Development of an integrated biomass refinery process for whole cell biomass utilization of Chlorella sp. ABC-001

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dc.contributor.authorSeon, Gyeonghoko
dc.contributor.authorKim, Minsikko
dc.contributor.authorLee, Yong Wookko
dc.contributor.authorCho, Jun Mukko
dc.contributor.authorKim, Hogiko
dc.contributor.authorPark, Won-Kunko
dc.contributor.authorChang, Yong Keunko
dc.date.accessioned2022-10-05T01:00:15Z-
dc.date.available2022-10-05T01:00:15Z-
dc.date.created2022-10-04-
dc.date.issued2023-01-
dc.identifier.citationCHEMICAL ENGINEERING JOURNAL, v.451-
dc.identifier.issn1385-8947-
dc.identifier.urihttp://hdl.handle.net/10203/298815-
dc.description.abstractMicroalgae are a promising source of biomass for the production of biofuels, but their use is currently infeasible because of changes in the biofuel market and the lack of an optimized refinery process. The biomass of oleag-inous microalgae consists of up to 50% lipids and 50% carbohydrates and proteins, so the biorefinery process must be able to use whole cell biomass. In this work, an alternative process to the standard biorefinery approach of lipid extraction and treatment of lipid-extracted residue was developed and tested using oleaginous Chlorella sp. ABC-001. First, a hydrolysis process was optimized to achieve cell lysis. At 170 C and 0.1 N H2SO4, 89.0% of total carbohydrates were hydrolyzed to monosaccharides within 4 min. Then, a volume reduction process (brief and mild centrifugation) was applied to reduce the extraction time and the use of organic solvent. By reducing the aqueous phase from the hydrolysate, all lipids were extracted by vortexing with just a quarter of the original volume (10 mL) within 20 min. Finally, after extraction the aqueous phase was utilized as the sole growth medium for ethanol production by Saccharomyces cerevisiae KL17. The resulting ethanol yield was 0.39 g ethanol/g sugar, comparable to that achieved using conventional yeast-peptone-dextrose (YPD) medium (0.41 g ethanol/g sugar). Furthermore, relative to the conventional process, techno-economic analysis confirmed that the newly developed process decreased operational expenditures by 82.7% and decreased capital expenditures by 70.1%.-
dc.languageEnglish-
dc.publisherELSEVIER SCIENCE SA-
dc.titleDevelopment of an integrated biomass refinery process for whole cell biomass utilization of Chlorella sp. ABC-001-
dc.typeArticle-
dc.identifier.wosid000856018700002-
dc.identifier.scopusid2-s2.0-85135932564-
dc.type.rimsART-
dc.citation.volume451-
dc.citation.publicationnameCHEMICAL ENGINEERING JOURNAL-
dc.identifier.doi10.1016/j.cej.2022.138543-
dc.contributor.localauthorChang, Yong Keun-
dc.contributor.nonIdAuthorKim, Minsik-
dc.contributor.nonIdAuthorLee, Yong Wook-
dc.contributor.nonIdAuthorCho, Jun Muk-
dc.contributor.nonIdAuthorPark, Won-Kun-
dc.description.isOpenAccessN-
dc.type.journalArticleArticle-
dc.subject.keywordAuthorHydrolysis-
dc.subject.keywordAuthorVolume reduction-
dc.subject.keywordAuthorExtraction-
dc.subject.keywordAuthorEthanol fermentation-
dc.subject.keywordAuthorTechno-economic analysis-
dc.subject.keywordAuthorChlorella sp. ABC-001-
dc.subject.keywordPlusBIOETHANOL PRODUCTION-
dc.subject.keywordPlusLIPID EXTRACTION-
dc.subject.keywordPlusBIODIESEL PRODUCTION-
dc.subject.keywordPlusRESIDUAL BIOMASS-
dc.subject.keywordPlusACID-HYDROLYSIS-
dc.subject.keywordPlusMICROALGAE-
dc.subject.keywordPlusBIOFUELS-
dc.subject.keywordPlusDISRUPTION-
dc.subject.keywordPlusETHANOL-
dc.subject.keywordPlusFERMENTATION-
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CBE-Journal Papers(저널논문)
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