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Plasma catalytic reforming of methane
Journal article   Open access   Peer reviewed

Plasma catalytic reforming of methane

L Bromberg, D.R Cohn, A Rabinovich and N Alexeev
International journal of hydrogen energy, v 24(12), pp 1131-1137
01 Dec 1999
url
https://www.osti.gov/biblio/305623View

Abstract

Thermal plasma technology can be efficiently used in the production of hydrogen and hydrogen-rich gases from methane and a variety of fuels. This article describes progress in plasma reforming experiments and calculations of high temperature conversion of methane using heterogeneous processes. The thermal plasma is a highly energetic state of matter that is characterized by extremely high temperatures (several thousand degrees Celsius), and a high degree of dissociation and a substantial degree of ionization. The high temperatures accelerate the reactions involved in the reforming process. Hydrogen-rich gas (40% H 2, 17% CO 2 and 33% N 2, for partial oxidation/water shifting) can be efficiently made in compact plasma reformers. Experiments have been carried out in a small device (2–3 kW) and without the use of efficient heat regeneration. For partial oxidation/water shifting, it was determined that the specific energy consumption in the plasma reforming processes is 16 MJ/kg H 2 with high conversion efficiencies. Larger plasmatrons, better reactor thermal insulation, efficient heat regeneration and improved plasma catalysis could also play a major role in specific energy consumption reduction and increasing the methane conversion. A system has been demonstrated for hydrogen production with low CO content (∼1.5%) with power densities of ∼30 kW (H 2 HHV)/l of reactor, or ∼10 m 3/h H 2 per liter of reactor. Power density should further increase with increased power and improved design.

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Collaboration types
Domestic collaboration
International collaboration
Web of Science research areas
Chemistry, Physical
Electrochemistry
Energy & Fuels
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