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Research on systems for producing liquid hydrogen and LNG from hydrogen-methane mixtures with hydrogen expansion refrigeration

机译:用氢气膨胀制冷制备液体氢气和LNG的系统研究

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摘要

In industrial production processes, gas mixtures with hydrogen and methane as main useful components are often obtained as by-products, which are often not well utilized. In this paper, an innovative approach is proposed to produce both liquid hydrogen and LNG from industrial by-products with H-2 and CH4 as main components. Taking the purified hydrogen-methane mixtures as the research object, four different separation-liquefaction processes (namely Open Loop-N-2, Open Loop-H-2, Closed Loop-N-2, Closed Loop-H-2) are constructed and optimized, with refrigeration supplied with hydrogen expansion at the cryogenic section and nitrogen or hydrogen expansion at the precooling section. A distillation column is set up before the mixture enters the cryogenic section to facilitate the production of high purity methane and hydrogen products. Every system achieves excellent energy integration, and the load of condenser and reboiler in the column is borne by the hydrogen expansion cycle in the cryogenic section. For each process, the influence of hydrogen mole proportion in feed gas between 10% and 90% on the process performance is analyzed. The results show that the purities of LNG and liquid hydrogen products obtained by the system are higher than 99.99%, and the specific energy consumption of the systems is within 18.01-41.72 kWh.kmol(-1) for different situations. At the same time, an open loop and a closed loop are constructed, respectively, to investigate the necessity of recovering cold energy of boil-off gas. The results suggest recommendation of open loop system with nitrogen precooling. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:在工业生产过程中,通常作为主要有用组分的氢气和甲烷的气体混合物通常作为副产物获得,这通常不会很好地利用。本文提出了一种创新的方法,以将工业副产物与H-2和CH4的工业副产物产生液体氢和LNG作为主要成分。将纯化的氢 - 甲烷混合物作为研究对象,构建了四种不同的分离液化过程(即开放环-N-2,开放环-H-2,闭环-N-2,闭环-H-2)并优化,用在低温截面和氮气或预冷部分的氮气膨胀中提供的制冷。在混合物进入低温截面以便于生产高纯度甲烷和氢产物之前,设置蒸馏塔。每个系统都能实现优异的能量整合,并且柱子中的冷凝器和再沸器的负载由低温截面中的氢膨胀循环承载。对于每种方法,分析了对工艺性能的10%至90%的进料气体中氢摩尔比例的影响。结果表明,由系统获得的LNG和液态氢产品的纯度高于99.99%,系统的特定能耗在18.01-41.72 kWh.kmol(-1)范围内。同时,分别构造开环和闭环,以研究蒸发气体冷能的必要性。结果表明开环系统与氮气预冷的建议。 (c)2020氢能量出版物LLC。 elsevier有限公司出版。保留所有权利。

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