氢液化中正交对氢连续转换换热器的三维颗粒数值模型

IF 6.1 2区 工程技术 Q2 ENERGY & FUELS
Junjie Teng, Xinyu Wei, Shaolong Zhu, Song Fang, Shiran Bao, Xiaoqin Zhi, Limin Qiu, Kai Wang
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引用次数: 0

摘要

液态氢(LH2)具有能量密度高、储运方便等优点,是一种很有前途的储氢选择。氢液化过程中邻对氢转化是降低LH2产物蒸发损失的关键,其中连续催化转化是最节能的。然而,现有的研究大多采用均匀多孔介质模型来描述催化剂填充区,这与催化颗粒的实际布局存在差异。堆积的催化颗粒的影响尚不清楚,需要进一步的揭示。考虑到催化颗粒的几何形状和空间布局,建立了基于颗粒的三维数值模型。评价了填充颗粒对传热和转化性能以及内部物理场的影响。增大流量比可以略微增强流体与颗粒之间的对流换热,并由于温度梯度增大而改善转化性能。此外,高雷诺数提高了传热性能,但限制了转换效率,即使转换热量增加。对氢的进口浓度对浓缩热分布和转化热分布都有影响。当进口成分明显偏离平衡状态时,大量热负荷集中在进口附近,在80 ~ 70 K范围内达到1.56 × 106 W/m3。浓度沿流动方向分布均匀。相反,当入口成分接近平衡时,热负荷显著降低,预计将在通道下游进一步释放,浓度呈抛物线分布。本研究为正交对氢连续转换换热器提供了一种新的模拟方法,为进一步研究颗粒孔隙尺度上的详细信息提供了依据。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
A three-dimensional particles-based numerical model for ortho-para hydrogen continuous conversion heat exchangers in hydrogen liquefaction
Liquid hydrogen (LH2) is a promising hydrogen storage option considering its high energy density and convenience in storage and transportation. Ortho-para hydrogen conversion during hydrogen liquefaction is essential for reducing the boil-off loss of the LH2 product, of which the continuous catalytic conversion is the most energy efficient. However, most existing researches adopted the homogeneous porous media model for the catalysts-filled zones, which is different from the actual layout of catalytic particles. The impact of packed catalytic particles remains unclear and requires further revelation. A three-dimensional particles-based numerical model, considering the geometry and space layout of catalytic particles, is constructed in this work. The impact of packed particles on heat transfer and conversion performance as well as internal physical fields are evaluated. Increasing flowrate ratios enhances convective heat transfer between the fluid and particles slightly and leads to improvements in conversion performance due to greater temperature gradient. Besides, a high Reynolds number enhances heat transfer performance but limits conversion efficiency, even though the conversion heat increases. Both of the concentration and conversion heat distributions are influenced by the inlet concentration of para-hydrogen. When the inlet composition deviates significantly from the equilibrium state, a substantial heat load is concentrated near the entrance, reaching 1.56 × 106 W/m3 within the 80 K to 70 K range. A uniform concentration distribution along the flow directions is observed. In contrast, when the inlet composition is closer to equilibrium, the heat load is significantly lower and is expected to be released further downstream in the channels and the concentration exhibits a parabolic distribution. The work offers a new simulation method for ortho–para hydrogen continuous conversion heat exchangers, which would be useful for studying more detailed information at the particle pore scale.
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来源期刊
Applied Thermal Engineering
Applied Thermal Engineering 工程技术-工程:机械
CiteScore
11.30
自引率
15.60%
发文量
1474
审稿时长
57 days
期刊介绍: Applied Thermal Engineering disseminates novel research related to the design, development and demonstration of components, devices, equipment, technologies and systems involving thermal processes for the production, storage, utilization and conservation of energy, with a focus on engineering application. The journal publishes high-quality and high-impact Original Research Articles, Review Articles, Short Communications and Letters to the Editor on cutting-edge innovations in research, and recent advances or issues of interest to the thermal engineering community.
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