dc.contributor.author | Ripoll Morales, Vanessa | |
dc.contributor.author | Rodríguez, Alberto | |
dc.contributor.author | Ladero, Miguel | |
dc.contributor.author | Santos, Victoria E. | |
dc.date.accessioned | 2020-05-09T17:32:48Z | |
dc.date.available | 2020-05-09T17:32:48Z | |
dc.date.issued | 2020 | |
dc.identifier.issn | 1615-7591 | spa |
dc.identifier.uri | http://hdl.handle.net/10641/1918 | |
dc.description.abstract | Bioconversion 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.iso | eng | spa |
dc.publisher | Bioprocess and Biosystems Engineering | spa |
dc.rights | Atribución-NoComercial-SinDerivadas 3.0 España | * |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/3.0/es/ | * |
dc.subject | Biorefinery | spa |
dc.subject | Raoultella terrigena | spa |
dc.subject | Raw glycerol | spa |
dc.title | High 2,3-butanediol production from glycerol by Raoultella terrigena CECT 4519. | spa |
dc.type | journal article | spa |
dc.type.hasVersion | SMUR | spa |
dc.rights.accessRights | open access | spa |
dc.description.extent | 478 KB | spa |
dc.identifier.doi | 10.1007/s00449-019-02266-8 | spa |
dc.relation.publisherversion | https://link.springer.com/article/10.1007/s00449-019-02266-8 | spa |