Modeling of ash agglomerating fluidized bed gasifier based on particle agglomerating

被引:0
|
作者
Zhang, Jiaqi [1 ]
Cao, Zhikai [1 ,2 ]
Zhou, Hua [1 ,2 ]
Zhang, Quancong [1 ,2 ]
机构
[1] Gulei Innovation Institute, Xiamen University, Zhangzhou,363200, China
[2] School of Chemistry and Chemical Engineering, Xiamen University, Xiamen,361005, China
来源
关键词
Coal gasification - Concrete construction - Emulsification - Emulsions;
D O I
10.13225/j.cnki.jccs.2024.0026
中图分类号
学科分类号
摘要
Fluidized bed gasification technology has wide applications on coal industry due to its excellent mixing and heat transfer performances. With the influence of strong gas-solid mixing, char content of discharged ash will increase at high temperature. The operating temperature of traditional fluidized bed gasification is low to decrease the carbon loss, but it will lead to a shortage of gasification efficiency. As a result, the ash agglomerating fluidized bed gasification allowing limited particle agglomeration is proposed to increase operating temperature. The agglomeration size is the core of ash agglomerating gasifier so it is important to investigate the process of ash agglomeration. Expensive costs will be required if the research of complicated particle behavior in the gasifier depends on experimental analysis only. Thus, it is necessary to combine reactor modeling with experiment to improve research efficiency. However, the actual reaction and transport process of ash agglomerating gasifier cannot be described by existing models because the particle agglomeration was neglected and particle size was average during the modeling process. In this paper, a novel model for ash agglomerating fluidized bed gasifier was proposed: (1) the gasifier is divided into bubbling region consisting of bubble and emulsion phases, and freeboard regarded as pseudo-homogeneous phase; (2) the particle agglomeration is described by the integration agglomeration mechanism considering the particle agglomerating phenomenon, and the initial size distribution of particle. The model was validated according to the comparison that the deviation of simulation results and practical data is within 10%. Finally, the agglomeration size and carbon conversion with different oxygen-coal ratio was calculated by the model. With the agglomeration size reaching the critical value, the maximum carbon conversion is observed. The fluidization of agglomeration cannot keep if the agglomeration size exceeds the critical value. © 2025 China Coal Society. All rights reserved.
引用
收藏
页码:1781 / 1793
相关论文
共 50 条
  • [41] Physicochemical Properties of Coal Gasification Fly Ash from Circulating Fluidized Bed Gasifier
    YANG Qiyao
    QI Xiaobin
    LYU Qinggang
    ZHU Zhiping
    JournalofThermalScience, 2023, 32 (04) : 1710 - 1720
  • [42] Physicochemical Properties of Coal Gasification Fly Ash from Circulating Fluidized Bed Gasifier
    Yang, Qiyao
    Qi, Xiaobin
    Lyu, Qinggang
    Zhu, Zhiping
    JOURNAL OF THERMAL SCIENCE, 2023, 32 (04) : 1710 - 1720
  • [43] Influence of pressure on fluidized bed gasifier: Specific coal throughput and particle behavior
    Li, Junguo
    Li, Fenghai
    Liu, Wenhong
    Liu, Zheyu
    Zhan, Haijuan
    Zhang, Yongqi
    Hao, Zhenhua
    Cheng, Zhonghu
    Huang, Jiejie
    Fang, Yitian
    FUEL, 2018, 220 : 80 - 88
  • [44] Hydrodynamics of a dual fluidized bed gasifier
    Karmakar, M. K.
    Datta, A. B.
    ADVANCED POWDER TECHNOLOGY, 2010, 21 (05) : 521 - 528
  • [45] Influence of fuel particle size on gasification in a dual fluidized bed steam gasifier
    Wilk, V.
    Hofbauer, H.
    FUEL PROCESSING TECHNOLOGY, 2013, 115 : 139 - 151
  • [46] BASIC LEAD SULFATES AS AGGLOMERATING AGENTS DURING THE FLUID-BED ROASTING OF ZINC CONCENTRATES
    CONDINA, VK
    JORGENSEN, FRA
    TURNER, TM
    METALLURGICAL TRANSACTIONS B-PROCESS METALLURGY, 1980, 11 (04): : 637 - 638
  • [47] Product design based on discrete particle modeling of a fluidized bed granulator
    Fries, Lennart
    Antonyuk, Sergiy
    Heinrich, Stefan
    Niederreiter, Gerhard
    Palzer, Stefan
    PARTICUOLOGY, 2014, 12 : 13 - 24
  • [48] Product design based on discrete particle modeling of a fluidized bed granulator
    Lennart Fries
    Sergiy Antonyuk
    Stefan Heinrich
    Gerhard Niederreiter
    Stefan Palzer
    Particuology, 2014, 12 (01) : 13 - 24
  • [49] Scanning electron microscopic determination of the particle size distribution of an agglomerating phase in a metallic melt
    Heyroth, W
    Gerloff, R
    ZEITSCHRIFT FUR METALLKUNDE, 1996, 87 (09): : 684 - 690
  • [50] Mathematical modeling for molten ash slagging moving bed coal gasifier considering the impact of particle behavior characteristics
    Zhang, Quancong
    Wei, Bin
    Cao, Zhikai
    Chen, Binghui
    Xue, Kang
    Zhou, Hua
    CHEMICAL ENGINEERING SCIENCE, 2022, 263