Thermally autonomous microchannel reactor to produce hydrogen in steam reforming of methanol

被引:53
作者
Gribovskiy, A. G. [1 ,2 ]
Makarshin, L. L. [1 ]
Andreev, D. V. [1 ]
Klenov, O. P. [1 ]
Parmon, V. N. [1 ,2 ]
机构
[1] Boreskov Inst Catalysis, Novosibirsk 630090, Russia
[2] Novosibirsk State Univ, Novosibirsk 630090, Russia
关键词
Catalyst; Catalytic multichannel reactor; Methanol steam reforming; Hydrogen production; Catalytic methanol combustion; Overall efficiency; CATALYTIC COMBUSTION; INTEGRATED METHANOL; MICROREACTORS; PERFORMANCE; OXIDATION;
D O I
10.1016/j.cej.2015.03.036
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A thermally autonomous microchannel reactor (AMR) for production of hydrogen in the steam reforming of methanol has been designed and tested. The reactor consists of an evaporator, a stirrer, and a microchannel catalytic unit (MCU) containing a catalyst deposited in short channels (10 mm in length and 1 mm in diameter). The MCU design makes it possible to conduct simultaneously endothermic and exothermic processes. The heat produced in the total oxidation of methanol is consumed for the heating of the reaction mixture and maintaining the steam reforming of methanol. A CFD simulation of hydrodynamic and thermal processes based on chemical reactions proceeding in the MCU channels showed that a temperature gradient in the reaction zone does not exceed 2 degrees C. The simulation results agree fairly well with experimental data. A maximum efficiency of the AMR is achieved at temperatures 260-290 degrees C and at a feed rate of the water-methanol mixture F-MeOH(0) = 10 mmol/min. Under these conditions, the overall efficiency of AMR is maximal and equals 57%, and the hydrogen production rate achieves 30.6 L/h at the methanol conversion of 82%. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:130 / 137
页数:8
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