Optimum Utilization of Biochemical Components in Chlorella sp KR1 via Subcritical Hydrothermal Liquefaction

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dc.contributor.authorJin, MinKyuko
dc.contributor.authorOh, You-Kwanko
dc.contributor.authorChang, Yong Keunko
dc.contributor.authorChoi, Minkeeko
dc.date.accessioned2017-09-25T05:13:13Z-
dc.date.available2017-09-25T05:13:13Z-
dc.date.created2017-08-10-
dc.date.created2017-08-10-
dc.date.issued2017-08-
dc.identifier.citationACS SUSTAINABLE CHEMISTRY & ENGINEERING, v.5, no.8, pp.7240 - 7248-
dc.identifier.issn2168-0485-
dc.identifier.urihttp://hdl.handle.net/10203/226019-
dc.description.abstractProduct distributions in bio-crude, aqueous phase, and solid residue were rigorously analyzed during the hydrothermal liquefaction (HTL) of Chlorella sp. KR1 in order to optimize utilization of energy and chemicals. A non-asphaltene (paraffinic) fraction in the bio-crude, which can be readily upgraded to high-quality fuels via a subsequent catalytic process, was mainly produced due to lipid extraction. Above 170 °C, lipid extraction was almost complete, and hence, the non-asphaltene content did not increase further with increasing temperature. Carbohydrates could be extracted, mainly as polysaccharides, in the aqueous phase at mild temperatures (<200 °C). At high temperatures (>200 °C), they decompose and react with proteins via the Maillard reaction to form asphaltene (polycyclic aromatics), which contains large amounts of heteroatoms such as N and S. Although high-temperature carbohydrate conversion could yield more bio-crude with high energy values, it dominantly contributed to formation of the asphaltene fraction, which is difficult to upgrade catalytically. As high-temperature HTL requires a large energy input, the recovery and utilization of intact carbohydrates and proteins at mild temperatures (<200 °C) appears to be more promising. Energy Return on Investment (EROI) analysis also showed that 170 °C is the optimum HTL temperature for maximizing the energy production.-
dc.languageEnglish-
dc.publisherACS Publication-
dc.subjectBIO-CRUDE OIL-
dc.subjectBIODIESEL PRODUCTION-
dc.subjectMAILLARD REACTION-
dc.subjectTHERMOCHEMICAL LIQUEFACTION-
dc.subjectORGANIC-SOLVENTS-
dc.subjectHIGH-TEMPERATURE-
dc.subjectALGAL BIOMASS-
dc.subjectLIPID-CONTENT-
dc.subjectFLOW REACTOR-
dc.subjectMICROALGAE-
dc.titleOptimum Utilization of Biochemical Components in Chlorella sp KR1 via Subcritical Hydrothermal Liquefaction-
dc.typeArticle-
dc.identifier.wosid000407410900097-
dc.identifier.scopusid2-s2.0-85026999001-
dc.type.rimsART-
dc.citation.volume5-
dc.citation.issue8-
dc.citation.beginningpage7240-
dc.citation.endingpage7248-
dc.citation.publicationnameACS SUSTAINABLE CHEMISTRY & ENGINEERING-
dc.identifier.doi10.1021/acssuschemeng.7b01473-
dc.contributor.localauthorChang, Yong Keun-
dc.contributor.localauthorChoi, Minkee-
dc.contributor.nonIdAuthorOh, You-Kwan-
dc.description.isOpenAccessN-
dc.type.journalArticleArticle-
dc.subject.keywordAuthorHydrothermal liquefaction-
dc.subject.keywordAuthorMicroalgae-
dc.subject.keywordAuthorCarbohydrate-
dc.subject.keywordAuthorNutrient recycle-
dc.subject.keywordAuthorEnergy-
dc.subject.keywordPlusBIO-CRUDE OIL-
dc.subject.keywordPlusBIODIESEL PRODUCTION-
dc.subject.keywordPlusMAILLARD REACTION-
dc.subject.keywordPlusTHERMOCHEMICAL LIQUEFACTION-
dc.subject.keywordPlusORGANIC-SOLVENTS-
dc.subject.keywordPlusHIGH-TEMPERATURE-
dc.subject.keywordPlusALGAL BIOMASS-
dc.subject.keywordPlusLIPID-CONTENT-
dc.subject.keywordPlusFLOW REACTOR-
dc.subject.keywordPlusMICROALGAE-
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