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dc.contributor.authorVan der Gryp, Percy
dc.contributor.authorBaumgarten, Ulrich
dc.contributor.authorMarx, Sanette
dc.contributor.authorSchabort, Corneels
dc.date.accessioned2020-09-01T10:59:43Z
dc.date.available2020-09-01T10:59:43Z
dc.date.issued2011
dc.identifier.citationVan der Gryp, P. et al. 2011. Bio-oil and bio-char production from sunflower hulls. Proceedings 19th European Biomass Conference and Exhibition, 6-10 June, Berlin, Germany: 1168-1171. [https://doi.org/10.5071/19thEUBCE2011-OB8.5]en_US
dc.identifier.isbn978-88-89407-55-4
dc.identifier.issn2282-5819
dc.identifier.urihttp://hdl.handle.net/10394/35680
dc.identifier.urihttp://www.etaflorence.it/proceedings/index.asp?detail=6494
dc.identifier.urihttps://doi.org/10.5071/19thEUBCE2011-OB8.5
dc.description.abstractIn this paper, the hydrothermal liquefaction of sunflower hulls into bio­oil and bio­char is presented. The main manipulated variables that were studied were biomass load, catalyst type and temperature. The experimental results show that an increase in temperature, increases bio­oil yield and decreases bio­char yield. An increase in biomass load decreases bio­oil yield. The highest bio­oil yield was observed when sodium carbonate was used as catalyst. The bio­oil yield was low in all instances with a maximum oil yield of 4.7 wt% at 340 ºC and 30 wt% biomass load. The bio­char yield showed very high yields with a maximum yield of 62 wt% at 280 ºC and 30 wt% biomass load. This study shows that liquefaction of sunflower hulls is a viable option for the production of bio­ charen_US
dc.language.isoenen_US
dc.publisherETA-Florence Renewable Energiesen_US
dc.subjectLiquefactionen_US
dc.subjectSunfloweren_US
dc.subjectBio-charen_US
dc.titleBio-oil and bio-char production from sunflower hullsen_US
dc.typePresentationen_US
dc.contributor.researchID10216847 - Marx, Sanette
dc.contributor.researchID11328819 - Van der Gryp, Percy
dc.contributor.researchID12380687 - Schabort, Cornelis Johannes


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