One hundred kilograms per second of a hydrocarbon are heated from 20°C to 40°C through the tubes of a multi-tube heat exchanger. Crude oil flow is divided evenly among all 100 tubes without a tube bundle. The inner diameter of each tube is 10 mm and the temperature at the inner wall of the tube is maintained at 100 °C.The thermophysical properties of crude oil at the average temperature are: Specific mass = 850 kg / m3 heat capacity = 1900 J / (kg.K) Conduction coefficient = 0.25 W / (m.K) Dynamic Viscosity = 0.012 Pa.s To determine: a) The convective coefficient; b) A rate of heat transfer by the convection mechanism; c) The length of the tube.
One hundred kilograms per second of a hydrocarbon are heated from 20°C to 40°C through the tubes of a multi-tube heat exchanger. Crude oil flow is divided evenly among all 100 tubes without a tube bundle. The inner diameter of each tube is 10 mm and the temperature at the inner wall of the tube is maintained at 100 °C.The thermophysical properties of crude oil at the average temperature are:
- Specific mass = 850 kg / m3
- heat capacity = 1900 J / (kg.K)
- Conduction coefficient = 0.25 W / (m.K)
- Dynamic Viscosity = 0.012 Pa.s
To determine:
a) The convective coefficient;
b) A rate of heat transfer by the convection
c) The length of the tube.
Given that
mass flow rate ,mT = 100 kg/s
T1 = 20 C
T2= 40 C
Crude oil flow is divided evenly among all 100 tubes without a tube bundle
D = 10 mm and the temperature at the inner wall of the tube is maintained at 100 °
- Specific mass = 850 kg / m3
- heat capacity,Cp = 1900 J / (kg.K)
- Conduction coefficient,K = 0.25 W / (m.K)
- Dynamic Viscosity,u = 0.012 Pa.s
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