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Design and thermodynamic analysis of coal-gasification assisted multigeneration system with hydrogen production and liquefaction

机译:煤气化辅助氢气生产和液化的设计与热力学分析

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摘要

The primary subject of this paper to investigate the coal gasification-based integrated power process for multigeneration aim, such as electricity, heating, cooling, fresh and hot water, hydrogen production and liquefaction. This suggested work consists of the gasification process, Rankine cycle with two turbines, organic Rankine cycle, single effect absorption cooling cycle, membrane distillation process, PEM electrolyzer and hydrogen liquefaction cycle. The thermodynamic assessment is utilized to examine the investigated system efficiency, and also the effects of some process indicators on the energetic and exergetic performance of integrated plant and its sub-systems are investigated. The energy and exergy efficiencies of the proposed plant are calculated as 58.47% and 55.72%. In addition, the overall irreversibility of system is found as 65126 kW. The outcomes of thermodynamic evaluation show that the varying temperature of coal gasifier, combustor and exhaust gas affect the whole system performance.
机译:本文的主要主题研究了基于煤气化的集成电源方法,用于多粒瞄准,如电力,加热,冷却,新鲜和热水,氢气产生和液化。这项建议的工作包括气化过程,具有两个涡轮机,有机朗肯循环,单一效果吸收冷却循环,膜蒸馏过程,PEM电解槽和氢液化循环的朗肯循环。热力学评估用于检查调查的系统效率,还研究了一些过程指标对综合植物和子系统的能量和前进性能的影响。所提出的植物的能量和漏洞效率计算为58.47%和55.72%。此外,系统的整体不可逆转性被发现为65126 kW。热力学评估的结果表明,煤气化器,燃烧器和废气的不同温度影响整个系统性能。

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