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dc.contributor.authorKarp, S G-
dc.contributor.authorIgashiyama, A H-
dc.contributor.authorSiqueira, P F-
dc.contributor.authorCarvalho, J C-
dc.contributor.authorVandenberghe, L P S-
dc.contributor.authorThomaz-Soccol, V-
dc.contributor.authorCoral, J-
dc.contributor.authorTholozan, J L-
dc.contributor.authorPandey, A-
dc.contributor.authorSoccol, C R-
dc.date.accessioned2014-01-22T07:16:29Z-
dc.date.available2014-01-22T07:16:29Z-
dc.date.issued2011-
dc.identifier.citationBioresource Technology 102(2):1765-1772;Jan 2011en_US
dc.identifier.issn0960-8524-
dc.identifier.urihttp://ir.niist.res.in:8080/jspui/handle/123456789/1106-
dc.description.abstractLactic acid is a product that finds several applications in food, cosmetic, pharmaceutical and chemical industries. The main objective of this work was the development of a bioprocess to produce L(+)-lactic acid using soybean vinasse as substrate. Among ten strains, Lactobacillus agilis LPB 56 was selected for fermentation, due to its ability to metabolize the complex oligosaccharides. Fermentation was conducted without need for supplementary inorganic nitrogen sources or yeast extract. Kinetic and yield parameters determined at laboratory scale were 0.864 and 0.0162 for Y-P/S and Y-X/S, 0.0145 g/L h (r(x)), 1.32 g/L h (r(s)) and 1.13 g/L h (r (p)). The use of vinasse enriched with soybean molasses provided higher lactic acid concentration (138 g/L), the best proportion of inoculum being 25% (v/v). After scale-up to a pilot plant, kinetic and yield parameters were 0.849 and 0.0353 for Y-P/S and Y-X/S, 0.0278 g/L h (r(x)), 0.915 g/L h (r(s)) and 0.863 g/L h (r (p)).en_US
dc.language.isoenen_US
dc.publisherElsevieren_US
dc.subjectSoybean vinasseen_US
dc.subjectSoybean molassesen_US
dc.subjectL(+)-lactic aciden_US
dc.subjectRhizopus-Oryzaeen_US
dc.subjectMolassesen_US
dc.titleApplication of the biorefinery concept to produce L-lactic acid from the soybean vinasse at laboratory and pilot scaleen_US
dc.typeArticleen_US
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