HYDRAULIC PERMEABILITY OF IMMOBILIZED BACTERIAL-CELL AGGREGATES

被引:13
作者
FOWLER, JD [1 ]
ROBERTSON, CR [1 ]
机构
[1] STANFORD UNIV,MED CTR,SCH MED,DEPT CHEM ENGN,STANFORD,CA 94305
关键词
D O I
10.1128/AEM.57.1.102-113.1991
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 dense aggregate of cells was retained in a reactor by a supported porous membrane. A continuous flow of nutrient medium was maintained through the cell aggregate and membrane. The hydraulic resistance of the cell aggregate was monitored throughout experiments with either growing or chemically cross-linked cells, under conditions of varying flow rates. Digital image analysis was used to characterize the sizes, separations, and orientations of several thousand individual cells in electron micrographs of chemically cross-linked cell aggregates. Two nonlinear phenomena were observed. First, the hydraulic resistance varied in direct relation to and reversibly with flow rate. Second, in constant flow-rate experiments the hydraulic resistance increased with time at a faster rate than could be attributed to cell growth. Both of these phenomena were dependent upon and could be explained by the ability of cells to move with respect to one another, under the influences of Brownian motion and of convection. Such relative motion could allow changes in net alignment of cells in the direction of flow and in the volume fraction of cells in the aggregate. This explanation is consistent with image analysis data. The observed sensitivity of hydraulic resistance to flow rate was inconsistent with a model that assumed elastic deformation of individual cells, and no evidence of cell deformation was found in electron micrographs.
引用
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页码:102 / 113
页数:12
相关论文
共 36 条
[1]   HYDROLYSIS OF LACTOSE IN SKIM MILK BY IMMOBILIZED BETA-GALACTOSIDASE IN A SPIRAL FLOW REACTOR [J].
BAKKEN, AP ;
HILL, CG ;
AMUNDSON, CH .
BIOTECHNOLOGY AND BIOENGINEERING, 1989, 33 (10) :1249-1257
[2]   MEMBRANES AND BIOREACTORS - A TECHNICAL CHALLENGE IN BIOTECHNOLOGY [J].
BELFORT, G .
BIOTECHNOLOGY AND BIOENGINEERING, 1989, 33 (08) :1047-1066
[3]  
BRIASCO CA, UNPUB
[4]   HYDRODYNAMIC STRESS CAPACITY OF MICROORGANISMS [J].
BRONNENMEIER, R ;
MARKL, H .
BIOTECHNOLOGY AND BIOENGINEERING, 1982, 24 (03) :553-578
[5]  
DEROSA M, 1981, BIOTECHNOL BIOENG, V23, P221
[6]   WHOLE CELL IMMOBILIZATION IN POLYURETHANE STRUCTURAL FOAM [J].
DRIOLI, E ;
IORIO, G ;
SANTORO, R ;
DEROSA, M ;
GAMBACORTA, A ;
NICOLAUS, B .
JOURNAL OF MOLECULAR CATALYSIS, 1982, 14 (02) :247-251
[7]   HIGH-TEMPERATURE IMMOBILIZED-CELL ULTRAFILTRATION REACTORS [J].
DRIOLI, E ;
IORIO, G ;
DEROSA, M ;
GAMBACORTA, A ;
NICOLAUS, B .
JOURNAL OF MEMBRANE SCIENCE, 1982, 11 (03) :365-370
[8]   THERMOPHILIC ENZYMATIC SEMIPERMEABLE MEMBRANES [J].
DRIOLI, E ;
GAETA, S ;
CARFAGNA, C ;
DEROSA, M ;
GAMBACORTA, A ;
NICOLAUS, B .
JOURNAL OF MEMBRANE SCIENCE, 1980, 6 (03) :345-350
[9]   CATION TRANSPORT IN ESCHERICHIA COLI .V. REGULATION OF CATION CONTENT [J].
EPSTEIN, W ;
SCHULTZ, SG .
JOURNAL OF GENERAL PHYSIOLOGY, 1965, 49 (02) :221-&
[10]   STEADY-STATE MODELING OF A HOLLOW FIBER ENZYMATIC REACTOR [J].
FABIANI, C ;
GIUBILEO, G ;
PIZZICHINI, M ;
VIOLANTE, V .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (03) :458-461