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CFD-PBM simulation of power law fluid in a bubble column reactor
被引:0
|作者:
Duan, Meng-Qiang
[2
]
Li, Shao-Bai
[1
]
Bhusal, Manju L.
[2
]
Zhang, Wei
[2
]
Ding, Yu-Huan
[2
]
机构:
[1] Guangxi Minzu Univ, Sch Chem & Chem Engn, Nanning 530006, Peoples R China
[2] Shenyang Aerosp Univ, Coll Energy & Environm, Nanning 110136, Peoples R China
基金:
美国国家科学基金会;
关键词:
bubble column;
CFD-PBM;
non-Newtonian;
bubble size distribution;
gas holdup;
LIQUID-PHASE RHEOLOGY;
GAS HOLD-UP;
MASS-TRANSFER;
SIZE DISTRIBUTIONS;
TRANSPORT-EQUATION;
FLOW;
MODEL;
HYDRODYNAMICS;
BEHAVIOR;
COEFFICIENT;
D O I:
10.1515/ijcre-2024-0010
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
A computational fluid dynamics coupled population balance model (CFD-PBM) was used to numerically simulate the fluid dynamics of bubble swarms in a bubble column containing non-Newtonian fluids. The effects of superficial gas velocity (U g ), the consistency index (K), and the flow index (n) on bubble size distribution (BSD), gas holdup, and fluid dynamic viscosity in a bubble column were analyzed at both local and overall scales. As U g increases, the bubble breakup occurs excessively, the gas holdup increases, and the dynamic viscosity decreases. K and n were used to characterize the rheological properties of power law fluid. As K increases, fluid viscosity increases, bubble breakup rate decreases, gas holdup in the top zone is slightly lower than in the middle zone, and dynamic viscosity increases. Within the range of n from 0.45 to 1.07, when n is smallest, the relative frequency of bubbles smaller than the initial size is relatively large, and the overall and local gas holdup are the highest. When n = 1.07, the fluid exhibits shear-thickening properties, and the dynamic viscosity variations are significant.
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页码:701 / 715
页数:15
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