Investigation of gas-solid flow characteristics in a novel internal fluidized bed combustor by experiment and CPFD simulation

被引:9
|
作者
Ding, Hongliang [1 ,2 ]
Ouyang, Ziqu [1 ,2 ,4 ]
Su, Kun [1 ,2 ]
Zhang, Jinyang [1 ,3 ]
机构
[1] Chinese Acad Sci, Inst Engn Thermophys, Beijing 100190, Peoples R China
[2] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
[3] Jiangsu Univ, Zhenjiang 212013, Peoples R China
[4] Chinese Acad Sci, Inst Engn Thermophys, 11 Beisihuanxi Rd, Beijing 100190, Peoples R China
关键词
Novel internal fluidized bed combustor; CPFD; ECT; Gas -solid flow; ELECTRICAL CAPACITANCE TOMOGRAPHY; PULVERIZED COAL COMBUSTION; LOOP SEAL; NOX EMISSIONS; DRAG MODEL; CFB; HYDRODYNAMICS; GASIFICATION; PERFORMANCE; BAFFLES;
D O I
10.1016/j.apt.2023.103962
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Based on the coal self-preheating combustion technology, this research proposed a novel internal flu-idized bed combustor (IFBC) with an internal separator for stable preheating of fuel. In order to verify fea-sibility and operation stability of IFBC, cold experiment, electrical capacitance tomography (ECT) and computational particle fluid dynamic (CPFD) simulation were performed in a laboratory-scale IFBC. The effects of superficial air velocity (Ug) and return valve structure on the operation and gas-solid flow characteristics were investigated. The results revealed that the CPFD prediction agreed well with the experiment values. The pressure balance curve presented an "800 shape distribution, and the particle vol-ume fraction (PVF) showed 'core-annular' distribution features. With the increase of Ug , the PVF in the standpipe increased, and the discharge pattern of the return valve changed from continuous discharge to intermittent discharge, and the solid circulation flux showed a trend of increasing first and then decreasing. With the decrease of the outlet opening of return valve (0), the gas-solid flow behavior in standpipe experienced a transition from gas leakage, stabilizing material seal, and blocking state. For Ug = 2 m/s, 0 = 50 %, an effective solid seal in the return valve was established and IFBC has a stable cir-culation and operation. (c) 2023 The Society of Powder Technology Japan. Published by Elsevier BV and The Society of Powder Technology Japan. All rights reserved.
引用
收藏
页数:17
相关论文
共 50 条
  • [21] A theoretical investigation of gas-solid flow exiting a fluidized bed into a standpipe
    Department of Chemical Engineering, Princeton University, Princeton, NJ 08544, United States
    Powder Technol., 3 (211-228):
  • [22] CFD simulation of bubbling and collapsing characteristics in a gas-solid fluidized bed
    Pei Pei1
    2 School of Engineering and Materials Science
    Petroleum Science, 2009, (01) : 69 - 75
  • [23] Numerical investigation of gas-solid flow hydrodynamics in a circulating fluidized bed
    Baysal, Oezguer
    Kosoglu, M. Fevzi
    Topal, Hueseyin
    Baskaya, Senol
    ISI BILIMI VE TEKNIGI DERGISI-JOURNAL OF THERMAL SCIENCE AND TECHNOLOGY, 2007, 27 (02) : 21 - 32
  • [24] A theoretical investigation of gas-solid flow exiting a fluidized bed into a standpipe
    Tsinontides, SC
    POWDER TECHNOLOGY, 1999, 101 (03) : 211 - 228
  • [25] Gas-solid flow characteristics in turbulent fluidized bed with variable gas velocity
    Zhao, Yunpeng
    Wang, Chengxiu
    Shi, Xiaogang
    Gao, Jinsen
    Lan, Xingying
    POWDER TECHNOLOGY, 2022, 402
  • [26] Numerical simulation of the gas-solid flow characteristics in fluidized bed with wide particle size distribution
    Wang, Wei-Wen
    Dong, Hai-Hong
    Chen, Guang-Hui
    Li, Jian-Long
    Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities, 2011, 25 (02): : 276 - 282
  • [27] CPFD Simulation on Effect of Riser Height on Gas-solid Flow and Combustion Characteristics in a CFB
    Han, Chengliang
    Zhang, Yang
    Yang, Hairui
    Zhang, Hai
    Kung Cheng Je Wu Li Hsueh Pao/Journal of Engineering Thermophysics, 2024, 45 (07): : 2033 - 2039
  • [28] Numerical Simulation of the Gas-Solid Flow in Fluidized-Bed Polymerization Reactors
    Shi, De-Pan
    Luo, Zheng-Hong
    Guo, An-Yi
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (09) : 4070 - 4079
  • [29] Numerical simulation of flow behavior of particles in a gas-solid stirred fluidized bed
    Wang, Shuyan
    Chen, Yujia
    Jia, Yubin
    Tian, Ruichao
    Sun, Qiji
    Fan, Jiawei
    Ma, Yimei
    POWDER TECHNOLOGY, 2018, 338 : 119 - 128
  • [30] Numerical simulation of the flow field in a circulating fluidized bed desulfurizer and its gas-solid separation characteristics
    Energy Source Science and Engineering College, Harbin Institute of Technology, Harbin 150001, China
    Reneng Dongli Gongcheng, 2006, 5 (487-490):