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Hydrogen production by the steam reforming of synthetic biogas in atmospheric-pressure microwave (915 MHz) plasma

This paper is a contribution to the development of microwave plasma-based technology aimed at efficient hydrogen (H(2)) production from a so-called synthetic biogas, considered a mixture of methane (CH(4)) and carbon dioxide (CO(2)), which can contain up to 70% CH(4). In this work, we tested the per...

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Detalles Bibliográficos
Autores principales: Hrycak, Bartosz, Mizeraczyk, J., Czylkowski, D., Dors, M., Budnarowska, M., Jasiński, M.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Nature Publishing Group UK 2023
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9905514/
https://www.ncbi.nlm.nih.gov/pubmed/36750627
http://dx.doi.org/10.1038/s41598-023-29433-y
Descripción
Sumario:This paper is a contribution to the development of microwave plasma-based technology aimed at efficient hydrogen (H(2)) production from a so-called synthetic biogas, considered a mixture of methane (CH(4)) and carbon dioxide (CO(2)), which can contain up to 70% CH(4). In this work, we tested the performance of a waveguide-supplied metal cylinder-based microwave plasma source (MPS) operating at 915 MHz at atmospheric pressure as a tool for the efficient production of H(2) in the steam reforming of the synthetic biogas. The test showed that the steam reforming of the synthetic biogas could be carried out under a wide range of working parameters without soot formation and extinction of the microwave discharge. We found that there is a minimal H(2)O(steam) consumption rate for a given CH(4) input volume content, which ensures stable operation of the MPS (no soot). The experiments did not show that increasing the amount of H(2)O(steam) rate above the minimal value for a given CH(4) input volume content results in an increase in the H(2) production rate, energy yield, CH(4) conversion degree, and H(2) output concentration. To describe the MPS performance, which also takes into account a factor of the utilization of the CH(4) feedstock, we introduced a new parameter, called an energy–CH(4) feedstock consumption yield. The best results in terms of the H(2) production rate, the energy yield, and the CH(4) conversion degree were 239 g[H(2)]/h 36.8 g[H(2)]/kWh, and 74.3%, respectively. This shows that the application of the steam reforming, instead of the dry reforming, resulted in a 1.5-fold increase of the H(2) production rate and the corresponding energy yield.