Three dimensional model of transport and chemical late phenomena on a MSW incinerator

被引:28
作者
Ismail, T. M. [1 ]
Abd El-Salam, M. [2 ]
El-Kady, M. A. [3 ]
El-Haggar, S. M. [1 ]
机构
[1] Amer Univ Cairo, Dept Mech Engn, Cairo, Egypt
[2] Cairo Univ, Dept Basic Sci, Giza, Egypt
[3] Misr Univ Sci & Technol, Dept Mech Engn, Giza, Egypt
关键词
Waste incineration; CFD; Kinetics theory of granular flow (KTGF); Turbulent combustion; Mathematical modeling; STRAW COMBUSTION; MASS-TRANSFER; BED; SIMULATION; BIOMASS; SYSTEMS; ENERGY;
D O I
10.1016/j.ijthermalsci.2013.10.019
中图分类号
O414.1 [热力学];
学科分类号
摘要
A mathematical model was developed of the drying, volatilization, and combustion phenomena on the packed bed of solid wastes on a moving grate. Gas-solid flow and the heterogeneous chemical reactions were considered. Since experimental work in this area of study is very difficult and costly, the development of such a model is very important. The gas phase turbulence was modeled using k-epsilon turbulent model and the particle phase was modeled using kinetic theory of granular flow. The reaction rates of heterogeneous reaction were determined by Arrhenius-eddy dissipation reaction rates and the Arrhenius-diffusion reaction rate. Flow patterns, gas velocities, particle velocities, composition profiles of gas product and distributions of reaction rates were obtained. Predicted values using the present code were compared with experimental data for validation. The results showed that the predicted exit gas compositions were in good agreement with the experiments. This indicates that the numerical model presented is valid and provides a promising way to simulate the combustion of solid waste on a moving grate, which is the dominant technology for waste incineration. (C) 2013 Elsevier Masson SAS. All rights reserved.
引用
收藏
页码:139 / 157
页数:19
相关论文
共 33 条
[1]   Numerical simulation and experimental analysis of gas/solid flow systems: 1999 Fluor-Daniel Plenary lecture [J].
Arastoopour, H .
POWDER TECHNOLOGY, 2001, 119 (2-3) :59-67
[2]   Heat and mass transfer in a high temperature packed moving bed subject to an external radiative source [J].
Belghit, A ;
Daguenet, M ;
Reddy, A .
CHEMICAL ENGINEERING SCIENCE, 2000, 55 (18) :3967-3978
[3]  
Bird R. B, 2002, Transport phenomena, V2nd
[4]  
Boateng Akwasi A., 2008, ROTARY KILNS TRANSPO
[5]   Modelling wood combustion under fixed bed conditions [J].
Bruch, C ;
Peters, B ;
Nussbaumer, T .
FUEL, 2003, 82 (06) :729-738
[6]   Simulation of the fluid dynamics of a bubbling fluidized bed. Experimental validation of the two-fluid model and evaluation of a parallel multiblock solver [J].
Enwald, H ;
Peirano, E ;
Almstedt, AE ;
Leckner, B .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (03) :311-328
[7]  
Gidaspow D, 1994, AICHE J, V32, P523
[8]  
Gidaspow D., 1994, Multiphase Flow and Fluidization, P1
[9]   Mixing, modelling and measurements of incinerator bed combustion [J].
Goh, YR ;
Lim, CN ;
Zakaria, R ;
Chan, KH ;
Reynolds, G ;
Yang, YB ;
Siddall, RG ;
Nasserzadeh, V ;
Swithenbank, J .
PROCESS SAFETY AND ENVIRONMENTAL PROTECTION, 2000, 78 (B1) :21-32
[10]   A MULTIPLE-STEP OVERALL KINETIC MECHANISM FOR THE OXIDATION OF HYDROCARBONS [J].
HAUTMAN, DJ ;
DRYER, FL ;
SCHUG, KP ;
GLASSMAN, I .
COMBUSTION SCIENCE AND TECHNOLOGY, 1981, 25 (5-6) :219-235