Journal
IEEE TRANSACTIONS ON PLASMA SCIENCE
Volume 42, Issue 12, Pages 3896-3900Publisher
IEEE-INST ELECTRICAL ELECTRONICS ENGINEERS INC
DOI: 10.1109/TPS.2014.2353042
Keywords
Conversion; gas-to-liquid; methane; natural gas; plasma; reformer; reforming; syngas
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Development and modeling have been performed for different schemes for a plasma-assisted, catalyst-free process for natural gas conversion into synthesis gas, at pressures up to 3 MPa. Two oxidizers, oxygen with different purity and oxygen-steam blends, have been used to obtain a H-2-to-CO ratio over 1.8. This ratio qualifies the synthesis gas as an appropriate feedstock for further direct liquefaction via Fisher-Tropsch processing. The results obtained can be used for development of the catalyst-free natural gas reformers for small scale, gas-to-liquid technologies.
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