ENHANCEMENT OF THE OXYGEN-TRANSFER IN A CIRCULATING 3-PHASE FLUIDIZED-BED BIOREACTOR

被引:0
作者
PAZ, EDD [1 ]
SANTANA, MHA [1 ]
EGUCHI, SY [1 ]
机构
[1] FDN TROP PESQUISAS & TECNOL ANDRE TOSELLO,TROP CULTURE COLLECT,CAMPINAS,BRAZIL
关键词
IMMOBILIZED CELLS; MASS TRANSFER; ACETOBACTER;
D O I
暂无
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
The addition of alpha-alumina to the aqueous solution of sodium alginate for immobilization of viable cells allows the production of denser particles than the ones obtained with sodium alginate alone. This biocatalyst was used in the continuous oxidation of ethanol to acetic add, by a strain of Acetobacter isolated from an ethanol plant. The continuous fermentation was carried out in a circulating three-phase fluidized bed bioreactor. Denser particles allow a greater oxygen transfer, resulting in increased volumetric production rate of acetic acid, because oxygen is usually the limiting factor of this process. The performance of the biocatalyst was analyzed in terms of respiration rate, oxyen diffusivity, volumetric mass-transfer coefficient, and global productivity.
引用
收藏
页码:455 / 466
页数:12
相关论文
共 12 条
[1]   PRACTICAL REACTOR SYSTEMS FOR YEAST-CELL IMMOBILIZATION USING BIOMASS SUPPORT PARTICLES [J].
BLACK, GM ;
WEBB, C ;
MATTHEWS, TM ;
ATKINSON, B .
BIOTECHNOLOGY AND BIOENGINEERING, 1984, 26 (02) :134-141
[2]  
FAN LT, 1981, ADV BIOTECHNOL, V1, P643
[3]  
FURUI M, 1985, J FERMENT TECHNOL, V63, P167
[4]   EFFECT OF INTRAPARTICLE MASS-TRANSFER RESISTANCE ON REACTIVITY OF IMMOBILIZED YEAST-CELLS [J].
FURUSAKI, S ;
SEKI, M .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1985, 18 (05) :389-393
[5]  
MORAES AM, 1991, THESIS STATE U CAMPI
[6]  
OMUNA M, 1985, BIOTECHNOL BIOENG, V27, P1523
[7]  
OSTERGAARD K, 1978, AICHE S SER, V74, P82
[8]  
OSUGA J, 1984, J FERMENT TECHNOL, V62, P139
[9]  
PARK YS, 1988, BIOTECH BIOTECH, V33, P918
[10]  
PAZ EDB, 1992, THESIS STATE U CAMPI