2013
DOI: 10.1021/ef302014n
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Zeolite Membrane Reactor for High-Temperature Water-Gas Shift Reaction: Effects of Membrane Properties and Operating Conditions

Abstract: Modified MFI-type zeolite membranes were investigated as high-temperature water-gas shift (WGS) membrane reactors (MRs) in combination with a nanocrystalline Fe/Ce WGS catalyst. The effects of the MR operating conditions and the membrane separation performance on the CO conversion (χCO) were studied experimentally and by calculations using a simple one-dimensional plug-flow reactor (PFR) model. The experimental results showed that, at high temperatures (e.g., >500 °C), the zeolite MR with moderate H2 selectivi… Show more

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Cited by 71 publications
(39 citation statements)
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References 21 publications
(55 reference statements)
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“…Particularly, it was emphasized that the prepared MFI membrane showed good resistance against H2S and was stable at the applied high temperatures and pressures.Recently, the same authors applied the model of one-dimensional plug-flow reactors (PFR) and related the results with data from MFI-type zeolite membranes. Simulations proved the potential of the membrane reactor, combining a modified MFI membrane and cerium-doped ferrite catalysts, to reach CO conversion above 99.5% at 550 °C and ~50 atm at a ratio of H2O/CO ~5.0 [155]. Similarly, Lin et al [156] evaluated the performance of ZSM-5/silicalite bilayer membranes packed with Fe-Cr-Cu catalysts combining experimental and theoretical studies and defined the optimal conditions under which CO conversion of over 95% together with H2 recovery of over 90% could be achieved.…”
Section: Hydrogen Permeation In Water Gas Shift Reactionmentioning
confidence: 86%
“…Particularly, it was emphasized that the prepared MFI membrane showed good resistance against H2S and was stable at the applied high temperatures and pressures.Recently, the same authors applied the model of one-dimensional plug-flow reactors (PFR) and related the results with data from MFI-type zeolite membranes. Simulations proved the potential of the membrane reactor, combining a modified MFI membrane and cerium-doped ferrite catalysts, to reach CO conversion above 99.5% at 550 °C and ~50 atm at a ratio of H2O/CO ~5.0 [155]. Similarly, Lin et al [156] evaluated the performance of ZSM-5/silicalite bilayer membranes packed with Fe-Cr-Cu catalysts combining experimental and theoretical studies and defined the optimal conditions under which CO conversion of over 95% together with H2 recovery of over 90% could be achieved.…”
Section: Hydrogen Permeation In Water Gas Shift Reactionmentioning
confidence: 86%
“…This membrane reactor showed good thermal stability during long-term operation at high temperature and in a humid environment [106]. At almost the same time, Dong et al reported similar work using a modified MFI membrane for a membrane reactor in high-temperature WGSR [108], while Xu et al used a modified ZSM-5 membrane-based reactor for low-temperature WGSR [109]. Table 5.…”
Section: Gas Kinetic Diameter (å)mentioning
confidence: 93%
“…Chemical vapour decomposition (CVD) and chemical cracking decomposition (CCD) are widely used to improve the performance of the ZSM-5 membrane, as these modification methods can result in an impressive improvement in H 2 /CO 2 selectivity [106][107][108][109]. Lin et al post-treated ZSM-5 membranes in two steps.…”
Section: Gas Kinetic Diameter (å)mentioning
confidence: 99%
“…Moreover, the product should have high purity and the reaction carried away in milder condition than traditional WGS reaction reactor [58,65,34]. At high temperature, transport of small molecules is governed by gaseous diffusion leads to low H 2 selectivity, while the other gases will permeate simultaneously [66-68, 63, 69].…”
Section: Optimization Of Zeolite Based Membrane In Hydrogen Productiomentioning
confidence: 99%