Modelling surface aeration rates in shaken microtitre plates using dimensionless groups

被引:62
作者
Doig, SD [1 ]
Pickering, SCR [1 ]
Lye, GJ [1 ]
Baganz, F [1 ]
机构
[1] UCL, Dept Biochem Engn, Adv Ctr 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
mass transfer; microtitre plates; bioreactor; modelling; surface tension; fermentation;
D O I
10.1016/j.ces.2004.12.025
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The volumetric oxygen transfer coefficient (k(L)a) in shaken microplate microbial cultivations has been modelled using dimensionless groups. The k(L)a correlation was derived from experimental measurements of air-liquid specific surface area and k(L)a values for three microwell geometries operated over a range of shaking frequencies and diameters. The air-liquid surface area was determined from the rate of evaporation and also from high-speed video photography. k(L)a values were calculated from the mass transfer limited growth rate of a strict aerobe, Bacillus subtilis, and were also directly measured using the dynamic gassing out technique. For both surface area and k(L)a measurements there was good agreement between each of the two methods used. The overall correlation for k(L)a values comprised two separate correlations based on different dimensionless groups. The first described the increase in specific air-liquid surface area (a(f)/a(i)) as a function of Froude (Fr) and Bond (Bo) numbers and is represented as: a(f)/a(i) = c(1)Fr(c2) Bo(c3) where c(1) is a geometry-dependent constant, c(2) ranged from 0.51 to 0.86 and c(3) ranged from 0.03 to 0.18. As expected, when the diameter of a microwell decreases, the significance of surface forces increases and the importance of inertial forces decrease. The second correlation related the Sherwood (Sh) number in terms of Reynolds (Re) and Schmidt (Sc) number and is represented as Sh = 0.19 Re(0.68) Sc(0.36). This correlation was independent of microwell geometry. By combining the two correlations it was possible to predict k(L)a values over a wide range of operating conditions. These models provide a rigorous engineering basis for more reproducible and rational selection of operating conditions for microplate scale cell cultivation. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2741 / 2750
页数:10
相关论文
共 25 条
[1]  
Bailey JE., 1986, BIOCH ENG FUNDAMENTA, P421
[2]  
Büchs J, 2000, BIOTECHNOL BIOENG, V68, P589, DOI 10.1002/(SICI)1097-0290(20000620)68:6<589::AID-BIT1>3.0.CO
[3]  
2-J
[4]   Out-of-phase operating conditions, a hitherto unknown phenomenon in shaking bioreactors [J].
Büchs, J ;
Lotter, S ;
Milbradt, C .
BIOCHEMICAL ENGINEERING JOURNAL, 2001, 7 (02) :135-141
[5]   Introduction to advantages and problems of shaken cultures [J].
Büchs, J .
BIOCHEMICAL ENGINEERING JOURNAL, 2001, 7 (02) :91-98
[6]   THE CONTINUOUS PHASE HEAT AND MASS-TRANSFER PROPERTIES OF DISPERSIONS [J].
CALDERBANK, PH ;
MOOYOUNG, MB .
CHEMICAL ENGINEERING SCIENCE, 1961, 16 (1-2) :39-54
[7]   Metabolic engineering and directed evolution for the production of pharmaceuticals [J].
Chartrain, M ;
Salmon, PM ;
Robinson, DK ;
Buckland, BC .
CURRENT OPINION IN BIOTECHNOLOGY, 2000, 11 (02) :209-214
[8]   Characterisation of a novel miniaturised bubble column bioreactor for high throughput cell cultivation [J].
Doig, SD ;
Diep, A ;
Baganz, F .
BIOCHEMICAL ENGINEERING JOURNAL, 2005, 23 (02) :97-105
[9]  
DOIG SD, 2004, BASIC BIOTECHNOLOGY
[10]   Methods for intense aeration, growth, storage, and replication of bacterial strains in microtiter plates [J].
Duetz, WA ;
Rüedi, L ;
Hermann, R ;
O'Connor, K ;
Büchs, J ;
Witholt, B .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 2000, 66 (06) :2641-2646