two-fluid model;
population balance;
CFD;
coalescence and break-up;
D O I:
10.1016/j.ces.2007.08.048
中图分类号:
TQ [化学工业];
学科分类号:
0817 ;
摘要:
In the present work, an attempt has been made to combine population balance and a CFD approach for simulating the flow in oscillatory baffled column (OBC). Three-dimensional Euler-Euler two-fluid simulations are carried out for the experimental data of Oliveira and Ni [2001. Gas hold-up and bubble diameter in a gassed oscillatory baffled column. Chemical Engineering Science 56, 6143-6148]. The experimental data include the average hold-up profile and bubble size distribution in the OBC. All the non-drag forces (turbulent dispersion force, lift force) and the drag force are incorporated in the model. The coalescence and breakage effects of the gas bubbles are modeled according to the coalescence by the random collision driven by turbulence and wake entrainment while for bubble breakage by the impact of turbulent eddies. Predicted liquid velocity and averaged gas hold-up are compared with the experimental data. The profile of the mean bubble diameter in the column and its variation with the superficial gas velocity is studied. Bubble size distribution obtained by the model is compared with the experimental data. (C) 2007 Elsevier Ltd. All rights reserved.
机构:
Beijing Key Laboratory of Green Reaction Engineering and Technology, Department of Chemical Engineering, Tsinghua UniversityBeijing Key Laboratory of Green Reaction Engineering and Technology, Department of Chemical Engineering, Tsinghua University
机构:
Univ Kebangsaan Malaysia, Dept Chem & Proc Engn, Bangi 43600, Selangor Darul, MalaysiaUniv Kebangsaan Malaysia, Dept Chem & Proc Engn, Bangi 43600, Selangor Darul, Malaysia
Takriff, MS
Masyithah, Z
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机构:
Univ Kebangsaan Malaysia, Dept Chem & Proc Engn, Bangi 43600, Selangor Darul, MalaysiaUniv Kebangsaan Malaysia, Dept Chem & Proc Engn, Bangi 43600, Selangor Darul, Malaysia