dc.creatorBusto, Mariana
dc.creatorSepulveda Flores, Jorge Humberto
dc.creatorCarrara, Nicolás Ricardo
dc.creatorVera, Carlos Roman
dc.date.accessioned2018-01-30T15:49:06Z
dc.date.accessioned2018-11-06T11:38:03Z
dc.date.available2018-01-30T15:49:06Z
dc.date.available2018-11-06T11:38:03Z
dc.date.created2018-01-30T15:49:06Z
dc.date.issued2015-01
dc.identifierBusto, Mariana; Sepulveda Flores, Jorge Humberto; Carrara, Nicolás Ricardo; Vera, Carlos Roman; Adsorption of Aromatics from Base Oil over Polymeric Resins. Equilibrium and kinetics.; American Chemical Society; Energy & Fuels (print); 29; 2; 1-2015; 1249-1256
dc.identifier0887-0624
dc.identifierhttp://hdl.handle.net/11336/34990
dc.identifierCONICET Digital
dc.identifierCONICET
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1856383
dc.description.abstractAdsorption of aromatic molecules from base oil over an acid resin (Amberlyst 15w) was studied, with a focus on reducing the aromatic content to that of a white mineral oil. It was found that the adsorption capacity of the resin was low. At saturation in the best condition the adsorption capacity corresponded to 10% de acid capacity. The effects of dilution, temperature and adsorption time were studied.In the absence of a diluting solvent the isotherm was unfavorable and the adsorption rate was low with a pseudo first order constant of about 0.1 h-1. Dilution of the oil with n-hexane had beneficial effects on the adsorption capacity, the adsorption rate and the yield of refined oil. The 1:1 (vol:vol) dilution was found to be optimal. Kinetic data were better explained by a model of dominant intraparticle diffusion, the adsorbate load being proportional to the square of the adsorption time. Dilution with n-hexane was thought to decrease the viscosity with a proportional increase of the diffusivity, and a decrease of the chemical affinity of the oil matrix.Estimations of the oil purity and refined oil yield after a series of equilibrium stages indicated that 3 stages with an adsorbent-to-oil ratio of 0.5 (g g-1) and a 1:1 dilution in nhexane could refine the studied base oil (initial aromatics content 0.136 mmol g-1) to a white mineral oil of food grade, with a yield of about 60%. Removal of the solvent was considered easy given the high volatility of n-hexane as compared to the oil.
dc.languagespa
dc.publisherAmerican Chemical Society
dc.relationinfo:eu-repo/semantics/altIdentifier/url/http://pubs.acs.org/doi/pdfplus/10.1021/ef502106n
dc.relationinfo:eu-repo/semantics/altIdentifier/doi/http://dx.doi.org/ 10.1021/ef502106n
dc.rightshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.rightsinfo:eu-repo/semantics/restrictedAccess
dc.subjectADSORPTION
dc.subjectPOLYMERIC RESINS
dc.subjectAROMATICS
dc.subjectKINETICS
dc.titleAdsorption of Aromatics from Base Oil over Polymeric Resins. Equilibrium and kinetics.
dc.typeArtículos de revistas
dc.typeArtículos de revistas
dc.typeArtículos de revistas


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