Theoretical model to estimate fluid distribution in compact heat exchangers

IF 1.7 4区 工程技术 Q3 MECHANICS
M. V. V. Mortean, G. F. Luvizon, D. Baraldi
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引用次数: 0

Abstract

One of the limitations to design a compact heat exchanger is the phenomenon of fluid maldistribution. Most research considers a uniform fluid distribution in the channels, which can be considered a wrong approximation, since the non-uniform fluid distribution can seriously affect the performance. There are few experimental and numerical studies related to fluid distribution in a compact heat exchanger, however, currently, there is no mathematical model capable of predicting the fluid distribution within the channels. The present work developed the first theoretical model capable to estimate the flow distribution inside compact heat exchanger channels. The model is based on the concept of the shape factor, relating the radiation ratio between surfaces with the mass flow rate. The model considers geometric parameters to estimate the fluid distribution, such as channel position, channel cross-sectional area, fluid inlet surface area, and inlet header depth. In order to verify the model's accuracy, comparisons with experimental and numerical data available in the literature were performed, besides, a test facility was produced and used to test two header configurations. The average error of the model was approximately 9%, having a better performance than the hypothesis of uniform distribution, which presented an average error of 13%. However, in cases where fluid maldistribution was pronounced, the model exhibited significantly better results, reducing the error from 29%, uniform distribution hypothesis, to 11%. This demonstrates that the model can be applied to estimate fluid distribution inside de core and enhance the design of heat exchangers.

Abstract Image

紧凑式换热器中流体分布的理论模型
设计紧凑型换热器的限制之一是流体不均匀分布现象。大多数研究认为通道内流体分布均匀,这可以被认为是错误的近似,因为流体分布不均匀会严重影响性能。关于紧凑型换热器内流体分布的实验和数值研究很少,但目前还没有能够预测管道内流体分布的数学模型。本文建立了第一个能够估计紧凑换热器通道内流量分布的理论模型。该模型基于形状因子的概念,将表面之间的辐射比与质量流量联系起来。该模型考虑几何参数来估计流体分布,如通道位置、通道横截面积、流体入口表面积和入口集箱深度。为了验证模型的准确性,与文献中的实验数据和数值数据进行了比较,并制作了一个测试装置,用于测试两种封头结构。模型的平均误差约为9%,优于均匀分布假设的平均误差13%。然而,在流体不均匀分布明显的情况下,模型显示出明显更好的结果,将误差从均匀分布假设的29%降低到11%。结果表明,该模型可用于估算堆芯内流体分布,提高换热器的设计效率。
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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来源期刊
Heat and Mass Transfer
Heat and Mass Transfer 工程技术-力学
CiteScore
4.80
自引率
4.50%
发文量
148
审稿时长
8.0 months
期刊介绍: This journal serves the circulation of new developments in the field of basic research of heat and mass transfer phenomena, as well as related material properties and their measurements. Thereby applications to engineering problems are promoted. The journal is the traditional "Wärme- und Stoffübertragung" which was changed to "Heat and Mass Transfer" back in 1995.
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