Production of synthesis gas by steam- and CO2-reforming of natural gas

被引：76

作者：

Froment, GF ^{[1
]}

机构：

[1] Texas A&M Univ, Dept Chem Engn, College Stn, TX 77843 USA

来源：

JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL | 2000年 / 163卷 / 1-2期

关键词：

synthesis gas; steam- and CO2-reforming (kinetics; coke formation; simulation);

D O I：

10.1016/S1381-1169(00)00407-6

中图分类号：

O64 [物理化学（理论化学）、化学物理学];

学科分类号：

070304 ; 081704 ;

摘要：

The simulation of a steam/CO2 reformer is based upon detailed intrinsic kinetics of reforming, including those of carbon deposition and -gasification. The internal diffusion limitations are accounted for through the modeling. The influence of the steam/methane and the CO2/methane ratio on the synthesis gas production and composition and on the net rate of carbon formation is illustrated. (C) 2000 Elsevier Science B.V. All rights reserved.

引用

页码：147 / 156

页数：10

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