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Effective separation of low hydrogen containing gases with proton exchange membrane electrochemical hydrogen pump
Authors: CUI Fujuna, FAN Shuaib, DAI Yanb, Pan Dongweib, WU Xuemeib*, HE Gaohong
Units: Panjin Institute of Industrial Technology, Liaoning Key Laboratory of Chemical Additive Synthesis and Separation, Dalian University of Technology, Panjin 124221, Liaoning, China; bState Key Laboratory of Fine Chemicals, Research and Development Center of Membrane Science and Technology, School of Chemical Engineering, Dalian University of Technology, Dalian 116024, China
KeyWords: Proton exchange membrane; hydrogen pump; high purity of hydrogen; energy efficiency
ClassificationCode:TQ028、TM912.1
year,volume(issue):pagination: 2021,41(2):81-87

Abstract:
 By far the most important resource for hydrogen fabrication is fossil fuels, but the conventional separation methods for low hydrogen containing gases have several disadvantages such as low separation efficiency and high energy consumption, thus result in the waste of the hydrogen containing gases. In this work, a novel method to separate low hydrogen containing gases in proton exchange membrane hydrogen pump (PEMHP) is proposed, in which atmospheric pressure could be applicated due to the extreme high electrochemical selective dissociation and conduction of hydrogen in EHP, and the proton exchange membrane (PEM) could act as gas penetration barrier between anode and cathode chambers. Experimental correlations of hydrogen recovery and energy efficiency as functions of operating voltage, inlet flow rate with different H2 to CO2 ratios are established. Within the low hydrogen content in the inlet H2/CO2 mixed gas (less than about 33.3 vol.%), the hydrogen recovery is up to 95%. The lower the hydrogen content in the feedstock, the higher the energy efficiency of the hydrogen pump, and the energy efficiency is close to about 65%. Further investigations on the non-fluorine PEM based EHP indicate that the purity of the hydrogen product could be elevated to 99.99%, owing to much less gas permeation across PEM caused by the steric hindrance of aromatic polymer backbone. The application of the non-fluorine PEMs in EHP also significantly reduces the cost of hydrogen pump, therefore makes it feasible to produce high purity of hydrogen with low cost.

Funds:
辽宁省化学助剂合成与分离省市共建重点实验室2020年开放课题(ZJKF2012),国家自然科学基金(面上21776034,创新群体22021005);国家自然科学基金联合基金(U1663223,U1808209);中央高校举报科研业务费(DUT21TD101);辽宁省教育厅(LT2015007);科技部重点领域创新团队(2016RA4053)

AuthorIntro:
崔福军(1970-),男,河北承德人,研究方向为气体膜分离及粘合剂,Email:1012293273@qq.com

Reference:
 [1] Sgobbi, A., Nijs, W., De Miglio, R., Chiodi, A., Gargiulo, M., and Thiel, C. How far away is hydrogen? Its role in the medium and long-term decarbonisation of the European energy system[J]. Int J Hydrogen Energy, 2016, 41: 19–35.
[2] Pivovar B (2017) H2@Scale, National Renewable Energy Laboratory, U.S. Department of Energy Fuel Cell Technologies Office, https://www.nrel.gov/docs/fy21osti/77610.pdf.
[3] B. Parkinson, P. Balcombe, J. F. Speirs, A. D. Hawkes, K. Hellgardta. Levelized cost of CO2 mitigation from hydrogen production routes[J].  Energy Environ Sci, 2019, 12: 19-40.
[4] Midilli, A., Green hydrogen energy system: A policy on reducing petroleum based global unrest[J]. Int. J. Global Warm. 2016,10: 354–370.
[5] James A. Ritter and Armin D. Ebner[J]. Sep Sci Tech., 2007, 42: 123.
[6] Tim C. Merkel, M. Zhou, Richard W. Baker[J]. J Membrane Sci, 2012, 389: 441.
[7] 银醇彪, 张东辉, 鲁东东等. 数值模拟和优化变压吸附流程研究进展[J]. 化工进展,2014,33(3): 550-557.
[8] 石宝明, 廖健, 白雪松. 炼厂氢气的管理[J]. Chemical Techno-economics, 2003,21(1): 55-59.
[9] 郑惠平, 变压吸附回收炼厂干气中乙烯和氢气的研究[D]. 广州: 华南理工大学, 2011.
[10] 沈光林, 陈勇, 吴鸣.国内炼厂气中氢气的回收工艺选择[J]. 石油与天然气化工,2003,32(4): 193-196.
[11] Abdulla A, Laney K, Padilla M, et al. Efficiency of hydrogen recovery from reformate with a polymer electrolyte hydrogen pump[J]. AIChE J, 2011, 57(7): 1767-1779.
[12] Sedlak J M, Austin J F, LaConti A B. Hydrogen recovery and purification using the solid polymer electrolyte electrolysis cell[J]. Int J Hydrogen Energy, 1981, 6(1): 45-51.
[13] Wu X, He G, Yu L, et al. Electrochemical hydrogen pump with SPEEK/CrPSSA semi-interpenetrating polymer network proton exchange membrane for H2/CO2 separation[J]. ACS Sustainable Chem Eng, 2014, 2: 75-79.
[14] Lee H K, Choi H Y, Choi K H, et al. Hydrogen separation using electrochemical method. J.Power Sources[J], 2004, 132(1-2): 92-98.
[15] Gardner C L, Ternan M. Electrochemical separation of hydrogen from reformate using PEM fuel cell technology[J]. J Power Sources, 2007, 171: 835-841.
[16] Barbir F, Gorgun H. Electrochemical hydrogen pump for recirculation of hydrogen in a fuel cell stack[J]. J Appl Electrochem, 2007, 7: 359-365.
[17] Ibeh B, Gardner C, Ternan M, Separation of hydrogen from a hydrogen/methane mixture using a PEM fuel cell[J]. Int J Hydrogen Energy, 2007, 32(7): 908-914.
[18] Wu X, He G, Benziger J. Comparison of Pt and Pd catalysts for hydrogen pump separation from reformate[J]. J Power Sources, 2012, 218: 424-434.
[19] Perry K A, Eisman G A, Benicewicz B C. Electrochemical hydrogen pumping using a high-temperature polybenzimidazole (PBI) membrane[J]. J Power Sources, 2008, 177: 478−484.
[20] https://www.energy.gov/eere/fuelcells/hydrogen-production-natural-gas-reforming
[21] Shikai Zhang, Gaohong He, Xue Gong, Xiaoping Zhu, Xuemei Wu*, Xinye Sun, Xueying Zhao, Huan Li, Electrospun nanofiber enhanced sulfonated poly(phthalazinone ether sulfone ketone) composite proton exchange membranes[J]. J Membr Sci, 2015, 493: 58–65.
[22] 王保国.电化学能源转化膜与膜过程研究进展[J].膜科学与技术, 2020,40(01);179-187.

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