Comparison of CFD simulations to experiment under methane steam reforming reacting conditions

被引:77
作者
Behnam, Mohsen [1 ]
Dixon, Anthony G. [1 ]
Wright, Paul M. [2 ]
Nijemeisland, Michiel [2 ]
Stitt, E. Hugh [2 ]
机构
[1] Worcester Polytech Inst, Dept Chem Engn, Worcester, MA 01609 USA
[2] Johnson Matthey, Billingham TS23 1LB, Cleveland, England
基金
美国国家科学基金会;
关键词
Methane steam reforming; Computational fluid dynamics; Chemical reaction simulation; Multiscale analysis; Experimental validation; COMPUTATIONAL FLUID-DYNAMICS; FIXED-BED REACTORS; HEAT-TRANSFER; PRESSURE-DROP; EXPERIMENTAL VALIDATION; CATALYST PARTICLES; DIAMETER RATIO; PACKED-BED; FLOW-FIELD; SMALL TUBE;
D O I
10.1016/j.cej.2012.07.038
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The highly endothermic commercial methane steam reforming (MSR) reaction was studied experimentally in a single-pellet-string fixed bed reactor. The temperatures inside the active catalyst particles, the temperatures on the outer surfaces of selected pellets and the exit gas composition were measured. The MSR reaction showed strong effects on the temperature profile along the reactor, causing it to decrease initially. A computational fluid dynamics (CFD) model was used to predict temperature and species profiles under the experimental MSR reaction conditions. Comparison of CFD and experimental data showed very good qualitative as well as quantitative agreement for temperature inside catalyst particles at different inlet gas temperatures, and for the temperature drop from outside to inside the pellets due to the reaction heat sink. Trends in methane conversion were also well-represented by the CFD simulation. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:690 / 700
页数:11
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