天然气化工2017，Vol.42Issue(5)：67-76,83,11.
甲烷蒸汽重整制氢反应器的模拟与分析
Simulation and analysis of reactor for methane steam reforming
雷晓健 1王元华 1张英 2厉勇 2徐宏1
作者信息
- 1. 华东理工大学,上海 200237
- 2. 中石化抚顺石化研究院,辽宁 抚顺 113001
- 折叠
摘要
Abstract
Base on the industrial top burning type furnace, a one-dimensional pseudo-homogeneous mathematical model of hydrogen production reactor was established. The model was calculated by the method of Runge-Kutta with Matlab. The concentration of each component and temperature distributionin of the reactor were analyzed. The influence of process conditions of methane steam reforming (MSR) on methane conversion and outlet temperature were studied. The results show that the methane conversion and outlet temperature increase with increasing steam-methane ratio, furnace temperature and inlet temperature, and decreasing space velocity. The effect of inlet pressure was not significant. The results will be helpful for optimization of process conditions of MSR.关键词
甲烷蒸汽重整/氢/反应器/数学模拟/优化设计Key words
methane-steam reforming/hydrogen/reactor/mathematical simulation/optimal design分类
化学化工引用本文复制引用
雷晓健,王元华,张英,厉勇,徐宏..甲烷蒸汽重整制氢反应器的模拟与分析[J].天然气化工,2017,42(5):67-76,83,11.
