Physical-Mathematical Model for Fixed-Bed Solid Fuel Gasification Process Simulation

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Abstract

Phycial-mathmatical model for fixed-bed coal gasification process simulation is proposed. The heterogeneous carbon oxidation chemical reactions were simulated via Arrhenius equation while homogeneous reactions in gas phase were calculated using Gibbs free energy minimization procedure. The syngas component concentration field and fuel conversion distribution as well as syngas final temperature and composition were defined for fixed bed gasification of T-grade coal of Kuznetskiy deposit. The optimal fuel residence time and gasifyer specific productivity were defined. The prevail reactions in oxidizing and reduction zones together with its height were defined.

Original languageEnglish
Article number01011
JournalMATEC Web of Conferences
Volume91
DOIs
Publication statusPublished - 20 Dec 2016

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Gasification
Mathematical models
Coal
Coal gasification
Gibbs free energy
Chemical reactions
Carbon
Deposits
Gases
Productivity
Oxidation
Chemical analysis
Temperature

ASJC Scopus subject areas

  • Chemistry(all)
  • Engineering(all)
  • Materials Science(all)

Cite this

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abstract = "Phycial-mathmatical model for fixed-bed coal gasification process simulation is proposed. The heterogeneous carbon oxidation chemical reactions were simulated via Arrhenius equation while homogeneous reactions in gas phase were calculated using Gibbs free energy minimization procedure. The syngas component concentration field and fuel conversion distribution as well as syngas final temperature and composition were defined for fixed bed gasification of T-grade coal of Kuznetskiy deposit. The optimal fuel residence time and gasifyer specific productivity were defined. The prevail reactions in oxidizing and reduction zones together with its height were defined.",
author = "Slyusarskiy, {Konstantin Vitalievich} and Korotkikh, {Alexander G.} and Sorokin, {Ivan V.}",
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