Experimental quantification of interparticle forces in gas-solid fluidized beds operating at temperatures from ambient to 1500 °C

被引:3
|
作者
Zhang, Qingjin [1 ,2 ]
Fu, Liangliang [1 ]
Xu, Guangwen [1 ]
Bai, Dingrong [1 ,3 ]
机构
[1] Shenyang Univ Chem Technol, Key Lab Resources Chem & Mat, Minist Educ, Shenyang 110142, Peoples R China
[2] Shenyang Univ Technol, Sch Mat Sci & Engn, Shenyang 110870, Peoples R China
[3] Ordos Lab, Ordos 017010, Peoples R China
来源
基金
中国国家自然科学基金;
关键词
High-temperature fluidized bed; Hydrodynamic force; Interparticle force; Pressure fluctuations; Bed pressure drop; DENSE PHASE PROPERTIES; PRESSURE; PARTICLE; AGGLOMERATION; HYDRODYNAMICS; EXPANSION; POWDERS;
D O I
10.1016/j.cherd.2024.10.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The successful design and operation of high-temperature gas-solid fluidized bed reactors require a deep understanding of interparticle forces (IPFs). However, experimentally quantifying IPFs at elevated temperatures has been a significant challenge due to the lack of suitable methods. This study addresses this gap by introducing a simple yet reliable experimental approach to quantify IPFs in a gas-solid fluidized bed across a temperature range from ambient to 1500 degrees C. The experimental results reveal that IPFs increase gradually with temperatures up to 1200 degrees C and become more pronounced at higher temperatures. Smaller particles, or those prone to changes in morphological, structural, and chemical properties-such as softening, sintering, or the formation of lowmelting-point eutectic compounds at high temperatures-intensify IPFs significantly. This phenomenon is corroborated by our experiments and comparison with literature data across various temperatures and particle types. Finally, two empirical correlations are proposed to predict IPFs as temperature and particle diameter functions for coarse particles in high-temperature fluidized beds. These findings enhance the understanding of IPFs in high-temperature fluidized beds and are valuable for developing such systems for industrial applications.
引用
收藏
页码:318 / 330
页数:13
相关论文
共 50 条
  • [1] Quantification of interparticle forces in gas-agglomerated particles fluidized beds
    Soleimani, Iman
    Shabanian, Jaber
    Chaouki, Jamal
    CHEMICAL ENGINEERING JOURNAL, 2023, 470
  • [2] Hydrodynamics of a gas-solid fluidized bed with thermally induced interparticle forces
    Shabanian, Jaber
    Chaouki, Jamal
    Chemical Engineering Journal, 2015, 259 : 135 - 152
  • [3] Hydrodynamics of a gas-solid fluidized bed with thermally induced interparticle forces
    Shabanian, Jaber
    Chaouki, Jamal
    CHEMICAL ENGINEERING JOURNAL, 2015, 259 : 135 - 152
  • [4] In-situ quantification of the magnitude of interparticle forces and its temperature variation in a gas-solid fluidized bed
    Soleimani, Iman
    Elahipanah, Navid
    Shabanian, Jaber
    Chaouki, Jamal
    CHEMICAL ENGINEERING SCIENCE, 2021, 232
  • [5] Performance of a Catalytic Gas-Solid Fluidized Bed Reactor in the Presence of Interparticle Forces
    Shabanian, Jaber
    Chaouki, Jamal
    INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING, 2016, 14 (01) : 433 - 444
  • [6] Effects of temperature, pressure, and interparticle forces on the hydrodynamics of a gas-solid fluidized bed
    Shabanian, Jaber
    Chaouki, Jamal
    CHEMICAL ENGINEERING JOURNAL, 2017, 313 : 580 - 590
  • [7] Influence of interparticle forces on solids motion in a bubbling gas-solid fluidized bed
    Shabanian, Jaber
    Chaouki, Jamal
    POWDER TECHNOLOGY, 2016, 299 : 98 - 106
  • [9] The transition to turbulent fluidization in a gas-solid fluidized bed operating from ambient temperature to 1600 °C
    Zhang, Qingjin
    Fu, Liangliang
    Xu, Guangwen
    Bai, Dingrong
    PARTICUOLOGY, 2024, 93 : 111 - 124
  • [10] Local characterization of a gas-solid fluidized bed in the presence of thermally induced interparticle forces
    Shabanian, Jaber
    Chaouki, Jamal
    CHEMICAL ENGINEERING SCIENCE, 2014, 119 : 261 - 273