STEAM REFORMING AND METHANATION EFFECTIVENESS FACTORS USING THE DUSTY GAS-MODEL UNDER INDUSTRIAL CONDITIONS

被引：42

作者：

ELNASHAIE, SSEH

ABASHAR, MEE

机构：

[1] Chemical Engineering Department, College of Engineering, King Saud University, Riyadh, 11421

来源：

CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION | 1993年 / 32卷 / 03期

关键词：

D O I：

10.1016/0255-2701(93)80014-8

中图分类号：

TE [石油、天然气工业]; TK [能源与动力工程];

学科分类号：

0807 ; 0820 ;

摘要：

A rigorous mathematical model based on the dusty gas model is developed to investigate the phenomenon of diffusion and chemical reaction in porous catalyst pellets for the steam reforming and methanation reactions under industrial conditions. Two simplified Fickian type diffusion reaction models are also developed and their results are compared with the results of the rigorous model. Parametric investigations on the single catalyst pellet are carried out using the dusty gas model as well as the simplified models in order to obtain a deeper insight into these complex catalytic gas-solid systems and to explore regions of applicability of the simplified models. The phenomenon of negative effectiveness factors is also investigated.

引用

页码：177 / 189

页数：13

共 25 条

[1]

Abashar M. E. E., 1990, THESIS U SALFORD UK

[2]

ALUBAID AS, 1987, METHANE CONVERSION S

[3] ON SHAPE FACTORS FOR IRREGULAR PARTICLES .1. THE STEADY STATE PROBLEM - DIFFUSION AND REACTION [J].