THE VOLUMETRIC OXYGEN MASS-TRANSFER COEFFICIENT IN ANTIBIOTIC BIOSYNTHESIS LIQUIDS

被引:29
作者
GAVRILESCU, M
ROMAN, RV
EFIMOV, V
机构
[1] Chemical Pharmaceutical Research Institute, Research Centre for Antibiotics 6647, Valea Lupului, Iasi
来源
ACTA BIOTECHNOLOGICA | 1993年 / 13卷 / 01期
关键词
D O I
10.1002/abio.370130114
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
This paper approaches the problem of oxygen mass transfer. This transfer is in antibiotic biosynthesis liquids produced by microorganisms belonging to the actinomycete and fungi classes, which exhibit a shear thinning non-Newtonian rheological behaviour. The volumetric oxygen mass transfer coefficients in these liquids (k(L)a(b)) change during biosynthesis processes. The change is mainly due to rheological parameter modifications, such as increasing the consistency index (K) and decreasing the flow behaviour index (n). The values of k(L)a(b) were 3.0-6.5 times lower than those recorded in water, and their decreasing depended on the k(L)a values obtained without biological liquid and on the nature of fermentation broths, as well. Starting from experimental data, two correlations were established between k(L)a(b) and P/V, upsilon(SG) and P/V, upsilon(SG), N, respectively. These correlations contain a dimensionless factor (eta(am)/eta(g))a6, which takes into account the rheological properties of the liquid phase and offers the possibility for a fast and sufficiently accurate estimation of k(L)a(b). The empirical correlations developed in the paper correspond reasonably well with the relatively wide variety of experimental data, as in the model proposed by PEREZ and SANDALL, and allow for the comparison of the fermentation batches of the same or different microorganisms; also, they may be applied to the workings of design, scale-up, control and monitoring of bioreactors.
引用
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页码:59 / 70
页数:12
相关论文
共 21 条
[1]  
ALLEN DG, 1990, CHEM ENG SCI, V45, P37
[2]   DYNAMIC MEASUREMENT OF VOLUMETRIC OXYGEN TRANSFER COEFFICIENT IN FERMENTATION SYSTEMS [J].
BANDYOPA.B ;
HUMPHREY, AE .
BIOTECHNOLOGY AND BIOENGINEERING, 1967, 9 (04) :533-&
[3]   METHANOGENESIS FROM VOLATILE FATTY-ACIDS IN DOWNFLOW STATIONARY FIXED-FILM REACTOR [J].
BHADRA, A ;
SCHARER, JM ;
MOOYOUNG, M .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (02) :314-319
[4]   THE CONTINUOUS PHASE HEAT AND MASS-TRANSFER PROPERTIES OF DISPERSIONS [J].
CALDERBANK, PH ;
MOOYOUNG, MB .
CHEMICAL ENGINEERING SCIENCE, 1961, 16 (1-2) :39-54
[5]  
CALDERBANK PH, 1967, BIOCH BIOL ENG SCI, V1, P101
[6]  
CHAPMAN CM, 1983, CHEM ENG RES DES, V61, P71
[7]  
GAVRILESCU M, 1989, REV CHIM-BUCHAREST, V40, P958
[8]   RHEOLOGICAL BEHAVIOR OF SOME ANTIBIOTIC BIOSYNTHESIS LIQUIDS [J].
GAVRILESCU, M ;
ROMAN, RV ;
EFIMOV, V .
ACTA BIOTECHNOLOGICA, 1992, 12 (05) :383-396
[9]  
GREAVES M, 1984, I CHEM ENG S SERIES, V89
[10]   A COMPARISON OF SOME METHODS OF ESTIMATING VOLUMETRIC MASS-TRANSFER COEFFICIENTS IN AN EXTERNAL-LOOP AIRLIFT FERMENTER [J].
KAMP, F ;
WASE, DAJ ;
MCMANAMEY, WJ ;
MENDOZA, O ;
THAYANITHY, K .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (02) :179-186