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Optimum energy evaluation and life cycle cost assessment of a hydrogen liquefaction system assisted by geothermal energy

机译:地热能辅助氢液化系统的最佳能量评估和生命周期成本评估

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In this study, analyses of the thermodynamic performance and life cycle cost of a geothermal energy-assisted hydrogen liquefaction system were performed in a computer environment. Geothermal water at a temperature of 200 degrees C and a flow rate of 100 kg/s was used to produce electricity. The produced electricity was used as a work input to liquefy the hydrogen in the advanced liquefaction cycle. The net work requirement for the liquefaction cycle was calculated as 8.6 kWh/kg LH2. The geothermal power plant was considered as the work input in the liquefaction cycle. The hydrogen could be liquefied at a mass flow rate of 0.2334 kg/s as the produced electricity was used directly to produce liquid hydrogen in the liquefaction cycle. The unit costs of electricity and liquefied hydrogen were calculated as 0.012 $/kWh and 1.44 $/kg LH2. As a result of the life cycle cost analysis of the system, the net present value (NPV) and levelized annual cost (LAC) were calculated as 123,100,000 and 14,450,000 $/yr. The simple payback period (N-spp) and discount payback period (N-dpp) of the system were calculated as 2.9 and 3.6 years, respectively. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:在这项研究中,在计算机环境中对地热能辅助氢液化系统的热力学性能和生命周期成本进行了分析。温度为200摄氏度,流速为100千克/秒的地热水用于发电。产生的电被用作在高级液化循环中液化氢气的功输入。液化循环的净功要求经计算为8.6 kWh / kg LH2。地热发电厂被认为是液化循环中的功投入。氢气可以以0.2334 kg / s的质量流速液化,因为在液化循环中,所产生的电能直接用于生产液态氢。电力和液化氢的单位成本计算为0.012 $ / kWh和1.44 $ / kg LH2。系统生命周期成本分析的结果是,净现值(NPV)和平均年度成本(LAC)计算为每年123,100,000和14,450,000 $。系统的简单投资回收期(N-spp)和折扣投资回收期(N-dpp)分别计算为2.9年和3.6年。 (C)2019氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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