基于正仲氢多级转化的低温压缩储氢系统研究

Research of Cryogenic Compressed Hydrogen Storage System Based on Multistage Ortho-para Hydrogen Conversion

  • 摘要: 低温压缩储氢技术是一种高密度的储氢方法,该方法结合了高压气态储氢和低温液态储氢的优点。然而,现有的研究主要集中在低温压缩氢存储装置的开发,对冷却过程的研究有限。为克服高压气态储氢密度低以及低温液态氢在存储过程中存在的易蒸发的难题,文中提出了一种基于正仲氢多级转化的低温压缩储氢系统,并运用HYSYS软件对该系统进行了流程模拟分析与优化。选取了9个关键参数,例如氦气的压力参数、换热器出口的氦气温度,以及氦气和液氮的质量流量等作为优化参数,以单位能耗为目标,采用遗传算法进行了全局优化,并在能耗分析、㶲分析以及传热分析等方面开展了研究,并对工艺进行了有效评价,得出换热器和水冷器的㶲损失最大。研究结果表明:该储氢系统氢的密度达到了液氢密度的90%,可有效解决液氢蒸发量大的技术难题。此外,与传统的氢液化流程相比,经过优化后系统的单位能耗和㶲效率分别为6.872 kW∙h∙kg−1和42.42%,展现出极大的优势。从传热分析结果得知,系统中换热器HEX1的温差最大,㶲损失和占比分别为105.98 kW和26.75%。由此可见,流程优化的关键在于提高传热效率。综上,本研究不仅创新性地提出了一种提高储氢密度和减少蒸发的方案,而且提供了一种通过建模和㶲分析来优化系统效率的方法。

     

    Abstract: Cryogenic-compressed hydrogen storage technology is a high-density hydrogen storage method that combines the advantages of high-pressure hydrogen storage and cryogenic liquid hydrogen storage. However, existing research has mainly focused on the development of storage devices for cryogenic-compressed hydrogen, with limited research on the cooling process. To address the challenges associated with low density in high-pressure gaseous hydrogen storage and the significant evaporation of low-temperature liquid hydrogen storage, this paper proposes a novel low-temperature compression hydrogen storage system based on multistage ortho-para-hydrogen conversion. The HYSYS software is utilized to simulate and optimize the system's process. For optimization, nine key parameters, including the helium pressure, outlet temperature of helium from the heat exchanger, mass flow of helium and liquid nitrogen, etc. are selected. With unit energy consumption as the target parameter, a genetic algorithm is employed for the global optimization. The exergy analysis of the energy consumption and heat transfer analysis, as well as the evaluation of processing technology are conducted, showing that the exergy losses of the heat exchanger and water coolers are the greatest. The results demonstrate that the hydrogen density within the storage system can reach up to 90% of the density of liquid hydrogen, effectively mitigating the issue of substantial liquid hydrogen evaporation. Moreover, compared to the conventional hydrogen liquefaction processes, the optimized system boasts a unit energy consumption of 6.872 kW∙h∙kg−1 and an exergy efficiency of 42.42%, showcasing significant advantages. According to the results of the heat transfer analysis, the heat exchanger (HEX1) exhibits the largest temperature difference within the system, resulting in the exergy losses of 105.98 kW, accounting for 26.75% of total exergy losses. This highlights that enhancing heat transfer efficiency is crucial for optimization. In summary, this study not only presents an innovative solution to improve hydrogen storage density and reduce evaporation but also offers insights into optimizing system efficiency through modeling and exergy analysis.

     

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