合成气
甲烷
甲醇
化学
醋酸
等离子管
化学工程
碳纤维
体积流量
材料科学
有机化学
催化作用
等离子体
热力学
工程类
物理
量子力学
复合数
复合材料
作者
Kaiyi Wang,Hao Zhang,J Ananthanarasimhan,Lakshminarayana Rao,Xiaoqing Lin,Jieying Wan,Yanhui Long,Ming Gao,Weitao Wang,Xin Tu,Xiaodong Li,Qunxing Huang
标识
DOI:10.1016/j.fuproc.2023.107826
摘要
An atmospheric plasmatron reactor with two-stage inlets was developed for bi-reforming of methane (CO2/CH4/H2O) to produce syngas (H2 + CO) and value-added liquid products. The influence of CH4 inlet position, gas flow rate and reactant composition were investigated. The results showed that the two-stage-inlet design allows for a wide range of operational conditions in terms of the CO2/CH4/H2O ratio (2–7:0–6:0–3) and total flow rate (4.5-11 L/min). A CO2 and CH4 conversion of 24% and 12.9%, respectively, was obtained at flow rates of up to 7-8 L/min, with no observable carbon deposit formed. A closer injection of CH4 to the core plasma area was more beneficial for both reactant conversion and syngas selectivity. Interestingly, value-added oxygenated products (e.g., methanol, ethanol, acetic acid) were produced simultaneously, offering a promising power-to-liquid (PtL) route. In particular, the direct synthesis of acetic acid from CH4 and CO2 was achieved, which is infeasible in thermocatalytic processes. A small addition of H2O (14.3%) favorably enhanced the formation of acetic acid by up to 160%, likely due to the improved generation of CH3 and COOH intermediates. Overall, this work offers a promising route for syngas and oxygenated products generation in a scalable plasmatron reactor with high operational adaptability.
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