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[Industrial scale-up of continuous ethanol fermentation using yeast flocs].
Wei Sheng Wu Xue Bao. 1999 Aug; 39(4):367-72.WS

Abstract

Inducing yeast cells to self-flocculate as a cell immobilization method, an industrial scale-up plant composed of 4 air-lift suspended-bed bioreactors in parallel and with a total volume of 400 m3 was established and operated. During a more than 6 months continuous operation, the effluent contained ethanol of 70-80 g/L and residual sugar less than 5 g/L and the ethanol productivity of 7-8 g/L.h-1 was achieved.

Authors+Show Affiliations

Institute of Biochemical Engineering, Dalian University of Technology, Dalian 116012.No affiliation info availableNo affiliation info availableNo affiliation info availableNo affiliation info available

Pub Type(s)

Journal Article

Language

chi

PubMed ID

12555578

Citation

Xie, J, et al. "[Industrial Scale-up of Continuous Ethanol Fermentation Using Yeast Flocs]." Wei Sheng Wu Xue Bao = Acta Microbiologica Sinica, vol. 39, no. 4, 1999, pp. 367-72.
Xie J, Bai F, Yun Z, et al. [Industrial scale-up of continuous ethanol fermentation using yeast flocs]. Wei Sheng Wu Xue Bao. 1999;39(4):367-72.
Xie, J., Bai, F., Yun, Z., Li, N., & He, X. (1999). [Industrial scale-up of continuous ethanol fermentation using yeast flocs]. Wei Sheng Wu Xue Bao = Acta Microbiologica Sinica, 39(4), 367-72.
Xie J, et al. [Industrial Scale-up of Continuous Ethanol Fermentation Using Yeast Flocs]. Wei Sheng Wu Xue Bao. 1999;39(4):367-72. PubMed PMID: 12555578.
* Article titles in AMA citation format should be in sentence-case
TY - JOUR T1 - [Industrial scale-up of continuous ethanol fermentation using yeast flocs]. AU - Xie,J, AU - Bai,F, AU - Yun,Z, AU - Li,N, AU - He,X, PY - 2003/1/31/pubmed PY - 2004/7/31/medline PY - 2003/1/31/entrez SP - 367 EP - 72 JF - Wei sheng wu xue bao = Acta microbiologica Sinica JO - Wei Sheng Wu Xue Bao VL - 39 IS - 4 N2 - Inducing yeast cells to self-flocculate as a cell immobilization method, an industrial scale-up plant composed of 4 air-lift suspended-bed bioreactors in parallel and with a total volume of 400 m3 was established and operated. During a more than 6 months continuous operation, the effluent contained ethanol of 70-80 g/L and residual sugar less than 5 g/L and the ethanol productivity of 7-8 g/L.h-1 was achieved. SN - 0001-6209 UR - https://www.unboundmedicine.com/medline/citation/12555578/[Industrial_scale_up_of_continuous_ethanol_fermentation_using_yeast_flocs]_ DB - PRIME DP - Unbound Medicine ER -
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