CFD predictions for cement kilns including flame modelling, heat transfer and clinker chemistry

被引:101
作者
Mastorakos, E
Massias, A
Tsakiroglou, CD
Goussis, DA
Burganos, VN
Payatakes, AC
机构
[1] Fdn Res & Technol, Inst Chem Engn & High Temp Chem Proc, Patras 26500, Greece
[2] Univ Patras, Dept Mech Engn, GR-26110 Patras, Greece
[3] Univ Patras, Dept Chem Engn, GR-26110 Patras, Greece
关键词
industrial CFD; rotary kilns; clinker formation; radiative heat transfer;
D O I
10.1016/S0307-904X(98)10053-7
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
Clinker formation in coal-fired rotary cement kilns under realistic operation conditions has been modelled with a commercial axisymmetric CFD code for the gaseous phase including a Monte Carlo method for radiation, a finite-volume code for the energy equation in the kiln walls, and a novel code for the species and energy conservation equations, including chemical reactions, for the clinker. An iterative procedure between the predictions for the temperature held of the gaseous phase, the radiative heat flux to the walls, and the kiln and clinker temperature is used to predict the distribution of the inner wall temperature explicitly, including the calculation of heat flow to the clinker. It was found that the dominant mode of heat transfer between the gas and the kiln walls is by radiation and that the heat lost through the refractories to the environment is about 10% of the heat input and a further 40% is used for charge heating and clinker formation. The predictions are consistent with trends based on experience and limited measurements in a full-scale cement kiln. (C) 1999 Elsevier Science Inc. All rights reserved.
引用
收藏
页码:55 / 76
页数:22
相关论文
共 18 条
[1]  
Avgeropoulos T., 1993, ENERGY EFFICIENCY PR, P767, DOI 10.1007/978-94-011-1454-7_68
[2]   A HEAT-TRANSFER MODEL FOR THE ROTARY KILN .2. DEVELOPMENT OF THE CROSS-SECTION MODEL [J].
BARR, PV ;
BRIMACOMBE, JK ;
WATKINSON, AP .
METALLURGICAL TRANSACTIONS B-PROCESS METALLURGY, 1989, 20 (03) :403-419
[3]   A thermal model for the rotary kiln including heat transfer within the bed [J].
Boateng, AA ;
Barr, PV .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1996, 39 (10) :2131-&
[4]  
Carvalho M.G., 1995, COMBUSTION TECHNOLOG, P146
[5]  
*CFDS, FLOW 3D US MAN
[6]  
FRISCH V, 1983, ZEM-KALK-GIPS, V36, P549
[7]  
JOHANSEN V, 1993, RAMBOLL B, V42
[8]  
JOHANSEN V, 1989, S CEM MAN CHEM AN NO
[9]  
JOHANSEN V, 1993, RAMBOLL B, V41
[10]  
LOCKWOOD FC, 1994, 25 S INT COMB COMB I, P503