A simplified CFD for three-dimensional analysis of fluid mixing, mass transfer and bioreaction in a fermenter equipped with triple novel geometry impellers

被引:18
作者
Hristov, HV
Mann, R [1 ]
Lossev, V
Vlaev, SD
机构
[1] Univ Manchester, Dept Chem Engn, Manchester M60 1QD, Lancs, England
[2] Biopharma, Razgrad, Bulgaria
[3] Bulgarian Acad Sci, Inst Chem Engn, Sofia, Bulgaria
关键词
fluid mixing; gas-liquid mixing; bioreactors; CFD; stirred vessel; novel impeller;
D O I
10.1205/096030804322985281
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
A Three-dimensional networks-of-zones model has been developed to describe the performance of a novel geometry Narcissus (NS) impeller when used for gas-liquid. mixing in a triple impeller bioreactor. The networks-of-zones can be simply adapted from an earlier version based upon the Rushton turbine. The adaptation is achieved by a conformal stretching of the zone volumes. This accommodates the complex up-down liquid flow pattern by a simple adjustment of the zone volumes matrix, whilst the underlying mass and component balances on every zone stay unchanged. Some results are presented for a pilot-scale Tylosin fermenter. Spatially complex fields in three-dimensions are visualized by solid-body graphics for gas hold-up, bubble phase oxygen, liquid-phase dissolved oxygen, nitrate nutrient and bioreaction rates for a 3 x 2 x (10 x 10) x 60 configuration comprising 36,000 zones. The triple NS impeller produces locally higher levels of dissolved oxygen than are achieved by triple Rushton turbines. In both cases, the behaviour predicted is completely different from that obtained by an oversimplified plug (gas)-backmixed-(liquid) bioreactor model.
引用
收藏
页码:21 / 34
页数:14
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