A Microplasma Reactor for Chemical Process Intensification

被引:12
|
作者
Lindner, Peter J. [1 ]
Besser, Ronald S. [1 ]
机构
[1] Stevens Inst Technol, Dept Chem Engn & Mat Sci, Hoboken, NJ 07030 USA
基金
美国国家科学基金会;
关键词
Hydrocarbon reforming; Hydrogen; Microhollow cathode discharge; Microplasma; Reforming; METHANOL DECOMPOSITION; PARTIAL OXIDATION; FUEL-CELL; PLASMA; PRESSURE; PERFORMANCE; GAS; GENERATION; DISCHARGE; ELECTRON;
D O I
10.1002/ceat.201100684
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A novel approach to chemical process intensification based on microplasma reactor systems is presented. Microplasmas (plasmas generated in sub-mm volumes) possess a favorable reaction environment because of high densities of reactive ions, radicals, and electrons. Moreover, operation under atmospheric pressure and near-room temperature makes them convenient for implementation. Experiments utilized a microfabricated microplasma reactor to intensify the reforming of methanol into a hydrogen-rich product stream useful for energy applications such as combustion or fuel cells. A reaction model elaborates the key mechanisms and demonstrates that reaction rates in the microplasma environment surpass those of conventional plasma reactors. The outcome is that microplasma chemical processing is a viable approach for hydrocarbon reforming and merits consideration for other chemical reaction applications.
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页码:1249 / 1256
页数:8
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