期刊
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
卷 51, 期 3, 页码 1364-1375出版社
AMER CHEMICAL SOC
DOI: 10.1021/ie201452y
关键词
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资金
- U.S. DOE/NETL [DE-FG36-GO15043]
- Ohio Air Quality Development Authority [AY08-09-C21]
- National Science Foundation [CBET-0854203]
- Div Of Chem, Bioeng, Env, & Transp Sys
- Directorate For Engineering [0854203] Funding Source: National Science Foundation
A water gas shift (WGS) membrane reactor (MR) has been constructed using a MFI-type zeolite disk membrane packed with a cerium-doped ferrite catalyst. The WGS reaction was performed at high temperatures of 400-550 degrees C, and the effect of reaction pressure on the MR performance was investigated in a range from 2 to 6 atm with the permeate side swept by nitrogen at atmospheric pressure. Increasing temperature and pressure enhance both the reaction rate and the rate of H-2 membrane permeation that in turn significantly enhances the CO conversion. The equilibrium limit of CO conversion can be surpassed in the MR at high pressure and/or high temperature. It has been demonstrated in this study that membranes with moderate H-2 selectivity can be effective for enhancing CO conversion at high operation temperature and pressure with the cost of low H-2 concentration in the permeate stream. The timely removal of H-2 from the catalyst bed dramatically reduced the undesirable methane production because H-2 is a reactant for methanation reactions in the WGS system. Both the zeolite membrane and the Fe/Ce catalyst also exhibited good resistances to high concentration of H2S in WGS reactions.
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