A new char combustion kinetic model 1. Formulation

被引:42
作者
Barranco, Richelieu [1 ]
Rojas, Andres [2 ]
Barraza, Juan [3 ]
Lester, Edward [1 ]
机构
[1] Univ Nottingham, Dept Chem & Environm Engn, Nottingham NG7 2RD, England
[2] Univ Nacl Colombia Palmira, Dept Ingn, Palmira, Colombia
[3] Univ Valle, Escuela Ingn Quim, Grp Ciencia & Tecnol Carbon, Cali, Colombia
关键词
Char combustion model; Intrinsic reactivity; Kinetic coefficient; DROP-TUBE FURNACE; REACTIVE FUSIBLE INERTINITE; PULVERIZED FUEL COMBUSTION; COAL COMBUSTION; BURNOUT; MACERALS; NITROGEN; RELEASE; RATES; RANK;
D O I
10.1016/j.fuel.2009.02.005
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
080707 [能源环境工程]; 082001 [油气井工程];
摘要
This paper describes the development and formulation of a novel char combustion kinetic model for pulverised coal. The chemical reaction rate was considered as a function of coal intrinsic reactivity and fuel mass for a global reaction order n. The equation for char combustion reaction rate was devised by dimensional analysis using the Rayleigh method. It shows the dependency of chemical reactivity on coal parameters, such as maceral and mineral composition; char parameters, such as specify surface area and apparent density; devolatilisation time; temperature; and activation energy. The char combustion reaction rate equation developed, unlike most models, is dimensionally homogenous and is expressed by three dimensionless numbers which have physical chemical meaning. The model also exhibit similarities with transport phenomena models described by dimensionless numbers. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2335 / 2339
页数:5
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