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Heat transfer
There is a tube and shell heat exchanger,and its outside area is A=40m2 . The tube is (25(2.5mm made up of steel. saturation steam which pressure is 2atm(a) in shell side is used to heat 2.5(104kg/h oil from 40(C to 80(C, and the individual coefficient of steam condensation is 1.2(104w/(m2K).Oil flows in tube side in turbulent flow, and its mean specific capacity is
1 The amount of oil treated increases one time, m(=2m, calculate the outlet temperature of the oil? If the outlet temperature of oil remains 80(C,whether heat exchanger is suitable?
2 Measures to be taken if the heat exchanger is unsuitable ?
3 Calculate A if another heat exchanger is added in series / parallel connection?What problems should be taken into consideration?
4 Whether the outlet temperature of oil remains 80(C if steam pressure is increased to 3atm?
5 Flowrate of the oil is fixed, and the oil viscosity is twice that of before. Other physical properties are fixed. please calculate outlet temperature of the oil .
6 After prolonged usage,there is thermal resistance of scale deposited on the outside surface of tubes, and the thickness is 1mm, k=0.2w/(mK) ,please calculate the outlet temperature of oil .
7 The atmosphere temperature is 10(C,and the individual coefficient by convection from surface to air is calculated according to the equ. :
The shell of the exchanger is 400 ( 8mm,and the temperature of the shell is 30(C after preservation. The thermal conductivity of the logging material is 0.058w/(mK)
Calculate the thickness of the logging material, and the steam saved per month.
1.The amount of oil treated increases one time, m(=2m ,calculate the outlet temperature of oil? If the outlet temperature of oil remains 80(C,whether heat exchanger is suitable?
To check whether heat exchanger is suitable
to maintain outlet temperature,check A
1)U
Thermal resistance mainly in tube side
(2) whether heat exchanger is suitable?
m(=2m ,
unsuitable
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