A probabilistic heat transfer model for turbulent fluidized beds

被引:6
|
作者
Stefanova, Ana [1 ,2 ]
Bi, Xiaotao T. [1 ]
Lim, C. Jim [1 ]
Grace, John R. [1 ]
机构
[1] Univ British Columbia, Dept Chem & Biol Engn, 2360 East Mall, Vancouver, BC V6T 1Z3, Canada
[2] NAIT, Sch Appl Sci & Technol, Dept Ind Automat & Design, 11762-106 St, Edmonton, AB T5G 2R1, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Turbulent fluidization; Heat transfer; Packet renewal; Void fraction; Contact time; PARTICLE-WALL CONTACT; TRANSFER COEFFICIENT; RESIDENCE TIME; TUBE; SOLIDS; FLOW; TRANSITION; HYDRODYNAMICS;
D O I
10.1016/j.powtec.2019.01.066
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A probabilistic heat transfer model was developed that allows for the gradual evolution of bed-to-surface heat transfer coefficients with increasing superficial gas velocity when bubbling and turbulent flow structures co-exist. The model is based on the packet renewal theory and the probability of particle packets for the specific hydrodynamic regime adjacent to the heat transfer surface. Assuming distinctive two-phase flow, dense packets at minimum fluidization voidage and voids almost free of particles, causes the heat transfer coefficients to be underestimated in the turbulent flow regime. By allowing for contributions of structures of intermediate voidage that reflect typical behavior in the turbulent flow regime of fluidization, heat transfer predictions are improved significantly. The resulting model is shown to give good agreement with experimental heat transfer data for fluidized beds of FCC and Alumina particles, changing smoothly from one flow regime to another in columns of different diameters and from the core of the bed to the wall. (C) 2019 Elsevier B.V. All rights reserved.
引用
收藏
页码:163 / 171
页数:9
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