Heat_Exchangers Sizing Suparma

5/28/2018 Heat_Exchangers Sizing Suparma

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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

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 REDtext. 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.

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

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

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

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

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

10. The Conversions worksheet is used for data, including the status of radio buttons and checkboxes, and must

not be deleted!

ChemEng Software sells an Excel template called TANKJKT

www.chemengsoftware.com

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.

Customary US SI
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Use this worksheet to define the components present in the hot and cold streams for a heat tra

Multiple components from the Fluid Data properties table can be specified, and their propertiesAverging properties for non-ideal solutions, such as polar mixtures (with water), gives poor resu

A better approach is to define the properties for the mixtures at several temperatures and add t

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

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 Components

Name in Data Table? Description1 Water YES City water

2 Methyl Alcohol YES pure component

3

4

5

6

7

8

9

Cold Fluid Components

Name in Data Table? Description

1 Water YES City water

2

3

4

5

6

7

8

9

Problem Statement:Define components for the hot and cold streams


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sfer problem.

will be averaged. lts.

em to the database.


6/85

Inputs

Hot Side

Fluid name Distilled Water

Flow Total lb/h 396,000

Temperature, in F 90

Temperature, out F 77

Pressure, in psig 29

Press Drop Allowed psig 2

Fouling Resistance ft-h-F/Btu 0.0005

Cold Side

Fluid name Raw Water

Flow Total lb/h 1,188,000

Temperature, in F 68Temperature, out F 72

Pressure, in psig 60

Press Drop Allowed psig 10

Fouling Resistance ft-h-F/Btu 0.0005

mass frac

Component Density

Hot Side Fluid Components mass fraction mole fracti lb/ft3

1 Water 1 61.91

2 Methyl Alcohol 0 -

3

4

5

6

7

8

9

OK 61.91

Cold Side Fluid Components

1 Water 1 62.25

2

3

4

56

7

8

9

OK 62.25

Problem Statement:Specify process conditions for a liquid-liquid heat exchangeproblem, 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


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Shell Side Tube

Parameter Units In Out In

Fluid Name Distilled Water Raw

Flow Total lb/h 396000 1188

Vapor lb/h

Liquid lb/hSteam lb/h

Water lb/h

Noncondensable lb/h

Evap/Cond lb/h

Temperature (In/Out) F 89.6 68

Density lb/ft3

Viscosity cP

Molecular Weight, vapor

Molecular Weight, noncondensibles

Specific Heat Btu/lb-F

Thermal Conductivity Btu/h-ft-F

Latent Heat Btu/lbInlet Pressure psig 29.00754 60

Velocity ft/s

Press Drop Allowed psig 1.5 10

Fouling Resistance ft-h-F/Btu 0.000499687 0.000499687


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Temp, C

Temp, C

Heat Transferred

5,002,748 Btu/h

Temp, CTemp, C

mass frac

Viscosity Sp Heat herm Con H Vap Density Viscosity Sp Heat

cP MW Btu/lb-F Btu/h-ft-F Btu/lb lb/ft3 cP MW Btu/lb-F

0.77409439 18.02 1.00 0.35 971.63 62.11 0.902497 18.02 1.00

0.51586441 32.04 - - 472.91 - 0.562399 32.04 -

0.77409439 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


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Side

Out

ater

000


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32.00

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

20.0022.33 Heat 5,002,748 Btu/h 1,466,306 Watts

(0)

herm Con Antoine Coefficients VP VP Partial P Viscosity u

Btu/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 -0.25606

- 7.97 1,515.29 232.99 180.57 (11.20) 0 0

0.35 -0.25606

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

0.34 0.015857


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Viscosity Based on the Wall Temperatures

ing Eq 27-3 If Shell Side If Tube Side

cP ln(cP) cP ln(cP)

-0.10259 0.94347 -0.05819 0.92645 -0.0764

0 0.576321 0 0.570588 0

-0.10259 0.94347 -0.05819 0.92645 -0.0764

-0.04041 0.94 -0.05819 0.93 -0.0764

-0.04041 0.94347 -0.05819 0.92645 -0.0764


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Inputs

Fluid flowing in tubes Raw WaterAssumed overall U Btu/h-ft-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 1.000Average 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

Calculations

Tube inside diameter in 0.584

Flow area per tube ft 0.00186

Tube area available ft/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 ft 906

Total tube length req ft 4,615

Number of tubes 308

Tubes per pass 308

Actual area ft 907

Flow rate per tube lb/h 3,857

Velocity in tube ft/s 9.26

Reynolds Number 42,215

Friction Factor 0.0221

Pressure Drop, tubes psig 3.92

Pressure drop, enter/exit ft fluid neglect

Enter/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

Total pressure drop, tube side psig 4.78

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

Result


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Inputs (copied from the Process Data and Tubes worksheets)

Hot Side

Fluid name Distilled Water

Temperature, in F 89.60

Temperature, out F 77.00

Cold Side

Fluid name Raw Water

Temperature, in F 68.00

Temperature, out F 72.20

Tube passes 1

Shell passes N 1

Calculations

Intermediate 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 Case

Numerator (1.042)

Denomenator (1.107)

General Case Answer F 0.942

R=1 Case

Numerator 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


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Inputs Fluid flowing in tubes Raw Water

Assumed inside heat transfer coef Btu/h-ft-F 1,057

Data (from the Process Data and Tubes Pressure Drop worksheets)

Assumed overall U Btu/h-ft-F 520.0

Outside surface area ft 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 1.00Bulk thermal conductivity Btu/h-ft-F 0.34


Calculations

Inside surface area ft 706.36

Overall U based on inside area Btu/h-ft-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 calculation

Inside heat transfer coefficient Btu/h-ft-F 27

Turbulent flow calculation

Inside heat transfer coefficient Btu/h-ft-F 1,569

Transition flow calculation


Choose which one


Problem Statement:Calculate the tube side heat transfer coefficient

Result


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Inputs

Number of shells 1Shell inside diameter in 21.25


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is 23.3 in


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Inputs Fluid flowing in shell Distilled Water

Assumed outside heat transfer coef Btu/h-ft-F 704Baffle hole clearance 0.03

Data

Flow rate lb/h 396,000

lb/s 110.00

Assumed overall U Btu/h-ft-F 520.0

Outside surface area ft 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 0.84lb/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

Calculations

Average 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 ft 0.4707


j-ideal factor coefficients a1 0.370a2 (0.395)

a3 1.187

a4 0.370

a 0.169

j-ideal factor 0.007


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

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


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Correction Factor for Baffle Cut and Spacing

Baffle 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 18.25

Angle 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 2.0943951

Tubes 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 69.34Free 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 Effects

Formula coefficient C 1.25

Number of bypass divider lanes Np -

Width of bypass divider lanes wp 1.50

Area of bypass divider lanes, Abp ft 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 Spacing

Assuming even number of baffles so shell nozzles are on opposite sides

Odd number of flow lanes

Assume equal spacing for inlet and outlet baffles

Number 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* 1.50Baffle Spacing Factor Js 0.96

Correction for Temperature Gradient if Laminar Flow

Number of tube rows in one crossflow section 10.65

Correction factor 1.00


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Overall losses 0.69

Outside he Btu/h-ft-F 1,182.81 6,742.00


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Equiv Diam 0.229264


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Inputs

Data (from Shell htc worksheet)


Number of baffles 16

Pitch Ratio 1.33

Tube Pitch in 1.00

Tube Outside Diameter in 0.75


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 32.17Flow area, crossflow section, As ft 0.471

Flow area, window, Aw ft 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

Calculations

Velocity in crossflow at widest diameter

Velocity ft/s 3.77

Ideal Pressure Drop per Crossflow Section

f-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 factor

Intermediate exponent 0.57

Leakage correction factor RL 0.40

Crossflow pressure drop, corrected psig 1.48

Problem Statement:Calculate the shell side pressure drop


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Window Pressure Drop

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


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Inputs

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

Data

Assumed U Btu/h-ft-F 520

Film coefficient, tubes Btu/h-ft-F 1,569

Fouling resistance, tubes 0.00050

Fouling resistance, shell 0.00050

Film coefficient, shell Btu/h-ft-F 1,183

Outside diameter, tubes in 0.75

Inside diameter, tubes in 0.58

Thermal conductivity, tubes Btu/h-ft-F 24Heat transferred Btu/h 5,002,748

Mean temperature difference F 12.74

Calculations

Overall U, calculated, clean Btu/h-ft-F 503

Overall U, calculated, dirty Btu/h-ft-F 319

Area required, clean ft 781.29

Area required, fouled ft 1,229.45

Area provided by the design ft 907.13

Oversurface 16%

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


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Inputs

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

Data

Tubeside

Flow rate lb/h 1,188,000

Inlet density lb/ft3 62.25

Outlet density lb/ft3 62.19

Shellside

Flow rate lb/h 396,000

Inlet density lb/ft3 61.91

Outlet density lb/ft3 62.11

Calculations

Tubeside

Volumetric flow rate, tubeside inlet ft3/s 5.30

Minimum ID of nozzle in 13.94

Selected nozzle in 15.624

Selected nozzle designation in 16

Velocity ft/s 3.98

rho-v2 lb/ft2-s 986.84

Weight lb 146

Volumetric flow rate, tubeside outlet ft3/s 5.31




Velocity ft/s 3.99


Weight lb 146

Shellside

Volumetric flow rate, shellside inlet ft3/s 1.78




Velocity ft/s 2.12

rho-v2 lb/ft2-s 278.80Weight lb 90

Volumetric flow rate, shellside outlet ft3/s 1.77




Velocity ft/s 2.12


Weight lb 90

Problem Statement:Specify the size of the nozzles


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Inputs

Tubesheet thickness in 1Baffle Thickness in 0.5

Data

Shell Inside Diameter ft 1.770833

Shell Thickness ft 0.0625

Shell Length ft 15

Number of Baffles 16

Tube Outside Diameter ft 0.0625

Tube Inside Diameter ft 0.048667

Number of Tubes 308

Weight of steel lb/ft3 489.5

Density of water lb/ft3 62.4

Calculations

Shell 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 tubesheets

Add for nozzles lb 292

Baffles lb 804

Total, Tube Bundle empty lb 4,229

Total Weight, empty lb 7,017

Shell inside volume ft3 36.94Heads 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


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SHELL-AND-TUBE HEAT EXCHANGER

CLIENT EQUIP. NO PAGE

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

0

1 UNIT AREA PROCURED BY INSTALLED BY

2

1 Size TEMA Type Connected in (series/parallel)

2 Surface per Unit 907.13 Shells per Unit 1 Surface per Shell 907.1 ft

3 Performance of One Unit

4 Fluid Allocation Shell Side Tube Side

6 Fluid Name Distilled Water Raw Water

7 Flow Total lb/h 396,000 1,188,000

8 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, vapor

17 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/lb

20 Inlet Pressure psigg (inlet) 29.0 60.0

21 Velocity ft/s 3.77 9.26

22 Press Drop Allow/Calc psig 1.5 3.5 10.0 4.8

23 Fouling Factor ft-h-F/Btu 0.0005 0.0005

24 Heat Exchanged Btu/hr 5,002,748 LMTD (corrected) F 12.74

25 Service Coeff. Btu/h-ft-F Dirty 319 Clean 503

26 Construction Data for One Shell

27 Shell Side Tube Side Sketch

28 Design/Test Press psigg

29 Design Temperature F30 No. Passes per Shell 1 1

31 Corrosion Allowance in

32 In inches 12.00 16.00

33 Out 12.00 16.00

34 Intermediate

35 Tubes No. 308 OD, in 0.75 Gauge 14 Length, ft. 15 Pitch layout, deg. 90

36 Type Material Cr-alloy (0.5% Cr) Pitch ratio 1.33

37 Shell OD, in ID, in 21.25 Material

38 Channel or Bonnet OD, in Thick Channel Cover

39 Tubesheet Type

40 Floating Heat Cover Impingement Protection

41 Baffles Cross (number) 16 % Cut (d) 25% Spacing C/C, in 10.00

42 Baffles Long Seal Type No

43 Supports Tube U-Bend Type

44 Bypass Seal Arrangement NA Tube-Tubesheet Joint45 Expansion Joint No. Type

46 Rho-V2-Inlet Nozzle 987 Bundle Entrance 279 Bundle Exit 278

47 Gaskets - Shell Side Tube Side

48 Floating Heat Cover Supports

49 Code Requirements TEMA Class

50 Weight per shell lb 7,000 Filled w/water 9,200 Bundle 4,200

51

52 Notes

53

54

Connections

Size & Rating
http://www.chemengsoftware.com/


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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 Conver

3 area ft 0.09290304 m =INDEX( units_conv, index,

4 heat flux Btu/h-ft-F 5.678263 W/m-C returns the second column (

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

6 Heat transfer Btu/hr 0.2931 W Example7 flowrate gal/min 3.785412 liters/min Index = 8 (fouling)

8 fouling ft-h-F/Btu 0.1761102 m-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 3.2808399

13 area ft 0.09290304 m

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 v isc lb/ft-h 0.00041338 kg/m-s

18 density lb/ft3

16.01846 kg/m3

Units 1 2 User Inputs FALSE

Solve For 6 Calc Results FALSE

Distilled WateShell 2 Mech Detail FALSE

Raw Water Tubes General Inputs FALSE

Tube Diameters Tube Gauges

in US SI US Min Max

0.25 0.250 6.35 0.250 18 27

0.375 0.375 9.53 0.375 14 24

0.5 0.500 12.70 0.500 13 24

0.625 0.625 15.88 0.625 12 24

0.75 0.750 19.05 0.750 10 24

1 1.000 25.40 1.000 8 241.25 1.250 31.75 1.250 8 24

1.5 1.500 38.10 1.500 8 24

2 2.000 50.80 2.000 4 24

Units Conversion to SI 19.05 10

to US #N/A 24

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


29/85

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 0.8660254 1

45 0.70710678 1.41421356

60 0.5 1.73205081

90 1 1

Standard Shell Sizes, Inside Diameter Shell Thickne

inches inches mm mm inches OD, inches

7.981 10.02 7.981 10.02 203 255 0.644 8.625

10.02 12 10.02 12 255 305 0.73 10.75

12 13.25 12 13.25 305 337 0.75 12.75

13.25 15.25 13.25 15.25 337 387 0.75 14

15.25 17.25 15.25 17.25 387 438 0.75 16

17.25 19.25 17.25 19.25 438 489 0.75 18

19.25 21.25 19.25 21.25 489 540 0.75 20

21.25 23.25 21.25 23.25 540 591 0.75 22

23.25 25 23.25 25 591 635 0.75 24


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25 27 25 27 635 686 1 26

27 29 27 29 686 737 1 28

29 31 29 31 737 787 1 30

31 33 31 33 787 838 1 32

33 35 33 35 838 889 1 34

35 37 35 37 889 940 1 36

37 39 37 39 940 991 1 3839 42 39 42 991 1067 1 40

42 45 42 45 1067 1143 1 43

45 48 45 48 1143 1219 1 46

48 54 48 54 1219 1372 1 49

54 60 54 60 1372 1524 1 55

60 66 60 66 1524 1676 1 61

66 72 66 72 1676 1829 1 67

72 78 72 78 1829 1981 1 73

78 84 78 84 1981 2134 1 79

84 90 84 90 2134 2286 1 85

90 96 90 96 2286 2438 1 91

96 108 96 108 2438 2743 1 97108 120 108 120 2743 3048 1 109

120 132 120 132 3048 3353 1 121

Correlation Coefficients for j-I and f-I

Pitch Layo Nre a1 a2 a3 a4 b1 b2

30 0 1.4 -0.667 1.45 0.519 48 -1

30 10 1.36 -0.657 1.45 0.519 45.1 -0.973

30 100 0.593 -0.477 1.45 0.519 4.57 -0.476

30 1000 0.321 -0.388 1.45 0.519 0.486 -0.152

30 10000 0.321 -0.388 1.45 0.519 0.372 -0.123

45 0 1.55 -0.667 1.93 0.5 32 -1

45 10 0.498 -0.656 1.93 0.5 26.2 -0.913

45 100 0.73 -0.5 1.93 0.5 3.5 -0.476

45 1000 0.37 -0.396 1.93 0.5 0.333 -0.136

45 10000 0.37 -0.396 1.93 0.5 0.303 -0.126

60 0 1.4 -0.667 1.45 0.519 48 -1

60 10 1.36 -0.657 1.45 0.519 45.1 -0.973

60 100 0.593 -0.477 1.45 0.519 4.57 -0.476

60 1000 0.321 -0.388 1.45 0.519 0.486 -0.152

60 10000 0.321 -0.388 1.45 0.519 0.372 -0.123

90 0 0.97 0.667 1.187 0.37 35 -1

90 10 0.9 -0.631 1.187 0.37 32.1 -0.0963

90 100 0.408 -0.46 1.187 0.37 6.09 -0.60290 1000 0.107 -0.266 1.187 0.37 0.0815 -0.022

90 10000 0.37 -0.395 1.187 0.37 0.391 -0.148

Tube Materials and Thermal Conductivities

Aluminum 130 130

Brass (75 72 72

Bronze (75 15 15


31/85

Cr-alloy (0. 24 24.4

Constanta 14 14

Copper 220 220

Iron 26 26

Magnesiu 95 95

Molybdenu 64 64

Nickel 43 43Steel (1% 20 20

Steel (1% 27 27

Steel (18% 12 12

Zinc 58 58

Pipe Sizes

ID Pipe Size Nozzle Wt ID Pipe Size Nozzle Wt ID

in in lb in in lb mm

1.049 1 3 1.049 1 3 26.6446

1.049 1.61 1.5 4 1.61 1.5 4 40.894

1.61 2.067 2 6 2.067 2 6 52.50182.067 3.26 3 12 3.26 3 12 82.804

3.26 4.26 4 17 4.26 4 17 108.204

4.26 6.357 6 28 6.357 6 28 161.4678

6.357 8.329 8 44 8.329 8 44 211.5566

8.329 10.42 10 56 10.42 10 56 264.668

10.42 12.39 12 90 12.39 12 90 314.706

12.39 13.624 14 118 13.624 14 118 346.0496

13.624 15.624 16 146 15.624 16 146 396.8496

15.624 17.624 18 170 17.624 18 170 447.6496

17.624 19.564 20 202 19.564 20 202 496.9256

19.564 23.5 24 275 23.5 24 275 596.9


32/85

sion table is:

2)

i.e., US units name)


33/85

ss Flange Weight

OD, mm lb lb kg

219.075 28 28 13

273.05 40 40 18

323.85 61 61 28

355.6 83 83 38

406.4 106 106 48

457.2 108 108 49

508 148 148 67

558.8 180 204 93

609.6 204 204 93


34/85

660.4 210 210 95

711.2 230 230 105

762 240 240 109

812.8 260 260 118

863.6 270 270 123

914.4 185 185 84

965.2 300 300 1361016 310 310 141

1092.2 330 330 150

1168.4 360 360 164

1244.6 380 380 173

1397 420 420 191

1549.4 460 460 209

1701.8 505 505 230

1854.2 550 550 250

2006.6 590 590 268

2159 630 630 286

2311.4 675 675 307

2463.8 720 720 3272768.6 805 805 366

3073.4 890 890 405

b3 b4

7 0.5

7 0.5

7 0.5

7 0.5

7 0.5

6.59 0.52

6.59 0.52

6.59 0.52

6.59 0.52

6.59 0.52

7 0.5

7 0.5

7 0.5

7 0.5

7 0.5

6.3 0.378

6.3 0.378

6.3 0.3786.3 0.378

6.3 0.378


35/85

Pipe Size Nozzle Wt

DN kg

25 1.363636

40 1.818182

50 2.72727380 5.454545

100 7.727273

150 12.72727

200 20

250 25.45455

300 40.90909

350 53.63636

400 66.36364

450 77.27273

500 91.81818

600 125


36/85

Use this area to enter raw data. The coefficients

To remove an entry from the database, use Tools Protection Unprotect, th


37/85

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



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 20/DOWFROST 20 - 30 vol% Dow Chemical

DOWCAL 20/DOWFROST 20 - 40 vol% Dow Chemical

DOWCAL 20/DOWFROST 20 - 50 vol% Dow ChemicalDOWCAL 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 HD - 30 vol% Dow Chemical



DOWTHERM 4000 - 30 Vol% Dow Chemical

DOWTHERM 4000 - 40 Vol% Dow Chemical

DOWTHERM 4000 - 50 Vol% Dow ChemicalDOWTHERM A Dow Chemical

DOWTHERM G Dow Chemical

DOWTHERM J Dow Chemical

DOWTHERM MX Dow Chemical

DOWTHERM Q Dow Chemical

DOWTHERM RP Dow Chemical

DOWTHERM SR-1 - 30 Vol% Dow Chemical




38/85

DOWTHERM T Dow Chemical

DURATHERM 450 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 EG - 20 Vol% Dynalene



Dynalene HC-10 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% DynaleneDynalene 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 MultiThermMultiTherm FF-1 MultiTherm

MultiTherm IG-1 MultiTherm

MultiTherm IG-4 MultiTherm

MultiTherm OG-1 MultiTherm

MultiTherm PG-1 MultiTherm

MultiTherm ULT-170 MultiTherm

MultiTherm WB+14 MultiTherm

MultiTherm WB-22 MultiTherm



39/85



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 D-12 Solutia

Therminol LT Solutia

Therminol VLT Solutia

Therminol VP-1 SolutiaTherminol 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


40/85

re calculated, ready to be pasted (use "Paste Special Values") onto the corresp

n delete the row with the offending compound Units that the original data a

Temperature

Density

Specific Heat

Thermal Conductivity

Viscosity

Heat of Vaporization

Fluid Name: Octane

Manufacturer:

Description: pure comp

Operating range:

Source: Yaw's Han

Liquid

Temp. Density Sp. Heat

C kg/cu.m. KJ/kg-K

Enter values at SIX temperatures -->>> -20 732.5191 2.128494

20 702.5186 2.218223

60 670.5874 2.315248

100 636.161 2.435187

120 617.7531 2.508629

140 598.3474 2.593657

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

0

100

200

300

400

500

600

700

800

-50 0 50 100 150

Density

0

0.5

1

1.5

2

2.5

3

-50 0 50 100

Specific Heat


41/85

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 93.3333333 315.555556

Premium high temperature oil resists oxidation 10 343.333333

Premium high temperature single compound formulation 37.7777778 351.666667

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



Propylene glycol with inhibitor package 0 170

Propylene glycol with inhibitor package -15 170

Propylene glycol with inhibitor package -30 170Propylene 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, dyed bright yellow -10 100



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 120Biphenyl 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

Synthetic diaryl alkyl liquid 10 350

Ethylene glycol with inhibitors, dyed fluorescent pink -10 120



Density Predicted Specific Heat Predicted


42/85

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 115.555556



Inhibited ethylene glycol -6.66666667 121.111111



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





Biodegradable aliphatic hydrocarbon blend, food grade -80 162.777778

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 162.777778

Propylene glycol with corrosion inhibitors -6.66666667 121.111111

Propylene glycol with corrosion inhibitors -6.66666667 121.111111Propylene glycol with corrosion inhibitors -28.8888889 121.111111

Propylene glycol with corrosion inhibitors -28.8888889 121.111111

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 260Flushing Fluid -18 260

White mineral oil -20 288


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




43/85



pure component 0 0

Synthetic hydrocarbon blend -95.5555556 218.333333

Alkylated aromatic for closed loop liquid phase heating 35 301.666667

Hydrotreated heavy paraffinic distillate - mineral oil 52.7777778 310

Alkylated aromatic, for closed loop heating 25 357.222222

Paraffinic hydrocarbon, for closed loop heating and cooling -49.4444444 248.888889

Linear alkene, food grade 2.22222222 304.444444

Linear alkene, fully saturated -3.88888889 248.888889

Hydrotreated mineral oil, food grade 35.5555556 332.222222

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



Premium heat transfer fluid, non-toxic, environmentally friendly 65.5555556 315.555556

Premium heat transfer fluid, non-toxic, environmentally friendly 65.5555556 315.555556

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 400Mixture of cyclohexylbenzene and bicyclohexyl 2 330


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


44/85

onding line in the HTF_properties table

e in:

5.16 38.5994677


45/85

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

A B C A B C m b m

7.095765 1455.314 219.7032524 -6.833946 3563.967 276.8476 -0.836933 718.2331 -0.00031032

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

A B C m b m

7.61280104 1673.3465 235.6539233 -1.77875697 139.628222 -239.507339 -1 1068.66667 0

6.83250565 946.409614 240.0761027 -5.3689507 1681.68714 167.152173 -1.03186377 601.637011 -0.000501779

7.91163548 1619.0414 204.0887995 -9.94017218 4947.16886 156.39307 -0.8 810 -0.000173074

2.26230342 59.8606199 -25.95580511 -2.81012363 862.729917 -172.158588 -0.61886679 876.709741 -5.39694E-05

2.14571749 63.3160876 -24.72735114 -3.01949171 971.167036 -162.441888 -0.63704744 880.380827 -5.24039E-05

-3.07699041 295.80735 -314.6610817 -2.94432736 771.280208 -150.474936 -0.65896583 829.792536 -8.58261E-05

-37.9837715 123237.007 -3346.097015 -2.72003397 756.18052 -187.060596 -0.63433102 909.784454 -7.53018E-059.48506388 4973.22315 486.5437469 -3.88723617 1148.41536 -77.458893 -0.7967977 998.969388 -0.000130758

28.9797843 69967.7155 2296.20798 -2.85235243 801.597857 -167.466984 -0.69941173 1043.82327 -0.000103607

7.20221146 1946.56786 193.68084 -2.95622194 695.510584 -136.279632 -1.02463504 1094.60097 -0.000163869

-5.09981535 4803.75401 -906.2417005 -2.63441952 587.992289 -159.411101 -0.87116438 1047.89247 -0.000144863

8.82454372 3748.71673 336.9459257 -3.29046723 883.473425 -119.018457 -0.78787671 1021.96438 -0.00013226

35.7643154 93078.0316 2471.74935 -2.56805621 631.444576 -209.147287 -0.76328811 1038.67039 -9.93216E-05

-4.18081142 909.733925 -107.595417 -0.69488127 1059.3277 0.000323694

-4.72704655 1202.56579 -83.1814303 -0.72116095 1073.66245 0.000282533

-5.29129088 1555.1265 -56.1413767 -0.74828496 1087.06684 0.000250237

-2.86784498 390.436942 -193.613817 -0.74307594 1043.92172 0.000306701

-2.20133794 260.582798 -221.938677 -0.79859604 1053.05786 0.000220421

-2.66533983 403.308763 -202.562555 -0.8417358 1060.73452 0.000146139-3.08252386 464.399539 -181.185017 -0.64370968 1040.8621 0.000527581

-2.87005695 429.310358 -194.091739 -0.69306452 1049.90565 0.000396129

-3.18080553 558.897515 -181.131448 -0.73548387 1056.85484 0.000273065

-3.045242 463.810598 -181.232182 -0.65730675 1042.75963 0.000492448

-2.9578147 466.738492 -188.559297 -0.64887019 1046.96257 0.000474057

-3.42416369 657.085113 -167.978944 -0.65769786 1050.3615 0.000385743

-3.045242 463.810598 -181.232182 -0.64224014 1052.61507 0.000492448

-2.9578147 466.738492 -188.559297 -0.63581858 1060.21744 0.000474057

-3.42416369 657.085113 -167.978944 -0.64961462 1067.10324 0.000385743

-3.99338037 832.566174 -119.083818 -0.58424609 1064.74959 0.000694745

-4.4123843 1071.20113 -98.7745604 -0.6082127 1080.97748 0.000627814

-4.25027294 991.8804 -118.108745 -0.61823431 1094.54251 0.000578445

8.72897534 3828.10537 392.5107135 -5.48503015 2637.3596 105.666504 -0.98934972 1091.5087 -0.00016

28.1430775 70966.9119 2506.647171 -4.208744 1446.74664 -80.3558975 -0.77471755 1062.346 -0.000115799

59.097408 290462.758 4950.07402 -3.07063398 638.520693 -77.403951 -0.91493913 873.679072 -0.000210713

-416.758373 15972102 -38392.31208 -4.54701255 1505.76821 -91.4516506 -0.77585921 979.0294 -0.000105072

25.6353331 53251.6069 2053.164001 -3.39154275 743.091582 -135.906784 -0.76281754 982.12802 -0.000148728

-15.6439238 25860.1396 -1755.479927 -3.19903031 983.170224 -141.828205 -0.7434472 1046.4705 -0.000129669

-3.99338037 832.566174 -119.083818 -0.54151408 1055.19949 0.000694745

-4.4123843 1071.20113 -98.7745604 -0.54963153 1068.6496 0.000627814

-4.25027294 991.8804 -118.108745 -0.54397093 1078.97886 0.000578445

Thermal Conductivity Predicted Viscosity


46/85

20.3132266 24800.7847 1071.483568 -3.37173363 1025.67055 -139.929331 -0.68913684 887.043789 -0.000220727

-6.65052916 8198.94117 -1156.00701 -2.74761032 674.268007 -150.950719 -0.67776556 874.500928 -7.52836E-05

-7.66614364 5665.64899 -900.1096362 -2.90618465 903.56193 -168.873971 -0.67433792 866.394492 -5.06875E-05

24.8346647 45060.3451 1649.092109 -2.99273743 972.314421 -160.441312 -0.6729646 870.14053 -5.29426E-05

24.8346647 45060.3451 1649.092109 -2.99273743 972.314421 -160.441312 -0.6729646 870.14053 -5.29426E-05

2.13587455 189.077565 17.01391236 -2.13317423 859.946884 -168.196304 -0.54570512 938.153151 -0.000149791

-7.66614364 5665.64899 -900.1096362 -2.90618465 903.56193 -168.873971 -0.67433792 866.394492 -5.06875E-05

14.9056254 16265.9291 1013.657369 -3.01482131 794.646368 -152.129254 -0.68415812 827.037921 -8.50181E-05

2.6299395 181.8693 58.26576228 -3.82938429 3727.45019 178.471948 -0.46997219 976.741862 -0.000201071

-3.01120449 165.766084 -95.92933945 -1.9215881 442.314778 -120.787412 -0.49885816 847.432843 -6.53313E-05

5.57763185 1026.16852 178.181417 -2.66100775 567.17649 -137.006506 -0.96414298 848.450174 -9.78985E-05

-1.97270453 2181.19609 29.0849155 -1 983 -0.000177332

-2.83906455 403.139039 -179.040208 -0.5605716 1029.82605 0.000753011

-1.76210182 259.453088 -209.449865 -0.64190891 1046.82337 0.000493144

-2.12735955 490.764922 -175.45123 -0.70769845 1058.28048 0.000233571

-3.51929213 637.366085 -135.037251 -0.52459314 1045.92863 0.000890948

-3.92835821 860.275658 -122.034579 -0.58864285 1080.85328 0.000694526

-4.39901578 1040.08743 -122.076833 -0.623489 1109.9764 0.000518207

-4.27578767 1294.15173 -23.8949564 -0.69130435 1363.17391 0.001

-5.29105882 2948.83834 163.736049 -0.498 1248.8 0.000954

-0.5122831 242.645316 -157.837138 -0.59558824 1282.94118 0.0011

-2.98689604 974.823436 -58.2554382 -0.7 1330 0.0009875

-8.68421954 4625.64436 162.883606 -0.55 1362.5 0.00098

10.4702484 4350.47796 388.8685902 -11.0043264 7574.14569 365.455443 -0.70241532 816.779716 -0.00019755

-3.80185344 919.152443 -81.3856983 -0.75981804 777.667147 -0.0002

-3.36183913 1050.83759 -143.20005 -0.71592357 1058.50955 -0.000131866

-4.00909241 975.004321 -100.530572 -0.50167515 784.007404 -0.0002

-3.18052868 851.714045 -146.012607 -0.69815357 814.927926 -0.0002

-27.8705129 38860.6487 -1417.676868 -4.49525801 1230.87547 -17.8291423 -0.77262148 860.838771 -0.00023774

-3.74394592 656.323421 -145.485726 -0.53046604 1028.41796 0.000828175

-4.05786883 747.147276 -159.321194 -0.60831178 1045.76259 0.000552562-4.27097369 936.234236 -150.361442 -0.65216852 1056.38287 0.000298992

-4.61030436 1143.83082 -143.218804 -0.79010375 1069.0127 2.6401E-06

-3.48506455 1205.75734 -123.228873 -0.67317309 890.394634 -7.98064E-05

8.24226184 1664.52116 232.3397815 -11.706753 8152.45002 393.04237 -0.859 806.45 0

-38.7259008 37120.5808 525.396605 -2.6132 1293.347 0

6.70328236 1088.11314 215.7520678 -6.66531604 3106.12647 275.229903 -0.920173 678.154718 -0.000367942

0.71075903 588.631148 -607.782559 -4.46280906 1669.13304 -79.9072873 -0.65682095 861.644336 -6.09013E-05

-2.76497138 699.238152 -125.207148 -0.80729276 1013.83001 -0.000115215

-4.37009218 1719.23359 -67.8658053 -0.67166842 890.128017 -8.13221E-05

-3.14384109 1006.84538 -143.852661 -0.71437566 1058.29801 -0.000130902

7.97490403 1515.29299 232.9925145 -3.74186653 790.395993 -48.5241917 -0.925 810.183333 0

-3.71515205 1037.38665 -112.624039 -0.65445205 806.945205 -6.17808E-057.51566896 3644.82103 270.4466347 -3.3434809 955.122738 -161.065638 -0.64814403 921.092095 -7.20142E-05

-2.89037717 907.431382 -174.35564 -0.52528383 871.656695 -7.58821E-05

-3.23842923 1030.80614 -162.583226 -0.7102096 877.674104 -7.31778E-05

-2.66844708 863.516386 -172.933185 -0.53597908 871.68433 -3.65204E-05

-3.15870057 876.135353 -167.030762 -0.42033079 881.665861 -7.23081E-05

-1.69617834 283.955002 -121.548471 -0.7704 860.46 -0.0002

-27.5351301 49896.876 1485.7617 -0.47945946 1200.67838 0.001

-1.54976022 217.121005 -191.167196 -0.49828571 1285.35238 0.001

-1.19730032 266.839119 -166.715718 -0.57375 1325.51875 0.001079375


47/85

-1.0665069 193.588581 -191.633517 -0.52806452 1249.57581 0.001

-2.01954397 517.644659 -128.383873 -0.6 1365 0.001032571

7.09576455 1455.31374 219.7032524 -6.83394648 3563.96711 276.847589 -0.83693261 718.23307 -0.000310324

5.92200603 1219.83799 210.0557232 -2.78483901 568.89108 -70.8208174 -1.00816159 848.287022 -7.65213E-05

8.35788197 3690.19194 318.4911918 -3.77429163 1137.44614 -140.259573 -0.69564974 892.810091 -0.0001413

-4.59859581 1009.03868 -476.9550459 -3.19587269 1055.90681 -156.107582 -0.64127846 875.94107 -7.54452E-05

19.1763873 25786.0495 1240.253276 -3.73340177 1159.41959 -121.829193 -0.76651297 971.079915 -9.94852E-05

7.49894628 2118.74094 241.8051037 -4.05132143 992.583192 -80.5601433 -0.73774932 777.637054 -7.74155E-05

15.5673243 14491.9443 814.9374854 -2.99507893 757.840553 -148.641263 -0.56305007 809.516314 -8.53552E-05

-2.79779088 620.439195 -163.735706 -0.73934467 816.409984 -5.5092E-05

3.5182312 568.508019 65.24581769 -11.0429218 7675.28364 244.627778 -0.6627339 897.731878 -5.09146E-05

6.81500108 1036.92193 227.6362862 -4.95789137 1823.41444 215.815164 -0.95760086 644.49611 -0.000241321

-2.60201382 745.236551 -188.098093 -0.63255801 878.7054 0

8.07089889 1562.67722 218.6912381 -13.528855 8140.33431 275.494016 -0.81794667 801.574133 -9.24639E-05

8.06026422 1608.42377 213.4908138 -9.37387247 4628.13723 160.10672 -0.78666667 819.433333 0.000184928

-3.59241473 600.966544 -417.3932335 -3.02443463 966.391274 -162.616211 -0.67728573 864.727449 -5.63707E-05

5.90147484 992.744157 125.6403618 -6.1614167 4125.90956 190.892692 -0.98671661 957.649212 -0.000188176

16.1064662 14388.5762 864.6650653 -4.13455407 1402.53671 2.08226064 -1.01099585 891.979253 -0.000247994

6.37879721 1168.29899 159.4351675 -3.69360075 958.056257 -54.5892356 -1.02722364 875.814952 -0.000234288

461.789872 15857160.6 34222.77315 -3.02053199 847.182818 -177.280191 -0.7076498 922.470464 -0.000200716

44.293078 139253.225 2981.159095 -2.88595158 889.156554 -145.172424 -0.65904521 826.583047 -0.000105031

8.3175096 3488.54355 290.5608401 -3.31866082 932.613387 -160.748737 -0.69514286 885.807143 -0.000116571

7.09788265 2163.09367 223.7400409 -3.74083482 1121.9099 -96.0447395 -0.77285714 989.878571 -0.000101429

8.02567772 3088.75921 267.471565 -4.4801125 1412.17851 -112.827625 -0.76952381 970.704762 -9.86667E-05

8.4916636 3904.17307 337.0985943 -2.9608184 798.131484 -188.788157 -0.70095238 1022.80952 -7.90952E-05

73.3828739 710633.507 9808.291687 -4.53930814 1495.13915 -83.805334 -0.90979592 1097.94966 -0.000121429

8.2089427 3443.03729 303.3211522 -4.97382691 2294.82476 4.20048226 -0.80095238 1109.21905 -8.92381E-05

6.80954825 1502.08653 190.3400131 -4.2424707 1070.61217 -58.8354033 -0.77828571 774.617143 -0.000168657

7.93448934 2207.44307 255.7319204 -4.45707701 1355.58565 16.3593493 -0.90647059 880.318627 -0.000199294

6.90777812 1331.29053 231.3813039 -4.8590801 1392.5267 19.0588276 -0.87885714 763.121905 -0.000212457

7.10362506 1867.1932 185.1089109 -4.08355007 1380.23833 -35.3400953 -0.92714286 1089.46857 -0.000153318.51891149 2824.42195 258.0411206 -5.23102849 2426.38103 97.6342913 -0.85238095 959.895238 -0.00013381

7.79228636 2928.89357 238.1674682 -3.26909023 948.082045 -162.954329 -0.65885714 891.837143 -9.46571E-05

8.02764442 1706.13419 231.4921834 -3.63376689 544.016678 -144.088981 -0.45804255 1006.34655 0.001175175

16.7829597 15071.0082 735.1176662 -2.99332524 961.181808 -171.127745 -0.48941719 875.565199 -6.21987E-05

13.3860976 9928.19374 645.8912869 -3.25910508 832.20635 -139.374148 -0.61042018 802.290832 -5.5929E-05

8.29858546 3733.13719 303.7074838 -3.85114017 1092.54133 -146.328925 -0.60779676 863.976275 -8.08511E-05

18.6859438 22435.3789 1102.3712 -3.10782307 665.013162 -170.702099 -0.71954928 1016.99503 -8.5958E-05

-4.00273756 1273.69155 -65.5433391 -0.83460737 1080.22954 -0.000152096

7.11697105 1876.73497 185.9894101 -4.11860533 1398.01059 -34.9854328 -0.95652688 1092.5879 -0.000157889

11.5928627 7224.24331 549.2732776 -3.78336706 1086.94269 -92.3971227 -0.72908055 1011.04999 -0.000154216


48/85

Intermediate

Visc. Calcs

mPa-s 0.666392

1.007647

0.559145

0.365747

0.259007 0.826086

0.220733

0.188481

100 150


49/85

y heat capacity

b m b

0.136418 0.002864 2.166097 13.33333 125.6667 114.231 302.38

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

b m b kJ/kg

0.17134277 0.00383989 1.95443811 39 118.1 60.05 395

0.11678845 0.00350187 2.30307202 -59.4444444 -0.44444444 58.123 386.116

0.17480424 0.01169313 2.09140629 29 117.5 74.12 581

0.14366314 0.00329847 1.83701911 225 365 Paraffinic

0.14403888 0.00329847 1.83701911 231 370 Paraffinic

0.1434942 0.00360723 1.99150405 176 318

0.13260865 0.0034882 1.85396289 172.777778 273.3333330.12835934 0.00373853 1.31179671 135 270

0.13287851 0.00353342 1.48242067 212.777778 360

0.14649635 0.00268394 1.50372384 115 257

0.13729795 0.00275548 1.53041781 135 284

0.1315863 0.00295 1.53 146 290

0.12405587 0.00337969 1.53515084 190 352

0.45846192 0.00275567 3.61765699

0.4218577 0.00325805 3.43954442

0.38885541 0.0037657 3.25266315

0.4497307 0.00268922 3.80991917

0.41041736 0.0032559 3.65933418

0.37350755 0.0038111 3.48797277

0.43979919 0.00265968 3.81265323

0.40073871 0.00317742 3.67072581

0.36499435 0.00374032 3.49934677

0.43525499 0.00274731 3.79344209

0.38573544 0.00330785 3.63518424

0.34400839 0.00385924 3.45484651

0.43525499 0.00285431 3.72730123

0.38573544 0.00369215 3.52681576

0.34400839 0.0045187 3.30051773

0.43474258 0.00289072 3.57107056

0.39588614 0.00342784 3.3754182

0.35847756 0.00395428 3.16979057

0.1419 0.00294673 1.50087617 113 257 Biphynyl, Diphenyl Oxide

0.12872088 0.00349706 1.47564273 280 552 Di- and Tr-aryl Ethers

0.13231658 0.0036267 1.80396464 57 181 Alkylated Aromatic

0.12502899 0.00325 1.545 165 328

0.12423762 0.0030301 1.59279456 120 267 Diphenylethane, Alkylated Aromatic

0.13397371 0.00297484 1.56102795 194 353

0.43474258 0.00283816 3.59049635

0.39588614 0.00335327 3.40287551

0.35847756 0.00386466 3.20613433

Predicted


50/85

0.13885091 0.00298109 1.90272364 188 345

0.1449552 0.00301606 2.02088761 150 250 Paraffinic

0.14317386 0.00329862 1.83834771 224 380 Paraffinic

0.14384338 0.00327941 1.84473494 229 380 Paraffinic

0.14384338 0.00327941 1.84473494 227 410 Paraffinic

0.16988251 0.00180192 1.90636279 267 370 Polyalkylene Glycol

0.14317386 0.00329862 1.83834771 224 380

0.14263538 0.0034339 2.01865812 165 325 Paraffinic

0.1360208 0.00170301 1.62867745 323 500 Silicone

0.13574114 0.00218345 2.02076553 98.8 500

0.13559653 0.00266144 2.01868793 98.8 500

0.15746727 0.00188535 1.2342126 315 315

0.47276726 0.00582464 4.0082944

0.38494439 0.005872 3.63075172

0.31460708 0.00579363 3.25831109

0.47398383 0.00233329 3.75889191

0.39517254 0.00342636 3.37573895

0.33280797 0.00446672 2.95325003

0.505 0.003 3.28

0.5021 0.00228 3.177

0.498 0.00269118 3.01911765

0.4895 0.0023 2.89

0.48433333 0.002 2.67

0.12428762 0.00454925 1.9236329 61 175

0.1126 0.0038003 2.01912312 61 191

0.13327172 0.00372567 1.4746586 200 385

0.1165 0.0038 1.804 77 223

0.151 0.0038 1.934 110 273

0.13761016 0.00354172 1.72359297 53 176

0.4679319 0.00219702 3.93138577

0.38295299 0.00329164 3.637705030.31243165 0.00440998 3.25285147

0.25753532 0.00505184 2.76340154

0.13640672 0.00365388 1.89392488 180 330

0.18172718 0.01502463 2.05504094 13 78.4 46.07 842

0.28384054 0.00516771 2.28694978 160 290 92.1 663

0.13034741 0.00308889 2.16912226 -21.6666667 68.7777778 86.177 334.944

0.13439586 0.00376492 1.83702801 216 340

0.13374607 0.00334785 1.54746065 130 278

0.13678069 0.00366527 1.89241343 180 330

0.13305666 0.00370619 1.47682057 200 385

0.21461114 0.00431839 2.41311202 12 64.7 32.04 1100

0.14259475 0.00381062 2.02410502 154 3380.12904705 0.00433615 1.72365933 160 271

0.13995684 0.00364154 1.81319481 228 374

0.13559878 0.0045476 1.86352603 227 411 Mineral Oil

0.13951144 0.00356313 1.79428338 235 373 Mineral Oil

0.13442697 0.00363286 1.80543579 171 349 Mineral Oil

0.1377 0.00350235 1.72495098 53 176

0.506 0.00252973 3.28047748

0.499 0.00222857 3.04142857

0.48637813 0.002195 2.891425


51/85

0.505 0.00226774 3.18140323

0.48445714 0.00208 2.662

0.13641828 0.00286394 2.16609689 13.3333333 125.666667 114.231 302.38

0.14164255 0.0037174 1.84633448 40 180

0.13285792 0.0032052 1.87404783 182 500

0.13425309 0.00364665 1.81142333 221 500 Mineral Oil

0.12234573 0.00222055 1.89941505 160 335

0.1526359 0.00387399 1.92479404 54 200

0.13505709 0.00202855 2.33376639 149 400

0.13418188 0.00191976 2.33863189 135 500

0.10576108 0.00528662 1.71808775 157 500 Mineral Oil

0.15371749 0.00316065 2.1967238 -49.4444444 36.0555556 72.15 357.5062

0 0.00327427 1.84241763 225 376

0.16129028 0.01273017 2.42855047 12 82.5 60.1 663

0.15683304 0.00977991 2.23169058 15 97.8 60.1 695

0.13906795 0.00339251 1.80609427 209 382

0.1387839 0.00170771 1.57416438 160 330

0.11195563 0.00246346 1.63259091 63 210

0.1135478 0.0021 1.73 47 175

0.17002444 0.00395114 1.69192974 176.666667 269.444444

0.15297588 0.0030145 2.18885904 229.444444 376.666667

0.13072857 0.00354229 1.83508571 177 340 Synthetic Hydrocarbon

0.12321429 0.00333429 1.61405714 138 289 Alkyl Substituted Aromatic

0.12509333 0.00221667 1.902 149 310

0.12014762 0.00357762 1.48585714 170 359 Modified Terphenyl

0.14198571 0.00270898 1.49818503 132 271

0.13859143 0.00241143 1.54337143 185 343

0.11206843 0.004052 2.02182 59 192

0.12841373 0.00370588 1.71905882 57 181

0.10692457 0.00422743 1.86639238 -6.2 99.2

0.14195257 0.00276405 1.49441714 110 2570.12027238 0.00405143 1.53084952 104 243

0.11761114 0.00422914 1.73669714 199 358

0.56890349 0.00017023 4.19298145 0 100 18.02 2260

0.1338866 0.00376284 2.04314311 229 357 Paraffinic

0.13773874 0.00418753 2.07618376 163 500 PAO Synthetic

0.13770646 0.00342547 1.92333177 193 301 Paraffinic

0.11911152 0.00331291 1.33668852 160 305

0.14060544 0.00280399 1.51670064 122 258

0.14225075 0.00280956 1.48942975 124 257

0.13665885 0.00309044 1.64091423 121 275


52/85

Selectio

Temperature

Specific Gravi

Specific Heat

Thermal Con

Viscosity

Heat of Vapor

Temp.

C

-20

20

60

100

120

140


53/85

-20 20 60 100

Raw Data - Units may be converted from original sou

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

37.7777778 93.3333333 148.888889 204.44444410 37.7777778 121.111111 204.444444

37.7777778 93.3333333 148.888889 204.444444

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 1000 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

10 70 130 190

-10 10 40 65

-20 10 40 65

-30 -20 10 65


54/85

-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 37.7777778 60

-17.7777778 -1.11111111 26.6666667 48.8888889

-28.8888889 -12.2222222 15.5555556 37.7777778

-6.66666667 4.44444444 21.1111111 37.7777778

-17.7777778 -1.11111111 21.1111111 37.7777778

-34.4444444 -17.7777778 10 32.2222222

-10 0 10 20

-20 0 10 20

-30 -10 10 20

-40 -20 0 20

-50 -30 -10 10

-62.2222222 -40 15.5555556 60

-73 -60 0 50

20 40 100 160

-40 -30 10 60

0 10 50 90

-106.666667 -84.4444444 -28.8888889 15.5555556

-6.66666667 -1.11111111 15.5555556 37.7777778

-17.7777778 -12.2222222 10 32.2222222-34.4444444 -28.8888889 -1.11111111 26.6666667

-34.4444444 -28.8888889 -1.11111111 26.6666667

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

-10 0 60 120

-30 -20 40 100

-125 -100 -75 -50

-10 0 25 50

-25 0 25 50

-40 -25 0 25


55/85

-20 0 25 50

-50 -25 0 25

-20 20 60 100

-101.111111 -73.3333333 -17.7777778 37.7777778

-6.66666667 37.7777778 93.3333333 148.888889

15.5555556 37.7777778 93.3333333 148.888889

10 37.7777778 121.111111 176.666667

-73.3333333 -40 15.5555556 93.3333333

-17.7777778 10 65.5555556 148.888889

-17.7777778 10 37.7777778 93.3333333

10 37.7777778 93.3333333 148.888889

-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

37.7777778 93.3333333 148.888889 204.444444

37.7777778 93.3333333 148.888889 204.444444

-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 1922 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


56/85

Values for Radio Buttons - this worksheet

2

ty 2

2

uctivity 2

1

ization 2

0

Predicted values in units of the table Predicted values in same units as input

Liquid 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

734.9717223 2.108818 0.142625 0.896327288 734.9717 2.108818 0.142625 0.89632729

701.4944179 2.223376 0.130212 0.559145157 701.4944 2.223376 0.130212 0.55914516

668.0171134 2.337934 0.117799 0.371073781 668.0171 2.337934 0.117799 0.37107378

634.539809 2.452491 0.105386 0.259007094 634.5398 2.452491 0.105386 0.25900709

617.8011567 2.50977 0.099179 0.219901963 617.8012 2.50977 0.099179 0.21990196

601.0625045 2.567049 0.092973 0.188480879 601.0625 2.567049 0.092973 0.18848088


57/85

120 140 732.5191 702.5186186 670.5874 636.161 617.753128 598.347424 2.12849379

rce

Density, kg/m3 Specific Heat,

5 6 1 2 3 4 5 6 1

80 100 1068.66667 1048.666667 1028.66667 1008.66667 988.666667 968.666667 1.9594224

-10 10 662.655526 643.1987777 633.154975 622.875617 612.338098 590.378636 2.10244957

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

260 315.555556 885.820838 850.580226 815.339614 780.099002 744.85839 709.617778 2.009664260 343.333333 986.737136 967.514984 906.644836 840.96915 794.515616 719.228854 1.318842

260 315.555556 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 3.49100 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

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


58/85

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

82.22222222 115.555556 1028.86569 1023.899963 1012.36667 1000.51301 986.096398 959.665939 3.97746

82.22222222 115.555556 1052.57301 1046.806361 1033.99159 1021.01664 996.668581 966.553876 3.516912

82.22222222 115.555556 1072.11553 1065.868328 1052.09245 1038.15639 1002.91578 969.917753 3.098232

60 104.444444 1046.96655 1042.801746 1036.07399 1028.38513 1016.69166 988.659351 3.7429992

60 104.444444 1088.13399 1081.085865 1070.3535 1061.22298 1047.76747 1016.2111 3.3159456

60 104.444444 1127.69958 1120.331092 1106.55522 1093.2599 1074.83867 1040.87953 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

104.4444444 148.888889 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

60 126.666667 943.487294 925.866988 882.617146 848.97838 815.339614 762.478696 1.3481496

71.11111111 104.444444 1028.86569 1027.424024 1021.81756 1012.36667 993.625074 969.11683 3.9188448

60 104.444444 1052.57301 1050.810976 1042.16101 1030.94809 1013.48796 977.12606 3.57971460 104.444444 1074.03774 1072.115528 1060.74242 1045.3647 1021.81756 981.611229 3.1024188

60 104.444444 1095.34229 1091.33768 1070.51368 1049.04895 1022.4583 985.295475 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 80 695.289958 678.3378428 660.759705 642.457878 623.307433 603.14435 2.11965704

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 40 819.433333 810.1833333 800.933333 791.683333 782.433333 773.183333 2.365542

180 260 820 807 768 728 689 637 1.948204 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

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


59/85

75 100 1258 1249 1240 1224 1210 1195 3.13

50 100 1395 1380 1365 1350 1335 1305 2.56

120 140 732.519128 702.5186186 670.5874 636.161025 617.753128 598.347424 2.12849379

93.33333333 204.444444 950.215047 922.1827422 866.278317 810.213707 754.149097 642.180061 1.47040416

226.6666667 315.555556 897.03376 864.99684 832.95992 784.90454 736.84916 672.77532 1.842192

226.6666667 315.555556 865.957948 851.7015182 816.140537 780.419371 730.601961 673.576243 1.86815016

260 371.111111 961.1076 945.08914 881.0153 832.95992 768.88608 688.79378 1.925928

148.8888889 232.222222 831.838628 807.0100148 766.162942 708.816855 667.809597 606.298711 1.64080692

232.2222222 315.555556 840.96915 810.534076 756.071312 700.006702 669.571628 655.155014 2.30274

148.8888889 204.444444 840.96915 810.534076 781.700848 735.247314 700.006702 677.580858 2.30274

232.2222222 315.555556 890.626376 873.00607 836.163612 799.321154 743.256544 688.79378 1.758456

30 50 691.026503 673.416052 655.144787 636.105515 616.159837 595.123966 2.05220124

316 316 869 855 714 714 679 679 1.89

60 80 809.7536 801.5741333 785.2152 768.856267 752.497333 736.1384 2.30274

60 80 827.3 819.4333333 803.7 787.966667 772.233333 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

260 315.555556 892.228222 856.98761 820.145152 780.099002 740.052852 695.201164 1.842192

260 315.555556 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 1.523242 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


60/85


61/85

2.2182232 2.315248324 2.43518687 2.50862922 2.59365655 0.14198014 0.13053412 0.11844908 0.10572504

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 0.17134277 0.17134277 0.17134277 0.17134277

2.1602883 2.192070262 2.22634224 2.26354046 2.34846045 0.14670974 0.13692707 0.13195986 0.12694206

2.323674 2.553948 2.805156 3.014496 3.265704 0.17480424 0.17134277 0.1678813 0.16441983

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 0.14365101 0.14192027 0.14192027 0.1384588

2.135268 2.135268 2.344608 2.93076 2.93076 0.14192027 0.14018954 0.14018954 0.13499733

2.177136 2.344608 2.553948 2.763288 2.972628 0.12980513 0.12547829 0.1214976 0.11717076

1.4528196 1.77939 2.114334 2.30274 2.553948 0.12755517 0.12322833 0.11249778 0.10090185

1.821258 2.0054772 2.19807 2.40741 2.595816 0.12893976 0.12322833 0.11734383 0.11163241

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 0.4013.88 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 0.40621.701 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

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


62/85

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 0.4794136 0.51056683 0.53479712

3.642516 3.76812 3.935592 4.103064 4.312404 0.36518509 0.38422317 0.40672273 0.41710714

3.181968 3.34944 3.475044 3.726252 3.935592 0.30114789 0.30980157 0.32364745 0.33057039

3.76812 3.809988 3.8476692 3.8979108 4.0025808 0.45691404 0.47422139 0.49845168 0.51748977

3.370374 3.4499232 3.5043516 3.579714 3.7346256 0.37383876 0.39287685 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 0.13067049 0.12288219 0.11509388

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 0.15836225 0.14365101 0.13413196

3.9272184 3.9648996 4.0151412 4.0863168 4.1616792 0.45345257 0.46210625 0.48633654 0.51056683

3.5964612 3.6718236 3.7429992 3.8351088 3.9816468 0.36518509 0.37210803 0.39287685 0.41018423.1233528 3.2489568 3.370374 3.516912 3.7136916 0.29595569 0.30114789 0.31672451 0.32710892

2.6083764 2.763288 2.9140128 3.098232 3.2615172 0.25441805 0.25614878 0.25961025 0.26134099

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 0.18172718 0.18172718 0.18172718 0.18172718

2.700486 2.805156 2.9056392 3.014496 3.1107924 0.28384054 0.28384054 0.28384054 0.28384054

2.16806332 2.221050007 2.28095643 2.3501219 2.43088573 0.13739396 0.13040986 0.1232384 0.11587957

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 0.13521.88 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

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


63/85

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

2.2182232 2.315248324 2.43518687 2.50862922 2.59365655 0.14198014 0.13053412 0.11844908 0.10572504

1.57381812 1.78022736 1.9866366 2.19346452 2.606283 0.14936243 0.14728555 0.14278564 0.13880495

2.009664 2.177136 2.344608 2.595816 2.888892 0.1332666 0.12807439 0.11942072 0.11249778

1.94937408 2.15159652 2.35423764 2.63810268 2.962161 0.13309352 0.13136279 0.12720902 0.12305526

1.967796 2.177136 2.30274 2.470212 2.72142 0.11768998 0.11768998 0.11249778 0.10903631

1.76976036 1.98496188 2.28641148 2.501613 2.82441528 0.15836225 0.15593922 0.15092009 0.14572789

2.344608 2.470212 2.637684 2.805156 2.972628 0.1332666 0.1332666 0.13153586 0.12634366

2.344608 2.428344 2.51208 2.637684 2.72142 0.1332666 0.1332666 0.1332666 0.13153586

1.925928 2.219004 2.51208 2.93076 3.391308 0.10557484 0.1038441 0.10038263 0.0986519

2.10069597 2.154309165 2.21553049 2.28684963 2.37075627 0.16520379 0.16107307 0.1565945 0.15176808

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 0.16095836 0.15922762 0.15749689

2.2273776 2.428344 2.6293104 2.8135296 3.014496 0.15403542 0.15749689 0.16095836 0.16441983

1.9384884 1.9384884 2.1394548 2.6879256 2.8805184 0.1384588 0.13672807 0.13672807 0.1332666

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 0.16095836 0.15143931 0.14192027 0.12980513

2.470212 2.637684 2.805156 2.972628 3.1401 0.14884321 0.14365101 0.13672807 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 0.1151.798 2.048 2.272 2.486 2.76 0.1197 0.112 0.1042 0.0962

1.864 2.096 2

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Heat_Exchangers Sizing Suparma