Hydrogen production in a reversible flow filtration combustion reactor

被引：4

作者：

Dmitrenko Yu.M. ^{[1
]}

Klevan P.A. ^{[1
]}

机构：

[1] A. V. Luikov Heat and Mass Transfer Institute, National Academy of Sciences of Belarus, Minsk, 220072

来源：

Journal of Engineering Physics and Thermophysics | 2011年 / 84卷 / 6期

关键词：

Conversion of methane; Filtration combustion wave; Inert porous packed bed; Partial oxidation reaction; Reversible flow reactor; Superadiabatic effect; Syngas;

D O I：

10.1007/s10891-011-0597-2

中图分类号：

学科分类号：

摘要：

The noncatalytic process of syngas production by means of partial oxidation of methane by air oxygen in a reversible flow filtration combustion reactor has been investigated experimentally. We have investigated the influence of the equivalent ratio and the specific mass flow of the fuel mixture on the composition of conversion products and the maximum temperature in the reaction zone. The optimal conditions for the process providing the most effective conversion of methane to syngas have been established. The concentration of hydrogen is maximal for the equivalent ratio ? = 2.8 and the specific flow rate γ = 1.8 kg / (m 2·s). ©2011 Springer Science+Business Media, Inc.

引用

页码：1296 / 1303

页数：7

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