dc.creatorClauser, Nicolás Martín
dc.creatorArea, Maria Cristina
dc.creatorFelissia, Fernando Esteban
dc.creatorVallejos, María Evangelina
dc.creatorGutiérrez, Soledad
dc.date.accessioned2019-10-28T20:41:17Z
dc.date.accessioned2022-10-15T13:24:11Z
dc.date.available2019-10-28T20:41:17Z
dc.date.available2022-10-15T13:24:11Z
dc.date.created2019-10-28T20:41:17Z
dc.date.issued2018-11
dc.identifierClauser, Nicolás Martín; Area, Maria Cristina; Felissia, Fernando Esteban; Vallejos, María Evangelina; Gutiérrez, Soledad; Techno-economic assessment of carboxylic acids, furfural, and pellet production in a pine sawdust biorefinery; John Wiley & Sons Ltd; Biofuels Bioproducts & Biorefining-biofpr; 12; 6; 11-2018; 997-1012
dc.identifier1932-104X
dc.identifierhttp://hdl.handle.net/11336/87438
dc.identifier1932-1031
dc.identifierCONICET Digital
dc.identifierCONICET
dc.identifier.urihttps://repositorioslatinoamericanos.uchile.cl/handle/2250/4391040
dc.description.abstractPine sawdust is an important lignocellulosic waste from the primary industrialization of wood, and its valorization using the biorefinery concept could add new value chains to the forest industry. Compared with large-scale biorefineries, small-scale ones involve lower capital and logistics costs, lower risk, and can increase the use of labor in rural areas. A scheme was proposed for the use of the hemicelluloses obtained from the spent liquor of a steam explosion pretreatment of pine sawdust. With the proposed scheme, levulinic acid (LA), formic acid (FA), acetic acid and furfural are obtained from the liquid fraction while pellets are produced from the solid fraction. This pine sawdust biorefinery allows about 747 kg of pellets, 57 kg of LA, 23 kg of FA, 18 kg of acetic acid, and 22 kg of furfural per 1000 kg of dry sawdust to be obtained. The energy used for LA production is one of the main production costs. When 95% of the residual solid is used to generate steam, there is an improvement in the internal rate of return (IRR). The heat integration allows a reduction of 10% in the steam consumption for LA, increasing the capacity for pellet production. The results obtained are therefore essential when seeking alternatives for pine sawdust biorefineries, focusing on the improvement of the production processes, satisfaction of energy requirements, and the reduction of the recovery costs. Three alternatives for the valorization of pine sawdust were analyzed and the best of them obtained an IRR of about 17%.
dc.languageeng
dc.publisherJohn Wiley & Sons Ltd
dc.relationinfo:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/10.1002/bbb.1915
dc.relationinfo:eu-repo/semantics/altIdentifier/url/https://onlinelibrary.wiley.com/doi/abs/10.1002/bbb.1915
dc.rightshttps://creativecommons.org/licenses/by/2.5/ar/
dc.rightsinfo:eu-repo/semantics/restrictedAccess
dc.subjectBIOREFINERY
dc.subjectLEVULINIC ACID
dc.subjectPELLETS
dc.subjectPINE SAWDUST
dc.subjectSTEAM EXPLOSION
dc.subjectTECHNO-ECONOMIC ASSESSMENT
dc.titleTechno-economic assessment of carboxylic acids, furfural, and pellet production in a pine sawdust biorefinery
dc.typeinfo:eu-repo/semantics/article
dc.typeinfo:ar-repo/semantics/artículo
dc.typeinfo:eu-repo/semantics/publishedVersion


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