A novel comprehensive CFD-based model for municipal solid waste incinerators based on the porous medium approach

被引:12
作者
Hoang, Quynh N. [1 ]
Van Caneghem, Jo [1 ]
Croymans, Tom [2 ]
Pittoors, Rudi [2 ]
Vanierschot, Maarten [3 ]
机构
[1] Katholieke Univ Leuven, Dept Mat Engn, Grp T Leuven Campus, Leuven, Belgium
[2] Keppel Seghers Belgium NV, Willebroek, Belgium
[3] Katholieke Univ Leuven, Dept Mech Engn, Grp T Leuven Campus, Leuven, Belgium
关键词
Municipal solid waste; Grate incinerator; Modeling; Packed bed; Porous medium; THERMAL-CONVERSION; PACKED-BED; GRATE; COMBUSTION; BIOMASS; SIMULATION; FLOW; PARTICLE; TRANSPORT; FUELS;
D O I
10.1016/j.fuel.2022.124963
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
Simulation of municipal solid waste (MSW) grate incinerators is important to enhance the energy and material recovery potential of waste to energy plants. A grate incinerator consists of the waste bed on a grate and the freeboard. While the gas combustion in the freeboard can be readily solved by available CFD codes, modeling the waste combustion has been a challenge. In this paper, a comprehensive 2D CFD-based model has been developed to simulate on-grate MSW incineration. The waste bed is modeled as a porous zone with local volume-averaged properties. The gas flow is obtained using a commercial CFD code, while the solid phase is solved using an inhouse code written in C. A new approach to characterize MSW is proposed to reduce the heterogeneity of waste while being capable of addressing its thermochemical characteristics. The model includes the effects of the bed packing on the gas flow. It also employs the mass movement approach and the walking column approach to account for the particle movement on the moving grate. A 33 MW waste incinerator under two operating conditions has been modeled, including an iterative coupling between the waste bed and the freeboard. The simulation results are compared with industrial measurements in the freeboard, and a discussion about the numerical and measurement uncertainty is provided. Given the complexity of the system, the agreement between numerical and measured results is fair. By means of the model, the trend of bed height, temperature, composition and decomposition rates along the grate were analyzed. It is shown that the primary air flows and grate speeds can be effectively controlled to ensure smooth operation of waste incinerators with varying waste compositions.
引用
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页数:13
相关论文
共 45 条
[1]   HEAT AND FLOW CHARACTERISTICS OF PACKED-BEDS [J].
ACHENBACH, E .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 1995, 10 (01) :17-27
[2]  
[Anonymous], 2016, Fluent Theory Guide
[3]   Mathematical modeling of reactants' transport and chemistry during oxidation of a millimeter-sized coal-char particle in a hot air stream [J].
Beckmann, An Marcel ;
Bibrzycki, Jakub ;
Mancini, Marco ;
Szlek, Andrzej ;
Weber, Roman .
COMBUSTION AND FLAME, 2017, 180 :2-9
[4]  
Beckmann M, 1995, 3 EUROPEAN C IND FUR, P61
[5]   Modeling thermally thick pyrolysis of wood [J].
Bryden, KM ;
Ragland, KW ;
Rutland, CJ .
BIOMASS & BIOENERGY, 2002, 22 (01) :41-53
[6]   Procedure for estimation and reporting of uncertainty due to discretization in CFD applications [J].
Celik, Ishmail B. ;
Ghia, Urmila ;
Roache, Patrick J. ;
Freitas, Christopher J. .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2008, 130 (07) :0780011-0780014
[7]   Numerical modeling of the combustion of densified wood under fixed-bed conditions [J].
Collazo, J. ;
Porteiro, J. ;
Patino, D. ;
Granada, E. .
FUEL, 2012, 93 (01) :149-159
[8]  
Cuoci A., 2007, TH MEET COMBUST, P1
[9]   Investigation of factors affecting channelling in fixed-bed solid fuel combustion using CFD [J].
Duffy, Neil T. M. ;
Eaton, John A. .
COMBUSTION AND FLAME, 2013, 160 (10) :2204-2220
[10]   CFD modelling of thermal conversion and packed bed compaction in biomass combustion [J].
Gomez, M. A. ;
Porteiro, J. ;
Patino, D. ;
Miguez, J. L. .
FUEL, 2014, 117 :716-732