Experimental and numerical study on unsteady natural convection heat transfer in helically coiled tube heat exchangers

被引:23
|
作者
Neshat, E. [1 ]
Hossainpour, S. [1 ]
Bahiraee, F. [1 ]
机构
[1] Sahand Univ Technol, Dept Mech Engn, Tabriz 513251996, Iran
关键词
Heat Transfer Coefficient; Heat Exchanger; Nusselt Number; Natural Convection; Rayleigh Number;
D O I
10.1007/s00231-014-1299-z
中图分类号
O414.1 [热力学];
学科分类号
摘要
Both of experimental and numerical investigations were performed to understand unsteady natural convection from outer surface of helical coils. Four helical coils with two different curvature ratios were used. Each coil was mounted in the shell both vertically and horizontally. The cold water was entered the coil and the hot water in the shell was cooling by unsteady natural convection. A CFD code was developed to simulate natural convection heat transfer. Equations of tube and shell are solved simultaneously. Statistical analyses have been done on data points of temperature and natural convection Nusselt number. It was revealed that shell-side fluid temperature and the Nusselt number of the outer surface of coils are functions of in-tube fluid mass flow rate, specific heat of fluids and geometrical parameters including length, inner diameter of the tube and the volume of the shell, and time.
引用
收藏
页码:877 / 885
页数:9
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