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Shell side inlet temperature 0.00 0C
Shell side outlet temperature 40.00 0C
Tube side inlet temperature 100.00 0C
Tube side outlet temperature 25.00 0C
Mass flowrate 350.00 kg/hr Shell side
0.10 kg/sec
Tube side Fluid CO + CS2
Density 1.18 Kg/m3
Viscosity 4.07E+01 Pa.s
Heat Capacity 1555.13 kJ/(kg.K)
Thermal Conductivity 0.02511 W/(m.K)
Calculation of Heat load
Heat load -9.74 kJ
Mass flowrate 0.00 kg/sec
LMTD Calculations
LMTD -39.98 0C
R 0.53
FT #DIV/0!
Correct LMTD #DIV/0! 0C
Area and Number of Tubes
Organic solvent-Water 250-750 W/m2.0C
Overall HTC 600.00 W/m2.0C
Provisional area #DIV/0! m2
Inside Diameter of Tube 16.00 mm
Tube Length 4.83
Area of one Tube 0.30 m2
Number of Tubes #DIV/0!
Number of passes 2.00
Pitch Type Triangular pitch
Tube Pitch 25.00mm
K1 0.25
n1 2.21
Estimation of wall Temperature
Mean temperature difference -42.50 0C
Across film temp. difference #DIV/0! 0C
Mean wall temperature #DIV/0! 0C
Viscosity at wall temperature #DIV/0! Pa.s
Correction factor #DIV/0!
Kern Method
Mean temperature on Shell side 20.00 0C
Mean temperature on Tube side 62.50 0C
Shell side fluid Methanol
Density 793.48 Kg/m3
Viscosity 5.77E-04 Pa.s
Heat Capacity 2.51 kJ/(kg.K)
Thermal Conductivity 0.20 W/(m.K)
counter current
S 0.75
L/D 241.50
Outside Diameter of Tube 20.00 mm
Baffle cut percent 25.00
L/D 240.00
Bundle Diameter #DIV/0! mm
Type of Head
Split ring floating
head
Clearance #DIV/0!
Shell Diameter #DIV/0! mm
Mass Flowrate 0.00 kg/sec
Tube C/s Area 2.01E-04 m2
Tubes per Pass #DIV/0!
Total flow area #DIV/0! m2
Mass Velocity #DIV/0! kg/m2.sec
Velocity #DIV/0! m/sec
Reynold's Number #DIV/0!
Prandlt Number ##########
Jh #DIV/0!
Nusselt Number #DIV/0!
Tube side HTC #DIV/0! W/m2.0C
Fluid type Sea water
Fouling coefficient 3000.00 W/m2.0C
Jf #DIV/0!
Tube side Pressure Drop #DIV/0! kPa
Material Construction
Thermal Conductivity of MOC
1/U
Overall Coefficient
Tube Side Heat Transfer Coefficient
Mass Flowrate 0.10 kg/sec
Baffle Spacing #DIV/0! mm
Cross flow area #DIV/0! m2
Mass Velocity #DIV/0! kg/m2.sec
Velocity #DIV/0! m/sec
Equivalent Diameter 14.20 mm
Reynold's Number #DIV/0!
Prandlt Number 7.18
Jh #DIV/0!
Nusselt Number #DIV/0!
Shell side HTC #DIV/0! W/m2.0C
Fluid type Light hydrocarbon
Fouling coefficient 5000.00 W/m2.0C
Jf #DIV/0!
Shell side Pressure Drop #DIV/0! kPa
Cupro Nickel 10% Ni
45 W/m.0C
#DIV/0!
#DIV/0! W/m2.0C
Shell Side Heat Transfer Coefficient
Shell side inlet temperature 0.00 0C
Shell side outlet temperature 40.00 0C
Tube side inlet temperature 100.00 0C
Tube side outlet temperature 25.00 0C
Mass flowrate 350.00 kg/hr Shell side
0.10 kg/sec
Tube side Fluid CO + CS2
Density 1.18 Kg/m3
Viscosity 4.07E+01 Pa.s
Heat Capacity 1555.13 kJ/(kg.K)
Thermal Conductivity 0.03 W/(m.K)
Calculation of Heat load
Heat load -9.74 kJ
Mass flowrate 0.00 kg/sec
LMTD Calculations
LMTD -39.98 0C
R 0.53
FT #DIV/0!
Correct LMTD #DIV/0! 0C
Area and Number of Tubes
Overall HTC 600.00 W/m2.0C
Provisional area #DIV/0! m2
Inside Diameter of Tube 16.00 mm
Tube Length 4.83
Area of one Tube 0.30 m2
Number of Tubes #DIV/0!
Number of passes 2.00
Pitch Type Triangular pitch
Tube Pitch 25.00 mm
K1 0.25
n1 2.21
Tube side HTC #DIV/0! W/m2.0C
Fluid type Sea water
Fouling coefficient 3000.00 W/m2.0C
Material Construction Cupro Nickel 10% Ni
Thermal Conductivity of MOC 45.00 W/m.0C
1/U #DIV/0!
Overall Coefficient #DIV/0! W/m2.0C
Bell's Method
Mean temperature on Shell side 20.00 0C
Mean temperature on Tube side 62.50 0C
Shell side fluid Methanol
Density 793.48 Kg/m3
Viscosity 5.77E-04 Pa.s
Heat Capacity 2.51 kJ/(kg.K)
Thermal Conductivity 0.20 W/(m.K)
counter current
S 0.75
Outside Diameter of Tube 20.00
Baffle cut percent 25.00
L/D 240.00
Bundle Diameter #DIV/0!
Type of Head Split ring floating head
Clearance #DIV/0!
Shell Diameter #DIV/0!
Shell side HTC #DIV/0! W/m2.0C
Fluid type Light hydrocarbon
Fouling coefficient 5000.00 W/m2.0C
Pressure Drop
Baffle spacing 360.00 mm Cross flow zone
Max.Area #DIV/0! m2 Frition factor
Mass Velocity #DIV/0! m/sec Mass Velocity
Reynold's no. #DIV/0! Velocity
Prandlt no. 7.18 Pressure drop
Heat transfer factor #DIV/0! Alpha
Ideal bank coeffcient #DIV/0! W/m2.0C Fb'
Bl'
Tube row correction factor Fl'
Tube vertical pitch 21.75 mm ΔPc
Baffle cut height #DIV/0! mm
Height b/w baffle tips #DIV/0! mm
No. of constriction #DIV/0! Window zone
Fn #DIV/0! Ra
Aw
Window correction factor uw
Hb #DIV/0! mm uz
Baffle cut #DIV/0! Nwv
Ra #DIV/0! ΔPw
Tubes in one window #DIV/0!
Tubes in cross flow area #DIV/0! End zone
Rw #DIV/0! ΔPe
Fw #DIV/0!
Total pressure drop
Bypass correction Number of baffles
Clearence area Ab #DIV/0! m2 ΔPs
Ab/As #DIV/0!
Alpha #DIV/0! Considering fouling
No. of sealing tubes 1.00 ΔPs
No. of constrction 5.00
Fb #DIV/0!
Leakage correction factor
tube to baffle clearance 0.80
Baffle to shell clearance 4.80
tube to baffle clearance area At #DIV/0! m2
angle 2.07
shell to baffle clearance area Asb #DIV/0! m2
Heat Transfer coefficient
total leakage area #DIV/0! m2
Al/As #DIV/0!
Bl #DIV/0!
Fl #DIV/0!
#DIV/0!
#DIV/0! kg/m2.sec
#DIV/0! m/sec
#DIV/0! Pa
#DIV/0!
#DIV/0!
#DIV/0!
#DIV/0!
#DIV/0! Pa
0.20
#DIV/0! m2
#DIV/0! m/sec
#DIV/0! m/sec
#DIV/0!
#DIV/0! Pa
#DIV/0! Pa
12.00
#DIV/0! kPa
#DIV/0! kPa
Tube side HTC #DIV/0! W/m2.0C
Shell side HTC #DIV/0! W/m2.0C
Overall HTC #DIV/0! W/m2.0C
Tube side #DIV/0! kPa
Shell side 0.00 kPa
Comparison between Kern and Bell method
Pressure Drop
Heat Transfer Coefficient
Kern Method
Tube side HTC #DIV/0! W/m2.0C
Shell side HTC #DIV/0! W/m2.0C
Overall HTC #DIV/0! W/m2.0C
Tube side #DIV/0! kPa
Shell side #DIV/0! kPa
Comparison between Kern and Bell method
Pressure Drop
Heat Transfer Coefficient
Bell Method
Name Property Unit Molecular Weight
Acetic acid Density Kg/m3 60.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Acetaldehyde Density Kg/m3 44.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Acetone Density Kg/m3 58.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Benzene Density Kg/m3 78.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
1-Butanol Density Kg/m3 74.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Cyclohexane Density Kg/m3 84.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Ethanol Density Kg/m3 46.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Ethylene glycol Density Kg/m3 62.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Formaldehyde Density Kg/m3 30.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Methanol Density Kg/m3 32.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Pentane Density Kg/m3 72.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Phenol Density Kg/m3 94.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Toluene Density Kg/m3 92.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Water Density Kg/m3 18.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
o-Xylene Density Kg/m3 106.00
Heat capacity J/kmol.K
Viscosity Pa.s
Thermal Conductivity W/m.K
Boiling Point 0C 273 283 293 303 313
118.10 1.07E+03 1.06E+03 1.05E+03 1.04E+03 1.03E+03
1.19E+05 1.21E+05 1.23E+05 1.25E+05 1.27E+05
1.67E-03 1.41E-03 1.20E-03 1.04E-03 9.05E-04
1.64E-01 1.62E-01 1.60E-01 1.58E-01 1.57E-01
20.20 8.06E+02 7.93E+02 7.80E+02 7.67E+02 7.53E+02
1.03E+05 1.07E+05 1.11E+05 1.15E+05 1.19E+05
2.81E-04 2.50E-04 2.24E-04 2.02E-04 1.83E-04
1.92E-01 1.88E-01 1.83E-01 1.79E-01 1.75E-01
56.50 8.13E+02 8.02E+02 7.91E+02 7.80E+02 7.68E+02
1.22E+05 1.24E+05 1.25E+05 1.27E+05 1.29E+05
3.99E-04 3.57E-04 3.23E-04 2.93E-04 2.68E-04
1.71E-01 1.67E-01 1.63E-01 1.58E-01 1.54E-01
80.10 8.96E+02 8.87E+02 8.77E+02 8.67E+02 8.57E+02
1.31E+05 1.33E+05 1.35E+05 1.38E+05 1.40E+05
8.40E-04 7.32E-04 6.41E-04 5.64E-04 5.00E-04
1.51E-01 1.48E-01 1.45E-01 1.42E-01 1.39E-01
117.00 8.23E+02 8.15E+02 8.07E+02 7.99E+02 7.90E+02
1.63E+05 1.69E+05 1.75E+05 1.81E+05 1.88E+05
5.00E-03 3.76E-03 2.88E-03 2.24E-03 1.76E-03
1.58E-01 1.56E-01 1.54E-01 1.52E-01 1.50E-01
81.00 7.94E+02 7.85E+02 7.76E+02 7.67E+02 7.58E+02
1.46E+05 1.50E+05 1.53E+05 1.57E+05 1.60E+05
2.53E-03 2.06E-03 1.71E-03 1.45E-03 1.24E-03
1.30E-01 1.27E-01 1.25E-01 1.22E-01 1.20E-01
78.40 8.06E+02 7.98E+02 7.89E+02 7.80E+02 7.71E+02
1.04E+05 1.07E+05 1.10E+05 1.14E+05 1.18E+05
1.79E-03 1.45E-03 1.19E-03 9.84E-04 8.21E-04
1.75E-01 1.72E-01 1.69E-01 1.67E-01 1.64E-01
1.13E+03 1.12E+03 1.11E+03 1.11E+03 1.10E+03
1.41E+05 1.44E+05 1.48E+05 1.51E+05 1.54E+05
1.11E-02 8.46E-03 6.56E-03 5.18E-03 4.16E-03
3.47E-01 3.56E-01 3.66E-01 3.75E-01 3.85E-01
Temperature(K)
-21.00 7.79E+02 7.61E+02 7.42E+02 7.23E+02 7.02E+02
6.96E+04 6.99E+04 7.02E+04 7.05E+04 7.08E+04
1.09E-05 1.13E-05 1.17E-05 1.21E-05 1.24E-05
1.40E-02 1.47E-02 1.55E-02 1.63E-02 1.71E-02
64.70 8.12E+02 8.03E+02 7.93E+02 7.84E+02 7.74E+02
7.68E+04 7.84E+04 8.02E+04 8.22E+04 8.43E+04
7.79E-04 6.66E-04 5.77E-04 5.05E-04 4.48E-04
2.07E-01 2.04E-01 2.01E-01 1.99E-01 1.96E-01
36.30 6.45E+02 6.35E+02 6.26E+02 6.16E+02 6.05E+02
1.59E+05 1.62E+05 1.65E+05 1.69E+05 1.72E+05
2.78E-04 2.54E-04 2.33E-04 2.14E-04 1.97E-04
9.65E-02 9.07E-02 8.49E-02 7.92E-02 7.34E-02
181.40 1.09E+03 1.08E+03 1.07E+03 1.07E+03 1.06E+03
1.88E+05 1.92E+05 1.95E+05 1.98E+05 2.01E+05
1.17E-02 8.33E-03 6.07E-03 4.55E-03 3.48E-03
1.61E-01 1.60E-01 1.59E-01 1.58E-01 1.57E-01
110.80 8.85E+02 8.76E+02 8.67E+02 8.58E+02 8.49E+02
1.50E+05 1.53E+05 1.55E+05 1.58E+05 1.61E+05
7.67E-04 6.68E-04 5.89E-04 5.25E-04 4.72E-04
1.38E-01 1.36E-01 1.34E-01 1.31E-01 1.29E-01
100.00 1.00E+03 1.00E+03 1.00E+03 9.99E+02 9.96E+02
7.62E+04 7.58E+04 7.55E+04 7.53E+04 7.53E+04
1.71E-03 1.31E-03 1.02E-03 8.22E-04 6.73E-04
1.13E+00 1.19E+00 1.25E+00 1.30E+00 1.36E+00
144.00 8.95E+02 8.87E+02 8.79E+02 8.71E+02 8.62E+02
1.80E+05 1.82E+05 1.85E+05 1.87E+05 1.90E+05
1.10E-03 9.41E-04 8.14E-04 7.10E-04 6.26E-04
1.37E-01 1.35E-01 1.33E-01 1.30E-01 1.28E-01
323 333 343 353 363 373
1.02E+03 1.00E+03 9.94E+02 9.83E+02 9.72E+02 9.60E+02
1.30E+05 1.32E+05 1.35E+05 1.38E+05 1.42E+05 1.45E+05
7.95E-04 7.03E-04 6.27E-04 5.62E-04 5.06E-04 4.59E-04
1.55E-01 1.53E-01 1.51E-01 1.49E-01 1.47E-01 1.46E-01
7.39E+02 7.25E+02 7.10E+02 6.94E+02 6.78E+02 6.61E+02
1.24E+05 1.29E+05 1.34E+05 1.40E+05 1.46E+05 1.52E+05
1.67E-04 1.53E-04 1.41E-04 1.30E-04 1.20E-04 1.12E-04
1.70E-01 1.66E-01 1.61E-01 1.57E-01 1.53E-01 1.48E-01
7.56E+02 7.44E+02 7.32E+02 7.19E+02 7.06E+02 6.93E+02
1.31E+05 1.34E+05 1.36E+05 1.39E+05 1.42E+05 1.45E+05
2.47E-04 2.29E-04 2.13E-04 1.99E-04 1.87E-04 1.76E-04
1.50E-01 1.46E-01 1.41E-01 1.37E-01 1.33E-01 1.29E-01
8.46E+02 8.36E+02 8.25E+02 8.14E+02 8.03E+02 7.92E+02
1.42E+05 1.45E+05 1.48E+05 1.50E+05 1.53E+05 1.56E+05
4.44E-04 3.97E-04 3.56E-04 3.21E-04 2.90E-04 2.63E-04
1.36E-01 1.33E-01 1.30E-01 1.27E-01 1.24E-01 1.21E-01
7.81E+02 7.73E+02 7.63E+02 7.54E+02 7.45E+02 7.35E+02
1.95E+05 2.03E+05 2.11E+05 2.20E+05 2.29E+05 2.39E+05
1.40E-03 1.13E-03 9.24E-04 7.61E-04 6.32E-04 5.30E-04
1.48E-01 1.46E-01 1.44E-01 1.42E-01 1.40E-01 1.38E-01
7.49E+02 7.39E+02 7.30E+02 7.20E+02 7.10E+02 7.00E+02
1.64E+05 1.68E+05 1.72E+05 1.76E+05 1.81E+05 1.86E+05
1.07E-03 9.42E-04 8.35E-04 7.48E-04 6.75E-04 6.15E-04
1.17E-01 1.15E-01 1.12E-01 1.10E-01 1.07E-01 1.05E-01
7.62E+02 7.52E+02 7.42E+02 7.32E+02 7.22E+02 7.11E+02
1.23E+05 1.28E+05 1.33E+05 1.39E+05 1.45E+05 1.52E+05
6.90E-04 5.85E-04 4.99E-04 4.29E-04 3.71E-04 3.22E-04
1.62E-01 1.59E-01 1.56E-01 1.54E-01 1.51E-01 1.48E-01
1.09E+03 1.08E+03 1.08E+03 1.07E+03 1.06E+03 1.05E+03
1.57E+05 1.60E+05 1.64E+05 1.67E+05 1.70E+05 1.73E+05
3.39E-03 2.80E-03 2.34E-03 1.98E-03 1.69E-03 1.45E-03
3.94E-01 4.03E-01 4.13E-01 4.22E-01 4.32E-01 4.41E-01
Temperature(K)
6.81E+02 6.58E+02 6.34E+02 6.09E+02 5.81E+02 5.49E+02
7.10E+04 7.13E+04 7.16E+04 7.19E+04 7.22E+04 7.25E+04
1.28E-05 1.32E-05 1.36E-05 1.40E-05 1.44E-05 1.47E-05
1.79E-02 1.88E-02 1.96E-02 2.05E-02 2.14E-02 2.23E-02
7.64E+02 7.54E+02 7.43E+02 7.32E+02 7.21E+02 7.09E+02
8.66E+04 8.92E+04 9.19E+04 9.48E+04 9.79E+04 1.01E+05
4.00E-04 3.61E-04 3.28E-04 3.00E-04 2.77E-04 2.56E-04
1.93E-01 1.90E-01 1.87E-01 1.85E-01 1.82E-01 1.79E-01
5.95E+02 5.84E+02 5.72E+02 5.61E+02 5.48E+02 5.36E+02
1.76E+05 1.79E+05 1.83E+05 1.88E+05 1.92E+05 1.97E+05
1.82E-04 1.67E-04 1.54E-04 1.42E-04 1.30E-04 1.20E-04
6.77E-02 6.19E-02 5.61E-02 5.04E-02 4.46E-02 3.89E-02
1.05E+03 1.04E+03 1.03E+03 1.02E+03 1.01E+03 1.00E+03
2.04E+05 2.07E+05 2.11E+05 2.14E+05 2.17E+05 2.20E+05
2.72E-03 2.17E-03 1.76E-03 1.45E-03 1.21E-03 1.02E-03
1.56E-01 1.55E-01 1.54E-01 1.53E-01 1.52E-01 1.51E-01
8.40E+02 8.30E+02 8.20E+02 8.10E+02 8.00E+02 7.90E+02
1.63E+05 1.66E+05 1.70E+05 1.73E+05 1.76E+05 1.80E+05
4.26E-04 3.87E-04 3.52E-04 3.21E-04 2.94E-04 2.68E-04
1.26E-01 1.24E-01 1.21E-01 1.19E-01 1.17E-01 1.14E-01
9.92E+02 9.87E+02 9.82E+02 9.77E+02 9.73E+02 9.68E+02
7.53E+04 7.53E+04 7.54E+04 7.56E+04 7.58E+04 7.60E+04
5.61E-04 4.75E-04 4.09E-04 3.56E-04 3.14E-04 2.80E-04
1.42E+00 1.47E+00 1.53E+00 1.59E+00 1.65E+00 1.70E+00
8.54E+02 8.46E+02 8.37E+02 8.28E+02 8.20E+02 8.11E+02
1.93E+05 1.95E+05 1.98E+05 2.01E+05 2.04E+05 2.07E+05
5.57E-04 4.99E-04 4.50E-04 4.08E-04 3.73E-04 3.42E-04
1.26E-01 1.23E-01 1.21E-01 1.19E-01 1.16E-01 1.14E-01
Triangular pitch
No of passes 1 2 4
K1 0.319 0.249 0.175
n1 2.142 2.207 2.285
Square pitch
No of passes 1 2 4
K1 0.215 0.156 0.158
n1 2.207 2.291 2.263
Thermal conductivity
Metals Temperature Avg. k
Aluminium 0-100 204
Brass 0-100 100.5
Copper 0-100 383
Nickel 0-100 60.5
Cupro Nickel 10% Ni 0-100 45
Monel 0-100 30
Stainless steel (18/8) 0-100 16
Steel 0-100 45
Titanium 0-100 16
Avg. k
Cupro Nickel 10% Ni 45
System U
Water-Water 800-500
Organic solvent-Organic solvent100-300
Light oil-Light oil 100-400
Heavy oil-Heavy oil 50-300
Organic solvent-Water250-750
Light oil-Water 350-900
Heavy oil-Water 60-300
Organic solvent-Water250-750
6 8 2
0.0743 0.0365 K1 0.249
2.499 2.675 n1 2.207
6 8
0.0402 0.0331 K1 0.156
2.617 2.463 n1 2.291
K1 0.249
n1 2.207
Triangular pitch
Square pitch
co current
counter current
Shell side
Tube side
Component Mol. Weight C1 C2 C3
Acetaldehyde 44 1.6994 0.26167 466
Acetic acid 60 1.4486 0.25892 591.95
Acetone 58 1.2332 0.25886 508.2
Benzene 78 1.0259 0.26666 562.05
1-Butanol 74 0.98279 0.2683 563.1
Cyclohexane 84 0.88998 0.27376 553.8
Cumene 120 0.58711 0.25583 631
Diethyl amine 73 0.85379 0.25675 496.6
Ethanol 46 1.6288 0.27469 514
Ethyl acetate 88 0.8996 0.25856 523.3
Ethyl benzene 106 0.70041 0.26162 617.15
Hexane 86 0.70824 0.26411 507.6
1-hexanol 102 0.70093 0.26776 611.3
Methanol 32 2.3267 0.27073 512.5
Pentane 72 0.84947 0.26726 469.7
Phenol 94 1.3798 0.31598 694.25
Styrene 104 0.7397 0.2603 636
Toluene 92 0.8792 0.27136 591.75
Water 18 -13.851 0.64038 -0.00191
o-Xylene 106 0.69962 0.26143 630.3
Component Mol. Weight C1 C2 C3
Shell side Methanol 32 2.3267 0.27073 512.5
Tube side CO + CS2 #N/A #N/A #N/A #N/A
Component Mol. Weight C1 C2 C3
Acetaldehyde 44 0.311 -0.000436 0
Acetic acid 60 0.214 -0.0001834 0
Acetone 58 0.2878 -0.000427 0
Benzene 78 0.23444 -0.0003057 0
1-Butanol 74 0.2136 -0.0002034 0
Cyclohexane 84 0.19813 -0.0002505 0
Cumene 120 0.1855 -0.000209 0
Diethyl amine 73 0.2587 -0.0005434 4.2097E-07
Ethanol 46 0.2468 -0.000264 0
Ethyl acetate 88 0.2501 -0.0003563 0
Ethyl benzene 106 0.1999 -0.0002382 0
Hexane 86 0.22492 -0.0003533 0
1-hexanol 102 0.2193 -0.00022 0
Density
Thermal Conductivity
Methanol 32 0.2837 -0.000281 0
Pentane 72 0.2537 -0.000576 0.000000344
Phenol 94 0.18831 -0.0001 0
Styrene 104 0.20215 -0.0002201 0
Toluene 92 0.20463 -0.0002425 0
Water 18 -0.432 0.0057255 -0.000008078
o-Xylene 106 0.19989 -0.0002299 0
Component Mol. Weight C1 C2 C3
Shell side Methanol 32 0.2837 -0.000281 0
Tube side CO + CS2 #N/A #N/A #N/A #N/A
C4 Component
0.2913 Acetaldehyde
0.2529 Acetic acid
0.2913 Acetone
0.28394 Benzene
0.25488 1-Butanol
0.28571 Cyclohexane
0.28498 Cumene
0.27027 Diethyl amine
0.23178 Ethanol
0.278 Ethyl acetate
0.28454 Ethyl benzene
0.27537 Hexane
0.23919 1-hexanol
0.24713 Methanol
0.27789 Pentane
0.32768 Phenol
0.3009 Styrene
0.29241 Toluene
1.8211E-06 Water
0.27365 o-Xylene
C4 Temp. Density Component
0.24713 293 793.4808958 kg/m3 Methanol
#N/A 335.5 1.182941781 kg/m3 CO + CS2
Methanol
C4 C5 Component
0 0 Acetaldehyde
0 0 Acetic acid
0 0 Acetone
0 0 Benzene
0 0 1-Butanol
0 0 Cyclohexane
0 0 Cumene
0 0 Diethyl amine
0 0 Ethanol
0 0 Ethyl acetate
0 0 Ethyl benzene
0 0 Hexane
0 0 1-hexanol
Density
Thermal Conductivity
0 0 Methanol
0 0 Pentane
0 0 Phenol
0 0 Styrene
0 0 Toluene
1.861E-09 0 Water
0 0 o-Xylene
C4 C5 Thermal Conductivity Component
0 0 0.201367 W/(m.K) Methanol
#N/A #N/A 0.02511 W/(m.K) CO + CS2
Mol. Weight C1 C2 C3 C4 C5
44 -5.895 668.21 -0.84323 0 0
60 -9.03 1212.3 -0.322 0 0
58 -14.918 1023.4 0.5961 0 0
78 7.5117 294.68 -2.794 0 0
74 0.87669 1602.9 -2.1475 0 0
84 -33.763 2497.2 3.2236 0 0
120 -24.988 1807.9 2.0556 0 0
73 -17.57 1385.7 0.85647 0 0
46 7.875 781.98 -3.0418 0 0
88 14.354 -154.6 -3.7887 0 0
106 -13.563 1208.6 0.377 0 0
86 -6.3276 640 0.694 5.6884E+21 -10
102 -39.324 3841 3.6933 -2.1166E-30 10.485
32 -25.317 1789.2 2.069 0 0
72 -53.509 1836.6 7.1409 -19627 2
94 -43.335 3881.7 4.3983 3.0548E+24 -10
104 -22.675 1758 1.6701 0 0
92 -226.08 6805.7 37.542 -0.060853 1
18 -52.843 3703.6 5.866 -5.879E-29 10
106 -15.489 1393.5 0.63711 0 0
Mol. Weight C1 C2 C3 C4 C5
32 -25.317 1789.2 2.069 0 0
#N/A #N/A #N/A #N/A #N/A #N/A
32 -25.317 1789.2 2.069 0 0
Mol. Weight C1 C2 C3 C4 C5
44 115100 -433 1.425 0 0
60 139640 -320.8 0.8985 0 0
58 135600 -177 0.2837 0.000689 0
78 129440 -169.5 0.64781 0 0
74 191200 -730.4 2.2998 0 0
84 -220600 3118.3 -9.4216 0.010687 0
120 61723 494.81 0 0 0
73 101330 243.18 0 0 0
46 102640 -139.63 -0.030341 0.0020386 0
88 226230 -624.8 1.472 0 0
106 154040 -142.29 0.80539 0 0
86 172120 -183.78 0.88734 0 0
102 1638600 -17261 71.721 -0.12026 0.000071087
Viscosity
Heat Capacity
32 105800 -362.23 0.9379 0 0
72 159080 -270.5 0.99537 0 0
94 101720 317.61 0 0 0
104 113340 290.2 -0.6051 0.0013567 0
92 140140 -152.3 0.695 0 0
18 276370 -2090.1 8.125 -0.014116 9.3701E-06
106 36500 1017.5 -2.63 0.00302 0
Mol. Weight C1 C2 C3 C4 C5
32 105800 -362.23 0.9379 0 0
#N/A #N/A #N/A #N/A #N/A #N/A
Diameter 200 1200
Pull through floating head 88 97
Split ring floating head 50 77
Outside packed head 38 38
Fixed and U tube 10 20
200 1200
Split ring floating head 50 77
Bundle Diameter #DIV/0!
Clearance #DIV/0!
Viscosity Temperature at wall #DIV/0!
0.000576671 Pa.s
4.07E+01 Pa.s
#DIV/0! Pa.s
Heat Capacity
2.505762097 J/(kg.K)
#N/A J/(kg.K)
Kern's method
Shell side
Heat transfer factor
Reynolds no. #DIV/0!
Baffle cut,% 15 25 35 45
Equation #DIV/0! #DIV/0! #DIV/0! #DIV/0!
R2 0.99804 0.99858 0.9988 0.99898
25
jh #DIV/0!
Friction factor
Baffle cut,% 15 25 35 45
Equation #DIV/0! #DIV/0! #DIV/0! #DIV/0!
R2 0.84065 0.8234 0.84808 0.84463
25
#DIV/0!
Fluid Fouling factor
River water 7500
Sea water 3000
Cooling water 4000
Town water soft 4000
Town water hard 2000
Light hydrocarbon 5000
Heavy hydrocarbon 2000
Sea water 3000
Light hydrocarbon 5000
Heat transfer factor Friction factorReynold's no #DIV/0!
Bell's method
Triangular #DIV/0! Triangular
Square #DIV/0! Square
Tube side
Heat transfer factor
Reynolds no. #DIV/0!
L/D 24 48
Equation #DIV/0! #DIV/0!
R2 0.89817 0.88485
L/D 240
jh #DIV/0!
Friction factor
Equation #DIV/0!
Friction factor
Bell's method
#DIV/0!
#DIV/0!
120 240 500
#DIV/0! #DIV/0! #DIV/0!
0.8514 0.78346 0.68186