1996
DOI: 10.1002/(sici)1097-0290(19960805)51:3<317::aid-bit7>3.0.co;2-g
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Xylitol production by immobilized recombinantSaccharomyces cerevisiae in a continuous packed-bed bioreactor

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Cited by 51 publications
(2 citation statements)
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“…198 S. cerevisiae expressing XR was entrapped in a packed-bed bioreactor for production of xylitol from xylose. 190 The highest productivity of 5.88 g/L h was achieved. In stability tests, the immobilized cells retained approximately 50% of the original activity after 15 days of continuous fermentation.…”
Section: Production Of Lignocellulosic Biomass-derived Productsmentioning
confidence: 97%
“…198 S. cerevisiae expressing XR was entrapped in a packed-bed bioreactor for production of xylitol from xylose. 190 The highest productivity of 5.88 g/L h was achieved. In stability tests, the immobilized cells retained approximately 50% of the original activity after 15 days of continuous fermentation.…”
Section: Production Of Lignocellulosic Biomass-derived Productsmentioning
confidence: 97%
“…However, organic platform chemical production processes require separation methods to isolate the chemicals of interest and recycle the unreacted feed materials and water, engendering challenges for economic viability and sustainability. Studies on biocatalytic processes are usually limited to biocatalyst design, performance optimization, kinetics, or reaction engineering. In our previous studies, the reduction of furfural (FAL) using ethanol (EtOH) as the terminal reductant was carried out using isolated enzyme yeast alcohol dehydrogenase (YADH) to produce furfuryl alcohol (FOL) and acetaldehyde (AcH) (Figure ). Although the reaction was performed in batch and fed-batch modes, continuous production and efficient downstream separation of the coproducts (FOL and AcH) will be critical to the techno-economic feasibility of the process.…”
Section: Introductionmentioning
confidence: 99%