Pressure Drop in Plate Heat Exchangers for Single-Phase Convection in Turbulent Flow Regime: Experiment and Theory

被引：12

作者：

Gusew, Sergej ^{[1
]}

Stuke, Rene ^{[1
]}

机构：

[1] FUNKE Warmeaustauscher Apparatebau GmbH, Dept Res & Dev, Dessel 1, D-31028 Gronau, Leine, Germany

来源：

INTERNATIONAL JOURNAL OF CHEMICAL ENGINEERING | 2019年 / 2019卷

关键词：

PERFORMANCE; CHANNELS;

D O I：

10.1155/2019/3693657

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

Plate heat exchangers (PHEs) play an important role in different technical fields, namely, in energetics, chemical industry, food industry, and others. To use PHE effectively, it is necessary to have correct data for pressure drop. Unfortunately, in open literature, a large difference among different authors occurs. In this work is shown that an essential portion of this difference lies in the choice of the typical length for the calculation of the friction coefficient. Care must be taken to consider the pressure drop of the distribution zone. A three-component model for hydraulic resistance of PHE in turbulent flow regime is proposed in this work. The proposed model shows good agreement with experimental data.

引用

页数：11

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