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Application of metal foam heat exchangers for a high-performance quefied natural gas regasification system

机译:金属泡沫热交换器在高性能液化天然气再气化系统中的应用

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摘要

The intermediate fluid vaporizer has wide applications in the regasification of LNG (liquefied natural gas). The heat exchanger performance is one of the main contributors to the thermodynamic and cost effectiveness of the entire LNG regasification system. Within the paper, the authors discuss a new concept for a compact heat exchanger with a micro-cellular structure medium to minimize volume and mass and to increase thermal efficiency. Numerical calculations have been conducted to design a metal foam filled plate heat exchanger and a shell-and-tube heat exchanger using published experimental correlations. The geometry of both heat exchangers was optimized using the conditions of thermolators in LNG regasification systems. The heat transfer and pressure drop performance was predicted to compare the heat exchangers. The results show that the metal-foam plate heat exchanger has the best performance at different channel heights and mass flow rates of fluid. In the optimized configurations, the metal-foam plate heat exchanger has a higher heat transfer rate and lower pressure drop than the shell-and-tube heat exchanger as the mass flow rate of natural gas is increased. (C) 2015 Elsevier Ltd. All rights reserved.
机译:中间流体蒸发器在LNG(液化天然气)的再气化中具有广泛的应用。热交换器的性能是整个LNG再气化系统热力学和成本效益的主要因素之一。在本文中,作者讨论了一种具有微孔结构介质的紧凑型热交换器的新概念,以最小化体积和质量并提高热效率。已经使用公开的实验相关性进行了数值计算,以设计金属泡沫填充板式热交换器和管壳式热交换器。使用LNG再气化系统中的恒温器条件优化了两个热交换器的几何形状。可以预测传热和压降性能来比较热交换器。结果表明,金属泡沫板式换热器在不同的通道高度和流体的质量流量下具有最佳性能。在优化配置中,随着天然气质量流量的增加,金属泡沫板式换热器比管壳式换热器具有更高的传热速率和更低的压降。 (C)2015 Elsevier Ltd.保留所有权利。

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