Hi,
Has anyone designed Water Bath Indirect Heater (Line Heater) using ProMax software? Any information is greatly appreciated.
Here are the Line Heater conditions:
Feed : Sour Gas and Liquids
Coil 1 Coil 2
Process Duty kW 412.8 412.8
Vapour Flow Rate kg/hr 10510 10510
Dry Gas Flow Rate MMSCFD 10 10
Density (Vapour) kg/m3 323.3 93.98
Viscosity cP 0.03497 0.01509
Specific Heat KJ/kg DegC 2.929 2.450
Operating Pres. kPag 30000 8796
Operating Temp. Deg C 30 33.16
Thermal Cond. W/m Deg C 0.08733 0.03946
Design Temp. degC 100 100
Design Pres. kPag 31500 13962
Shell Side
Feed: EG/Water (50/50)
Density (Vapour) kg/m3 1019
Viscosity cP 0.8407
Specific Heat KJ/kg DegC 3.575
Vap. Pres. kPaa 45.68
Operating Temp. Deg C 85
Thermal Cond. W/m Deg C 0.5507
Design Temp. degC 100
Design Pres. kPag Atms
This is the information what I have. It's my first time designing Line Heater. Thank you in advance.
Thanks
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Line Heater
Started by chemdesign, Dec 02 2008 09:47 AM
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Posted 02 December 2008 - 09:47 AM
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