用于研究横流波纹板式热交换器中流量分布不均问题的耦合建模框架

Haowen Li, Xiaomei Guo, Marat A. Belotserkovsky, Aleksandr N. Grigorchik, V. Kukareko, Zheng Bo
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引用次数: 0

摘要

在许多实际应用中,准确预测流量分布不均对板式热交换器热-水力行为的影响对于热设计和优化非常重要。本文提出了一个由传热模型和水力模型组成的耦合建模框架,用于定量评估错流对横流波纹板式热交换器热工水力性能的影响。通过与实验数据对比,验证了所提方法的数值结果。利用耦合模型,分析了流动分布的不均匀性、换热器效果的恶化以及压降偏差。此外,还研究了不同入口雷诺数和入口温度下侧流分布不良的综合影响。结果表明,当入口气体雷诺数在 1100-2700 之间时,气体侧的不均匀分布会导致空气分布不均,并造成 10%-30% 的效率下降。研究发现,当入口空气雷诺数在 6000-18000 之间时,空气分布不良不会导致气体分布不良,但空气不均匀度的增加。将导致热交换器的效果越来越差。在空气和气体流动不均匀的情况下,气体和空气侧的压降分别增加 5%和小于 12.4%。这项研究为优化横流波纹板热交换器提供了一个计算框架,以实现理想的热液性能。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
A coupled modeling framework for investigating flow maldistribution in cross-flow-corrugated plate heat exchangers
Accurate prediction of the impact of flow maldistribution on the thermo-hydraulic behavior of plate heat exchangers is important for thermal design and optimization in a number of practical applications. In this paper, a coupled modeling framework, consisting of a heat transfer model and a hydraulic model, is proposed for quantitatively evaluating the impact of maldistribution on the thermo-hydraulic performance of a cross-flow-corrugated plate heat exchanger. The numerical results of the proposed approach are validated by comparison with experimental data. Using the coupled model, the flow distribution nonuniformity, heat exchanger effectiveness deteriorations, and pressure drop deviations are analyzed. Furthermore, the combined effects of side stream maldistribution are investigated for different inlet Reynolds numbers and inlet temperatures. The results demonstrate that when the inlet gas Reynolds number is in the range of 1100–2700, nonuniform distribution of the gas side will cause air maldistribution, and a 10%–30% effectiveness deterioration rate. It is found that air maldistribution will not result in gas maldistribution when the inlet air Reynolds number is in the range of 6000–18 000, but increasing air nonuniformity. Will lead to increasing deterioration in heat exchanger effectiveness. In the presence of air and gas flow maldistribution, the pressure drops on the gas and air sides increase by 5% and less than 12.4%, respectively. This work provides a computational framework for optimization of cross-flow-corrugated plate heat exchangers to achieve desired thermo-hydraulic performance.
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