass Factor Jb 0.89

Correction for Variations in Baffle SpacingAssuming even number of baffles so shell nozzles are on opposite sidesOdd number of flow lanesAssume equal spacing for inlet and outlet bafflesNumber of baffles 16 Length of center section, baffled in 150.00 Inlet and Outlet baffle spacing in 15.00 Exponent n 0.60 Li* 1.50 Lo* 1.50 Baffle Spacing Factor Js 0.96

Correction for Temperature Gradient if Laminar FlowNumber of tube rows in one crossflow section 10.65

Page 21: 02 Heat Exchangers

Correction factor 1.00

Page 22: 02 Heat Exchangers

Overall losses 0.69

Page 23: 02 Heat Exchangers

Outside heatBtu/h-ft²-°F 1,182.81 6,742.00

Equiv Diam 0.229264

Page 24: 02 Heat Exchangers

Inputs

Data (from Shell htc worksheet)Reynolds Number 25,929 Number of baffles 16 Pitch Ratio 1.33 Tube Pitch in 1.00 Tube Outside Diameter in 0.75 Sieder-Tate term (visc ratio^0.14) 0.98 Flow rate lb/s 110.00 Tubes in one crossflow section Nr,cc 10.65 Tube crossings in window Nr,tw 3.06 Density lb/ft3 62.01 Conversion factor gc 32.17 Flow area, crossflow section, As ft² 0.471 Flow area, window, Aw ft² 0.297 Ratio, bypass to crossflow area rc 0.33 Ratio of sealing strips to tubes 0.19 Intermediate ra 0.54 Intermediate rb 0.24 Baffle spacing, center 10.00 Baffle spacing, inlet zone 15.00 Baffle spacing, outlet zone 15.00

CalculationsVelocity in crossflow at widest diameter

Velocity ft/s 3.77

Ideal Pressure Drop per Crossflow Sectionf-ideal factor coefficients b1 0.391

b2 (0.148)b3 6.300 b4 0.378 b 0.837

f-ideal factor 0.087 Pressure Drop, one crossflow section psig 0.35 Crossflow pressure drop, ideal psig 5.19

Bypass correction factorCoefficient Cbp 3.7 Bypass correction factor RB 0.71

Leakage correction factorIntermediate exponent 0.57 Leakage correction factor RL 0.40

Crossflow pressure drop, corrected psig 1.48

Window Pressure Drop

Problem Statement:Calculate the shell side pressure drop

Page 25: 02 Heat Exchangers

Average flow per window mw 294 Equivalent diameter of baffle window ft 0.10 Window pressure drop psig 2.03

End Zones Pressure DropExponent 0.2 Correction factor, baffle spacing RS 0.96 End zones pressure drop psig 0.002

TOTAL Shell Side Pressure Drop psig 3.51

Page 26: 02 Heat Exchangers

InputsMaterial of construction, tubes Cr-alloy (0.5% Cr)

DataAssumed U Btu/h-ft²-°F 520 Film coefficient, tubes Btu/h-ft²-°F #VALUE!Fouling resistance, tubes 0.00050 Fouling resistance, shell 0.00050 Film coefficient, shell Btu/h-ft²-°F 1,183 Outside diameter, tubes in 0.75 Inside diameter, tubes in 0.58 Thermal conductivity, tubes Btu/h-ft-°F 24 Heat transferred Btu/h 5,002,748 Mean temperature difference °F 12.74

Calculations

Overall U, calculated, clean Btu/h-ft²-°F #VALUE!Overall U, calculated, dirty Btu/h-ft²-°F #VALUE!

Area required, clean ft² #VALUE!Area required, fouled ft² #VALUE!Area provided by the design ft² 907.13 Oversurface #VALUE!

Problem Statement:Calculate the overall heat transfer coefficient and compare with the assumed value

Page 27: 02 Heat Exchangers

InputsMax Velocity, tubeside nozzles ft/s 5.00 Max Velocity, shellside nozzles ft/s 3.00

DataTubeside

Flow rate lb/h 1,188,000 Inlet density lb/ft3 62.25 Outlet density lb/ft3 62.19

ShellsideFlow rate lb/h 396,000 Inlet density lb/ft3 61.91 Outlet density lb/ft3 62.11

CalculationsTubeside

Volumetric flow rate, tubeside inlet ft3/s 5.30 Minimum ID of nozzle in 13.94 Selected nozzle in 15.624Selected nozzle designation in 16Velocity ft/s 3.98 rho-v2 lb/ft2-s 986.84 Weight lb 146Volumetric flow rate, tubeside outlet ft3/s 5.31 Minimum ID of nozzle in 13.95 Selected nozzle in 15.624Selected nozzle designation in 16Velocity ft/s 3.99 rho-v2 lb/ft2-s 987.90 Weight lb 146

ShellsideVolumetric flow rate, shellside inlet ft3/s 1.78 Minimum ID of nozzle in 10.42 Selected nozzle in 12.39Selected nozzle designation in 12Velocity ft/s 2.12 rho-v2 lb/ft2-s 278.80 Weight lb 90Volumetric flow rate, shellside outlet ft3/s 1.77 Minimum ID of nozzle in 10.40 Selected nozzle in 12.39Selected nozzle designation in 12Velocity ft/s 2.12 rho-v2 lb/ft2-s 277.90 Weight lb 90

Problem Statement:Specify the size of the nozzles

Page 28: 02 Heat Exchangers

InputsTubesheet thickness in 1Baffle Thickness in 0.5

DataShell Inside Diameter ft 1.770833Shell Thickness ft 0.0625Shell Length ft 15Number of Baffles 16Tube Outside Diameter ft 0.0625Tube Inside Diameter ft 0.048667Number of Tubes 308

Weight of steel lb/ft3 489.5Density of water lb/ft3 62.4

CalculationsShell metal volume ft3 2.65 Shell weight lb 1,299 Add for heads lb 456 Add for four flanges lb 720 Add for nozzles lb 180.00 Total, Shell lb 2,788

Tube volume (inside the tubes) ft3 8.59 Tube volume (outside the tubes)ft3 14.17 Tube Weight lb 2,731 Tubesheet lb 201 assumes two tubesheetsAdd for nozzles lb 292 Baffles lb 804 Total, Tube Bundle empty lb 4,229

Total Weight, empty lb 7,017

Shell inside volume ft3 36.94 Heads volume ft3 3.69 Less volume of tube metal ft3 (5.58)Weight of Water filling the void lb 2,188

Total Weight, full of water lb 9,205

Problem Statement:Estimate the weight of the heat exchanger

Page 29: 02 Heat Exchangers

SHELL-AND-TUBE HEAT EXCHANGERCLIENT EQUIP. NO PAGE

REV PREPARED BY DATE APPROVAL W.O. REQUISITION NO. SPECIFICATION NO.

0 1 UNIT AREA PROCURED BY INSTALLED BY2

1 Size TEMA Type Connected in (series/parallel)2 Surface per Unit 907.13 Shells per Unit 1 Surface per Shell 907.1 ft²3 Performance of One Unit4 Fluid Allocation Shell Side Tube Side6 Fluid Name Distilled Water Raw Water7 Flow Total lb/h 396,000 1,188,0008 Vapor lb/h (in/out)

9 Liquid lb/h (in/out) 396,000 1,188,000

10 Steam lb/h (in/out)

11 Water lb/h (in/out)

12 Noncondensable lb/h (in/out)

13 Temperature (In/Out) °F (in/out) 89.6 77.0 68.0 72.2 14 Density lb/ft3 61.91 62.11 62.25 62.19 15 Viscosity cP 0.77 0.90 1.02 0.96 16 Molecular Weight, vapor17 Specific Heat Btu/lb-°F 1.00 1.00 1.00 1.00 18 Thermal Conductivity Btu/h-ft-°F 0.4 0.3 0.3 0.3 19 Latent Heat Btu/lb20 Inlet Pressure psigg (inlet) 29.0 60.021 Velocity ft/s 3.77 9.2622 Press Drop Allow/Calc psig 1.5 3.5 10.0 #VALUE!23 Fouling Factor ft²-h-°F/Btu 0.0005 0.000524 Heat Exchanged Btu/hr 5,002,748 LMTD (corrected) °F 12.74

25 Service Coeff. Btu/h-ft²-°F Dirty #VALUE! Clean #VALUE!26 Construction Data for One Shell27 Shell Side Tube Side Sketch28 Design/Test Press psigg29 Design Temperature °F30 No. Passes per Shell 1 131 Corrosion Allowance in32 In inches 12.00 16.0033 Out 12.00 16.0034 Intermediate35 Tubes No. 308 OD, in 0.75 Gauge 14 Length, ft. 15 Pitch layout, deg. 9036 Type Material Cr-alloy (0.5% Cr) Pitch ratio 1.3337 Shell OD, in ID, in 21.25 Material38 Channel or Bonnet OD, in Thick Channel Cover39 Tubesheet Type40 Floating Heat Cover Impingement Protection41 Baffles Cross (number) 16 % Cut (d) 25% Spacing C/C, in 10.00 42 Baffles Long Seal Type No43 Supports Tube U-Bend Type44 Bypass Seal Arrangement NA Tube-Tubesheet Joint45 Expansion Joint No. Type46 Rho-V2-Inlet Nozzle 987 Bundle Entrance 279 Bundle Exit 278 47 Gaskets - Shell Side Tube Side48 Floating Heat Cover Supports49 Code Requirements TEMA Class50 Weight per shell lb 7,000 Filled w/water 9,200 Bundle 4,200 5152 Notes5354

Connections Size & Rating

Page 30: 02 Heat Exchangers

Units conversion table. Do not change the SI units;

You may change the SI Units (and corresponding "Multiply to =")

but be very careful!

DO NOT INSERT ROWS INTO THIS TABLE!

Table Name: UNITS_CONV

Units Conversion

Index Customary US Multiply to = SI Unit

1 volume gallons 3.785412 liters

2 length in 25.4 mm The format for accessing the Units Conversion table is:

3 area ft² 0.09290304 m² =INDEX( units_conv, index, 2)

4 heat flux Btu/h-ft²-°F 5.678263 W/m²-°C returns the second column (i.e., US units name)

5 conductivity Btu/h-ft-°F 1.730735 W/m-°C

6 Heat transfer Btu/hr 0.2931 W Example

7 flowrate gal/min 3.785412 liters/min Index = 8 (fouling)

8 fouling ft²-h-°F/Btu 0.1761102 m²-°C/W formula:

9 pipe sizes inches DN result:

10 spec heat Btu/lb-°F 4.1868 kJ/kg-°C

11 length feet 304.8 millimeters

12 velocity ft/s 0.3048 m/s 3.280839895

13 area ft² 0.09290304 m²

14 pressure psig 6.894757 kPa(g)

15 mass flow lb/h 0.4535924 kg/h

16 heat of vap Btu/lb 2.326 kJ/kg

17 dynamic viscolb/ft-h 0.000413379 kg/m-s

18 density 16.01846 kg/m3

Units 1 2 User Inputs 0

Solve For 6 Calc Results 0

Distilled Wate Shell 2 Mech Detail 0

Raw Water Tubes General Inputs 0

Tube Diameters Tube Gaugesin US SI US Min Max

0.25 0.250 6.35 0.250 18 270.375 0.375 9.53 0.375 14 24

0.5 0.500 12.70 0.500 13 240.625 0.625 15.88 0.625 12 24

0.75 0.750 19.05 0.750 10 241 1.000 25.40 1.000 8 24

1.25 1.250 31.75 1.250 8 241.5 1.500 38.10 1.500 8 24

2 2.000 50.80 2.000 4 24

Units Conversion to SI 19.05 10to US #N/A 24

lb/ft3

This worksheet has intermediate values and radio button links; do not change or delete

Page 31: 02 Heat Exchangers

Wall Thickness

Gauge BWG ISG Brown&Sharp

4 0.238 0.232 0.204

5 0.220 0.212 0.182

6 0.203 0.192 0.162

7 0.180 0.176 0.144

8 0.165 0.160 0.128

9 0.148 0.144 0.114

10 0.134 0.128 0.102

11 0.120 0.116 0.091

12 0.109 0.104 0.081

13 0.095 0.092 0.072

14 0.083 0.080 0.064

15 0.072 0.072 0.057

16 0.065 0.064 0.051

17 0.058 0.056 0.045

18 0.049 0.048 0.040

19 0.042 0.040 0.036

20 0.035 0.036 0.032

21 0.032 0.032 0.029

22 0.028 0.028 0.025

23 0.025 0.024 0.023

24 0.022 0.022 0.020

25 0.020 0.020 0.018

26 0.018 0.018 0.016

27 0.016 0.016 0.014

Tube Parameters based on PitchArrangement Parallel Normal

30 0.866025404 1

45 0.707106781 1.414213562

60 0.5 1.732050808

90 1 1

Standard Shell Sizes, Inside Diameter Shell Thicknessinches inches mm mm inches OD, inches OD, mm

7.981 10.02 7.981 10.02 203 255 0.644 8.625 219.07510.02 12 10.02 12 255 305 0.73 10.75 273.05

12 13.25 12 13.25 305 337 0.75 12.75 323.8513.25 15.25 13.25 15.25 337 387 0.75 14 355.615.25 17.25 15.25 17.25 387 438 0.75 16 406.417.25 19.25 17.25 19.25 438 489 0.75 18 457.2

Page 32: 02 Heat Exchangers

19.25 21.25 19.25 21.25 489 540 0.75 20 50821.25 23.25 21.25 23.25 540 591 0.75 22 558.823.25 25 23.25 25 591 635 0.75 24 609.6

25 27 25 27 635 686 1 26 660.427 29 27 29 686 737 1 28 711.229 31 29 31 737 787 1 30 76231 33 31 33 787 838 1 32 812.833 35 33 35 838 889 1 34 863.635 37 35 37 889 940 1 36 914.437 39 37 39 940 991 1 38 965.239 42 39 42 991 1067 1 40 101642 45 42 45 1067 1143 1 43 1092.245 48 45 48 1143 1219 1 46 1168.448 54 48 54 1219 1372 1 49 1244.654 60 54 60 1372 1524 1 55 139760 66 60 66 1524 1676 1 61 1549.466 72 66 72 1676 1829 1 67 1701.872 78 72 78 1829 1981 1 73 1854.278 84 78 84 1981 2134 1 79 2006.684 90 84 90 2134 2286 1 85 215990 96 90 96 2286 2438 1 91 2311.496 108 96 108 2438 2743 1 97 2463.8

108 120 108 120 2743 3048 1 109 2768.6120 132 120 132 3048 3353 1 121 3073.4

Correlation Coefficients for j-I and f-IPitch LayouNre a1 a2 a3 a4 b1 b2 b3

30 0 1.4 -0.667 1.45 0.519 48 -1 730 10 1.36 -0.657 1.45 0.519 45.1 -0.973 730 100 0.593 -0.477 1.45 0.519 4.57 -0.476 730 1000 0.321 -0.388 1.45 0.519 0.486 -0.152 730 10000 0.321 -0.388 1.45 0.519 0.372 -0.123 745 0 1.55 -0.667 1.93 0.5 32 -1 6.5945 10 0.498 -0.656 1.93 0.5 26.2 -0.913 6.5945 100 0.73 -0.5 1.93 0.5 3.5 -0.476 6.5945 1000 0.37 -0.396 1.93 0.5 0.333 -0.136 6.5945 10000 0.37 -0.396 1.93 0.5 0.303 -0.126 6.5960 0 1.4 -0.667 1.45 0.519 48 -1 760 10 1.36 -0.657 1.45 0.519 45.1 -0.973 760 100 0.593 -0.477 1.45 0.519 4.57 -0.476 760 1000 0.321 -0.388 1.45 0.519 0.486 -0.152 760 10000 0.321 -0.388 1.45 0.519 0.372 -0.123 790 0 0.97 0.667 1.187 0.37 35 -1 6.390 10 0.9 -0.631 1.187 0.37 32.1 -0.0963 6.390 100 0.408 -0.46 1.187 0.37 6.09 -0.602 6.390 1000 0.107 -0.266 1.187 0.37 0.0815 -0.022 6.390 10000 0.37 -0.395 1.187 0.37 0.391 -0.148 6.3

Page 33: 02 Heat Exchangers

Tube Materials and Thermal ConductivitiesAluminum 130 130Brass (75% 72 72Bronze (75 15 15Cr-alloy (0 24 24.4Constantan 14 14Copper 220 220Iron 26 26Magnesium 95 95Molybdenu 64 64Nickel 43 43Steel (1% 20 20Steel (1% C 27 27Steel (18% 12 12Zinc 58 58

Pipe SizesID Pipe Size Nozzle Wt ID Pipe Size Nozzle Wt ID Pipe Sizein in lb in in lb mm DN1.049 1 3 1.049 1 3 26.6446 25

1.049 1.61 1.5 4 1.61 1.5 4 40.894 401.61 2.067 2 6 2.067 2 6 52.5018 50

2.067 3.26 3 12 3.26 3 12 82.804 803.26 4.26 4 17 4.26 4 17 108.204 1004.26 6.357 6 28 6.357 6 28 161.4678 150

6.357 8.329 8 44 8.329 8 44 211.5566 2008.329 10.42 10 56 10.42 10 56 264.668 25010.42 12.39 12 90 12.39 12 90 314.706 30012.39 13.624 14 118 13.624 14 118 346.0496 350

13.624 15.624 16 146 15.624 16 146 396.8496 40015.624 17.624 18 170 17.624 18 170 447.6496 45017.624 19.564 20 202 19.564 20 202 496.9256 50019.564 23.5 24 275 23.5 24 275 596.9 600

Page 34: 02 Heat Exchangers

returns the second column (i.e., US units name)

Page 35: 02 Heat Exchangers

Flange Weightlb lb kg

28 28 1340 40 1861 61 2883 83 38

106 106 48108 108 49

Page 36: 02 Heat Exchangers

148 148 67180 204 93204 204 93210 210 95230 230 105240 240 109260 260 118270 270 123185 185 84300 300 136310 310 141330 330 150360 360 164380 380 173420 420 191460 460 209505 505 230550 550 250590 590 268630 630 286675 675 307720 720 327805 805 366890 890 405

b40.50.50.50.50.5

0.520.520.520.520.52

0.50.50.50.50.5

0.3780.3780.3780.3780.378

Page 37: 02 Heat Exchangers

Nozzle Wtkg

1.3636361.8181822.7272735.4545457.72727312.72727

2025.4545540.9090953.6363666.3636477.2727391.81818

125

Page 38: 02 Heat Exchangers

Use this area to enter raw data. The coefficients are calculated, ready to be pasted (use "Paste Special… Values") onto the corresponding line in the HTF_properties table

To remove an entry from the database, use Tools… Protection… Unprotect, then delete the row with the offending compound

-40 -20 0 20 40 60 80 100 120 140 1600

100

200

300

400

500

600

700

800

Density

Density Predicted

Page 39: 02 Heat Exchangers

Octane 0

Fluid Name Manufacturer

Acetic Acid 0

Butane, n 0

Butyl Alcohol, n- 0

CALFLO™ AF Petro-Canada

CALFLO™ HTF Petro-Canada

CALFLO™ LT Petro-Canada

Chemtherm® 550 Coastal Chemical

Chemtherm® 650 Coastal Chemical

Chemtherm® 700 Coastal Chemical

Diphyl® LANXESS Deutschland GmbH

Diphyl® DT LANXESS Deutschland GmbH

Diphyl® KT LANXESS Deutschland GmbH

Diphyl® THT LANXESS Deutschland GmbH

DOWCAL™ 10/DOWTHERM™ 10 - 30 vol% Dow Chemical

DOWCAL™ 10/DOWTHERM™ 10 - 40 vol% Dow Chemical

DOWCAL™ 10/DOWTHERM™ 10 - 50 vol% Dow Chemical

DOWCAL™ 20/DOWFROST™ 20 - 30 vol% Dow Chemical

DOWCAL™ 20/DOWFROST™ 20 - 40 vol% Dow Chemical

DOWCAL™ 20/DOWFROST™ 20 - 50 vol% Dow Chemical

DOWCAL™ N/DOWFROST™ - 30 vol% Dow Chemical

DOWCAL™ N/DOWFROST™ - 40 vol% Dow Chemical

DOWCAL™ N/DOWFROST™ - 50 vol% Dow Chemical

DOWFROST™ - 30 vol% Dow Chemical

DOWFROST™ - 40 vol% Dow Chemical

DOWFROST™ - 50 vol% Dow Chemical

DOWFROST™ HD - 30 vol% Dow Chemical

DOWFROST™ HD - 40 vol% Dow Chemical

DOWFROST™ HD - 50 vol% Dow Chemical

DOWTHERM™ 4000 - 30 Vol% Dow Chemical

DOWTHERM™ 4000 - 40 Vol% Dow Chemical

DOWTHERM™ 4000 - 50 Vol% Dow Chemical

DOWTHERM™ A Dow Chemical

DOWTHERM™ G Dow Chemical

DOWTHERM™ J Dow Chemical

DOWTHERM™ MX Dow Chemical

DOWTHERM™ Q Dow Chemical

-40 -20 0 20 40 60 80 100 120 140 1600

100

200

300

400

500

600

700

800

Density

Density Predicted

Page 40: 02 Heat Exchangers

DOWTHERM™ RP Dow Chemical

DOWTHERM™ SR-1 - 30 Vol% Dow Chemical

DOWTHERM™ SR-1 - 40 Vol% Dow Chemical

DOWTHERM™ SR-1 - 50 Vol% Dow Chemical

DOWTHERM™ T Dow Chemical

DURATHERM 450 Duratherm, division of Frontier

DURATHERM 600 Duratherm, division of Frontier

DURATHERM 630 Duratherm, division of Frontier

DURATHERM FG Duratherm, division of Frontier

DURATHERM G Duratherm, division of Frontier

DURATHERM Lite Duratherm, division of Frontier

DURATHERM LT Duratherm, division of Frontier

DURATHERM S Duratherm, division of Frontier

DURATHERM XLT-120 Duratherm, division of Frontier

DURATHERM XLT-50 Duratherm, division of Frontier

Dynalene® 600 Dynalene

Dynalene® BioGlycol - 20 Vol% Dynalene

Dynalene® BioGlycol - 40 Vol% Dynalene

Dynalene® BioGlycol - 60 Vol% Dynalene

Dynalene® EG - 20 Vol% Dynalene

Dynalene® EG - 40 Vol% Dynalene

Dynalene® EG - 60 Vol% Dynalene

Dynalene® HC-10 Dynalene

Dynalene® HC-20 Dynalene

Dynalene® HC-30 Dynalene

Dynalene® HC-40 Dynalene

Dynalene® HC-50 Dynalene

Dynalene® HF Dynalene

Dynalene® HF-LO Dynalene

Dynalene® HT Dynalene

Dynalene® LO-170 Dynalene

Dynalene® LO-230 Dynalene

Dynalene® MV Dynalene

Dynalene® PG - 20 Vol% Dynalene

Dynalene® PG - 40 Vol% Dynalene

Dynalene® PG - 60 Vol% Dynalene

Dynalene® PG - 80 Vol% Dynalene

Dynalene® SF Dynalene

Ethyl Alcohol 0

Glycerol 0

Hexane 0

Marlotherm® FP Sasol

Marlotherm® LH Sasol

Marlotherm® N Sasol

Marlotherm® SH Sasol

Methyl Alcohol 0

MultiTherm® 503 MultiTherm

MultiTherm® FF-1 MultiTherm

MultiTherm® IG-1 MultiTherm

MultiTherm® IG-4 MultiTherm

Page 41: 02 Heat Exchangers

MultiTherm® OG-1 MultiTherm

MultiTherm® PG-1 MultiTherm

MultiTherm® ULT-170 MultiTherm

MultiTherm® WB+14 MultiTherm

MultiTherm® WB-22 MultiTherm

MultiTherm® WB-40 MultiTherm

MultiTherm® WB-5 MultiTherm

MultiTherm® WB-58 MultiTherm

Octane 0

Paratherm CR™ Paratherm

Paratherm GLT™ Paratherm

Paratherm HE™ Paratherm

Paratherm HR™ Paratherm

Paratherm LR™ Paratherm

Paratherm MG™ Paratherm

Paratherm MR™ Paratherm

Paratherm NF™ Paratherm

Pentane 0

Petro-Therm™ Petro-Canada

Propyl Alcohol, i- 0

Propyl Alcohol, n- 0

PURITY™ FG Petro-Canada

SYLTHERM™ 800 Dow Chemical

SYLTHERM™ HF Dow Chemical

SYLTHERM™ XLT Dow Chemical

Thermalane® 600 Coastal Chemical

Thermalane® 800 Coastal Chemical

Therminol™ 55 Solutia

Therminol™ 59 Solutia

Therminol™ 62 Solutia

Therminol™ 66 Solutia

Therminol™ 72 Solutia

Therminol™ 75 Solutia

Therminol™ D-12 Solutia

Therminol™ LT Solutia

Therminol™ VLT Solutia

Therminol™ VP-1 Solutia

Therminol™ VP-3 Solutia

Therminol™ XP Solutia

Water NA

XCELTHERM® 445FP Radco

XCELTHERM® 500 Radco

XCELTHERM® 600 Radco

XCELTHERM® HT Radco

XCELTHERM® LV1 Radco

XCELTHERM® MK1 Radco

XCELTHERM® XT Radco

Page 42: 02 Heat Exchangers
Page 43: 02 Heat Exchangers

Use this area to enter raw data. The coefficients are calculated, ready to be pasted (use "Paste Special… Values") onto the corresponding line in the HTF_properties table

To remove an entry from the database, use Tools… Protection… Unprotect, then delete the row with the offending compound Units that the original data are in:

Temperature

Density

Specific Heat

Thermal Conductivity

Viscosity

Heat of Vaporization

Fluid Name: Octane

Manufacturer:Description: pure component

Operating range:

Source: Yaw's Handbook, 2003

Liquid

Temp. Density Sp. Heat

°C kg/cu.m. KJ/kg-°KEnter values at SIX temperatures -->>> -20 732.5191 2.128494

20 702.5186 2.21822360 670.5874 2.315248

100 636.161 2.435187120 617.7531 2.508629140 598.3474 2.593657

The charts graph the input and predicted data. Large deviations may indicate a data entry error

-40 -20 0 20 40 60 80 100 120 140 1600

100

200

300

400

500

600

700

800

Density

Density Predicted

-40 -20 0 20 40 60 80 100 120 140 1600

0.5

1

1.5

2

2.5

3

Specific Heat

Specific Heat Predicted

degrees F

lb/cu.ft.

Btu/lb-F = cal/g-C

Btu/ft-hr-F

cP

Btu/lb

Page 44: 02 Heat Exchangers

pure component 0 0

Description Temp Use Range (deg C)

Liquid

Low High

pure component 0 0

pure component 0 0

pure component 0 0

99.9% pure base oils, crystal-clear, free of aromatic compounds with additives 15 315

99.9% pure base oils, crystal-clear, free of aromatic compounds with additives 15 326

Synthetic poly-alpha-olefins 4 288

Premium oil more thermally stable than mineral oils 93.33333333 315.5555556

Premium high temperature oil resists oxidation 10 343.3333333

Premium high temperature single compound formulation 37.77777778 351.6666667

High-temperature HTF based on diphenyl oxide/diphenyl eutectic for liq and vap phase 13 400

Isomeric ditolyl ethers with broad spectrum of applications in liq phase -30 330

Synthetic mixture of isomeric bynzyl toluenes with high thermal stability -45 350

Partially hydrogenated terphenyls for pressureless high temperature applications 0 345

Ethylene glycol with inhibitor package -10 170

Ethylene glycol with inhibitor package -20 170

Ethylene glycol with inhibitor package -35 170

Propylene glycol with inhibitor package 0 170

Propylene glycol with inhibitor package -15 170

Propylene glycol with inhibitor package -30 170

Propylene glycol with inhibitor package, food grade -10 100

Propylene glycol with inhibitor package, food grade -20 100

Propylene glycol with inhibitor package, food grade -30 100

Propylene glycol with inhibitor package -10 100

Propylene glycol with inhibitor package -20 100

Propylene glycol with inhibitor package -30 100

Propylene glycol with inhibitor package, dyed bright yellow -10 100

Propylene glycol with inhibitor package, dyed bright yellow -20 100

Propylene glycol with inhibitor package, dyed bright yellow -30 100

Ethylene glycol with inhibitors, dyed fluorescent orange -10 120

Ethylene glycol with inhibitors, dyed fluorescent orange -20 120

Ethylene glycol with inhibitors, dyed fluorescent orange -30 120

Biphenyl and diphenyl oxide eutectic mixture - liquid phase properties 15 400

Di- and tri-aryl compounds mixture -6 360

Mixture of isomers of an alkylated aromatic -80 315

Mixture of alkylated aromatics -20 330

Mixture of diphenylethane and alkylated aromatics -35 330

-40 -20 0 20 40 60 80 100 120 140 1600

100

200

300

400

500

600

700

800

Density

Density Predicted

-40 -20 0 20 40 60 80 100 120 140 1600

0.5

1

1.5

2

2.5

3

Specific Heat

Specific Heat Predicted

Page 45: 02 Heat Exchangers

Synthetic diaryl alkyl liquid 10 350

Ethylene glycol with inhibitors, dyed fluorescent pink -10 120

Ethylene glycol with inhibitors, dyed fluorescent pink -20 120

Ethylene glycol with inhibitors, dyed fluorescent pink -30 120

Mixture of C14-C30 alkyl benzenes -10 288

Refined oil, non-aromatic 0 230

Refined and hydrotreated paraffinic oils, non-toxic and non-reportable 0 315

Refined and hydrotreated paraffinic oils, non-toxic and non-reportable 20 332

Refined paraffinic oils with additives, food grade 20 332

Polyalkylene glycol based fluid with additives 20 260

Same as Duratherm 600, but with fewer additives 0 315

Refined oil, non-aromatic -35 315

Refined oil, non-aromatic especially resistant to oxidation -40 340

Refined silocone oil, for cryogenic applications, food & pharma -84 65

Refined silocone oil, for cryogenic applications, food & pharma -46 176

Silicone-based product with enhanced resistance to oxidation 70 288

Produced from corn, better performance than propylene glycol -6.66666667 115.5555556

Produced from corn, better performance than propylene glycol -17.7777778 115.5555556

Produced from corn, better performance than propylene glycol -28.8888889 115.5555556

Inhibited ethylene glycol -6.66666667 121.1111111

Inhibited ethylene glycol -17.7777778 121.1111111

Inhibited ethylene glycol -34.4444444 121.1111111

Aqueous-based, engineered for low temperature applications -10 60

Aqueous-based, engineered for low temperature applications -20 60

Aqueous-based, engineered for low temperature applications -30 60

Aqueous-based, engineered for low temperature applications -40 60

Aqueous-based, engineered for low temperature applications -50 60

Biodegradable aliphatic hydrocarbon blend, food grade -80 162.7777778

Aliphatic hydrocarbon blend, non-toxic, odorless -73 177

Synthetic organic hydrocaron 20 177

Aliphatic hydrocarbon blend -40 205

Aliphatic hydrocarbon blend 0 205

Biodegradable hydrocarbon blend -112.222222 162.7777778

Propylene glycol with corrosion inhibitors -6.66666667 121.1111111

Propylene glycol with corrosion inhibitors -6.66666667 121.1111111

Propylene glycol with corrosion inhibitors -28.8888889 121.1111111

Propylene glycol with corrosion inhibitors -28.8888889 121.1111111

Synthetic alkylated aromatics 0 315

pure component 0 0

pure component 0 0

pure component 0 0

Isoparaffinic chemical structure, clear liquid, bland odor 60 300

Skynthetic, organic, heat transfer medium 0 280

Skynthetic, organic, heat transfer medium, ideal 150 to 300 deg C range 20 300

Skynthetic, organic, heat transfer medium 20 340

pure component 0 0

Paraffinic hydrocarbon -5 260

Flushing Fluid -18 260

White mineral oil -20 288

White mineral oil -10 316

Page 46: 02 Heat Exchangers

Hydrocracked mineral oil with oxidation inhibitor/stabilizer 0 290

White mineral oil, food grade -20 316

Hydrocarbon blend -112 38

Water based, no flash point, for low temperature performance -10 121

Water based, no flash point, for low temperature performance -30 121

Water based, no flash point, for low temperature performance -40 121

Water based, no flash point, for low temperature performance -20 121

Water based, no flash point, for low temperature performance -50 121

pure component 0 0

Synthetic hydrocarbon blend -95.5555556 218.3333333

Alkylated aromatic for closed loop liquid phase heating 35 301.6666667

Hydrotreated heavy paraffinic distillate - mineral oil 52.77777778 310

Alkylated aromatic, for closed loop heating 25 357.2222222

Paraffinic hydrocarbon, for closed loop heating and cooling -49.4444444 248.8888889

Linear alkene, food grade 2.222222222 304.4444444

Linear alkene, fully saturated -3.88888889 248.8888889

Hydrotreated mineral oil, food grade 35.55555556 332.2222222

pure component 0 0

Mixture of severely hydrotreated and hydrocracked petroleum 25 315

pure component 0 0

pure component 0 0

Pure base oil, food grade, with additives 4 326

Silicone fluid - dimethyl polysiloxane -40 400

Silicone fluid - dimethyl polysiloxane -73 260

Silicone fluid - dimethyl polysiloxane -100 260

Premium heat transfer fluid, non-toxic, environmentally friendly 65.55555556 315.5555556

Premium heat transfer fluid, non-toxic, environmentally friendly 65.55555556 315.5555556

Alkyl aromatic derivatives -25 290

Mixture of diphenyl alkanes -45 315

Mixture of di- and tri-isopropyl biphenyl -20 325

Hydrogenated terphenyl and polyphenyls 0 345

Mixture of diphenyl ether, terphenyl, biphenyl, and phenanthrene -10 380

Mixture of terphenyl, quaterphenyl, and phenanthrene 80 385

Hydrotreated heavy naphtha (petroleum) -85 230

Diethyl benzene -75 315

Mixture of methyl cyclohexane and trimethyl pentane -115 175

Mixture of diphenyl ether and biphenyl 12 400

Mixture of cyclohexylbenzene and bicyclohexyl 2 330

White mineral oil -20 315

City water 4 150

Hydroprocessed napthenic mineral oil; high flash point 20 288

Hydrogenated polyalpha olefin -62 260

Hydroprocessed paraffinic white mineral oil 50 343

Synthetic alkyl aromatic -37 349

Diphenyl ethane and diphenyl oxide mixture 7 371

Diphenyl oxide and diphenyl 15 400

Synthetic alkyl aromatic -57 343

Page 47: 02 Heat Exchangers
Page 48: 02 Heat Exchangers

Use this area to enter raw data. The coefficients are calculated, ready to be pasted (use "Paste Special… Values") onto the corresponding line in the HTF_properties table

Units that the original data are in:

5.16 38.59946769

<-- Already in the database

pure component Heat Vap 302.38

°C minimum FP 13.33333333

°C maximum BP 125.6666667

Yaw's Handbook, 2003 Mol Wt 114.231

Values converted to SI units for the htf_properties tableThermal Vapor Vapor ThermalConduct. Visc. Pressure Temperature Density Sp. Heat Conduct.W/m-°K cP mm Hg deg C deg K kg/m3 kJ/kg-K W/m-K0.14198 1.007647 0.679361559745 -20 253.15 732.5191 2.128494 0.141980143

0.130534 0.559145 10.58 20 293.15 702.5186 2.218223 0.1305341170.118449 0.365747 77.80815537732 60 333.15 670.5874 2.315248 0.1184490830.105725 0.259007 349.69 100 373.15 636.161 2.435187 0.1057250410.099123 0.220733 648.616631807 120 393.15 617.7531 2.508629 0.0991233920.092362 0.188481 1,121.74 140 413.15 598.3474 2.593657 0.092361991

-40 -20 0 20 40 60 80 100 120 140 1600

0.5

1

1.5

2

2.5

3

Specific Heat

Specific Heat Predicted

-40 -20 0 20 40 60 80 100 120 140 1600

0.02

0.04

0.06

0.08

0.1

0.12

0.14

0.16

Thermal Conductivity

Thermal Conductivity Predicted

-40 -20 0 20 40 60 80 100 120 140 160

0.1

1

10

Viscosity

Viscosity Predicted

degrees F degrees C

lb/cu.ft. kg/cu.m.

Btu/lb-F = cal/g-C kJ/kg-K

Btu/ft-hr-F W/m-K

cP centi Stokes = mm2/s

Btu/lb kJ/kg

Page 49: 02 Heat Exchangers

Antoine Coefficients Viscosity Constants Density = mt(deg C) + b thermal conductivity

A B C A B C m b m

7.09576 1455.31 219.703252 -6.833946 3563.967 276.8476 -0.836933 718.2331 -0.000310324

LOG(VP, mm Hg) = A + B / ((t, deg C) + C) cP = EXP(A+B/((T, deg K)+C)) kg/m3 = mt(deg C) + b W/m-K = mt(deg C) + b

A B C m b m

7.612801042 1673.346503 235.6539233009 -1.77875697 139.628222 -239.507339 -1 1068.666667 0

6.832505648 946.4096141 240.0761026727 -5.3689507 1681.687142 167.1521733 -1.03186377 601.6370107 -0.000501779233

7.911635485 1619.041401 204.0887995323 -9.94017218 4947.168858 156.3930704 -0.8 810 -0.0001730735

2.262303417 59.86061988 -25.9558051073 -2.81012363 862.7299166 -172.158588 -0.61886679 876.7097415 -5.39694403E-05

2.145717493 63.31608757 -24.7273511364 -3.01949171 971.1670361 -162.441888 -0.63704744 880.3808274 -5.24038822E-05

-3.07699041 295.8073505 -314.661081699 -2.94432736 771.280208 -150.474936 -0.65896583 829.7925355 -8.58260809E-05

-37.9837715 123237.0069 -3346.0970147 -2.72003397 756.1805202 -187.060596 -0.63433102 909.7844542 -7.53018074E-05

9.485063877 4973.223153 486.5437468684 -3.88723617 1148.415359 -77.458893 -0.7967977 998.9693879 -0.000130758215

28.97978432 69967.71548 2296.207979748 -2.85235243 801.5978566 -167.466984 -0.69941173 1043.823266 -0.000103606742

7.202211465 1946.567862 193.6808400359 -2.95622194 695.510584 -136.279632 -1.02463504 1094.600973 -0.000163868613

-5.09981535 4803.754006 -906.241700528 -2.63441952 587.9922893 -159.411101 -0.87116438 1047.892466 -0.000144863014

8.824543716 3748.716733 336.9459257155 -3.29046723 883.4734248 -119.018457 -0.78787671 1021.964384 -0.000132260274

35.7643154 93078.03163 2471.749350311 -2.56805621 631.4445755 -209.147287 -0.76328811 1038.670391 -9.93216281E-05

-4.18081142 909.7339247 -107.595417 -0.69488127 1059.327704 0.000323693931

-4.72704655 1202.565787 -83.1814303 -0.72116095 1073.662445 0.000282532982

-5.29129088 1555.126505 -56.1413767 -0.74828496 1087.066843 0.000250237467

-2.86784498 390.4369421 -193.613817 -0.74307594 1043.921719 0.000306700702

-2.20133794 260.5827978 -221.938677 -0.79859604 1053.05786 0.000220421187

-2.66533983 403.308763 -202.562555 -0.8417358 1060.734525 0.000146139119

-3.08252386 464.3995388 -181.185017 -0.64370968 1040.862097 0.000527580645

-2.87005695 429.3103577 -194.091739 -0.69306452 1049.905645 0.000396129032

-3.18080553 558.8975154 -181.131448 -0.73548387 1056.854839 0.000273064516

-3.045242 463.8105983 -181.232182 -0.65730675 1042.759627 0.000492448027

-2.9578147 466.7384919 -188.559297 -0.64887019 1046.962568 0.000474056928

-3.42416369 657.0851132 -167.978944 -0.65769786 1050.3615 0.000385743228

-3.045242 463.8105983 -181.232182 -0.64224014 1052.615074 0.000492448027

-2.9578147 466.7384919 -188.559297 -0.63581858 1060.217444 0.000474056928

-3.42416369 657.0851132 -167.978944 -0.64961462 1067.103239 0.000385743228

-3.99338037 832.5661743 -119.083818 -0.58424609 1064.749586 0.000694744526

-4.4123843 1071.201128 -98.7745604 -0.6082127 1080.977479 0.000627813575

-4.25027294 991.8803997 -118.108745 -0.61823431 1094.54251 0.000578445276

8.728975338 3828.105374 392.5107134818 -5.48503015 2637.359604 105.6665045 -0.98934972 1091.508696 -0.00016

28.14307754 70966.91185 2506.647170731 -4.208744 1446.746639 -80.3558975 -0.77471755 1062.346004 -0.000115799279

59.09740797 290462.7583 4950.074020188 -3.07063398 638.520693 -77.403951 -0.91493913 873.6790725 -0.000210713043

-416.758373 15972102 -38392.3120759 -4.54701255 1505.768212 -91.4516506 -0.77585921 979.0293996 -0.000105072464

25.63533305 53251.60693 2053.16400104 -3.39154275 743.091582 -135.906784 -0.76281754 982.1280197 -0.000148727623

-40 -20 0 20 40 60 80 100 120 140 1600

0.5

1

1.5

2

2.5

3

Specific Heat

Specific Heat Predicted

-40 -20 0 20 40 60 80 100 120 140 1600

0.02

0.04

0.06

0.08

0.1

0.12

0.14

0.16

Thermal Conductivity

Thermal Conductivity Predicted

-40 -20 0 20 40 60 80 100 120 140 160

0.1

1

10

Viscosity

Viscosity Predicted

Page 50: 02 Heat Exchangers

-15.6439238 25860.13955 -1755.47992696 -3.19903031 983.1702242 -141.828205 -0.7434472 1046.470497 -0.000129668737

-3.99338037 832.5661743 -119.083818 -0.54151408 1055.199489 0.000694744526

-4.4123843 1071.201128 -98.7745604 -0.54963153 1068.649603 0.000627813575

-4.25027294 991.8803997 -118.108745 -0.54397093 1078.978861 0.000578445276

20.31322658 24800.78469 1071.483567672 -3.37173363 1025.670554 -139.929331 -0.68913684 887.0437895 -0.000220727273

-6.65052916 8198.941169 -1156.00701017 -2.74761032 674.2680072 -150.950719 -0.67776556 874.5009276 -7.52836084E-05

-7.66614364 5665.648991 -900.109636171 -2.90618465 903.5619303 -168.873971 -0.67433792 866.3944924 -5.06875118E-05

24.83466474 45060.34506 1649.092109238 -2.99273743 972.3144213 -160.441312 -0.6729646 870.1405299 -5.29425557E-05

24.83466474 45060.34506 1649.092109238 -2.99273743 972.3144213 -160.441312 -0.6729646 870.1405299 -5.29425557E-05

2.135874547 189.0775653 17.01391236327 -2.13317423 859.946884 -168.196304 -0.54570512 938.153151 -0.000149791461

-7.66614364 5665.648991 -900.109636171 -2.90618465 903.5619303 -168.873971 -0.67433792 866.3944924 -5.06875118E-05

14.90562541 16265.92913 1013.657369496 -3.01482131 794.6463678 -152.129254 -0.68415812 827.0379206 -8.50180505E-05

2.629939501 181.8693003 58.26576227891 -3.82938429 3727.450185 178.4719478 -0.46997219 976.7418617 -0.000201070574

-3.01120449 165.7660841 -95.9293394501 -1.9215881 442.3147778 -120.787412 -0.49885816 847.4328427 -6.53313347E-05

5.577631845 1026.16852 178.1814169594 -2.66100775 567.1764897 -137.006506 -0.96414298 848.4501738 -9.7898454E-05

-1.97270453 2181.196089 29.0849155 -1 983 -0.000177331627

-2.83906455 403.1390392 -179.040208 -0.5605716 1029.826048 0.000753011027

-1.76210182 259.4530877 -209.449865 -0.64190891 1046.823369 0.000493144186

-2.12735955 490.7649224 -175.45123 -0.70769845 1058.280485 0.000233571264

-3.51929213 637.3660848 -135.037251 -0.52459314 1045.928633 0.000890947613

-3.92835821 860.2756579 -122.034579 -0.58864285 1080.853276 0.000694526026

-4.39901578 1040.087431 -122.076833 -0.623489 1109.9764 0.000518206793

-4.27578767 1294.151729 -23.8949564 -0.69130435 1363.173913 0.001

-5.29105882 2948.838335 163.7360489 -0.498 1248.8 0.000954

-0.5122831 242.6453163 -157.837138 -0.59558824 1282.941176 0.0011

-2.98689604 974.823436 -58.2554382 -0.7 1330 0.0009875

-8.68421954 4625.644362 162.8836058 -0.55 1362.5 0.00098

10.47024835 4350.477961 388.8685901874 -11.0043264 7574.14569 365.4554434 -0.70241532 816.7797164 -0.000197550135

-3.80185344 919.1524433 -81.3856983 -0.75981804 777.6671466 -0.0002

-3.36183913 1050.837594 -143.20005 -0.71592357 1058.509554 -0.000131866242

-4.00909241 975.0043208 -100.530572 -0.50167515 784.007404 -0.0002

-3.18052868 851.7140453 -146.012607 -0.69815357 814.9279256 -0.0002

-27.8705129 38860.64873 -1417.67686805 -4.49525801 1230.87547 -17.8291423 -0.77262148 860.8387708 -0.000237739723

-3.74394592 656.3234212 -145.485726 -0.53046604 1028.417964 0.000828174911

-4.05786883 747.1472763 -159.321194 -0.60831178 1045.762586 0.000552562241

-4.27097369 936.2342355 -150.361442 -0.65216852 1056.382866 0.000298991805

-4.61030436 1143.830819 -143.218804 -0.79010375 1069.012698 2.640104237E-06

-3.48506455 1205.757335 -123.228873 -0.67317309 890.3946335 -7.98064204E-05

8.242261841 1664.521156 232.3397814505 -11.706753 8152.450017 393.0423698 -0.859 806.45 0

-38.7259008 37120.5808 525.3966053 -2.6132 1293.347 0

6.703282362 1088.113137 215.7520677693 -6.66531604 3106.126473 275.2299026 -0.920173 678.1547178 -0.000367941523

0.710759026 588.6311478 -607.782559027 -4.46280906 1669.133043 -79.9072873 -0.65682095 861.6443362 -6.09013398E-05

-2.76497138 699.2381518 -125.207148 -0.80729276 1013.83001 -0.00011521511

-4.37009218 1719.233593 -67.8658053 -0.67166842 890.1280168 -8.13221406E-05

-3.14384109 1006.845383 -143.852661 -0.71437566 1058.298006 -0.000130902413

7.974904035 1515.292988 232.9925144622 -3.74186653 790.3959928 -48.5241917 -0.925 810.1833333 0

-3.71515205 1037.386654 -112.624039 -0.65445205 806.9452055 -6.17808219E-05

7.515668958 3644.821025 270.446634655 -3.3434809 955.1227381 -161.065638 -0.64814403 921.0920945 -7.20141513E-05

-2.89037717 907.4313825 -174.35564 -0.52528383 871.6566949 -7.58821409E-05

-3.23842923 1030.806139 -162.583226 -0.7102096 877.6741041 -7.31778229E-05

Page 51: 02 Heat Exchangers

-2.66844708 863.5163865 -172.933185 -0.53597908 871.6843302 -3.65203548E-05

-3.15870057 876.1353531 -167.030762 -0.42033079 881.6658614 -7.23081212E-05

-1.69617834 283.955002 -121.548471 -0.7704 860.46 -0.0002

-27.5351301 49896.87604 1485.7617 -0.47945946 1200.678378 0.001

-1.54976022 217.1210049 -191.167196 -0.49828571 1285.352381 0.001

-1.19730032 266.8391189 -166.715718 -0.57375 1325.51875 0.001079375

-1.0665069 193.5885813 -191.633517 -0.52806452 1249.575806 0.001

-2.01954397 517.6446589 -128.383873 -0.6 1365 0.001032571429

7.09576455 1455.313737 219.7032523647 -6.83394648 3563.967105 276.8475889 -0.83693261 718.2330701 -0.000310323647

5.922006034 1219.837987 210.0557231748 -2.78483901 568.89108 -70.8208174 -1.00816159 848.287022 -7.65212871E-05

8.357881974 3690.191938 318.4911917714 -3.77429163 1137.446138 -140.259573 -0.69564974 892.8100911 -0.000141299938

-4.59859581 1009.038677 -476.955045898 -3.19587269 1055.906811 -156.107582 -0.64127846 875.94107 -7.54451637E-05

19.17638732 25786.04954 1240.253275717 -3.73340177 1159.419592 -121.829193 -0.76651297 971.0799153 -9.94852119E-05

7.498946283 2118.740944 241.805103732 -4.05132143 992.5831924 -80.5601433 -0.73774932 777.637054 -7.74155305E-05

15.56732425 14491.9443 814.9374854432 -2.99507893 757.8405527 -148.641263 -0.56305007 809.5163136 -8.53551655E-05

-2.79779088 620.4391947 -163.735706 -0.73934467 816.4099844 -5.50920278E-05

3.518231204 568.5080193 65.24581768838 -11.0429218 7675.283643 244.6277778 -0.6627339 897.731878 -5.09146072E-05

6.815001077 1036.921935 227.6362861892 -4.95789137 1823.414442 215.8151637 -0.95760086 644.49611 -0.000241320903

-2.60201382 745.2365509 -188.098093 -0.63255801 878.7054 0

8.070898891 1562.677224 218.6912380682 -13.528855 8140.334312 275.4940161 -0.81794667 801.5741333 -9.24639247E-05

8.060264217 1608.423767 213.4908138165 -9.37387247 4628.137228 160.10672 -0.78666667 819.4333333 0.000184927849

-3.59241473 600.9665436 -417.393233539 -3.02443463 966.3912742 -162.616211 -0.67728573 864.7274491 -5.63706678E-05

5.901474836 992.7441571 125.6403617999 -6.1614167 4125.909563 190.8926925 -0.98671661 957.6492123 -0.00018817637

16.10646624 14388.57618 864.6650652821 -4.13455407 1402.53671 2.082260641 -1.01099585 891.9792531 -0.000247993736

6.378797206 1168.298992 159.4351675271 -3.69360075 958.0562569 -54.5892356 -1.02722364 875.8149521 -0.00023428754

461.7898719 15857160.59 34222.77314643 -3.02053199 847.1828181 -177.280191 -0.7076498 922.4704643 -0.00020071581

44.29307796 139253.2253 2981.159095466 -2.88595158 889.1565539 -145.172424 -0.65904521 826.5830474 -0.00010503089

8.317509603 3488.543552 290.5608400942 -3.31866082 932.6133869 -160.748737 -0.69514286 885.8071429 -0.000116571429

7.097882648 2163.093672 223.7400408742 -3.74083482 1121.909895 -96.0447395 -0.77285714 989.8785714 -0.000101428571

8.025677723 3088.759214 267.4715649728 -4.4801125 1412.178507 -112.827625 -0.76952381 970.7047619 -9.86666667E-05

8.491663596 3904.17307 337.0985942979 -2.9608184 798.1314837 -188.788157 -0.70095238 1022.809524 -7.90952381E-05

73.38287395 710633.5074 9808.291686869 -4.53930814 1495.139149 -83.805334 -0.90979592 1097.94966 -0.000121428571

8.208942696 3443.037294 303.3211522193 -4.97382691 2294.824764 4.200482262 -0.80095238 1109.219048 -8.92380952E-05

6.809548245 1502.086534 190.3400131344 -4.2424707 1070.61217 -58.8354033 -0.77828571 774.6171429 -0.000168657143

7.934489338 2207.443066 255.7319204318 -4.45707701 1355.585653 16.35934932 -0.90647059 880.3186275 -0.000199294118

6.907778119 1331.290532 231.3813039053 -4.8590801 1392.526697 19.0588276 -0.87885714 763.1219048 -0.000212457143

7.103625061 1867.193197 185.1089109065 -4.08355007 1380.238329 -35.3400953 -0.92714286 1089.468571 -0.000153309524

8.51891149 2824.42195 258.0411205736 -5.23102849 2426.381031 97.63429134 -0.85238095 959.8952381 -0.000133809524

7.792286358 2928.893565 238.1674681764 -3.26909023 948.0820446 -162.954329 -0.65885714 891.8371429 -9.46571429E-05

8.027644417 1706.134188 231.492183432 -3.63376689 544.0166779 -144.088981 -0.45804255 1006.346546 0.00117517497

16.78295974 15071.00822 735.1176662401 -2.99332524 961.1818081 -171.127745 -0.48941719 875.5651989 -6.21986571E-05

13.38609757 9928.193743 645.8912869417 -3.25910508 832.2063505 -139.374148 -0.61042018 802.2908324 -5.59289885E-05

8.298585459 3733.137191 303.7074837571 -3.85114017 1092.541329 -146.328925 -0.60779676 863.9762751 -8.08511295E-05

18.68594384 22435.37895 1102.371200423 -3.10782307 665.0131622 -170.702099 -0.71954928 1016.995025 -8.59580271E-05

-4.00273756 1273.691552 -65.5433391 -0.83460737 1080.229542 -0.000152096189

7.116971045 1876.734969 185.9894100865 -4.11860533 1398.010591 -34.9854328 -0.95652688 1092.587897 -0.000157889271

11.59286273 7224.243307 549.2732776366 -3.78336706 1086.942692 -92.3971227 -0.72908055 1011.049988 -0.000154215681

Page 52: 02 Heat Exchangers
Page 53: 02 Heat Exchangers

Intermediate

Visc. CalcsmPa-s 0.66639

1.0076470.5591450.3657470.259007 0.8260860.2207330.188481

-40 -20 0 20 40 60 80 100 120 140 160

0.1

1

10

Viscosity

Viscosity Predicted

Page 54: 02 Heat Exchangers

thermal conductivity heat capacity

b m b

0.136418 0.002864 2.166097 13.33333 125.6667 114.231 302.38

W/m-K = mt(deg C) + b kJ/kg-K = mt(deg C) + b Flash Point Boiling Point Type Molecular Wt Heat Vap

b m b kJ/kg

0.171342765 0.003839894 1.954438114 39 118.1 60.05 395

0.116788454 0.003501872 2.30307202 -59.4444444 -0.44444444 58.123 386.116

0.174804235 0.011693134 2.091406286 29 117.5 74.12 581

0.143663138 0.003298466 1.837019115 225 365 Paraffinic

0.144038876 0.003298466 1.837019115 231 370 Paraffinic

0.143494203 0.003607233 1.991504054 176 318

0.132608652 0.003488203 1.853962889 172.7777778 273.3333333

0.128359337 0.003738526 1.311796705 135 270

0.132878515 0.00353342 1.482420675 212.7777778 360

0.14649635 0.002683942 1.503723844 115 257

0.137297945 0.002755479 1.530417808 135 284

0.131586301 0.00295 1.53 146 290

0.124055866 0.003379689 1.535150838 190 352

0.458461917 0.002755673 3.617656992

0.421857696 0.003258047 3.439544415

0.388855409 0.003765699 3.252663149

0.449730696 0.002689215 3.809919166

0.410417358 0.003255903 3.659334184

0.373507552 0.003811104 3.487972772

0.439799194 0.002659677 3.812653226

0.40073871 0.003177419 3.670725806

0.364994355 0.003740323 3.499346774

0.435254985 0.002747306 3.793442087

0.385735439 0.003307851 3.635184235

0.34400839 0.003859238 3.45484651

0.435254985 0.002854306 3.72730123

0.385735439 0.003692149 3.526815765

0.34400839 0.004518696 3.300517727

0.434742579 0.002890719 3.57107056

0.395886143 0.003427839 3.375418205

0.35847756 0.003954283 3.169790575

0.1419 0.002946733 1.500876167 113 257 Biphynyl, Diphenyl Oxide

0.128720883 0.003497055 1.475642728 280 552 Di- and Tr-aryl Ethers

0.13231658 0.003626696 1.803964638 57 181 Alkylated Aromatic

0.125028986 0.00325 1.545 165 328

0.124237623 0.003030103 1.592794559 120 267 Diphenylethane, Alkylated Aromatic

-40 -20 0 20 40 60 80 100 120 140 160

0.1

1

10

Viscosity

Viscosity Predicted

Page 55: 02 Heat Exchangers

0.133973706 0.002974845 1.56102795 194 353

0.434742579 0.002838165 3.59049635

0.395886143 0.003353269 3.402875508

0.35847756 0.003864655 3.206134332

0.138850909 0.002981091 1.902723636 188 345

0.144955197 0.003016058 2.020887613 150 250 Paraffinic

0.143173856 0.003298625 1.838347711 224 380 Paraffinic

0.143843376 0.003279414 1.844734936 229 380 Paraffinic

0.143843376 0.003279414 1.844734936 227 410 Paraffinic

0.169882509 0.001801916 1.906362788 267 370 Polyalkylene Glycol

0.143173856 0.003298625 1.838347711 224 380

0.142635379 0.003433899 2.018658123 165 325 Paraffinic

0.136020796 0.001703006 1.628677445 323 500 Silicone

0.135741139 0.002183449 2.020765525 98.8 500

0.135596528 0.002661436 2.018687927 98.8 500

0.157467275 0.001885349 1.234212603 315 315

0.472767264 0.005824645 4.008294404

0.384944391 0.005872 3.630751717

0.314607083 0.005793626 3.258311092

0.47398383 0.002333291 3.758891909

0.395172539 0.00342636 3.375738946

0.332807973 0.004466716 2.953250031

0.505 0.003 3.28

0.5021 0.00228 3.177

0.498 0.002691176 3.019117647

0.4895 0.0023 2.89

0.484333333 0.002 2.67

0.124287618 0.004549249 1.9236329 61 175

0.1126 0.0038003 2.019123117 61 191

0.13327172 0.003725669 1.474658599 200 385

0.1165 0.0038 1.804 77 223

0.151 0.0038 1.934 110 273

0.137610158 0.003541716 1.723592974 53 176

0.467931901 0.002197019 3.931385769

0.382952985 0.003291642 3.637705029

0.312431647 0.004409978 3.25285147

0.257535324 0.005051835 2.76340154

0.136406716 0.00365388 1.89392488 180 330

0.181727175 0.015024631 2.055040937 13 78.4 46.07 842

0.28384054 0.005167707 2.286949783 160 290 92.1 663

0.130347409 0.003088894 2.169122258 -21.6666667 68.77777778 86.177 334.944

0.134395859 0.003764921 1.837028015 216 340

0.133746065 0.003347849 1.547460651 130 278

0.136780693 0.003665268 1.892413431 180 330

0.133056663 0.003706191 1.476820567 200 385

0.21461114 0.004318385 2.413112023 12 64.7 32.04 1100

0.142594749 0.003810616 2.024105023 154 338

0.129047046 0.004336149 1.723659332 160 271

0.139956839 0.003641539 1.81319481 228 374

0.135598783 0.0045476 1.863526031 227 411 Mineral Oil

Page 56: 02 Heat Exchangers

0.13951144 0.003563134 1.794283375 235 373 Mineral Oil

0.134426965 0.003632856 1.805435793 171 349 Mineral Oil

0.1377 0.003502353 1.72495098 53 176

0.506 0.00252973 3.280477477

0.499 0.002228571 3.041428571

0.486378125 0.002195 2.891425

0.505 0.002267742 3.181403226

0.484457143 0.00208 2.662

0.136418283 0.002863944 2.166096891 13.33333333 125.6666667 114.231 302.38

0.141642551 0.003717397 1.846334475 40 180

0.132857923 0.003205203 1.874047828 182 500

0.134253087 0.00364665 1.811423332 221 500 Mineral Oil

0.122345728 0.002220555 1.899415046 160 335

0.152635898 0.003873995 1.92479404 54 200

0.135057086 0.002028552 2.333766392 149 400

0.134181881 0.001919758 2.338631894 135 500

0.105761083 0.005286616 1.718087749 157 500 Mineral Oil

0.153717492 0.003160654 2.196723796 -49.4444444 36.05555556 72.15 357.5062

0 0.003274269 1.842417629 225 376

0.161290277 0.012730166 2.428550472 12 82.5 60.1 663

0.156833041 0.009779906 2.231690578 15 97.8 60.1 695

0.139067947 0.003392507 1.806094268 209 382

0.138783904 0.001707705 1.574164384 160 330

0.111955627 0.002463458 1.632590905 63 210

0.113547796 0.0021 1.73 47 175

0.170024439 0.003951143 1.691929742 176.6666667 269.4444444

0.152975876 0.003014496 2.18885904 229.4444444 376.6666667

0.130728571 0.003542286 1.835085714 177 340 Synthetic Hydrocarbon

0.123214286 0.003334286 1.614057143 138 289 Alkyl Substituted Aromatic

0.125093333 0.002216667 1.902 149 310

0.120147619 0.003577619 1.485857143 170 359 Modified Terphenyl

0.141985714 0.00270898 1.498185034 132 271

0.138591429 0.002411429 1.543371429 185 343

0.112068429 0.004052 2.02182 59 192

0.128413725 0.003705882 1.719058824 57 181

0.106924571 0.004227429 1.866392381 -6.2 99.2

0.141952571 0.002764048 1.494417143 110 257

0.120272381 0.004051429 1.530849524 104 243

0.117611143 0.004229143 1.736697143 199 358

0.568903491 0.000170226 4.192981454 0 100 18.02 2260

0.133886605 0.003762842 2.043143105 229 357 Paraffinic

0.137738737 0.004187528 2.076183757 163 500 PAO Synthetic

0.137706463 0.003425471 1.923331769 193 301 Paraffinic

0.119111518 0.003312905 1.336688519 160 305

0.140605437 0.002803986 1.516700643 122 258

0.142250753 0.002809556 1.489429746 124 257

0.136658852 0.003090441 1.640914231 121 275

Page 57: 02 Heat Exchangers
Page 58: 02 Heat Exchangers

Selection Values for Radio Buttons - this worksheet

Temperature

Specific Gravity

Specific Heat

Thermal Conductivity

Viscosity

Heat of Vaporization

Temp.°C

-202060

100120140

Page 59: 02 Heat Exchangers

-20 20 60 100

Raw Data - Units may be converted from original source

Temperature Points, deg C

1 2 3 4

0 20 40 60

-60 -40 -30 -20

0 20 40 60

15 40 40 100

15 40 40 100

15 40 40 100

37.77777778 93.33333333 148.8888889 204.4444444

10 37.77777778 121.1111111 204.4444444

37.77777778 93.33333333 148.8888889 204.4444444

20 60 100 200

-30 10 90 170

-40 0 80 160

20 60 100 180

0 25 50 100

0 25 50 100

0 25 50 100

0 25 50 100

0 25 50 100

0 25 50 100

0 25 50 75

0 25 50 75

0 25 50 75

10 10 40 65

-20 10 40 65

-30 -20 10 65

10 10 40 65

-20 10 40 65

-30 -20 10 65

-10 10 40 65

-20 10 40 65

-30 -20 10 65

15 65 155 205

-5 15 115 195

-80 -60 0 80

-20 40 160 220

-35 0 80 160

Page 60: 02 Heat Exchangers

10 70 130 190

-10 10 40 65

-20 10 40 65

-30 -20 10 65

-10 40 140 190

-1 49 99 149

-20 10 80 160

15 75 145 205

15 75 145 205

10 38 93 143

-20 10 80 160

-40 -10 60 140

-40 -12 60 138

-84 -68 -29 -1

-40 -29 38 77

70 100 130 170

-6.66666667 10 37.77777778 60

-17.7777778 -1.11111111 26.66666667 48.88888889

-28.8888889 -12.2222222 15.55555556 37.77777778

-6.66666667 4.444444444 21.11111111 37.77777778

-17.7777778 -1.11111111 21.11111111 37.77777778

-34.4444444 -17.7777778 10 32.22222222

-10 0 10 20

-20 0 10 20

-30 -10 10 20

-40 -20 0 20

-50 -30 -10 10

-62.2222222 -40 15.55555556 60

-73 -60 0 50

20 40 100 160

-40 -30 10 60

0 10 50 90

-106.666667 -84.4444444 -28.8888889 15.55555556

-6.66666667 -1.11111111 15.55555556 37.77777778

-17.7777778 -12.2222222 10 32.22222222

-34.4444444 -28.8888889 -1.11111111 26.66666667

-34.4444444 -28.8888889 -1.11111111 26.66666667

0 20 90 160

-10 0 10 20

60 80 100 120

-20 0 20 40

20 60 100 160

0 40 100 160

0 40 100 160

0 40 100 160

-10 0 10 20

-20 0 60 120

-18 38 93 149

-20 -10 40 120

-10 0 60 140

Page 61: 02 Heat Exchangers

-10 0 60 120

-30 -20 40 100

-125 -100 -75 -50

-10 0 25 50

-25 0 25 50

-40 -25 0 25

-20 0 25 50

-50 -25 0 25

-20 20 60 100

-101.111111 -73.3333333 -17.7777778 37.77777778

-6.66666667 37.77777778 93.33333333 148.8888889

15.55555556 37.77777778 93.33333333 148.8888889

10 37.77777778 121.1111111 176.6666667

-73.3333333 -40 15.55555556 93.33333333

-17.7777778 10 65.55555556 148.8888889

-17.7777778 10 37.77777778 93.33333333

10 37.77777778 93.33333333 148.8888889

-50 -30 -10 10

15 38 260 260

-10 0 20 40

-10 0 20 40

15 40 40 100

-40 0 120 240

-73 -70 -20 80

-100 -20 60 140

37.77777778 93.33333333 148.8888889 204.4444444

37.77777778 93.33333333 148.8888889 204.4444444

-25 25 75 125

-45 15 75 135

-20 40 100 160

0 60 120 180

-10 60 130 200

80 140 200 260

-85 -35 15 65

-75 -25 25 75

-115 -65 -15 35

12 72 132 192

2 62 122 182

-20 30 80 130

4 25 50 80

10 26.7 104.4 171.1

-62 -40 -17.8 71.1

10 26.7 104.4 171.1

-37.2 -17.8 48.9 148.9

7.2 48.9 126.7 204.4

15.6 48.9 126.7 204.4

-45.6 -17.8 48.9 148.9

Page 62: 02 Heat Exchangers
Page 63: 02 Heat Exchangers

Selection Values for Radio Buttons - this worksheet

2

Specific Gravity 2

Specific Heat 2

Thermal Conductivity 2

1

Heat of Vaporization 2

0

Predicted values in units of the table Predicted values in same units as inputLiquid Thermal Liquid Thermal

Density Sp. Heat Conduct. Visc. Density Sp. Heat Conduct. Visc.kg/m3 kJ/kg-K W/m-K mPa-s kg/cu.m. kJ/kg-K W/m-K cP

734.97172232 2.108818 0.142625 0.8963272876 734.9717 2.108818 0.142625 0.896327288

701.49441786 2.223376 0.130212 0.559145157143 701.4944 2.223376 0.130212 0.559145157

668.01711341 2.337934 0.117799 0.371073781049 668.0171 2.337934 0.117799 0.371073781

634.53980896 2.452491 0.105386 0.259007093553 634.5398 2.452491 0.105386 0.259007094

617.80115674 2.50977 0.099179 0.219901963396 617.8012 2.50977 0.099179 0.219901963

601.06250451 2.567049 0.092973 0.188480878573 601.0625 2.567049 0.092973 0.188480879

Page 64: 02 Heat Exchangers

120 140 732.5191 702.5186186 670.5874 636.161 617.7531281 598.3474242 2.12849379

Raw Data - Units may be converted from original source

Density, kg/m3 Specific Heat, kJ/kg-K

5 6 1 2 3 4 5 6 1

80 100 1068.666667 1048.666666667 1028.666667 1008.666667 988.6666667 968.6666667 1.9594224

-10 10 662.6555257 643.1987777327 633.154975 622.8756173 612.3380982 590.3786359 2.102449575

80 100 0 0 0 0 0 0 2.0934

260 316 866.598686 852.182072 852.182072 815.339614 716.025162 680.78455 1.88406

260 316 869.802378 855.385764 855.385764 816.94146 714.423316 679.182704 1.88406

260 260 818.543306 804.126692 804.126692 764.080542 658.358706 658.358706 2.051532

260 315.5555556 885.820838 850.580226 815.339614 780.099002 744.85839 709.617778 2.009664

260 343.3333333 986.737136 967.514984 906.644836 840.96915 794.515616 719.228854 1.318842

260 315.5555556 1017.17221 978.727906 940.283602 900.237452 861.793148 823.348844 1.611918

300 400 1061 1031 998 905 796 670 1.557

250 330 1062 1037 980 913 835 746 1.448

240 320 1046 1021 965 904 836 761 1.412

260 360 1018 992 965 907 844 758 1.603

150 170 1051 1042 1031 999 955 934 3.62

150 170 1065 1056 1044 1011 965 944 3.44

150 170 1078 1069 1056 1022 975 952 3.25

130 160 1036 1026 1013 977 949 917 3.81

130 160 1045 1034 1019 981 951 917 3.66

130 160 1053 1040 1025 984 953 918 3.49

100 120 1036 1026 1013 996 977 959 3.81

100 120 1045 1034 1019 1002 981 962 3.67

100 120 1052 1040 1024 1005 984 964 3.5

90 120 1033.71 1033.71 1019.56 1004.26 985.77 959.35 3.821

90 120 1053.16 1042.14 1026.49 1009.9 990.1 962.08 3.569

90 120 1064.83 1061.71 1049.25 1014.4 993.42 964 3.339

90 120 1043.85 1043.85 1029.85 1014.87 996.86 971.26 3.756

90 120 1066.76 1055.38 1039.77 1023.55 1004.39 977.53 3.453

90 120 1081.98 1078.51 1065.4 1030.83 1010.61 982.63 3.165

90 120 1067.26 1058.99 1044.22 1029.74 1013.29 990.96 3.542

90 120 1089.06 1075.9 1059.95 1044.52 1027.16 1003.77 3.307

90 120 1109.98 1105.84 1091.59 1058.37 1040.23 1015.96 3.051

305 405 1063.5 1023.7 947.8 902.5 801.3 672.5 1.558

275 375 1066.2 1050.7 973.3 911.3 849.3 771.8 1.458

160 320 931.3 921 878.5 817.4 749.2 560.4 1.584

280 340 989.8 948.2 860.4 813.2 763 708.2 1.48

240 360 1011.4 980.5 920 859.5 799 708.3 1.478

Page 65: 02 Heat Exchangers

310 370 1036.2 994.2 951.7 908.3 817.4 768.1 1.591

90 120 1055.47 1049.91 1037.92 1024.59 1008.2 984.53 3.562

90 120 1073.23 1064.73 1051.85 1037.76 1020.63 996.06 3.336

90 120 1090.31 1088.15 1078.72 1050.05 1032.15 1006.66 3.09

290 320 893.9 859.5 790.6 756.1 687.2 666.5 1.873

199 232 877.01 842.89 800.92 774.81 740.69 717.95 2.018

240 320 879.86 859.64 812.48 758.52 704.55 650.59 1.772

265 335 860.04 819.69 772.53 732.18 691.84 644.68 1.892

265 335 860.04 819.69 772.53 732.18 691.84 644.68 1.892

199 260 931 915 888.01 863.72 836.73 789 1.913

240 320 879.86 859.64 812.48 758.52 704.55 650.59 1.772

220 310 854.13 833.71 786.05 731.68 677.22 614.21 1.882

221 310 997.36 982.38 947.43 909.98 872.54 832.59 1.561

32 65 889 881 862 849 832 814 1.842

121 176 868 863 830 808 750 641 1.926

230 288 913 883 853 813 753 695 1.366

82.2222222222222 115.5555556 1028.865686 1023.8999632 1012.366672 1000.513012 986.0963976 959.6659386 3.97746

82.2222222222222 115.5555556 1052.573007 1046.806361 1033.991593 1021.01664 996.6685812 966.5538764 3.516912

82.2222222222222 115.5555556 1072.115528 1065.8683284 1052.092453 1038.156393 1002.915781 969.917753 3.098232

60 104.4444444 1046.966546 1042.801746 1036.073993 1028.385132 1016.691656 988.6593512 3.7429992

60 104.4444444 1088.133988 1081.0858654 1070.353497 1061.222975 1047.767469 1016.211102 3.3159456

60 104.4444444 1127.699584 1120.3310924 1106.555217 1093.259895 1074.838666 1040.879531 2.8009692

40 50 1370 1364 1358 1346 1335 1330 3.25

40 50 1259 1249 1244 1238 1228 1225 3.13

40 50 1305 1285 1275 1270 1260 1255 2.94

40 50 1358 1344 1330 1316 1302 1295 2.798

30 50 1390 1379 1368 1357 1346 1335 2.57

104.444444444444 148.8888889 860.191302 845.774688 805.728538 773.691618 743.256544 712.82147 1.6454124

110 177 833 823 778 740 694 643 1.742

220 280 1044 1030 987 944 901 858 1.549

120 205 804 799 779 754 724 681 1.652

150 205 815 808 780 752 710 672 1.934

60 126.6666667 943.487294 925.866988 882.617146 848.97838 815.339614 762.478696 1.3481496

71.1111111111111 104.4444444 1028.865686 1027.4240244 1021.817563 1012.366672 993.6250738 969.11683 3.9188448

60 104.4444444 1052.573007 1050.810976 1042.161008 1030.948086 1013.487964 977.12606 3.579714

60 104.4444444 1074.037743 1072.1155278 1060.742421 1045.3647 1021.817563 981.6112288 3.1024188

60 104.4444444 1095.342295 1091.3376798 1070.513682 1049.048945 1022.458302 985.2954746 2.574882

240 315 890 877 830 783 729 678 1.894

30 40 815.04 806.45 797.86 789.27 780.68 772.09 1.9133676

140 160 1136.555 1084.291 1032.027 979.763 927.499 875.235 2.595816

60 80 695.2899584 678.3378428392 660.7597049 642.4578783 623.3074328 603.1443504 2.119657041

220 300 847 822 797 758 718 663 1.95

220 300 1010 980 936 890 839 766 1.55

220 300 890 863 823 783 743 688 1.89

220 300 1058 1030 987 944 901 844 1.48

30 40 819.4333333 810.1833333333 800.9333333 791.6833333 782.4333333 773.1833333 2.365542

180 260 820 807 768 728 689 637 1.948

204 260 932 897 861 825 789 752 1.63

220 320 884 879 850 805 752 708 1.742

200 300 882 875 837 783 740 659 1.818

Page 66: 02 Heat Exchangers

200 300 879 872 839 805 763 713 1.777

180 320 894 890 865 840 806 747 1.696

0 50 956.76 937.5 918.24 898.98 860.46 821.94 1.287

75 100 1205 1200 1190 1177 1165 1152 3.25

75 100 1298 1285 1273 1260 1249 1235 3

50 100 1350 1340 1325 1310 1295 1270 2.8

75 100 1258 1249 1240 1224 1210 1195 3.13

50 100 1395 1380 1365 1350 1335 1305 2.56

120 140 732.5191282 702.5186185803 670.5873998 636.1610249 617.7531281 598.3474242 2.12849379

93.3333333333333 204.4444444 950.2150472 922.1827422 866.2783168 810.2137068 754.1490968 642.1800614 1.47040416

226.666666666667 315.5555556 897.03376 864.99684 832.95992 784.90454 736.84916 672.77532 1.842192

226.666666666667 315.5555556 865.9579476 851.7015182 816.140537 780.4193712 730.6019606 673.576243 1.86815016

260 371.1111111 961.1076 945.08914 881.0153 832.95992 768.88608 688.79378 1.925928

148.888888888889 232.2222222 831.8386278 807.0100148 766.1629418 708.816855 667.8095974 606.298711 1.64080692

232.222222222222 315.5555556 840.96915 810.534076 756.071312 700.006702 669.571628 655.155014 2.30274

148.888888888889 204.4444444 840.96915 810.534076 781.700848 735.247314 700.006702 677.580858 2.30274

232.222222222222 315.5555556 890.626376 873.00607 836.163612 799.321154 743.256544 688.79378 1.758456

30 50 691.0265028 673.4160519725 655.1447874 636.1055147 616.159837 595.1239659 2.052201239

316 316 869 855 714 714 679 679 1.89

60 80 809.7536 801.5741333333 785.2152 768.8562667 752.4973333 736.1384 2.30274

60 80 827.3 819.4333333333 803.7 787.9666667 772.2333333 756.5 2.135268

260 316 853.783918 837.765458 837.765458 797.719308 688.79378 650.349476 1.8673128

320 400 990.61 953.16 846.35 734.35 648.24 547 1.506

180 260 965.78 962.75 912.2 811.1 710 629.12 1.453

220 280 978.5 896.4 814.2 732 649.8 588.2 1.52

260 315.5555556 892.228222 856.98761 820.145152 780.099002 740.052852 695.201164 1.842192

260 315.5555556 800.923 765.682388 728.83993 691.997472 655.155014 618.312556 2.30274

175 275 901 868 835 801 766 692 1.744

195 315 1020 978 934 890 843 741 1.472

220 280 982 940 897 852 803 750 1.832

240 300 1020 981 941 899 856 809 1.495

270 340 1110 1040 979 916 853 789 1.471

320 380 1040 998 953 905 855 799 1.709

115 215 835 801 766 729 691 600 1.694

175 275 939 901 862 821 732 619 1.432

85 135 862 820 778 735 690 641 1.374

252 372 1070 1020 972 920 865 733 1.523

242 302 942 909 869 819 759 684 1.516

180 280 903 872 840 808 775 705 1.617

100 100 1000 997.045 988.037 971.83 958.365 958.365 4.216

226.7 287.8 870.7 862.51 824.42 791.8 764.63 734.73 2.0817

143.3 260 840.23 826.67 813.11 758.87 714.8 643.61 1.816

226.7 315 857.81 847.72 800.56 760.09 726.32 672.36 1.956

248.9 349 1043.8 1029.8 981.8 909.8 837.9 765.9 1.213

304.4 371.1 1074.2 1039.43 974.52 909.61 826.16 770.52 1.532

304.4 398.9 1068.5 1041.3 977.2 909.9 812.2 695.3 1.532

248.9 343.3 1044.16 1024.18 976.22 904.27 823.33 764.39 1.5

Page 67: 02 Heat Exchangers
Page 68: 02 Heat Exchangers

2.218223196 2.3152483235986 2.435186875 2.508629215 2.593656549 0.141980143 0.130534117 0.118449083 0.105725041

Specific Heat, kJ/kg-K Thermal Conductivity, W/m-K

2 3 4 5 6 1 2 3 4

2.030598 2.1059604 2.177136 2.260872 2.344608 0.171342765 0.171342765 0.171342765 0.171342765

2.160288302 2.19207026228672 2.226342241 2.263540455 2.348460454 0.146709741 0.136927066 0.131959856 0.126942063

2.323674 2.553948 2.805156 3.014496 3.265704 0.174804235 0.171342765 0.167881295 0.164419825

1.967796 1.967796 2.177136 2.679552 2.888892 0.14192027 0.14192027 0.14192027 0.1384588

1.967796 1.967796 2.177136 2.679552 2.888892 0.143651005 0.14192027 0.14192027 0.1384588

2.135268 2.135268 2.344608 2.93076 2.93076 0.14192027 0.140189535 0.140189535 0.13499733

2.177136 2.344608 2.553948 2.763288 2.972628 0.129805125 0.125478287 0.121497597 0.117170759

1.4528196 1.77939 2.114334 2.30274 2.553948 0.12755517 0.123228332 0.112497775 0.10090185

1.821258 2.0054772 2.19807 2.40741 2.595816 0.128939757 0.123228332 0.117343833 0.111632408

1.665 1.772 2.041 2.309 2.577 0.144 0.137 0.13 0.112

1.558 1.778 1.999 2.219 2.44 0.142 0.136 0.124 0.112

1.53 1.766 2.002 2.238 2.474 0.136 0.131 0.122 0.112

1.738 1.873 2.143 2.414 2.752 0.12 0.118 0.115 0.108

3.69 3.75 3.89 4.03 4.09 0.437 0.467 0.491 0.514

3.52 3.6 3.77 3.93 3.99 0.404 0.43 0.449 0.469

3.35 3.44 3.63 3.82 3.89 0.374 0.396 0.412 0.43

3.88 3.94 4.08 4.16 4.24 0.431 0.459 0.479 0.499

3.74 3.82 3.99 4.08 4.18 0.395 0.417 0.433 0.448

3.58 3.68 3.87 3.98 4.1 0.361 0.378 0.39 0.401

3.88 3.95 4.01 4.08 4.13 0.428 0.456 0.476 0.489

3.75 3.83 3.91 3.99 4.05 0.391 0.413 0.429 0.438

3.59 3.69 3.78 3.87 3.95 0.357 0.374 0.385 0.392

3.821 3.903 3.972 4.041 4.123 0.4344 0.4344 0.4622 0.4771

3.668 3.768 3.85 3.933 4.032 0.3635 0.3936 0.415 0.4262

3.378 3.493 3.706 3.802 3.918 0.3246 0.3336 0.356 0.3792

3.756 3.841 3.913 3.984 4.07 0.4344 0.4344 0.4622 0.4771

3.564 3.674 3.767 3.859 3.97 0.3635 0.3936 0.415 0.4262

3.21 3.346 3.594 3.707 3.843 0.3246 0.3336 0.356 0.3792

3.6 3.687 3.759 3.831 3.918 0.4154 0.442 0.4731 0.4909

3.41 3.512 3.598 3.684 3.787 0.3707 0.4053 0.4312 0.4462

3.091 3.209 3.427 3.526 3.644 0.3333 0.3442 0.3724 0.4062

1.701 1.954 2.083 2.373 2.725 0.1395 0.1315 0.1171 0.1091

1.528 1.878 2.158 2.437 2.787 0.1293 0.127 0.1154 0.1061

1.616 1.769 2.023 2.315 3.04 0.1485 0.1453 0.1326 0.1156

1.675 2.065 2.26 2.455 2.65 0.127 0.121 0.108 0.102

1.589 1.842 2.088 2.327 2.672 0.128 0.1244 0.1143 0.1028

Page 69: 02 Heat Exchangers

1.769 1.948 2.126 2.483 2.662 0.1327 0.1249 0.1171 0.1093

3.619 3.704 3.775 3.846 3.931 0.4154 0.442 0.4731 0.4909

3.436 3.537 3.621 3.705 3.805 0.3707 0.4053 0.4312 0.4462

3.129 3.245 3.457 3.554 3.67 0.3333 0.3442 0.3724 0.4062

2.022 2.32 2.469 2.767 2.857 0.141 0.13 0.108 0.097

2.169 2.319 2.47 2.621 2.721 0.145 0.142 0.137 0.133

1.872 2.103 2.363 2.633 2.893 0.144 0.143 0.139 0.135

2.093 2.323 2.513 2.714 2.944 0.143 0.14 0.136 0.133

2.093 2.323 2.513 2.714 2.944 0.143 0.14 0.136 0.133

1.968 2.079 2.18 2.292 2.345 0.169 0.164 0.156 0.148

1.872 2.103 2.363 2.633 2.893 0.144 0.143 0.139 0.135

1.983 2.223 2.503 2.774 3.082 0.146 0.143 0.138 0.131

1.614 1.724 1.862 2.005 2.159 0.144 0.138 0.125 0.108

1.879 1.95 2.01 2.081 2.177 0.141 0.14 0.138 0.136

1.95 2.093 2.211 2.345 2.5 0.138 0.138 0.133 0.13

1.423 1.479 1.555 1.668 1.777 0.1451 0.1397 0.1344 0.1273

4.061196 4.228668 4.354272 4.479876 4.689216 0.45345257 0.479413595 0.510566825 0.534797115

3.642516 3.76812 3.935592 4.103064 4.312404 0.365185085 0.38422317 0.406722725 0.417107135

3.181968 3.34944 3.475044 3.726252 3.935592 0.30114789 0.309801565 0.323647445 0.330570385

3.76812 3.809988 3.8476692 3.8979108 4.0025808 0.45691404 0.47422139 0.49845168 0.517489765

3.370374 3.4499232 3.5043516 3.579714 3.7346256 0.37383876 0.392876845 0.4153764 0.42922228

2.8721448 2.9977488 3.098232 3.2196492 3.4206156 0.30807083 0.32191671 0.34268553 0.35653141

3.28 3.31 3.34 3.4 3.43 0.495 0.505 0.515 0.525

3.18 3.2 3.22 3.27 3.29 0.483 0.502 0.512 0.521

2.99 3.04 3.08 3.13 3.15 0.465 0.487 0.509 0.52

2.844 2.89 2.936 2.982 3.005 0.45 0.46975 0.4895 0.50925

2.61 2.65 2.69 2.73 2.77 0.435 0.455 0.475 0.494

1.737522 1.98873 2.19807 2.40741 2.595816 0.13499733 0.130670492 0.122882185 0.115093878

1.791 2.019 2.209 2.437 2.692 0.1272 0.1246 0.1126 0.1026

1.624 1.847 2.071 2.294 2.518 0.1306 0.128 0.1201 0.1122

1.69 1.842 2.032 2.26 2.583 0.1245 0.1225 0.1145 0.1045

1.972 2.124 2.276 2.504 2.713 0.151 0.149 0.141 0.133

1.4276988 1.611918 1.77939 1.9384884 2.1729492 0.16268909 0.158362253 0.143651005 0.134131962

3.9272184 3.9648996 4.0151412 4.0863168 4.1616792 0.45345257 0.462106245 0.486336535 0.510566825

3.5964612 3.6718236 3.7429992 3.8351088 3.9816468 0.365185085 0.372108025 0.392876845 0.410184195

3.1233528 3.2489568 3.370374 3.516912 3.7136916 0.295955685 0.30114789 0.316724505 0.327108915

2.6083764 2.763288 2.9140128 3.098232 3.2615172 0.254418045 0.25614878 0.25961025 0.261340985

1.967 2.223 2.478 2.771 3.045 0.1361 0.1347 0.1295 0.124

2.051532 2.19807 2.3529816 2.5037064 2.6628048 0.181727175 0.181727175 0.181727175 0.181727175

2.700486 2.805156 2.9056392 3.014496 3.1107924 0.28384054 0.28384054 0.28384054 0.28384054

2.168063316 2.22105000678014 2.280956428 2.350121896 2.430885726 0.137393959 0.130409865 0.123238402 0.115879572

2.07 2.19 2.4 2.64 3.01 0.133 0.131 0.128 0.125

1.68 1.88 2.08 2.29 2.55 0.134 0.129 0.122 0.115

2.04 2.26 2.48 2.7 2.99 0.136 0.134 0.129 0.124

1.62 1.85 2.07 2.29 2.59 0.133 0.128 0.12 0.112

2.4199704 2.4618384 2.4869592 2.5455744 2.5874424 0.21461114 0.21461114 0.21461114 0.21461114

2.024 2.253 2.481 2.71 3.015 0.1438 0.1426 0.1389 0.1352

1.88 2.14 2.39 2.64 2.81 0.1303 0.1264 0.1223 0.1184

1.777 1.959 2.248 2.612 2.981 0.1416 0.1412 0.1359 0.1312

1.864 2.136 2.5 2.773 3.228 0.1363 0.1356 0.1312 0.1254

Page 70: 02 Heat Exchangers

1.813 2.01 2.177 2.47 2.906 0.1412 0.1388 0.1365 0.1353

1.733 1.951 2.169 2.459 2.968 0.1366 0.1359 0.1315 0.1272

1.375 1.462 1.55 1.725 1.9 0.1627 0.1577 0.1527 0.1477

3.28 3.35 3.41 3.47 3.53 0.496 0.506 0.531 0.556

3.03 3.09 3.15 3.21 3.27 0.474 0.499 0.524 0.549

2.84 2.89 2.95 3 3.11 0.437 0.463 0.489 0.515

3.19 3.24 3.29 3.35 3.41 0.485 0.505 0.53 0.555

2.61 2.66 2.71 2.77 2.87 0.433 0.459 0.484 0.51

2.218223196 2.3152483235986 2.435186875 2.508629215 2.593656549 0.141980143 0.130534117 0.118449083 0.105725041

1.57381812 1.78022736 1.9866366 2.19346452 2.606283 0.149362431 0.147285548 0.142785638 0.138804947

2.009664 2.177136 2.344608 2.595816 2.888892 0.133266595 0.12807439 0.119420715 0.112497775

1.94937408 2.15159652 2.35423764 2.63810268 2.962161 0.133093521 0.131362787 0.127209023 0.123055258

1.967796 2.177136 2.30274 2.470212 2.72142 0.11768998 0.11768998 0.112497775 0.109036305

1.76976036 1.98496188 2.28641148 2.501613 2.82441528 0.158362253 0.155939224 0.150920092 0.145727887

2.344608 2.470212 2.637684 2.805156 2.972628 0.133266595 0.133266595 0.13153586 0.126343655

2.344608 2.428344 2.51208 2.637684 2.72142 0.133266595 0.133266595 0.133266595 0.13153586

1.925928 2.219004 2.51208 2.93076 3.391308 0.105574835 0.1038441 0.10038263 0.098651895

2.100695974 2.15430916504956 2.215530492 2.286849634 2.370756271 0.165203791 0.161073069 0.156594499 0.151768081

1.97 2.69 2.69 2.88 2.88 0 0 0 0

2.428344 2.6837388 2.9391336 3.181968 3.45411 0.16268909 0.160958355 0.15922762 0.157496885

2.2273776 2.428344 2.6293104 2.8135296 3.014496 0.154035415 0.157496885 0.160958355 0.164419825

1.9384884 1.9384884 2.1394548 2.6879256 2.8805184 0.1384588 0.136728065 0.136728065 0.133266595

1.574 1.779 1.984 2.121 2.257 0.1463 0.1388 0.1162 0.0936

1.46 1.583 1.83 2.076 2.273 0.1301 0.1293 0.1169 0.0921

1.688 1.856 2.024 2.192 2.318 0.1341 0.1192 0.1019 0.0827

2.051532 2.281806 2.51208 2.72142 2.93076 0.160958355 0.151439312 0.14192027 0.129805125

2.470212 2.637684 2.805156 2.972628 3.1401 0.14884321 0.143651005 0.136728065 0.13153586

1.924 2.102 2.28 2.456 2.807 0.1336 0.1278 0.122 0.1162

1.665 1.86 2.057 2.257 2.674 0.1253 0.1217 0.1171 0.1115

1.997 2.144 2.276 2.393 2.499 0.1263 0.1212 0.1158 0.1101

1.699 1.908 2.122 2.342 2.569 0.1183 0.1158 0.1121 0.1074

1.661 1.85 2.04 2.23 2.419 0.1432 0.1347 0.1262 0.1177

1.887 2.048 2.191 2.319 2.434 0.1307 0.1262 0.1213 0.1161

1.881 2.073 2.271 2.476 2.911 0.1244 0.118 0.1107 0.1027

1.629 1.82 2.004 2.357 2.74 0.1429 0.1334 0.1237 0.1138

1.594 1.808 2.018 2.225 2.433 0.1304 0.1208 0.1109 0.1004

1.696 1.864 2.027 2.186 2.523 0.137 0.1309 0.1236 0.115

1.798 2.048 2.272 2.486 2.76 0.1197 0.112 0.1042 0.0962

1.864 2.096 2.314 2.519 2.886 0.118 0.1148 0.1109 0.1065

4.183 4.183 4.199 4.219 4.219 0.56421961 0.59883431 0.642102685 0.669794445

2.1428 2.4358 2.6869 2.8961 3.1263 0.1333 0.1322 0.1274 0.1232

1.909 2.002 2.374 2.676 3.165 0.1412 0.14 0.1387 0.1338

2.013 2.285 2.511 2.699 3.001 0.1369 0.1355 0.1293 0.1239

1.278 1.499 1.83 2.161 2.493 0.12 0.122 0.116 0.107

1.656 1.877 2.091 2.365 2.559 0.1372 0.1329 0.1233 0.112

1.632 1.85 2.059 2.327 2.624 0.1371 0.1336 0.1244 0.1132

1.586 1.792 2.101 2.41 2.702 0.1437 0.1394 0.1291 0.1137

Page 71: 02 Heat Exchangers
Page 72: 02 Heat Exchangers

0.099123392 0.092361991 1.007647456 0.559145157 0.365746993 0.259007094 0.220732832 0.188480879 10.58

Viscosity, Pa-s Vapor Pressure, mmHg

5 6 1 2 3 4 5 6 1

0.171342765 0.171342765 1.8 2.28 0.95 0.75 0.6 0.48 11.68

0.121873689 0.111585194 0.396195334 0.311017391 0.280380799 0.254663465 0.232471159 0.195074077 126.5486454

0.160958355 0.157496885 4.7 2.9 1.8 1.18 0.79 0.55 4.86

0.129805125 0.126343655 0 27.35504451 0 4.402833916 0 0.476549185 0.01

0.129805125 0.12807439 0 30.70834893 0 4.90164876 0 0.475427893 0.01

0.12115145 0.12115145 0 6.03095019 0 1.680977192 0 0.395015224 0.01

0.113016996 0.108863231 30.20649058 4.457040384 1.655139416 0.889312862 0.588438128 0.432866845 0.8

0.094325057 0.083940647 4.736338253 2.805793454 0.752515214 0.361616735 0.254244997 0.172614925 1

0.106440203 0.09986341 14.24041094 3.239589369 1.410425403 0.765201834 0.517075889 0.386973957 0.5

0.097 0.082 4.26 1.78 0.99 0.41 0.26 0.19 0.338

0.101 0.09 71.21 8.31 1.31 0.57 0.36 0.27 1.82

0.1 0.088 84.76 11.49 1.63 0.62 0.35 0.24 0.005

0.1 0.086 135.78 12.48 3.62 1.02 0.53 0.34 0.1

0.507 0.495 3.82 1.81 1.03 0.47 0.28 0.23 0

0.464 0.455 5.41 2.38 1.31 0.56 0.31 0.25 0

0.426 0.419 7.21 3.11 1.68 0.68 0.35 0.28 0

0.494 0.479 6.19 2.38 1.2 0.5 0.37 0.29 0

0.443 0.429 11 3.38 1.53 0.62 0.46 0.38 0

0.396 0.383 15.57 4.73 2.07 0.74 0.51 0.4 0

0.493 0.492 6.43 2.43 2.22 0.74 0.51 0.41 0

0.441 0.439 11.4 3.51 1.59 0.92 0.62 0.49 0

0.393 0.39 16.33 4.93 2.14 1.18 0.76 0.58 0

0.4846 0.4838 4.5068 4.5068 1.6295 0.9144 0.604 0.4246 0

0.4313 0.4294 48.9043 7.2173 2.2389 1.1762 0.7462 0.5084 0

0.3821 0.3792 172.8273 73.0193 10.6481 1.5483 0.9339 0.6029 0

0.4846 0.4838 4.5068 4.5068 1.6295 0.9144 0.604 0.4246 0

0.4313 0.4294 48.9043 7.2173 2.2389 1.1762 0.7462 0.5084 0

0.3821 0.3792 172.8273 73.0193 10.6481 1.5483 0.9339 0.6029 0

0.5015 0.5044 6.1788 2.9482 1.3398 0.8246 0.5599 0.3846 0

0.4552 0.4582 15.7533 4.0451 1.7731 1.0646 0.7013 0.4614 0

0.4139 0.4168 43.997 22.0816 5.5071 1.2936 0.8227 0.5252 0

0.0931 0.0771 5 1.58 0.56 0.38 0.2 0.12 2.3

0.0969 0.0853 55.9 15.7 1.45 0.62 0.34 0.19 1

0.0987 0.0647 8.43 5.12 1.23 0.47 0.28 0.16 0.5

0.096 0.089 213.9 9.44 0.85 0.45 0.28 0.19 0.5

0.0843 0.0719 46.6 7.56 1.07 0.41 0.24 0.15 0.5

Page 73: 02 Heat Exchangers

0.0938 0.086 88.17 5.39 1.71 0.87 0.38 0.29 0.5

0.5015 0.5044 6.1788 2.9482 1.3398 0.8246 0.5599 0.3846 0

0.4552 0.4582 15.7533 4.0451 1.7731 1.0646 0.7013 0.4614 0

0.4139 0.4168 43.997 22.0816 5.5071 1.2936 0.8227 0.5252 0

0.075 0.068 251.68 12.8 1.45 0.82 0.39 0.33 0.01

0.13 0.128 18.59 3.29 1.36 0.77 0.52 0.43 5.7

0.131 0.127 2691 148.51 7.05 1.67 0.76 0.46 0.05

0.13 0.126 123.54 8.91 2.17 1.07 0.66 0.44 0.05

0.13 0.126 123.54 8.91 2.17 1.07 0.66 0.44 0.05

0.139 0.132 220.78 48.54 8.91 3.8 2.05 1.25 0.05

0.131 0.127 2691 148.51 7.05 1.67 0.76 0.46 0.05

0.124 0.116 999.67 62.98 3.73 1.03 0.52 0.31 0.05

0.091 0.074 287.03 104.52 28.77 12.09 6.34 2.9 0.05

0.134 0.131 70.28 27.7 5.19 2.72 1.62 1.12 0.01

0.125 0.116 59.49 13.91 1.51 1 0.68 0.43 0.05

0.1167 0.1064 48.6 31.5 21.6 14.1 8.4 5.6 0

0.53998932 0.54345079 5.07 2.81 1.28 0.8 0.57 0.4 0

0.430953015 0.430953015 24.31 10.84 3.38 1.72 0.93 0.73 0

0.337493325 0.334031855 146 37.12 10.57 4.46 1.5 1.19 0

0.538258585 0.555565935 3.9 2.59 1.61 1.11 0.74 0.41 0

0.44306816 0.458644775 13.76 6.09 2.87 1.87 1.17 0.57 0

0.368646555 0.379030965 89.67 30.08 7.85 3.58 1.69 0.72 0

0.545 0.555 3 2.5 2.05 1.7 1.2 1.05 0

0.54 0.55 6 4.3 3.6 3.2 2.4 2.15 0

0.542 0.553 8.3 6 4.1 3.6 2.9 2.6 0

0.529 0.538875 13 7.5 5 3.2 2.2 2 0

0.514 0.533 28 15 8.7 5.4 3.6 2.3 0

0.10730557 0.08999822 13 5.2 1.6 0.85 0.46 0.25 0.01

0.0906 0.0772 70.2 23.9 2.5 1 0.49 0.27 0

0.1043 0.0963 49 16.8 3.3 1.3 0.72 0.45 0

0.0925 0.0755 33.2 16.9 3.4 1.2 0.53 0.24 0

0.121 0.11 34.1 20.7 5 2.1 0.92 0.54 0

0.123747552 0.10730557 88 15 2 1.05 0.66 0.28 0.01

0.534797115 0.54345079 5.36 4.23 2.32 1.25 0.64 0.4 0

0.424030075 0.430953015 40.92 26.99 7.21 2.88 1.31 0.53 0

0.334897223 0.336627958 497.57 298.75 33.68 7.34 2.22 0.86 0

0.25961025 0.254418045 1363.75 820.58 80.66 14.79 3.82 1.31 0

0.1174 0.1109 160 37 4.1 1.5 0.69 0.41 0

0.181727175 0.181727175 2.07 1.7 1.4 1.19 0.98 0.85 11.97

0.28384054 0.28384054 92 34 13.5 5.4 2.4 1 0

0.108333373 0.100599807 0.464622731 0.367464429 0.300027364 0.250023884 0.210819882 0.178664587 45.70172723

0.121 0.116 40.1 8.4 3.3 1.3 0.71 0.34 61

0.109 0.099 8.3 2.6 1.1 0.61 0.43 0.3 0

0.119 0.112 123 14 3 1.4 0.73 0.38 0

0.104 0.094 321 16.5 3.1 1.4 0.77 0.45 0

0.21461114 0.21461114 0.92 0.8 0.69 0.6 0.52 0.47 29.6

0.1315 0.1265 45 15.6 2.49 0.983 0.529 0.287 0

0.1142 0.1104 1412 20.5 3.53 1.37 0.73 0.46 0.00005

0.1234 0.1156 2679 1524 33.94 3.515 1.002 0.485 0

0.121 0.1136 1121 439 15.6 2.4 1.13 0.483 0

Page 74: 02 Heat Exchangers

0.1319 0.1289 1524 383 15.6 3.5 1.3 0.6 0

0.1214 0.1113 4113 1113 16 2.98 0.975 0.332 0

0.1377 0.1277 0 45 8 3 1.2 0.75 0

0.581 0.606 3 2.3 1.5 1.05 0.7 0.5 0

0.574 0.599 10 3 1.9 1.1 0.9 0.7 0

0.541 0.592 15 8 4 2.3 1.7 1.1 0

0.58 0.605 5 3.7 2.2 1.5 1.2 1 0

0.536 0.588 40 10 4.5 2.8 2 1.1 0

0.099123392 0.092361991 1.007647456 0.559145157 0.365746993 0.259007094 0.220732832 0.188480879 10.57914194

0.134824257 0.125824435 36 5.08 1.58 0.66 0.42 0.25 0.001

0.10038263 0.088267485 254 18 3.2 1.3 0.58 0.29 0.01

0.117170759 0.110420893 126 37.5 6.01 2.17 0.94 0.47 0.005

0.098651895 0.081344545 50 11 1.5 0.82 0.42 0.22 0.1

0.141054903 0.134651183 138.19 11.63 1.83 0.56 0.32 0.18 0.001

0.11768998 0.1038441 60 14 2.9 0.8 0.39 0.28 0.01

0.126343655 0.12115145 40 11 4.3 1.3 0.66 0.44 0

0.09345969 0.08999822 83 16 3.2 1.6 0.53 0.16 0.01

0.146593814 0.1410717 0.464663289 0.373435731 0.314359551 0.271579846 0.237190291 0.207066649 37.0155235

0 0 86.9 31.635 0.6426 0.6426 0.4753 0.4753 0

0.15576615 0.154035415 4.8 3.7 2.25 1.35 0.87 0.56 8.42

0.167881295 0.171342765 4.7 3.7 2.35 1.5 1 0.7 3.36

0.12461292 0.12115145 0 29.8244503 0 4.786315848 0 0.468251623 0.01

0.0786 0.0635 51.05 15.33 2.36 0.74 0.41 0.25 0.01

0.0673 0.0475 16.46 14.87 3.88 0.83 0.35 0.22 0.01

0.062 0.0455 78.6 3.1 0.8 0.36 0.22 0.17 0.01

0.11768998 0.105574835 29.84503403 4.293507926 1.541872886 0.819103952 0.532838053 0.38236064 0.5

0.126343655 0.119420715 13.2953218 3.101013671 1.392084266 0.809637042 0.563433312 0.414269413 0.1

0.1104 0.0986 1250 32.1 5.14 1.84 0.963 0.402 0.00183

0.1049 0.0888 991 8.16 1.92 0.864 0.496 0.232 0.0109

0.1037 0.0965 1180 10.1 2.26 0.931 0.48 0.28 0.00955

0.1015 0.0946 1320 11.5 2.42 1.06 0.611 0.413 0.0457

0.1092 0.1007 383 3.5 1.05 0.497 0.284 0.18 23.5

0.1103 0.1038 4.29 1.69 0.847 0.495 0.322 0.227 2.77

0.0939 0.0738 359 5.63 1.38 0.664 0.395 0.174 0.00138

0.0938 0.0732 11 1.95 0.831 0.478 0.223 0.128 0.0233

0.0892 0.0771 45.4 3.56 1.12 0.547 0.319 0.202 0.0806

0.1052 0.0818 5.48 1.45 0.693 0.418 0.284 0.209 0.694

0.088 0.0795 5.08 1.29 0.67 0.431 0.292 0.197 0.494

0.1015 0.0896 1840 32.9 5.33 1.97 1.03 0.432 0.000742

0.680178855 0.680178855 1.5674 0.8937 0.5494 0.3565 0.2838 0.2838 23.76

0.1198 0.116 318.94 87.687 5.306 1.692 0.931 0.59 0.001

0.1297 0.1232 3137 274.6 48.229 2.232 0.828 0.318 0.001

0.1194 0.1122 75.697 26.191 2.191 0.832 0.483 0.252 0.001

0.097 0.089 1601.8 115.4 2.246 0.63 0.314 0.195 0.01

0.0948 0.0818 8.416 2.619 0.872 0.402 0.226 0.165 0

0.0957 0.076 4.961 2.12 0.73 0.383 0.216 0.146 0.134

0.0983 0.0837 114.95 17.938 2.264 0.615 0.282 0.181 0.01

Page 75: 02 Heat Exchangers
Page 76: 02 Heat Exchangers

349.69 1,121.74 Yaw's Handbook, 2003 114.231

Vapor Pressure, mmHg Source MW

2 3

89.74 424.1 Perry's, 6th Ed

340.5111654 1116.912703 Yaw's Handbook, 2003

60.39 386.72 Perry's, 6th Ed

28.43537415 113.7414966 Petro-Canada, TechData Sheet IM-7852E (06.08)

20.16326531 84.78911565 Petro-Canada, TechData Sheet IM-7851E (07.06)

0.02 216.1088435 Petro-Canada, TechData Sheet IM-7874E (07.07)

17.5 480 Chemtherm 550 Data Sheet, 2010

194 3107 Chemtherm 650 Data Sheet, 2010

10 155 Chemtherm 700 Data Sheet, 2010

181 8383 DIPHYL® database Version 2.3 - August 2005

26.6 1724 DIPHYL® database Version 2.3 - August 2005

19.1 1313 DIPHYL® database Version 2.3 - August 2005

4.61 785 DIPHYL® database Version 2.3 - August 2005

0 0 DOWCAL™ 10/DOWTHERM™ 10 Product Information Sheet, Dec 2009

0 0 DOWCAL™ 10/DOWTHERM™ 10 Product Information Sheet, Dec 2009

0 0 DOWCAL™ 10/DOWTHERM™ 10 Product Information Sheet, Dec 2009

0 0 DOWCAL™ 20/DOWFROST™ Product Information Sheet, Jan 2008

0 0 DOWCAL™ 20/DOWFROST™ Product Information Sheet, Jan 2008

0 0 DOWCAL™ 20/DOWFROST™ Product Information Sheet, Jan 2008

0 0 DOWCAL™ N/DOWFROST™ Product Information Sheet, Mar 2007

0 0 DOWCAL™ N/DOWFROST™ Product Information Sheet, Mar 2007

0 0 DOWCAL™ N/DOWFROST™ Product Information Sheet, Mar 2007

0 0 DOWFROST™ Product Information Sheet, Nov 2001

0 0 DOWFROST™ Product Information Sheet, Nov 2001

0 0 DOWFROST™ Product Information Sheet, Nov 2001

0 0 DOWFROST™ HD Product Information Sheet, Nov 2001

0 0 DOWFROST™ HD Product Information Sheet, Nov 2001

0 0 DOWFROST™ HD Product Information Sheet, Nov 2001

0 0 Dow, DOWTHERM™ 4000 Product Information Sheet, Nov 2001

0 0 Dow, DOWTHERM™ 4000 Product Information Sheet, Nov 2001

0 0 Dow, DOWTHERM™ 4000 Product Information Sheet, Nov 2001

210 8490 Dow, DOWTHERM™ A Product Information Sheet, Nov 2001

75 3280 Dow, DOWTHERM™ G Product Information Sheet, Dec 2001

22.5 9592 Dow, DOWTHERM™ J Product Information Sheet, Nov 2001

46 960 Dow, DOWTHERM™ MX Product Information Sheet, Nov 2001

37.5 3700 Dow, DOWTHERM™ Q Product Information Sheet, Nov 2001

Page 77: 02 Heat Exchangers

7.5 1050 Dow, DOWTHERM™ RP Product Information Sheet, Nov 2001

0 0 Dow, DOWTHERM™ SR-1 Product Information Sheet, Jun 2002

0 0 Dow, DOWTHERM™ SR-1 Product Information Sheet, Jun 2002

0 0 Dow, DOWTHERM™ SR-1 Product Information Sheet, Jun 2002

4.5 309 Dow, DOWTHERM™ T Product Information Sheet, Apr 2004

31 167 Duratherm 450 Data Sheet, 2010

0.975 126 Duratherm 600 Data Sheet, 2010

3.4 133 Duratherm 630 Data Sheet, 2010

3.4 133 Duratherm FG Data Sheet, 2010

9 28.4 Duratherm G Data Sheet, 2010

0.975 126 Duratherm Lite Data Sheet, 2010

6.4 414 Duratherm LT Data Sheet, 2010

50.5 136.8 Duratherm S Data Sheet, 2010

0.05 223 Duratherm XLT-120 Data Sheet, 2010

36 479 Duratherm XLT-50 Data Sheet, 2010

0 0 Dynalene 600 Data Sheet, 2010

0 0 Dynalene BioGlycol Data Sheet, 2010

0 0 Dynalene BioGlycol Data Sheet, 2010

0 0 Dynalene BioGlycol Data Sheet, 2010

0 0 Dynalene EG Data Sheet

0 0 Dynalene EG Data Sheet

0 0 Dynalene EG Data Sheet

0 0 Dynalene HC Engineering Guide

0 0 Dynalene HC Engineering Guide

0 0 Dynalene HC Engineering Guide

0 0 Dynalene HC Engineering Guide

0 0 Dynalene HC Engineering Guide

6 240 Dynalene HF and Dynalene MV Engineering Guide

0 0 Dynalene HF-LO Data Sheet

0 0 Dynalene HT Data Sheet

0 0 Dynalene LO-170 Data Sheet

0 0 Dynalene LO-230 Data Sheet

0.7 170 Dynalene HF and Dynalene MV Engineering Guide

0 0 Dynalene PG Data Sheet

0 0 Dynalene PG Data Sheet

0 0 Dynalene PG Data Sheet

0 0 Dynalene PG Data Sheet

0 0 Dynalene SF Data Sheet

44.25 135 Perry's, 6th Ed

0 0 Perry's, 6th Ed

281.0088133 1057.165029 Yaw's Handbook, 2003

106 420 Marlotherm FP Technical Data Sheet, Rev: 11-May-2004

0 0 Marlotherm LH Product Information, Rev: 09.04

0 0 Marlotherm N Product Information, Rev: 01.06.2007

0 0 Marlotherm SH Product Information, Rev: 09/04

96.7 265.6 Perry's, 6th Ed

0 0 MultiTherm 503 7/04 Data Sheet

0.067 4.41 MultiTherm FF-1 7/04 Data Sheet

0 0 MultiTherm IG-1 Web Page (2010)

0 0 MultiTherm IG-4 Web Page (2010)

Page 78: 02 Heat Exchangers

0 0 MultiTherm OG-1 7/04 Data Sheet

0 0 MultiTherm PG-1 7/04 Data Sheet

0 0 MultiTherm ULT-170 7/04 Data Sheet

0 0 MultiThermWB 7/04 Data Sheet

0 0 MultiThermWB 7/04 Data Sheet

0 0 MultiThermWB 7/04 Data Sheet

0 0 MultiThermWB 7/04 Data Sheet

0 0 MultiThermWB 7/04 Data Sheet

349.6937053 1121.73787 Yaw's Handbook, 2003

10 953 Engineering Bulleting CR 809

2.9 345 Engineering Bulleting GLT 309

0.03 45 Engineering Bulleting HE 809

9.5 1492 Engineering Bulleting HR 309

15.03 1069.76 Engineering Bulleting LR 809

3.4 560 Engineering Bulleting MG 709

0 0 Engineering Bulleting MR 909

7.3 106 Engineering Bulleting NF 809

282.8250742 1202.762024 Yaw's Handbook, 2003

0 0 0

107.2 690.48 Perry's, 6th Ed

51.9 380.14 Perry's, 6th Ed

0.02 216.1088435 Petro-Canada, TechData Sheet IM-7877E (04.03)

1536 10300 Dow, SYLTHERM™ 800 Product Information Sheet, Nov 2001

7.5 2055 Dow, SYLTHERM™ HF Product Information Sheet, Nov 2001

300 5250 Dow, SYLTHERM™ XLT Product Information Sheet, Dec 2003

15.5 470 Thermalane 600 Data Sheet, 2010

3.8 113 Thermalane 800 Data Sheet, 2010

0.837 141 Therminol Reference Disk, Version 5.0

11.7 1210 Therminol Reference Disk, Version 5.0

6.31 242 Therminol Reference Disk, Version 5.0

8.74 231 Therminol Reference Disk, Version 5.0

239 2280 Therminol Reference Disk, Version 5.0

125 1480 Therminol Reference Disk, Version 5.0

8.45 1270 Therminol Reference Disk, Version 5.0

18.2 5960 Therminol Reference Disk, Version 5.0

81.3 1880 Therminol Reference Disk, Version 5.0

142 5650 Therminol Reference Disk, Version 5.0

126 2990 Therminol Reference Disk, Version 5.0

0.687 138 Therminol Reference Disk, Version 5.0

355.1 760 0

1.42 112.1 www.radcoind.com

0.346 267 www.radcoind.com

2.73 184 www.radcoind.com

5.7 1690 www.radcoind.com

0 0 www.radcoind.com

204 8096 0

17.6 3156 www.radcoind.com

Page 79: 02 Heat Exchangers
Page 80: 02 Heat Exchangers

Fluid Name: Acetic Acid <-- Already in the database

Manufacturer:

Description: pure component Heat Vap 395

Operating range: °C minimumFP 39

°C maximumBP 118.1

Source:Perry's, 6th Ed Mol Wt 60.05

Liquid Thermal Vapor

Temp. Density Sp. Heat Conduct. Visc. Pressure

°C kg/cu.m. KJ/kg-°K W/m-°K cP mm Hg

0 1068.667 0.468 0.099 1.820 1048.667 0.485 0.099 2.28 11.6840 1028.667 0.503 0.099 0.9560 1008.667 0.52 0.099 0.75 89.7480 988.6667 0.54 0.099 0.6

100 968.6667 0.56 0.099 0.48 424.10

Fluid Name: Methyl Alcohol <-- Already in the database

Manufacturer:Description: Heat Vap 1100

Operating range: °C minimum FP 12

°C maximum BP 64.7

Source: Mol Wt 32.04

Liquid Thermal Vapor

Temp. Density Sp. Heat Conduct. Visc. Pressure

°C kg/cu.m. KJ/kg-°K W/m-°K cP mm Hg

-10 819.4333 0.565 0.124 0.920 810.1833 0.578 0.124 0.8 29.60

10 800.9333 0.588 0.124 0.6920 791.6833 0.594 0.124 0.6 96.7030 782.4333 0.608 0.124 0.5240 773.1833 0.618 0.124 0.47 265.60

Fluid Name: Ethyl Alcohol <-- Already in the database

Manufacturer:Description: pure component Heat Vap 842

Operating range: °C minimum FP 13

°C maximum BP 78.4

Source: Perry's, 6th Ed Mol Wt 46.07

Liquid Thermal Vapor

Temp. Density Sp. Heat Conduct. Visc. Pressure

°C kg/cu.m. KJ/kg-°K W/m-°K cP mm Hg

Page 81: 02 Heat Exchangers

-10 815.04 0.457 0.105 2.070 806.45 0.49 0.105 1.7 11.97

10 797.86 0.525 0.105 1.420 789.27 0.562 0.105 1.19 44.2530 780.68 0.598 0.105 0.9840 772.09 0.636 0.105 0.85 135.00

Fluid Name: Propyl Alcohol, n- <-- Already in the database

Manufacturer:Description: pure component Heat Vap 695

Operating range: °C minimum FP 15

°C maximum BP 97.8

Source: Perry's, 6th Ed Mol Wt 60.1

Liquid Thermal Vapor

Temp. Density Sp. Heat Conduct. Visc. Pressure

°C kg/cu.m. KJ/kg-°K W/m-°K cP mm Hg

-10 827.3 0.51 0.089 4.70 819.4333 0.532 0.091 3.7 3.36

20 803.7 0.58 0.093 2.3540 787.9667 0.628 0.095 1.5 51.9060 772.2333 0.672 0.097 180 756.5 0.72 0.099 0.7 380.14

Page 82: 02 Heat Exchangers

Fluid Name: Propyl Alcohol, i- <-- Already in the database

Manufacturer:

Description: pure component Heat Vap 663

Operating range: °C minimumFP 12

°C maximumBP 82.5

Source:Perry's, 6th Ed Mol Wt 60.1

Liquid Thermal Vapor

Temp. Density Sp. Heat Conduct. Visc. Pressure

°C kg/cu.m. KJ/kg-°K W/m-°K cP mm Hg

-10 809.7536 0.55 0.094 4.80 801.5741 0.58 0.093 3.7 8.42

20 785.2152 0.641 0.092 2.2540 768.8563 0.702 0.091 1.35 107.2060 752.4973 0.76 0.09 0.8780 736.1384 0.825 0.089 0.56 690.48

Fluid Name: Glycerol <-- Already in the database

Manufacturer:Description: pure component Heat Vap 663

Operating range: °C minimum FP 160

°C maximum BP 290

Source: Perry's, 6th Ed Mol Wt 92.1

Liquid Thermal Vapor

Temp. Density Sp. Heat Conduct. Visc. Pressure

°C kg/cu.m. KJ/kg-°K W/m-°K cP mm Hg

60 1136.555 0.62 0.164 9280 1084.291 0.645 0.164 34

100 1032.027 0.67 0.164 13.5120 979.763 0.694 0.164 5.4140 927.499 0.72 0.164 2.4160 875.235 0.743 0.164 1

Fluid Name: Butyl Alcohol, n- <-- Already in the database

Manufacturer:Description: pure component Heat Vap 581

Operating range: °C minimum FP 29

°C maximum BP 117.5

Source: Perry's, 6th Ed Mol Wt 74.12

Liquid Thermal Vapor

Temp. Density Sp. Heat Conduct. Visc. Pressure

°C kg/cu.m. KJ/kg-°K W/m-°K cP mm Hg

Page 83: 02 Heat Exchangers

0 0.5 0.101 4.720 0.555 0.099 2.9 4.8640 0.61 0.097 1.860 0.67 0.095 1.18 60.3980 0.72 0.093 0.79

100 0.78 0.091 0.55 386.72

15 1264.15 60 1136.555

20 1261.08 1293.347 80 1084.291

25 1158.02 -2.6132 100 1032.027

30 1254.95 120 979.763

140 927.499

160 875.235

Page 84: 02 Heat Exchangers

Use this worksheet to capture parameters from Yaws publications, such as "Yaws' Handbook of Thermodynamic and Physical Properties of Chemical Compounds", then copy to the Fluid Data sheet for entry into the database.

Heat Capacity of Liquid Density of LiquidCp = A + BT + CT2 + DT3 density = A B^(-(1-T/Tc)^n)

A B C D Temp J/mol-K AButane, n C4H10 62.873 5.89E-01 -2.36E-03 4.23E-06 2.98E+02 1.41E+02 2.28E-01Pentane C5H12 80.641 6.22E-01 -2.27E-03 3.74E-06 2.98E+02 1.64E+02 2.31E-01Hexane C6H14 78.848 8.87E-01 -2.95E-03 4.20E-06 2.98E+02 1.93E+02 2.32E-01Octane C8H18 82.736 1.30E+00 -3.83E-03 4.65E-06 2.98E+02 2.55E+02 2.28E-01

Fluid Name: Octane

Manufacturer:Description: pure component

Operating range: °C minimum°C maximum

Source: Yaw's Handbook, 2003

Liquid Thermal

Temp. Density Sp. Heat Conduct.K °C kg/cu.m. KJ/kg-°K W/m-°K

Row 4 253.15 -20 732.52 2.13 0.142 293.15 20 702.52 2.22 0.131 333.15 60 670.59 2.32 0.118 373.15 100 636.16 2.44 0.106 393.15 120 617.75 2.51 0.099 413.15 140 598.35 2.59 0.092

Page 85: 02 Heat Exchangers

Use this worksheet to capture parameters from Yaws publications, such as "Yaws' Handbook of Thermodynamic and Physical Properties of Chemical Compounds", then copy to the Fluid Data sheet for entry into the database.

Density of Liquid Liquid Viscositydensity = A B^(-(1-T/Tc)^n) log10(cP) = a + B/T + CT + DT2

B n Tc Temp g/cc A B C D2.72E-01 2.86E-01 4.25E+02 2.50E+01 5.73E-01 -6.86E+00 6.74E+02 2.20E-02 -3.07E-052.69E-01 2.82E-01 4.70E+02 2.50E+01 6.21E-01 -7.17E+00 7.47E+02 2.17E-02 -2.72E-052.65E-01 2.78E-01 5.07E+02 2.50E+01 6.56E-01 -5.07E+00 6.55E+02 1.23E-02 -1.50E-052.55E-01 2.69E-01 5.69E+02 2.50E+01 6.99E-01 -5.92E+00 8.88E+02 1.30E-02 -1.36E-05

Heat Vap 302.38

FP 13.33333333

BP 125.6666667

Mol Wt 114.231

VaporVisc. PressurecP mm Hg

1.01 0.68

0.56 10.58

0.37 77.81

0.26 349.69

0.22 648.62

0.19 1,121.74

Page 86: 02 Heat Exchangers

Use this worksheet to capture parameters from Yaws publications, such as "Yaws' Handbook of Thermodynamic and Physical Properties of Chemical Compounds", then copy to the Fluid Data sheet for entry into the database.

Liquid thermal conductivity Vapor Pressurek = A + BT + CT^2, W/(m-K) log10(mm Hg) = A + B/T + ClogT + DT + ET^2

Temp cP MW A B C Temp W/m-K A2.98E+02 1.71E-01 5.81E+01 2.38E-01 -3.76E-04 -2.53E-07 2.98E+02 1.04E-01 2.70E+012.98E+02 2.45E-01 7.22E+01 1.88E-01 -3.78E-06 -4.35E-07 2.98E+02 1.48E-01 3.33E+012.98E+02 2.86E-01 86.177 2.10E-01 -2.26E-04 -2.34E-07 2.98E+02 1.21E-01 6.97E+012.98E+02 5.27E-01 1.14E+02 2.00E-01 -1.77E-04 -2.00E-07 2.98E+02 1.29E-01 2.91E+01

Page 87: 02 Heat Exchangers

Vapor Pressurelog10(mm Hg) = A + B/T + ClogT + DT + ET^2 Heat Vap FP BP

B C D E Temp mm Hg kJ/kg C C-1.90E+03 -7.18E+00 -6.68E-11 4.22E-06 2.98E+02 1.83E+03 386.116 -59.44444 -0.444444-2.42E+03 -9.24E+00 9.02E-11 4.11E-06 2.98E+02 5.14E+02 357.5062 -49.44444 36.05556-3.63E+03 -2.39E+01 1.28E-02 -1.68E-13 2.98E+02 1.53E+02 334.944 -21.66667 68.77778-3.01E+03 -7.27E+00 -2.27E-11 1.47E-06 2.98E+02 1.41E+01 302.38 13.33333 125.6667