Direct nonoxidative conversion of methane to hydrogen and higher hydrocarbons by dielectric barrier discharge plasma with plasma catalysis promoters

被引:23
|
作者
Chiremba, Elijah [1 ]
Zhang, Kui [1 ]
Kazak, Canan [1 ,2 ]
Akay, Galip [1 ,3 ]
机构
[1] Newcastle Univ, Sch Chem Engn & Adv Mat, Newcastle Upon Tyne NE1 7RU, Tyne & Wear, England
[2] Ondokuz Mayis Univ, Physc Dept, TR-55139 Samsun, Turkey
[3] Ondokuz Mayis Univ, Blacksea Ctr Adv Technol Res & Applicat KITAM, TR-55139 Samsun, Turkey
关键词
catalysis; fuels; hydrocarbon processing; petroleum; plasma; PROCESS INTENSIFICATION; NATURAL-GAS; PHASE-TRANSITION; DECOMPOSITION; TRANSFORMATIONS; REACTORS; FUELS;
D O I
10.1002/aic.15769
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Direct nonoxidative conversion of methane to hydrogen and hydrocarbons was achieved at atmospheric pressure and 120 degrees C using nonthermal plasma sustained by plasma catalysis promoters (PCPs). Reactors had two different electrode configurations. Methane conversion correlated well with the specific energy density (SED). Methane conversion was independent of plasma power, flow rate, electrode configuration, or the type of PCPs. Hydrogen selectivity (ca. 60%) was dependent significantly on PCP and electrode configuration. The ethane/ethylene molar ratio increased from 0 to 0.15 with increasing SED. When the SED value was below ca. 100 kJ/L, ethylene was the only C-2 hydrocarbon. These results are similar to the recently reported nonoxidative catalytic methane conversion at ca. 1000 degrees C. Therefore, these results represent process intensification in methane conversion. PCPs underwent structural and chemical changes but their performances are not affected during an 80-h experimental period. (c) 2017 American Institute of Chemical Engineers AIChE J, 63: 4418-4429, 2017
引用
收藏
页码:4418 / 4429
页数:12
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