Production of synthesis gas by conversion of methane in a steam-carbon dioxide plasma

Experimental setup and results of methane conversion in a steam-carbon dioxide plasma are briefly described. Mass-flow rate of CH 4 was varied from 2.5 to 3.7 g/s while mass-flow rates of H 2 O of ∼3 g/s and CO 2 of ∼3 g/s were maintained constant. The energy consumption was 29–42 MJ per 1 kg of CH...

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Veröffentlicht in:Technical physics letters 2014-09, Vol.40 (9), p.725-729
Hauptverfasser: Rutberg, Ph. G., Bratsev, A. N., Kuznetsov, V. A., Nakonechnyi, G. V., Nikonov, A. V., Popov, V. E., Popov, S. D., Serba, E. O., Subbotin, D. I., Surov, A. V.
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container_end_page 729
container_issue 9
container_start_page 725
container_title Technical physics letters
container_volume 40
creator Rutberg, Ph. G.
Bratsev, A. N.
Kuznetsov, V. A.
Nakonechnyi, G. V.
Nikonov, A. V.
Popov, V. E.
Popov, S. D.
Serba, E. O.
Subbotin, D. I.
Surov, A. V.
description Experimental setup and results of methane conversion in a steam-carbon dioxide plasma are briefly described. Mass-flow rate of CH 4 was varied from 2.5 to 3.7 g/s while mass-flow rates of H 2 O of ∼3 g/s and CO 2 of ∼3 g/s were maintained constant. The energy consumption was 29–42 MJ per 1 kg of CH 4 . The H 2 /CO ratio in the produced synthesis gas was 2.2–2.4. The conversion rate of CH 4 was 90.8–99.8%. The content of H 2 and CO in the synthesis gas was ∼95%.
doi_str_mv 10.1134/S1063785014090132
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title Production of synthesis gas by conversion of methane in a steam-carbon dioxide plasma
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