Direct production of lactic acid based on simultaneous saccharification and fermentation of mixed restaurant food waste

dc.bibliographicCitation.firstPage615
dc.bibliographicCitation.journalTitleJournal of Cleaner Productioneng
dc.bibliographicCitation.lastPage623
dc.bibliographicCitation.volume143
dc.contributor.authorPleissner, Daniel
dc.contributor.authorDemichelis, Francesca
dc.contributor.authorMariano, Silvia
dc.contributor.authorFiore, Silvia
dc.contributor.authorGutiérrez, Ivette Michelle Navarro
dc.contributor.authorSchneider, Roland
dc.contributor.authorVenus, Joachim
dc.date.accessioned2017-07-03T23:57:25Z
dc.date.available2019-06-28T13:38:19Z
dc.date.issued2016
dc.description.abstractThis study introduces to a one-step process for the fermentative production of L(+)-lactic acid from mixed restaurant food waste. Food waste was used as carbon and nitrogen source in simultaneous saccharification and fermentation (SSF) using Lactobacillus sp. or Streptococcus sp. strains for L(+)-lactic acid production. Waste consisted of (w/w) 33.5% starch, 14.8% proteins, 12.9% fat and 8.5% free sugars. Lactobacillus sp. strains showed a productivity of 0.27–0.53 g L−1 h−1 and a yield of 0.07–0.14 g g−1 of theoretically available sugars, while Streptococcus sp. more efficiently degraded the food waste material and produced lactic acid at a maximum rate of 2.16 g L−1 h−1 and a yield of 0.81 g g−1. For SSF, no enzymes were added or other hydrolytic treatments were carried out. Outcomes revealed a linear relationship between lactic acid concentration and solid-to-liquid ratio when Streptococcus sp. was applied. Statistically, from a 20% (w/w) dry food waste blend 52.4 g L−1 lactic acid can be produced. Experimentally, 58 g L−1 was achieved in presence of 20% (w/w), which was the highest solid-to-liquid ratio that could be treated using the equipment applied. Irrespective if SSF was performed at laboratory or technical scale, or under non-sterile conditions, Streptococcus sp. efficiently liquefied food waste and converted the released nutrients directly into lactic acid without considerable production of other organic acids, such as acetic acid. Downstream processing including micro- and nanofiltration, electrodialysis, chromatography and distillation gave a pure 702 g L−1 L(+)-lactic acid formulation.eng
dc.description.versionpublishedVersioneng
dc.formatapplication/pdf
dc.identifier.urihttps://doi.org/10.34657/218
dc.identifier.urihttps://oa.tib.eu/renate/handle/123456789/4524
dc.language.isoengeng
dc.publisherAmsterdam : Elseviereng
dc.relation.doihttps://doi.org/10.1016/j.jclepro.2016.12.065
dc.rights.licenseCC BY-NC-ND 4.0 Unportedeng
dc.rights.urihttps://creativecommons.org/licenses/by-nc-nd/4.0/eng
dc.subject.ddc630eng
dc.subject.otherFood wasteeng
dc.subject.otherLarger scale fermentationeng
dc.subject.otherLactic acideng
dc.subject.otherDownstream processingeng
dc.titleDirect production of lactic acid based on simultaneous saccharification and fermentation of mixed restaurant food wasteeng
dc.typeArticleeng
dc.typeTexteng
tib.accessRightsopenAccesseng
wgl.contributorATBeng
wgl.subjectLandwirtschafteng
wgl.typeZeitschriftenartikeleng
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