Impact of Chemistry-Turbulence Interaction Modeling Approach on the CFD Simulations of Entrained Flow Coal Gasification

被引:13
作者
Mularski, Jakub [1 ]
Modlinski, Norbert [1 ]
机构
[1] Wroclaw Univ Sci & Technol, Dept Mech Machines Devices & Energy Proc, Wybrzeze Wyspianskiego 27, PL-50370 Wroclaw, Poland
关键词
CFD; coal gasification; entrained flow reactor; PFR; PSR; turbulence; PULVERIZED COAL; NUMERICAL-SIMULATION; MILD COMBUSTION; OXIDATION; DEVOLATILIZATION; MECHANISMS; KINETICS; TEMPERATURE; PERFORMANCE; PARTICLES;
D O I
10.3390/en13236467
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
This paper examines the impact of different chemistry-turbulence interaction approaches on the accuracy of simulations of coal gasification in entrained flow reactors. Infinitely fast chemistry is compared with the eddy dissipation concept considering the influence of turbulence on chemical reactions. Additionally, ideal plug flow reactor study and perfectly stirred reactor study are carried out to estimate the accuracy of chosen simplified chemical kinetic schemes in comparison with two detailed mechanisms. The most accurate global approach and the detailed one are further implemented in the computational fluid dynamics (CFD) code. Special attention is paid to the water-gas shift reaction, which is found to have the key impact on the final gas composition. Three different reactors are examined: a pilot-scale Mitsubishi Heavy Industries reactor, a laboratory-scale reactor at Brigham Young University and a Conoco-Philips E-gas reactor. The aim of this research was to assess the impact of gas phase reaction model accuracy on simulations of the entrained flow gasification process. The investigation covers the following issues: impact of the choice of gas phase kinetic reactions mechanism as well as influence of the turbulence-chemistry interaction model. The advanced turbulence-chemistry models with the complex kinetic mechanisms showed the best agreement with the experimental data.
引用
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页数:25
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