Longevity Demonstration of Methane to C2 via a Nonthermal Plasma Microreactor

被引:0
|
作者
Reddick, Ian [1 ]
Mohamed, Omar [1 ]
Pommerenck, Justin [1 ]
Coblyn, Matthew [1 ]
Yokochi, Alexandre [2 ]
Von Jouanne, Annette [2 ]
Jovanovic, Goran N. [1 ]
AuYeung, Nick [1 ]
机构
[1] Oregon State Univ, Sch Chem Biol & Environm Engn, Corvallis, OR 97331 USA
[2] Baylor Univ, Sch Engn & Comp, Sci, Waco, TX 76798 USA
来源
ACS OMEGA | 2023年 / 8卷 / 08期
关键词
CATALYTIC REACTOR; PARTIAL OXIDATION; CARBON-DIOXIDE; CONVERSION; CORONA; ETHYLENE; SYNGAS; AIR;
D O I
10.1021/acsomega.2c07265
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
Hydrocarbon processing using plasmas has tremendous potential, yet there still exist many uncertainties pertaining to practical operation over long durations. Previously, it has been demonstrated that a nonthermal plasma operating in a DC glow regime can transform methane into C2 species (acetylene, ethylene, ethane) in a microreactor. Using a DC glow regime in a microchannel reactor allows for lower power consumption, at the expense of greater consequence of fouling. Since biogas can be a source of methane, a longevity study was undertaken to understand how the microreactor system would change over time with a feed mixture of simulated biogas (CO2, CH4) and air. Two different biogas mixtures were used, one of which contained 300 ppm H2S, while the other had no H2S. Potential difficulties observed from previous experiments included carbon deposition on the electrodes, which could interfere with the electrical characteristics of the plasma discharge as well as material deposition in the microchannel, which could affect gas flow. It was found that raising the temperature of the system to 120 degrees C helped prevent hydrocarbon deposition in the reactor. Purging the reactor periodically with dry air was also found to have positive effects as it removed carbon buildup on the electrodes themselves. Successful operation over a 50 h time period without any significant deterioration was demonstrated.
引用
收藏
页码:7657 / 7665
页数:9
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