Heterogeneous catalysis in multi-stage fluidized bed reactors: From fundamental study to industrial application

被引:11
|
作者
Zhang, Chenxi [1 ]
Qian, Weizhong [1 ]
Wang, Yao [1 ]
Luo, Guohua [1 ]
Wei, Fei [1 ]
机构
[1] Tsinghua Univ, Beijing Key Lab Green React Engn & Technol, Dept Chem Engn, Beijing 100084, Peoples R China
来源
关键词
multi-stage fluidized bed reactors; back-mixing; phase separation; heterogeneous catalysis; PRESSURE-DROP; NO REDUCTION; GAS; AROMATICS; METHANOL; TIME; REGENERATION; CONVERSION; COLUMN; RANGE;
D O I
10.1002/cjce.23425
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The multi-stage fluidized bed (MSFB) reactor with several stages connected in series prevents gas and solids back-mixing effectively and obtains the plug-flow reactor performance. Besides, different process steps can be accomplished in a single reactor by establishing different temperatures and/or concentrations in each stage. Therefore, multi-stage fluidized bed reactors are acknowledged as novel and flexible multi-phase flow reactors for heterogeneous catalytic processes, especially with the intermediates as the desired products. Typical process developments in the industry involve the methanol to aromatics (MTA), regeneration in fluid catalytic cracking (FCC), and hydrogenation of nitrobenzene to aniline. The purpose of this article is to provide a comprehensive review of the fundamental research as well as particular industrial applications on multi-stage fluidized bed reactors in the Fluidization Laboratory of Tsinghua University (FLOTU).
引用
收藏
页码:636 / 644
页数:9
相关论文
共 50 条
  • [31] Gas mixing in a multi-stage conversion fluidized bed (MFB) with secondary air injection. Part I: an experimental study
    Zhang, Rong
    Hao, Zhenhua
    Wang, Zhiyu
    Huo, Xiaodong
    Li, Junguo
    Song, Sufang
    Fang, Yitian
    RSC ADVANCES, 2016, 6 (43) : 36642 - 36655
  • [32] Evolution of deposited carbon during multi-stage fluidized-bed reduction of iron ore fines
    Du, Zhan
    Zhu, Qingshan
    Pan, Feng
    Zou, Zheng
    Xie, Zhaohui
    Li, Hongzhong
    PARTICUOLOGY, 2018, 41 : 11 - 19
  • [33] Application of multi-stage fuzzy comprehensive evaluation in industrial distribution and its research
    Deng, Fumin
    PROCEEDINGS OF THE FIFTH INTERNATIONAL CONFERENCE ON MANAGEMENT SCIENCE AND ENGINEERING MANAGEMENT, 2011, : 227 - 229
  • [34] Maintenance Strategies for Industrial Multi-Stage Machines: The Study of a Thermoforming Machine
    Alvarez Garcia, Francisco Javier
    Rodriguez Salgado, David
    SENSORS, 2021, 21 (20)
  • [35] A study on the fundamental surge frequencies in multi-stage axial flow compressor systems
    Yamaguchi, Nobuyuki
    International Journal of Fluid Machinery and Systems, 2014, 7 (04) : 160 - 173
  • [36] Pharmaceutical industrial experiments on continuous cryogenic reactions using mini-sized multi-stage reactors
    Takasuga, Masahiro
    Yabuki, Yasuaki
    Kato, Yoshiaki
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2006, 39 (07) : 772 - 776
  • [37] Two-stage modeling strategy for industrial fluidized bed reactors in gas-phase ethylene polymerization processes
    Kusolsongtawee, Thirasit
    Bumroongsri, Pornchai
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2018, 140 : 68 - 81
  • [38] Pressure drop characteristics of a multi-stage counter-current fluidized bed reactor for control of gaseous pollutants
    Mohanty, C. R.
    Meikap, B. C.
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2009, 48 (01) : 209 - 216
  • [39] Numerical analysis of gas–solid hydrodynamics and heat transfer characteristics in a multi-stage fluidized bed temperature stabilizer
    Indra Jeet Yadav
    Pavitra Singh
    Bhupendra Singh Chauhan
    Journal of Thermal Analysis and Calorimetry, 2024, 149 : 1617 - 1627
  • [40] High-yield production of aromatics from methanol using a temperature-shifting multi-stage fluidized bed reactor technology
    Chen, Zhaohui
    Hou, Yilin
    Song, Wenlong
    Cai, Dali
    Yang, Yifeng
    Cui, Yu
    Qian, Weizhong
    CHEMICAL ENGINEERING JOURNAL, 2019, 371 : 639 - 646