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Conceptual design of a Ca-Cu chemical looping process for hydrogen production in integrated steelworks

机译:用于集成钢厂制氢的Ca-Cu化学循环工艺的概念设计

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A novel configuration of the Ca-Cu looping process is proposed for the production of a H-2 enriched fuel gas by means of the sorption enhanced water gas shift (SEWGS) of blast furnace gas (BFG) in steel mills. CO2 is simultaneously removed from the gas using a CaO-based sorbent. A Cu/CuO chemical loop supplies the energy required for the regeneration of the sorbent via the exothermic reduction of CuO with coke oven gas (GOG). The process is carried out in an arrangement of interconnected fluidized-bed reactors operating at atmospheric pressure, which allows for a solids' segregation step to be introduced that will reduce significantly the solid circulation between reactors A reference case study is presented, where the SEWGS is operated at 600 degrees C and the regeneration of the sorbent at 870 degrees C. About 27% of the BFG can be decarbonized in the SEWGS reactor producing 110 Nm(3) of H-2 per tonne of steel. A CO2 capture ratio of 31% with respect to the total carbon emissions in the steel mill can be achieved. More than 60% of the thermal input can be recovered as high-temperature heat, which could be efficiently recovered for producing electricity. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:提出了一种新颖的Ca-Cu循环工艺配置,用于通过钢铁厂中高炉煤气(BFG)的吸附增强水煤气变换(SEWGS)生产富含H-2的燃料气体。使用基于CaO的吸附剂同时从气体中去除CO2。 Cu / CuO化学回路通过用焦炉气(GOG)放热还原CuO来提供吸附剂再生所需的能量。该过程在相互连接的流化床反应器中进行,该反应器在大气压下运行,这允许引入固体的分离步骤,这将显着减少反应器之间的固体循环。提供了一个参考案例研究,其中SEWGS为在600摄氏度下运行,吸附剂在870摄氏度下再生。SEWGS反应器中约有27%的高炉煤气可以脱碳,每吨钢产生110 Nm(3)H-2。相对于钢铁厂的总碳排放量,可实现31%的CO2捕集率。超过60%的热输入可以作为高温热回收,可以有效地回收以产生电力。 (C)2017氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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