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Abstract

The work concerned the introduction of simplifications in a one-dimensional mathematical model of a chemical reactor. Fecralloy foam with a pore density of 16 PPC (pores per centimetre) was used as catalyst support. The analysed process was the combustion of methane with a typical concentration found in the ventilation air of hard coal mines. The process was carried out using a palladium catalyst.
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Authors and Affiliations

Mateusz Korpyś
1
ORCID: ORCID
Marzena Iwaniszyn
1
ORCID: ORCID
Katarzyna Sindera
1
ORCID: ORCID
Andrzej Kołodziej
1
ORCID: ORCID
Adam Rotkegel
1
ORCID: ORCID
Joanna Profic-Paczkowska
2
ORCID: ORCID
Maciej Sitarz
3
ORCID: ORCID
Anna Gancarczyk
1
ORCID: ORCID

  1. Polish Academy of Sciences, Institute of Chemical Engineering, Bałtycka 5, 44-100 Gliwice, Poland
  2. Jagiellonian University, Faculty of Chemistry, Gronostajowa 2, 30-387 Kraków, Poland
  3. AGH University of Science and Technology, Faculty of Materials Science and Ceramics, Mickiewicza 30, 30-059 Kraków, Poland
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Abstract

In this review, research carried out on sorption-enhanced steam methane reforming (SESMR) process is presented and discussed. The reactor types employed to carry out this process, fixed packed bed and fluidized bed reactors, are characterized as well as their main operating conditions indicated. Also the concepts developed and investigations performed by the main research groups involved in the subject are summarized. Next the catalysts and CO2 sorbents developed to carry out SE-SMR are characterized and the relationships describing the reaction and sorption kinetics are collected. A general approach to model the process is presented as well as results obtained for a calculation example, which demonstrate the main properties of SE-SMR.

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Authors and Affiliations

Robert Cherbański
Eugeniusz Molga

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