Multiscale Coupling Framework for Modeling of Large-Size Biomass Particle Gasification in Fluidized Beds

被引:7
|
作者
Jin, Guodong [1 ]
机构
[1] Chinese Acad Sci, Inst Mech, LNM, Beijing 100190, Peoples R China
关键词
WOOD GASIFICATION; NUMERICAL-MODEL; SIMULATION; FLOW; CHAR; COMBUSTION; REACTOR;
D O I
10.1021/ie400420p
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper is devoted to addressing a multiscale coupling framework for modeling of large-size biomass particle gasification in fluidized beds, where the large diffusions due to the temperature and concentration gradients in large-size particles strongly affect gasification process. Directly incorporating a single particle model (SPM) into a conventional fluidized-bed model tremendously increases the computational cost. In this paper, we propose a loose coupling framework between the SPM and the discrete element method (DEM)-Eulerian continuum model. The SPM is based on detailed reaction mechanisms and has been validated against experimental results. The rationality of the coupling is based on the observations from the SPM that the temperature is the dominating factor and the surrounding gas velocity is a secondary one to the gasification. For this purpose, we use sand particles as thermal carrier to keep the surrounding temperature statistically stable. We then simulated the gasification of beech wood particles mixed with sand particles in a bubbling fluidized bed. The entrainment and mixing of wood particles with sand particles can be observed and the particle distribution and the composition of gas phase can be obtained. The proposed method provides a potential way to account for the gasification process of large-size biomass particles in fluidized beds.
引用
收藏
页码:11344 / 11353
页数:10
相关论文
共 50 条
  • [41] Kinetic modeling of steam gasification of cokes in fluidized beds. II. Modeling the hydrodynamic behavior of fluidized beds during the chemical reaction
    Modelisation cinetique de la gaseification a la vapeur d'eau de cokes en lit fluidise. II. Modelisation du comportement hydrodynamique du lit fluidise au cours de la reaction
    Le Bolay, N., 1600, (41):
  • [42] Coupling DAEM and CFD for simulating biomass fast pyrolysis in fluidized beds
    Xiong, Qingang (xiongq@ornl.gov), 1600, Elsevier B.V., Netherlands (117):
  • [43] Coupling DAEM and CFD for simulating biomass fast pyrolysis in fluidized beds
    Xiong, Qingang
    Zhang, Jingchao
    Xu, Fei
    Wiggins, Gavin
    Daw, C. Stuart
    JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2016, 117 : 176 - 181
  • [44] Effect of particle size on solids mixing in bubbling fluidized beds
    Shen, LH
    Zhang, MY
    POWDER TECHNOLOGY, 1998, 97 (02) : 170 - 177
  • [45] PARTICLE-SIZE SEGREGATION IN BAFFLED FLUIDIZED-BEDS
    NAVEH, E
    RESNICK, W
    TRANSACTIONS OF THE INSTITUTION OF CHEMICAL ENGINEERS, 1974, 52 (01): : 58 - 66
  • [46] Random Walk Model for Biomass Particle Mixing in Bubbling Fluidized Beds
    Daw, C. Stuart
    Halow, Jack
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (41) : 15836 - 15844
  • [47] 2-D CFD modeling for steam gasification of a large biomass char particle
    Kamila, Biswajit
    Mandal, Arindam
    Prabhakar, Ashok
    Sadhukhan, Anup Kumar
    Gupta, Parthapratim
    APPLIED THERMAL ENGINEERING, 2025, 271
  • [48] Empirical and chemical equilibrium modelling for prediction of biomass gasification products in bubbling fluidized beds
    Pio, D. T.
    Tarelho, L. A. C.
    ENERGY, 2020, 202 (202)
  • [49] Effect of bed material density on the performance of steam gasification of biomass in bubbling fluidized beds
    Soria-Verdugo, Antonio
    Von Berg, Lukas
    Serrano, Daniel
    Hochenauer, Christoph
    Scharler, Robert
    Anca-Couce, Andres
    FUEL, 2019, 257
  • [50] BUBBLE PROPERTIES IN LARGE-PARTICLE FLUIDIZED-BEDS
    GLICKSMAN, LR
    LORD, WK
    SAKAGAMI, M
    CHEMICAL ENGINEERING SCIENCE, 1987, 42 (03) : 479 - 491