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  3. Department Chemie- und Bioingenieurwesen
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Catalytic hydrogen purification

In page navigation: Catalytic Systems for Chemical Energy Storage
  • Research topics
    • BMBF Junior Research Group FAIR-H₂
      • Catalytic dehydrogenation of formic acid
      • Catalytic dehydration of formic acid with WGS reaction
      • Catalytic hydrogen purification
      • Techno-economic and ecological evaluation
      • Demonstration of novel hydrogen generation process
    • DME als H₂-Transportmolekül
    • LOHC for Hydrogen Storage
    • Phosphorus-containing heterogeneous catalysts
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Catalytic hydrogen purification

Lukas Popp, M.Sc.

Lukas Popp, M. Sc.

  • Email: lukas.lp.popp@fau.de

Dr.-Ing. Patrick Schühle, Akad. Rat

Dr.-Ing. Patrick Schühle, Akad. Rat

  • Phone number: +49 9131 85-67417
  • Email: patrick.schuehle@fau.de

Within the scope of this work package, the purification of the gas mixture generated thus far is being investigated, with a focus on the selective material storage and release of hydrogen from the generated mixed gas stream.

The biomass-derived formic acid obtained from the OxFA process is initially converted into mixtures consisting of H2 and varying proportions of CO2 or CO in a pre-treatment step. Since most common fuel cells are sensitive to CO poisoning and exhibit a decrease in performance or even a complete loss of performance when the hydrogen stream is diluted, a pre-treatment of the gas stream with selective separation of hydrogen from the product stream is essential.

As part of the BMBF project FAIR-H2, hydrogen purification is carried out using selective hydrogenation and subsequent dehydrogenation of a hydrogen purification liquid (HPL). Suitable catalysts for the hydrogenation step are to be identified, which do not show significant activity drops in the presence of gas impurities and are long-term stable under the existing reaction conditions. Phosphorus-modified supported Pd catalysts, which have already demonstrated stable conversion in similar applications, are being investigated. After identifying suitable catalysts and optimal operating conditions, which represent a compromise between the energy used (pressure, temperature) and high (de)hydrogenation rates, the coupling of dehydrogenation and hydrogenation, the implementation and testing of the technical cyclic operation unit will be carried out.

Addition information

Image Movie

The institute wants to thank Stephanie Sinzger and Sandra Rachinger for designing and shooting the image movie. It was part of a semester project in the fields of multimedia and communication (FH Ansbach).

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Erlangen-Nürnberg

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