CFD simulation and optimization of effective parameters for biomass production in a horizontal tubular loop bioreactor

被引:14
作者
Mousavi, S. M. [1 ]
Shojaosadati, S. A. [1 ]
Golestani, J. [1 ]
Yazdian, F. [1 ]
机构
[1] Tarbiat Modares Univ, Biotechnol Grp, Dept Chem Engn, Tehran, Iran
关键词
CFD simulation; Optimization; Gas hold up; Biomass production; Forced-liquid horizontal tubular loop bioreactor; Taguchi method; GAS-LIQUID FLOW; DYNAMIC SIMULATION; MULTIPHASE FLOW; MASS-TRANSFER; 2-PHASE FLOW; NATURAL-GAS; REACTORS; GEOMETRY; EPSILON;
D O I
10.1016/j.cep.2010.09.013
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 focus of the current study was to perform an experimental investigation and computational fluid dynamic (CFD) simulation of flow hydrodynamics in a forced-liquid horizontal tubular loop bioreactor for the production of biomass. The simulations were performed using the FLUENT commercial CFD package, a segregated unsteady solver and a two-phase Eulerian multiphase model. To validate the simulation results, several experiments were performed in a pilot bioreactor. In addition, the design of experiments methodology using a Taguchi orthogonal array (OA) was applied to evaluate the influence of four factors on the hydrodynamic behavior of the bioreactor. The effective parameters considered for optimization were air inlet velocity, liquid inlet velocity, bubble diameter, and viscosity. An L-9 OA was used to conduct the Taguchi experiments to study the significance of these parameters and the possible effects of any two-factor interactions. The optimum conditions and most significant process parameters affecting the hydrodynamic behavior were determined using an analysis of variance model. The results showed that the liquid inlet velocity had the most influence on the air volume fraction in the bioreactor. A subsequent confirmatory test demonstrated that the results were within the confidence interval. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:1249 / 1258
页数:10
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