微型反应器
甲烷
部分氧化
甲醇
催化作用
化学工程
甲烷厌氧氧化
化学
材料科学
有机化学
工程类
作者
Kelly Cohen,Justin Blanchard,Pedro Rodriguez,Kevin Kelly,James A. Dorman,Kerry M. Dooley
标识
DOI:10.1016/j.cej.2024.149049
摘要
An integrated mixer-reactor-heat exchanger microtube scalable system for the non-catalytic direct partial oxidation of methane to methanol was developed. With this module one can control the five key parameters (temperature, pressure, residence time, wall inertness and methane:air ratio) to selectively produce methanol at greater than 8 % per-pass yield (product of conversion and selectivity), under optimal conditions. For this module, these conditions were 80 bar, ∼420 °C outer wall temperature, a methane/air molar ratio of 2.9 and a residence time of 0.8 min. At lower methane/air molar ratios good yields were still possible, but at lower methanol selectivities. The walls were rendered inert using a carbiding process based on the decomposition of propane at 700 °C. While this carbide layer is not stable under long-term, repeated use, it is currently stable for about two days of operation.
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