The sorption-enhanced method can change the thermodynamic equilibrium by absorbing CO2. However, it also brings about the problems of high regeneration temperature of adsorbent and large regeneration energy con-sumption. In order to study the impact of enhanced adsorption methods on the overall energy cost of the system in the hydrogen production process, this paper analyzes and compares steam methane reforming and reactive adsorption-enhanced steam methane reforming with the energy consumption of hydrogen production products as the evaluation index. The results showed that the energy consumption per unit hydrogen production decreased from 276.21 MJ/kmol to 131.51 MJ/kmol, and the decomposition rate of H2O increased by more than 20% after the addition of adsorption enhancement method. It is proved that the advantage of sorption enhanced method on pre-separation of CO2 in the product makes up for the disadvantage of energy consumption of adsorbent regeneration. In addition, the ability of the process to obtain H element is improved by the high decomposition rate of H2O, which realizes a more rational distribution of the element.
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E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Xu, Pan
Zhou, Zhiming
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E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Zhou, Zhiming
Zhao, Changjun
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E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
Zhao, Changjun
Cheng, Zhenmin
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E China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R ChinaE China Univ Sci & Technol, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
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Univ Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USAUniv Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USA
Alshafei, Faisal H.
Minardi, Luke T.
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Univ Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USAUniv Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USA
Minardi, Luke T.
Rosales, Derrick
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Univ Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USAUniv Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USA
Rosales, Derrick
Chen, Gen
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Univ Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USAUniv Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USA
Chen, Gen
Simonetti, Dante A.
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Univ Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USAUniv Calif Los Angeles, Chem & Biomol Engn Dept, Los Angeles, CA 90095 USA
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Georgia Inst Technol, George W Woodruff Sch Mech Engn, Atlanta, GA 30332 USAGeorgia Inst Technol, George W Woodruff Sch Mech Engn, Atlanta, GA 30332 USA
Gunawan, Andrey
Singh, Abhishek K.
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Univ Twente, Dept Thermal & Fluid Engn, Fac Engn Technol, Postbus 217, NL-7500 AE Enschede, NetherlandsGeorgia Inst Technol, George W Woodruff Sch Mech Engn, Atlanta, GA 30332 USA