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@ARTICLE{Huang:910294,
      author       = {Huang, Hong and Samsun, Remzi Can and Peters, Ralf and
                      Stolten, Detlef},
      title        = {{CFD} modeling of a membrane reactor concept for integrated
                      {CO} 2 capture and conversion},
      journal      = {Reaction chemistry $\&$ engineering},
      volume       = {7},
      number       = {12},
      issn         = {2058-9883},
      address      = {Cambridge},
      publisher    = {Royal Society of Chemistry},
      reportid     = {FZJ-2022-03729},
      pages        = {2573-2581},
      year         = {2022},
      abstract     = {Capturing CO2 and converting it into valuable products
                      represents a future direction of carbon emissions reduction.
                      The emergence of CO2-permeable membranes has opened up a
                      broad range of new opportunities for efficient CO2 capture
                      and conversion. In this context, this study develops a
                      membrane reactor concept using a ceramic–carbonate
                      dual-phase membrane for integrated CO2 capture and
                      conversion. The membrane reactor has two concentric tubes,
                      with the inner tube being for the flue gas to provide a CO2
                      source and the outer for the CO2 conversion. The catalyst is
                      coated on the membrane surface instead of being packed in
                      the reactor bed so that the permeated CO2 can be immediately
                      converted, and the CO2 permeation flux can be significantly
                      promoted in this manner. The performance of the developed
                      membrane reactor concept is evaluated based on CFD
                      simulations. The membrane reactor can achieve high CO2
                      capture rates of over $90\%$ and conversions of up to $95\%$
                      for the reaction of the reverse water gas shift. The CO
                      productivity is limited by the membrane permeation flux and
                      large reactor volume, and can be increased by compact
                      designs that increase the ratio of the membrane area to the
                      reactor volume, which are simple but effective approaches to
                      increasing CO productivity, but maintain high CO2 capture
                      rates and conversions. The developed membrane reactor
                      concept can be readily applied to any other reaction for
                      integrated CO2 capture and conversion.},
      cin          = {IEK-14 / IEK-3},
      ddc          = {540},
      cid          = {I:(DE-Juel1)IEK-14-20191129 / I:(DE-Juel1)IEK-3-20101013},
      pnm          = {1232 - Power-based Fuels and Chemicals (POF4-123) / 1111 -
                      Effective System Transformation Pathways (POF4-111) / 1112 -
                      Societally Feasible Transformation Pathways (POF4-111)},
      pid          = {G:(DE-HGF)POF4-1232 / G:(DE-HGF)POF4-1111 /
                      G:(DE-HGF)POF4-1112},
      typ          = {PUB:(DE-HGF)16},
      UT           = {WOS:000849927700001},
      doi          = {10.1039/D2RE00282E},
      url          = {https://juser.fz-juelich.de/record/910294},
}