Show simple item record

dc.contributor.authorXu, Jingyang
dc.contributor.authorLiu, Nian
dc.contributor.authorQiao, Kangjian
dc.contributor.authorVogg, Sebastian
dc.contributor.authorStephanopoulos, Gregory
dc.date.accessioned2018-04-05T15:21:50Z
dc.date.available2018-04-05T15:21:50Z
dc.date.issued2017-07
dc.date.submitted2017-03
dc.identifier.issn0027-8424
dc.identifier.issn1091-6490
dc.identifier.urihttp://hdl.handle.net/1721.1/114567
dc.description.abstractAcetic acid can be generated through syngas fermentation, lignocellulosic biomass degradation, and organic waste anaerobic digestion. Microbial conversion of acetate into triacylglycerols for biofuel production has many advantages, including low-cost or even negative-cost feedstock and environmental benefits. The main issue stems from the dilute nature of acetate produced in such systems, which is costly to be processed on an industrial scale. To tackle this problem, we established an efficient bioprocess for converting dilute acetate into lipids, using the oleaginous yeast Yarrowia lipolytica in a semicontinuous system. The implemented design used low-strength acetic acid in both salt and acid forms as carbon substrate and a cross-filtration module for cell recycling. Feed controls for acetic acid and nitrogen based on metabolic models and online measurement of the respiratory quotient were used. The optimized process was able to sustain high-density cell culture using acetic acid of only 3% and achieved a lipid titer, yield, and productivity of 115 g/L, 0.16 g/g, and 0.8 g·L −1 ·h −1 , respectively. No carbon substrate was detected in the effluent stream, indicating complete utilization of acetate. These results represent a more than twofold increase in lipid production metrics compared with the current best-performing results using concentrated acetic acid as carbon feed.en_US
dc.description.sponsorshipUnited States. Department of Energy (Grant DE-SC0008744)en_US
dc.publisherNational Academy of Sciences (U.S.)en_US
dc.relation.isversionofhttp://dx.doi.org/10.1073/PNAS.1703321114en_US
dc.rightsArticle is made available in accordance with the publisher's policy and may be subject to US copyright law. Please refer to the publisher's site for terms of use.en_US
dc.sourceNational Academy of Sciencesen_US
dc.titleApplication of metabolic controls for the maximization of lipid production in semicontinuous fermentationen_US
dc.typeArticleen_US
dc.identifier.citationXu, Jingyang et al. “Application of Metabolic Controls for the Maximization of Lipid Production in Semicontinuous Fermentation.” Proceedings of the National Academy of Sciences 114, 27 (June 2017): E5308–E5316 © 2017 National Academy of Sciencesen_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Chemical Engineeringen_US
dc.contributor.mitauthorXu, Jingyang
dc.contributor.mitauthorLiu, Nian
dc.contributor.mitauthorQiao, Kangjian
dc.contributor.mitauthorVogg, Sebastian
dc.contributor.mitauthorStephanopoulos, Gregory
dc.relation.journalProceedings of the National Academy of Sciencesen_US
dc.eprint.versionFinal published versionen_US
dc.type.urihttp://purl.org/eprint/type/JournalArticleen_US
eprint.statushttp://purl.org/eprint/status/PeerRevieweden_US
dc.date.updated2018-03-30T18:37:06Z
dspace.orderedauthorsXu, Jingyang; Liu, Nian; Qiao, Kangjian; Vogg, Sebastian; Stephanopoulos, Gregoryen_US
dspace.embargo.termsNen_US
dc.identifier.orcidhttps://orcid.org/0000-0002-1164-8692
dc.identifier.orcidhttps://orcid.org/0000-0001-6909-4568
mit.licensePUBLISHER_POLICYen_US


Files in this item

Thumbnail

This item appears in the following Collection(s)

Show simple item record