Three Stage Equilibrium Model for Coal Gasification in Entrained Flow Gasifiers Based on Aspen Plus

孔祥东; 钟伟民; 杜文莉; 钱锋

doi:10.1016/S1004-9541(13)60444-9

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Three Stage Equilibrium Model for Coal Gasification in Entrained Flow Gasifiers Based on Aspen Plus

过程系统工程与过程安全 | Updated：2026-01-06

- Three Stage Equilibrium Model for Coal Gasification in Entrained Flow Gasifiers Based on Aspen Plus
- Three Stage Equilibrium Model for Coal Gasification in Entrained Flow Gasifiers Based on Aspen Plus
- 中国化学工程学报（英文版） 2013年21卷第1期页码：79-841004-954160444-9
- Affiliations：
  
  2 Automation Institute, East China University of Science and Technology,Shanghai,China,200237
- Author bio：
- Funds：
- DOI：10.1016/S1004-9541(13)60444-9
  中图分类号：
- 纸质出版：2013
- Accepted：
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孔祥东, 钟伟民, 杜文莉, 等. Three Stage Equilibrium Model for Coal Gasification in Entrained Flow Gasifiers Based on Aspen Plus[J]. 中国化学工程学报（英文版）, 2013,21(1):79-841004-954160444-9.

KONG Xiangdong, ZHONG Weimin, DU Wenli, QIAN Feng . Three Stage Equilibrium Model for Coal Gasification in Entrained Flow Gasifiers Based on Aspen Plus[J]. Chin.J.Chem.Eng., 2013, 21(1): 79-84.
孔祥东, 钟伟民, 杜文莉, 等. Three Stage Equilibrium Model for Coal Gasification in Entrained Flow Gasifiers Based on Aspen Plus[J]. 中国化学工程学报（英文版）, 2013,21(1):79-841004-954160444-9. DOI： 10.1016/S1004-9541(13)60444-9.

KONG Xiangdong, ZHONG Weimin, DU Wenli, QIAN Feng . Three Stage Equilibrium Model for Coal Gasification in Entrained Flow Gasifiers Based on Aspen Plus[J]. Chin.J.Chem.Eng., 2013, 21(1): 79-84. DOI： 10.1016/S1004-9541(13)60444-9.

摘要

Abstract

A three stage equilibrium model is developed for coal gasification in the Texaco type coal gasifiers based on Aspen Plus to calculate the composition of product gas

carbon conversion

and gasification temperature. The model is divided into three stages including pyrolysis and combustion stage

char gas reaction stage

and gas phase reaction stage. Part of the water produced in the pyrolysis and combustion stage is assumed to be involved in the second stage to react with the unburned carbon. Carbon conversion is then estimated in the second stage by steam participation ratio expressed as a function of temperature. And the gas product compositions are calculated from gas phase reactions in the third stage. The simulation results are consistent with published experimental data.

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