Single-step hydrogen production from NH <sub>3</sub> , CH <sub>4</sub> , and biogas in stacked proton ceramic reactors

  • Daniel Clark
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Harald Malerød-Fjeld
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Michael Budd
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Irene Yuste-Tirados
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Dustin Beeaff
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Simen Aamodt
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Kevin Nguyen
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Luca Ansaloni
    Department of Sustainable Energy Technology, SINTEF Industry, 0314 Oslo, Norway.
  • Thijs Peters
    Department of Sustainable Energy Technology, SINTEF Industry, 0314 Oslo, Norway.
  • Per K. Vestre
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Dimitrios K. Pappas
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • María I. Valls
    Instituto de Tecnologia Química, Consejo Superior de Investigaciones Científicas-Universitat Politècnica de València, 46022 Valencia, Spain.
  • Sonia Remiro-Buenamañana
    Instituto de Tecnologia Química, Consejo Superior de Investigaciones Científicas-Universitat Politècnica de València, 46022 Valencia, Spain.
  • Truls Norby
    Department of Chemistry, Centre for Materials Science and Nanotechnology, University of Oslo, 0316 Oslo, Norway.
  • Tor S. Bjørheim
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.
  • Jose M. Serra
    Instituto de Tecnologia Química, Consejo Superior de Investigaciones Científicas-Universitat Politècnica de València, 46022 Valencia, Spain.
  • Christian Kjølseth
    CoorsTek Membrane Sciences AS, 0349 Oslo, Norway.

抄録

<jats:p>Proton ceramic reactors offer efficient extraction of hydrogen from ammonia, methane, and biogas by coupling endothermic reforming reactions with heat from electrochemical gas separation and compression. Preserving this efficiency in scale-up from cell to stack level poses challenges to the distribution of heat and gas flows and electric current throughout a robust functional design. Here, we demonstrate a 36-cell well-balanced reactor stack enabled by a new interconnect that achieves complete conversion of methane with more than 99% recovery to pressurized hydrogen, leaving a concentrated stream of carbon dioxide. Comparable cell performance was also achieved with ammonia, and the operation was confirmed at pressures exceeding 140 bars. The stacking of proton ceramic reactors into practical thermo-electrochemical devices demonstrates their potential in efficient hydrogen production.</jats:p>

収録刊行物

  • Science

    Science 376 (6591), 390-393, 2022-04-22

    American Association for the Advancement of Science (AAAS)

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