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H-2 pressure swing adsorption for high pressure syngas from an integrated gasification combined cycle with a carbon capture process

机译:H-2变压吸附,用于集成气化联合循环和碳捕集过程的高压合成气

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The integrated gasification combined cycle (IGCC) process, possessing high efficiency and environmental advantages, produces H-2-rich syngas at high pressures (30-35 bar) after capturing CO2. Since the syngas pressure is very high for conventional PSA processes, development of an efficient PSA process at the pressure conditions is required for H-2 production. In this study, the H-2 PSA process for IGCC syngas was developed experimentally and theoretically. Breakthrough and PSA experiments using activated carbon or activated carbon/zeolite LiX were performed at 25-35 bar by using a five-component hydrogen mixture (H-2:CO:N-2:CO2:Ar = 88:3:6:2:1 mol%) as a simulated syngas. The overall PSA performance was evaluated in terms of the purity, recovery and productivity of H-2 product. According to the results from using single or layered beds, the two-bed PSA process produced 99.77-99.95% H-2 with 73.30-77.64% recovery experimentally. A four-layered bed PSA at 35 bar was able to produce 99.97%-purity H-2 with 79% recovery, and it contained Ar and N-2 impurities. The quality of tail gas from the PSA process could be used for the gas turbine without losing H-2 and CO. A rigorous mathematical model that included mass, energy, and momentum balances was employed to elucidate the dynamic behaviors and separation performance of the adsorption bed and PSA process. (C) 2016 Elsevier Ltd. All rights reserved.
机译:集成气化联合循环(IGCC)工艺具有高效和环保优势,在捕获二氧化碳后,可在高压(30-35 bar)下产生富含H-2的合成气。由于常规PSA工艺的合成气压力很高,因此在H-2生产中需要在压力条件下开发有效的PSA工艺。在这项研究中,IGCC合成气的H-2 PSA工艺是通过实验和理论开发的。通过使用五组分氢气混合物(H-2:CO:N-2:CO2:Ar = 88:3:6:2),在25-35 bar下使用活性炭或活性炭/沸石LiX进行突破和PSA实验:1 mol%)作为模拟合成气。根据H-2产品的纯度,回收率和生产率评估了PSA的总体性能。根据使用单床或分层床的结果,两床PSA工艺可生产99.77-99.95%的H-2,实验回收率为73.30-77.64%。 35 bar的四层床PSA能够生产99.97%纯度的H-2,回收率为79%,并且其中包含Ar和N-2杂质。 PSA工艺产生的尾气质量可以用于燃气轮机而不会损失H-2和CO。采用包括质量,能量和动量平衡的严格数学模型来阐明吸附的动力学行为和分离性能床和PSA流程。 (C)2016 Elsevier Ltd.保留所有权利。

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