Biotechnology Progress · 2003 · 53 citations · 16 references
Life SciencesBioengineeringBiotechnologyBiochemical EngineeringBioprocess EngineeringEnzymologyBiofuel ProductionBioreaction EngineeringBioreactor OperationEnzyme ImmobilizationEnzyme ProductionThermostable EnzymesDilution Rate OptimizationEnzyme Production OptimizationImmobilized Enzyme ReactorsImmobilized Enzyme SystemsOperational StabilityProductivityReactor Design For Immobilized EnzymesSubstrate Concentration Control
D-Tagatose was continuously produced using thermostable L-arabinose isomerase immobilized in alginate with D-galactose solution in a packed-bed bioreactor. Bead size, L/D (length/diameter) of reactor, dilution rate, total loaded enzyme amount, and substrate concentration were found to be optimal at 0.8 mm, 520/7 mm, 0.375 h(-1), 5.65 units, and 300 g/L, respectively. Under these conditions, the bioreactor produced about 145 g/L tagatose with an average productivity of 54 g tagatose/L x h and an average conversion yield of 48% (w/w). Operational stability of the immobilized enzyme was demonstrated, with a tagatose production half-life of 24 days.
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Bioconversion of d-galactose into d-tagatose
P.S.J. Cheetham, A.Nicola Wootton · Enzyme and Microbial Technology · 1993 · 111 citations