Characterisation of a novel miniaturised bubble column bioreactor for high throughput cell cultivation

被引:40
作者
Doig, SD [1 ]
Diep, A [1 ]
Baganz, F [1 ]
机构
[1] UCL, Adv Ctr Biochem Engn, Dept Biochem Engn, London WC1E 7JE, England
基金
英国工程与自然科学研究理事会;
关键词
bioreactors; bubble columns; gas-liquid mass transfer; fermentation; mass transfer;
D O I
10.1016/j.bej.2004.10.014
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 miniature (2 ml) bioreactor has been developed for the high throughput cultivation of microorganisms. The microplate bubble column bioreactor (MBCB) consists of a static deep well microtiter plate with polyethylene frits (pore size 20 mum) inserted into the base of each of the 48 wells. Air was supplied at a controlled flow rate to the underside of each well and in this way the air passing through the pores of the frit formed bubbles in the liquid biomedium. A volumetric mass transfer coefficient for oxygen (k(L)a) of up to 220 h(-1) could be achieved in this novel system. Since the system was not shaken, as is usually required with cell cultivations in microtiter plates, its performance was simpler to model and predict. A miniature optical oxygen probe was used to measure the dissolved oxygen concentration and it was found that the derived k(L)a values were proportional to the superficial gas velocity over the range 0-0.02 m s(-1). The usefulness of this new device was demonstrated by carrying out 25 parallel experiments to optimise the growth conditions of Bacillus subtilis ATCC6633, a strict aerobe, over a range of pH values and C/N ratios. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:97 / 105
页数:9
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