Non-Catalytic direct partial oxidation of methane to methanol in a Wall-Coated microreactor

被引:3
作者
Cohen, Kelly [1 ]
Blanchard, Justin [1 ]
Rodriguez, Paul [2 ]
Kelly, Kevin [2 ]
Dorman, James A. [1 ]
Dooley, Kerry M. [1 ]
机构
[1] Louisiana State Univ, Dept Chem Engn, Baton Rouge, LA 70803 USA
[2] Mezzo Technol, 10246 Mammoth Ave, Baton Rouge, LA 70814 USA
关键词
Methane to methanol; Microreactor; Carbiding tubes; CATALYTIC CONVERSION; SELECTIVE OXIDATION; CHEMICALS; SINGLE; GAS; PRESSURE; ROUTES;
D O I
10.1016/j.cej.2024.149049
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
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, similar to 420 degrees 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 degrees C. While this carbide layer is not stable under long-term, repeated use, it is currently stable for about two days of operation.
引用
收藏
页数:10
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