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dc.contributor.authorRipoll Morales, Vanessa
dc.contributor.authorRodríguez, Alberto
dc.contributor.authorLadero, Miguel
dc.contributor.authorSantos, Victoria E.
dc.date.accessioned2020-05-09T17:32:48Z
dc.date.available2020-05-09T17:32:48Z
dc.date.issued2020
dc.identifier.issn1615-7591spa
dc.identifier.urihttp://hdl.handle.net/10641/1918
dc.description.abstractBioconversion of biodiesel-derived glycerol into 2,3-butanediol has received recently much attention due to its increasing surplus and its multiple uses in industry as bulk chemical. The influence of initial glycerol concentration on 2,3-butanediol production in batch runs has been studied. A concentration higher than 140 g/L produces an inhibitory effect on the final 2,3-butanediol concentration and its production rate. In batch mode, the highest yield respect to the theoretical maximum yield (71%) was reached employing 140 g/L as initial concentration 140 g/L. Based on these results, a high 2,3-butanediol production has been achieved through a fed-batch strategy. The reached 2,3-butanediol concentration was 90.5 g/L from pure glycerol and 80.5 g/L from raw glycerol. The 2,3-butanediol yield respect to the theoretical maximum yield was also improved through the fed-batch operation (90%). To date, this concentration is the highest produced amount employing as biocatalyst a non-pathogenic bacterium (level 1).spa
dc.language.isoengspa
dc.publisherBioprocess and Biosystems Engineeringspa
dc.rightsAtribución-NoComercial-SinDerivadas 3.0 España*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/3.0/es/*
dc.subjectBiorefineryspa
dc.subjectRaoultella terrigenaspa
dc.subjectRaw glycerolspa
dc.titleHigh 2,3-butanediol production from glycerol by Raoultella terrigena CECT 4519.spa
dc.typejournal articlespa
dc.type.hasVersionSMURspa
dc.rights.accessRightsopen accessspa
dc.description.extent478 KBspa
dc.identifier.doi10.1007/s00449-019-02266-8spa
dc.relation.publisherversionhttps://link.springer.com/article/10.1007/s00449-019-02266-8spa


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