INCREASED OXYGEN MASS TRANSFER RATES FROM SINGLE BUBBLES IN MICROBIAL SYSTEMS AT LOW REYNOLDS NUMBERS

被引:29
作者
WISE, DL
WANG, DIC
MATELLES, RI
机构
[1] Dynatech R D Co, Cambridge, Massachusetts, 02189
[2] Massachusetts Institute of Technology, Dept. of Nutrition and Food Science, Biochemical Engineering Group, Cambridge, Massachusetts
关键词
D O I
10.1002/bit.260110411
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
The presence of microorganisms have been shown to increase by over 40% the mass transfer rates from small oxygen bubbles at low Reynolds number flow. This increase was found to be due only to the microbe cells as inert particles disrupting the quasi‐static liquid surface film surrounding the gas bubble and thus decreasing the gas‐liquid interfacial resistance. The observed increase in oxygen mass transfer rates was not dependent on cell viability, no effect was noted due to cell‐liquid interfacial resistance, nor was the phenomenon due to altering the physical properties of the liquid during cell propagation. These results were obtained in a unique plexiglass apparatus designed for observing under a microscope a small (0.4 mm dia.) stationary oxygen bubble collapsing into a flowing fluid. The oxygen bubble was injected by a small hypodermic needle and the fluid was suspensions of the yeast Candida intermedia, the bacterium Pseudomonas ovalis, 0.3μ alumina, as well as base points of cell free broth and pure water. Several well‐known chemical inhibitors of oxidative phosphorylation were used to limit cell oxygen uptake. Calculations of oxygen mass transfer rates were compared with the semi‐empirical model of Frössling, the circulating sphere model of Levich, and the rigid sphere concentration boundary layer model of Fried‐lander, the latter two showing strong Reynolds number dependence that may be due to radial fluid motion. Copyright © 1969 John Wiley & Sons, Inc.
引用
收藏
页码:647 / &
相关论文
共 41 条
[1]  
AUGENSTEIN DC, 1967, THESIS MIT
[2]  
BAIRD MHI, 1962, CAN J CHEM ENG, V40, P119, DOI DOI 10.1002/CJCE.V40:3
[3]   OXYGEN TRANSFER AND AGITATION IN SUBMERGED FERMENTATIONS - MASS TRANSFER OF OXYGEN IN SUBMERGED FERMENTATION OF STREPTOMYCES-GRISEUS [J].
BARTHOLOMEW, WH ;
KAROW, EO ;
SFAT, MR ;
WILHELM, RH .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1950, 42 (09) :1801-1809
[4]   OXYGEN TRANSFER MECHANISMS IN GLUCONIC ACID FERMENTATION BY PSEUDOMONAS OVALIS [J].
BENNETT, GF ;
KEMPE, LL .
BIOTECHNOLOGY AND BIOENGINEERING, 1964, 6 (03) :347-&
[5]  
Bird R.B., 2007, TRANSPORT PHENOMENA, V2nd
[6]  
Cochran W.G., 1957, EXPT DESIGNS
[7]  
DANKWERTS PV, 1951, IND ENGNG CHEM IND E, V43, P1460
[8]   MASS AND HEAT TRANSFER TO SINGLE SPHERES AND CYLINDERS AT LOW REYNOLDS NUMBERS [J].
FRIEDLANDER, SK .
AICHE JOURNAL, 1957, 3 (01) :43-48
[9]   A NOTE ON TRANSPORT TO SPHERES IN STOKES FLOW [J].
FRIEDLANDER, SK .
AICHE JOURNAL, 1961, 7 (02) :347-348
[10]  
Frossling N., 1938, GERL BEITR GEOPHYS, V52, P170