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波形折流杆换热器的开发和工业化实验研究 总被引：1，自引：1，他引：1
The conventional heat exchanger with segmental baffles is prone to bring forth fluid-induced vibration of heat transfer tubes and increase the pressure drop of shell-side greatly at higher fluid flow velocity. In order to avoid the above defects, the ROD-baffle heat exchanger has been developed. However, its collocation of heat transfer tubes is conventionally in square, which leads to fewer heat transfer area per unit volume. Based on the ROD-baffle heat exchanger, a new type curve-ROD baffle has been developed, and an industrial investigation of the curve-ROD baffle heat exchanger with normal triangular collocation has been carried into execution. In this paper, two equations using the Reynolds number were acquired to predict the heat transfer coefficients of the shell-side and tubeside. The experimental results show that the shell-side heat transfer and pressure drop characteristics of the curve-ROD baffle heat exchanger are superior to those of the segmental baffle one. 相似文献
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Because of the complexities of fluid dynamics equations and the structure of heat exchangers, few theoretical
solutions have been acquired to specify the shell side characteristics of the rod baffle heat exchanger (RBHE)．Based on the
platform of PHEONICS version 3.5.1, a three-dimensional numerical method for predicting the turbulent fluid flow behavior
in the shell side of the rod baffle heat exchangers is developed in this paper. With this method, modeling of the tube bundle
is carried out based on the porous media concept using volumetric porosities and applicable flow resistance correlations.
Turbulence effects are modeled using a standard κ-ε model. It is shown that the simulation results and experimental results
are in good agreement in the shell side. The maximum absolute deviation value of pressure drops is less than 5%, and that
of the heat transfer coefficients is less than 8%. Furthermore, the numerical model is used to optimize the structure of the
RBHE and improves its performance. 相似文献
solutions have been acquired to specify the shell side characteristics of the rod baffle heat exchanger (RBHE)．Based on the
platform of PHEONICS version 3.5.1, a three-dimensional numerical method for predicting the turbulent fluid flow behavior
in the shell side of the rod baffle heat exchangers is developed in this paper. With this method, modeling of the tube bundle
is carried out based on the porous media concept using volumetric porosities and applicable flow resistance correlations.
Turbulence effects are modeled using a standard κ-ε model. It is shown that the simulation results and experimental results
are in good agreement in the shell side. The maximum absolute deviation value of pressure drops is less than 5%, and that
of the heat transfer coefficients is less than 8%. Furthermore, the numerical model is used to optimize the structure of the
RBHE and improves its performance. 相似文献
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