Pressure fluctuations in a gas-solid fluidized bed at temperatures up to 1650 °C

被引:22
作者
Fu, Liangliang [1 ,2 ]
Zhang, Qingjin [2 ,3 ]
Xu, Guangwen [2 ]
Bai, Dingrong [2 ]
机构
[1] Univ Sci & Technol Liaoning, Sch Chem Engn, Anshan 114051, Peoples R China
[2] Shenyang Univ Chem Technol, Key Lab Resources Chem & Mat, Minist Educ, Shenyang 110142, Peoples R China
[3] Shenyang Univ Technol, Sch Mat Sci & Engn, Shenyang 110142, Peoples R China
基金
中国国家自然科学基金;
关键词
Fluidized beds; Ultra-high temperatures; Pressure fluctuations; Hydrodynamic characteristics; Thermally induced interparticle forces; Flow dynamics of particle agglomerate; DEFLUIDIZATION; REGIMES; HYDRODYNAMICS; AGGLOMERATION; PREDICTION; PARTICLES; DYNAMICS; BEHAVIOR;
D O I
10.1016/j.cej.2023.143806
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Fluidized beds operating at ultra-high temperatures have great application potential for synthesizing essential materials and chemicals, but they are relatively unexplored. This study, for the first time, investigates fluid-ization characteristics at temperatures up to 1650 degrees C by measurement and analysis of pressure fluctuations in a laboratory fluidized bed of 30 mm diameter with corundum particles of an average size of 900 mu m. Standard statistical and spectral methods are used to analyze pressure fluctuation signals and characterize fluidization behavior based on the effect of temperature on pressure fluctuation parameters, including the probability density function, standard deviation, autocorrelation, power spectra density, amplitude, dominant frequency, and average cycle frequency. The results indicate that, for the coarse corundum particles used in this study, fluid-ization behavior inverts at a crucial temperature of approximately 1400 degrees C. Below this temperature, gas-solid flows in the bed are predominantly controlled by gas bubble movements. In this temperature range, periodicity and maximum amplitude decrease and dominant frequency increases with temperature. Above 1400 degrees C, inter-particle forces, such as van der Waals and viscous forces, are significantly strengthened due to changes in the structural and physiochemical properties of solid materials. The greatly enhanced interparticle forces at ultra-high temperatures promote the dominance of microstructured flows over the overall pressure fluctuations, making interparticle forces the controlling factor influencing gas-solid flows in fluidized beds at ultra-high temperatures. These findings provide a better understanding of ultra-high temperature fluidized beds and can promote their research and development for industrial applications.
引用
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页数:12
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共 50 条
[1]   Early detection of agglomeration in a polyethylene fluidized bed at high temperature and pressure by vibration signature analysis [J].
Alamolhoda, Fatemeh ;
Shamiri, Ahmad ;
Hussain, Mohd Azlan ;
Sotudeh-Gharebagh, Rahmat ;
Mostoufi, Navid .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2015, 104 :156-163
[2]  
Bae K, 2017, KOREAN J CHEM ENG, V34, P566
[3]   Characteristics of gas-fluidized beds in different flow regimes [J].
Bai, D ;
Issangya, AS ;
Grace, JR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (03) :803-811
[4]   Flow structure in a fast fluidized bed [J].
Bai, D ;
Shibuya, E ;
Masuda, Y ;
Nakagawa, N ;
Kato, K .
CHEMICAL ENGINEERING SCIENCE, 1996, 51 (06) :957-966
[5]   Characterization of gas fluidization regimes using pressure fluctuations [J].
Bai, D ;
Shibuya, E ;
Nakagawa, N ;
Kato, K .
POWDER TECHNOLOGY, 1996, 87 (02) :105-111
[6]   Chaotic behavior of fluidized beds based on pressure and voidage fluctuations [J].
Bai, D ;
Bi, HT ;
Grace, JR .
AICHE JOURNAL, 1997, 43 (05) :1357-1361
[7]   Characterization of gas fluidized beds of group C, A and B particles based on pressure fluctuations [J].
Bai, DR ;
Grace, JR ;
Zhu, JX .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (02) :319-324
[8]   A critical review of the complex pressure fluctuation phenomenon in gas-solids fluidized beds [J].
Bi, Hsiaotao T. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (13) :3473-3493
[9]   MECHANISM OF FLOW REGIME TRANSITION FROM BUBBLING TO TURBULENT FLUIDIZATION [J].
CAI, P ;
JIN, Y ;
YU, ZQ ;
WANG, ZW .
AICHE JOURNAL, 1990, 36 (06) :955-956
[10]   Analysis of pressure fluctuations in fluidized beds [J].
Falkowski, D ;
Brown, RC .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (18) :5721-5729