Effects of liquid content and surface tension on fluidization characteristics in a liquid-containing gas-solid fluidized bed: A CFD-DEM study

被引:28
作者
Zhou , Yefeng [1 ]
Li, Han [1 ]
Zhu, Mengyu [1 ]
Hu , Xiayi [1 ]
Yuan, Haizhuan [2 ]
Jiang, Shengqiang [3 ]
Han, Luchang [1 ]
机构
[1] Xiangtan Univ, Natl & Local United Engn Res Ctr Chem Proc Simula, Chem Proc Simulat & Optimizat Engn Res Ctr, Chinese Minist Educ, Xiangtan 411105, Peoples R China
[2] Xiangtan Univ, Sch Math & Computat Sci, Xiangtan 411105, Peoples R China
[3] Xiangtan Univ, Sch Mech Engn, Xiangtan 411105, Peoples R China
基金
中国国家自然科学基金;
关键词
Liquid-containing gas-solid fluidized bed reactor (LC-GSFBR); Liquid content; Surface tension; Fluidization characteristics; Stagnation zone; DISCRETE PARTICLE SIMULATION; COHESIVE PARTICLES; NUMERICAL-SIMULATION; GRANULE CONSOLIDATION; AGGLOMERATE STABILITY; INTERPARTICLE FORCES; FLOW BEHAVIORS; WET PARTICLES; MODEL; DYNAMICS;
D O I
10.1016/j.cep.2020.107928
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The fluidization process within gas-solid fluidized bed reactor can be intensified by adding liquid, as it can enhance mass and heat transfer between gas phase and solid phase. With the help of computational fluid dynamics(CFD) and discrete element methods(DEM), fluidization characteristics are investigated at different liquid contents((V) over cap) and surface tension(Bo(g)). To be specific, the bed expansion ratio, particle concentration and particle velocity profiles are compared and analyzed. Numerical simulations show that Bo(g) should be less than 5 at (V) over cap = 0.013. At this recommended range, liquid addition makes interparticle force increase and has little effect on fluidization performance. From transient particle agglomeration behavior, the Bo(g) increase is more likely to enhance interparticle force, resulting in obvious particle agglomerations during fluidization process. The variation of stagnation zone height can be reflected from the abrupt increase of particle velocity in annulus region. It can be found that (V) over cap increase reduces particle velocity at critical height but Bo(g) increase is more likely to cause larger stagnation region. By analyzing the distribution of spout, annulus and fountain regions at different (V) over cap and Bo(g), the annulus region expands with (V) over cap increase below the initial bed height while the spout region expands with Bo(g) increase.
引用
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页数:18
相关论文
共 71 条
[1]   A FLUID MECHANICAL DESCRIPTION OF FLUIDIZED BEDS [J].
ANDERSON, TB ;
JACKSON, R .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1967, 6 (04) :527-&
[2]   Fluidized bed granulation - the importance of a drying zone for the particle growth mechanism [J].
Becher, RD ;
Schlunder, EU .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1998, 37 (01) :1-6
[3]   Fluidized bed granulation: Gas flow, particle motion and moisture distribution [J].
Becher, RD ;
Schlunder, EU .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1997, 36 (04) :261-269
[4]   Effects of hydrocarbon liquid feed in polyethylene polymerization process on particle surface temperature [J].
Botros, K. K. ;
Price, G. ;
Ker, V. ;
Jiang, Y. ;
Goyal, S. K. .
CHEMICAL ENGINEERING COMMUNICATIONS, 2006, 193 (12) :1612-1634
[5]   Effect of liquid bridging on bubbles injected into a fluidized bed: A magnetic resonance imaging study [J].
Boyce, C. M. ;
Penn, A. ;
Lehnert, M. ;
Pruessmann, K. P. ;
Mueller, C. R. .
POWDER TECHNOLOGY, 2019, 343 :813-820
[6]   Gas-solid fluidization with liquid bridging: A review from a modeling perspective [J].
Boyce, C. M. .
POWDER TECHNOLOGY, 2018, 336 :12-29
[7]   Analysis of the Effect of Small Amounts of Liquid on Gas-Solid Fluidization Using CFD-DEM Simulations [J].
Boyce, C. M. ;
Ozel, A. ;
Kolehmainen, J. ;
Sundaresan, S. .
AICHE JOURNAL, 2017, 63 (12) :5290-5302
[8]  
CUNDALL PA, 1980, GEOTECHNIQUE, V30, P335
[9]   THE INFLUENCE OF VISCOSITY ON THE STRENGTH OF AN AXIALLY STRAINED PENDULAR LIQUID BRIDGE [J].
ENNIS, BJ ;
LI, JL ;
TARDOS, GI ;
PFEFFER, R .
CHEMICAL ENGINEERING SCIENCE, 1990, 45 (10) :3071-3088
[10]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89