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Large-scale liquid hydrogen production methods and approaches: A review

机译:大规模液氢生产方法和方法综述

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摘要

Large-scale hydrogen liquefaction (LHL) methods and different approaches of the configuration of hydrogen liquefaction cycles are chronicled. History landmarks of permanent gases liquefaction are quick reviewed and the basic hydrogen liquefaction cycles, the existing in-service LHL plants around the world, and LHL conceptual proposed plants, including the state of the art plants, are recorded and categorized based on the systems' main parameters. In addition, a novel classification of hydrogen liquefaction systems in terms of heat exchange and expansion process method is introduced. As well as, the authors infer that renewable energy technologies section should be added to the old sectioning of the hydrogen liquefaction plants. In addition, hybrid conceptual hydrogen liquefaction plants, combining with renewable power cycles are reviewed and the increasing contribution of this new approach is demonstrated. Finally, the operational costs of the plants considering the systems' efficiency are examined, and a trend in specific energy consumption (SEC) and exergy efficiency of hydrogen liquefiers is discussed. Accordingly, considering the existing technologies, SEC reduction of hydrogen liquefaction will not be abrupt in near future and it will remain within the range of 5-8 kWh/kg(LH2). Moreover, exploiting of isentropic expansion processes instead of isenthalpic one, cascading of refrigerating cycles, using of new mixed refrigerants as working fluid of refrigeration cycles, and hybridization of renewable energy power cycles to refrigeration cycles are the main four growing approaches in the hydrogen liquefaction context.
机译:记录了大规模的氢液化(LHL)方法和氢液化循环构型的不同方法。快速回顾了永久性气体液化的历史地标,并根据系统的记录,对基本氢液化周期,全球现有的在役LHL工厂以及LHL概念性拟建工厂(包括最先进的工厂)进行了记录和分类。主要参数。此外,根据热交换和膨胀工艺方法,对氢液化系统进行了新的分类。同时,作者推断应将可再生能源技术部分添加到氢液化厂​​的旧部分中。此外,还对混合概念氢液化厂与可再生能源循环相结合进行了综述,并证明了这种新方法的日益增长的贡献。最后,研究了考虑系统效率的工厂的运营成本,并讨论了氢液化器的单位能耗(SEC)和火用效率的趋势。因此,考虑到现有技术,SEC在不久的将来不会突然减少氢的液化,并且将保持在5-8kWh / kg(LH 2)的范围内。此外,利用等熵膨胀工艺代替等焓膨胀工艺,级联制冷循环,使用新的混合制冷剂作为制冷循环的工作流体以及将可再生能源发电循环与制冷循环混合是氢液化的四个主要增长途径。 。

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