Optimization of the microbial synthesis of dihydroxyacetone in a semi-continuous repeated-fed-batch process by in situ immobilization of Gluconobacter oxydans
- 1 January 2007
- journal article
- Published by Elsevier in Process Biochemistry
- Vol. 42 (1) , 71-76
- https://doi.org/10.1016/j.procbio.2006.07.026
Abstract
No abstract availableKeywords
This publication has 15 references indexed in Scilit:
- Diacylglycerol production in a packed bed bioreactorProcess Biochemistry, 2005
- Continuous nisin production in laboratory media and whey permeate by immobilized Lactococcus lactisProcess Biochemistry, 2005
- Optimization of the microbial synthesis of dihydroxyacetone from glycerol with Gluconobacter oxydansBioprocess and Biosystems Engineering, 2003
- Determination of apparent kinetic parameters for competitive product inhibition in packed-bed immobilized enzyme reactorsBiochemical Engineering Journal, 2003
- Effect of processing parameters on the feasibility and operational stability of immobilized viable microbial cellsEnzyme and Microbial Technology, 1998
- Continuous propionic acid fermentation by immobilizedPropionibacterium acidipropionici in a novel packed-bed bioreactorBiotechnology & Bioengineering, 1992
- Production of a high concentration acetic acid by Acetobacter aceti using a repeated fed-batch culture with cell recyclingApplied Microbiology and Biotechnology, 1991
- Acetic acid production using a fermentor equipped with a hollow fiber filter moduleBiotechnology & Bioengineering, 1989
- Continuous production of l-phenylalanine from acetamidocinnamic acid using co-immobilized cells of Corynebacterium sp. and Paracoccus denitrificansEnzyme and Microbial Technology, 1987
- Citric acid production from glucose. II. Growth and excretion kinetics in a trickleflow fermentorBiotechnology & Bioengineering, 1979