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Thermochemical Hydrogen Production With A Copper-chlorine Cycle. Ⅰ: Oxygen Release From Copper Oxychloride Decomposition

机译:铜-氯循环的热化学制氢。 Ⅰ:氯氧化铜分解释放的氧气

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摘要

A key challenge facing the future hydrogen economy is a sustainable, lower-cost method of hydrogen production, with reduced dependence on fossil fuels. Thermochemical water splitting with a copper-chlorine (Cu-Cl) cycle is a promising alternative that could be linked with nuclear reactors to thermally decompose water into oxygen and hydrogen, through intermediate copper and chlorine compounds. Heat is transferred between various endothermic and exothermic reactors in the Cu-Cl cycle, through heat exchangers that supply or recover heat from individual processes. This paper examines the heat requirements of these steps, in efforts to recover as much heat as possible and minimize the net heat supply to the cycle, thereby improving its overall efficiency. Also, this paper examines the thermal design of the oxygen production reactor, which is a key process to split water by decomposing an intermediate compound, copper oxychloride (Cu_2OCl_2), into oxygen gas and molten cuprous chloride. The equipment design is analyzed to scale-up past work in small proof-of-principle test tubes, up to larger capacities of oxygen production with engineering lab-scale equipment.
机译:未来氢经济面临的主要挑战是可持续,低成本的氢生产方法,同时减少对化石燃料的依赖。利用铜-氯(Cu-Cl)循环进行热化学水分解是一种很有前途的替代方案,可以与核反应堆连接,以通过中间的铜和氯化合物将水热分解为氧气和氢气。热量通过提供各个过程热量或从各个过程中回收热量的热交换器在Cu-Cl循环中的各种吸热和放热反应器之间传递。本文研究了这些步骤的热量需求,以努力回收尽可能多的热量并最大程度地减少循环的净热量,从而提高其整体效率。此外,本文还研究了制氧反应器的热设计,这是通过将中间化合物氯氧化铜(Cu_2OCl_2)分解为氧气和熔融氯化亚铜来分解水的关键过程。对设备设计进行了分析,以扩大在小型原理验证试管中的过去工作,并通过工程实验室规模的设备扩大到更大的制氧能力。

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