Heat Transfer Characteristics in a Plate-Fin Heat Exchanger with Single-Phase Flow

C. Son, J. Kong, Sang-Woo Lee, Chang-Soo Kim, Byoung-Soo Koo, J. Yoon
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引用次数: 2

Abstract

High-efficiency heat exchangers are essential to liquefy hydrogen, which is spotlighted as a next-generation energy source. Among the heat exchangers, plate-fin heat exchanger has a very large effective heat transfer area per unit volume, which allows the simultaneous exchange of several fluids, so it is specialized in the hydrogen liquefaction process. However, very few studies have been conducted for heat transfer analysis of plate-fin heat exchangers. Therefore, in this paper, the single-phase convective heat transfer coefficients were calculated using the modified Wilson plot method, and pressure drop was compared with other correlations. The main results are summarized as follows. The pressure drop agrees well with the previous correlation, but the convective heat transfer coefficients has different from others. Therefore, based on the experimental results, a new single-phase heat transfer correlation for the plate fin heat exchanger is presented.
单相流板翅式换热器的换热特性
高效热交换器是液化氢的必要条件,是下一代能源的焦点。在换热器中,板翅式换热器单位体积的有效换热面积非常大,可以同时交换几种流体,因此专门用于氢气液化过程。然而,对于板翅式换热器的传热分析研究却很少。因此,本文采用改进的Wilson图法计算单相对流换热系数,并将压降与其他相关系数进行比较。主要研究结果总结如下:压降与上述相关关系吻合较好,但对流换热系数不同。因此,在实验结果的基础上,提出了一种新的板翅式换热器单相传热关系式。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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