Coupling hydrogen separation with butanone hydrogenation in an electrochemical hydrogen pump with sulfonated poly (phthalazinone ether sulfone ketone) membrane
发表时间:2019-03-13
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- 论文类型:
- 期刊论文
- 第一作者:
- Huang, Shiqi
- 通讯作者:
- He, GH (reprint author), Dalian Univ Technol, Sch Chem Engn, R&D Ctr Membrane Sci & Technol, State Key Lab Fine Chem, Dalian 116023, Peoples R China.
- 合写作者:
- Wang, Tao,Wu, Xuemei,Xiao, Wu,Yu, Miao,Chen, Wei,Zhang, Fengxiang,He, Gaohong
- 发表时间:
- 2016-09-30
- 发表刊物:
- JOURNAL OF POWER SOURCES
- 收录刊物:
- SCIE、EI、Scopus
- 文献类型:
- J
- 卷号:
- 327
- 页面范围:
- 178-186
- ISSN号:
- 0378-7753
- 关键字:
- Electrochemical hydrogen pump (EHP); SPPESK membrane; Hydrogenation; Hydrogen separation; Electrochemistry
- 摘要:
- This work reports the novel work of coupling H-2/CO2 separation with biomass-derived butanone hydrogenation in non-fluorinated sulfonated poly (phthalazinone ether sulfone ketone) (SPPESK) electro-chemical hydrogen pump (EHP) reactor. Due to higher resistance to swelling, SPPESK-based EHP reactor exhibits more excellent reaction rate in elevated temperature (60 degrees C) and higher butanone concentration (2 M) as 270, 260 nmol cm(-2) s(-1), respectively, higher than 240, 200 nmol cm(-2) s(-1) of Nafion-based EHP reactors. Also, the SPPESK-based EHP reactor remains 90% of initial hydrogenation rate after 4 batches, better than that of Nafion-based EHP reactors, which is only 62%. The energy efficiency of EHP separator reaches 40% under H-2/CO2 mixture feed mode, and electricity of about 0.3 kWh is consumed per Nm(3) H-2 product, being superior to energy consumption compared with alternative processes like PSA and electrolysis of water. In addition, SPPESK-based EHP exhibits better hydrogenation stability due to lower CO2 permeation than Nafion. With increasing CO2 content in H-2 feed, hydrogenation rate almost keeps constant at around 210 nmol cm(-2) s(-1) in SPPESK-based EHP reactor while decreases fast to 50 nmol cm(-2) s(-1) in Nafion/PTFE-based EHP reactor. These results show integration of gas separation with hydrogenation reactor is feasible in SPPESK-based EHP reactor. (C) 2016 Elsevier B.V. All rights reserved.
- 是否译文:
- 否