Parameter Study of Geometrically Induced Flow Maldistribution in Shell and Tube Heat Exchangers

被引:2
|
作者
Schab, Richard [1 ]
Dorau, Tim [1 ]
Unz, Simon [1 ]
Beckmann, Michael [1 ]
机构
[1] Tech Univ Dresden, Chair Energy Proc Engn, D-01069 Dresden, Saxony, Germany
基金
欧盟地平线“2020”;
关键词
energy efficiency; energy systems; experimental techniques; fouling; heat and mass transfer; heat exchangers; heat recovery; heat transfer enhancement; heat transfer in manufacturing; thermal systems; shell-and-tube heat exchanger; flow maldistribution;
D O I
10.1115/1.4053633
中图分类号
O414.1 [热力学];
学科分类号
摘要
Shell and tube heat exchangers (STHEs) are the most common type of heat exchanger in preheat trains (PHT) of oil refineries and in chemical process plants. Most commercial design software tools for STHE assume uniform distribution over all tubes of a tube bundle. This leads to various challenges in the operation of the affected devices. Flow maldistribution reduces heat duty of STHE in many applications and supports fouling buildup in fluids that tend to particle, bio, and crystallization fouling (Verein Deutscher Ingenieure, ed., 2010, Heat Atlas, 2nd ed., VDI-Buch., Springer-Verlag). In this article, a fluid mechanics study about tube side flow distribution of crude oil and related hydrocarbons in two-pass PHT heat exchangers is described. It is shown that the amount of flow maldistribution varies significantly between the different STHE designs. Therefore, a parameter study was conducted to investigate reasons for maldistribution. For instance, the nozzles diameter, type, and orientation were identified as crucial parameters. In consequence, simple design suggestions for reducing tube side flow maldistribution are proposed.
引用
收藏
页数:8
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