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dc.contributor.authorSravanthi Veluturla, Kailasen
dc.contributor.authorArchna Narulaen
dc.contributor.authorSubba Rao Den
dc.contributor.authorShetty, Sunianaen
dc.date.accessioned2018-08-31T04:02:37Z-
dc.date.available2018-08-31T04:02:37Z-
dc.date.issued2017-
dc.identifier.citationKinetic study of synthesis of bio-fuel additives from glycerol using a hetropolyacid / Sravanthi Veluturla [et al.] // Resource-Efficient Technologies. — 2017. — Vol. 3, iss. 3. — [P. 337-341].en
dc.identifier.issn2405-6537-
dc.identifier.urihttp://earchive.tpu.ru/handle/11683/50311-
dc.description.abstractConcerns about the ever increasing quantities of glycerol produced as a by-product of the process of manufacture of bio-diesel serve as a fuel for research about the alternative uses of glycerol. The esterification of glycerol with acetic acid over Cesium supported heteropolyacid (CsPWA) serving as the catalyst was carried out. The products obtained were mono, di and tri acetins which have wide application as biofuels. A series of experiments were carried out with CsPWA as catalyst and parameters considered for studies were temperature, molar ratio of reactants (acetic acid:glycerol) and the catalyst loading weight percent. Each parameter was varied keeping the other two constant and the results were recorded. Temperature was varied from 80°C to 110°C; molar ratio of glycerol to acetic acid is between 3:1 and 9:1 and catalyst loading of 3%w/w to 7%w/w. The yield and conversion varied for different conditions, but in general, the yield of diacetin and triacetin increased with time. Optimum parameters were adjudged to be 110°C with a molar ratio of 9:1 of the reactants and catalyst loading being 5% weight of reaction mixture where maximum glycerol conversion of 98% was obtained. The results obtained indicate that the esterification of glycerol with acetic acid is a consecutive reaction and the kinetic model was developed based on homogeneous first order reaction series by optimization method using MATLAB, and rate constants (k1, k2 and k3) were determined. From the rate constants at different temperatures, using Arrhenius equation the activation energies (E1, E2 and E3) were also determined.en
dc.format.mimetypeapplication/pdf-
dc.language.isoenen
dc.publisherТомский политехнический университетru
dc.relation.ispartofResource-Efficient Technologies. 2017. Vol. 3, iss. 3en
dc.rightsinfo:eu-repo/semantics/openAccessen
dc.sourceResource-Efficient Technologiesen
dc.subjectesterificationru
dc.subjectbiofuelru
dc.subjectproduct distributionru
dc.subjectactivation energyru
dc.subjectэтерификацияru
dc.subjectбиотопливоru
dc.subjectкинетическая модельru
dc.subjectэнергия активацииru
dc.titleKinetic study of synthesis of bio-fuel additives from glycerol using a hetropolyaciden
dc.typeArticleen
dc.typeinfo:eu-repo/semantics/publishedVersionen
dc.typeinfo:eu-repo/semantics/articleen
dcterms.audienceResearchesen
local.description.firstpage337-
local.description.lastpage341-
local.filepathhttps://doi.org/10.1016/j.reffit.2017.02.005-
local.identifier.bibrecRU\TPU\prd\274482-
local.issue3-
local.localtypeСтатьяru
local.volume3-
dc.identifier.doi10.1016/j.reffit.2017.02.005-
Располагается в коллекциях:Resource-Efficient Technologies

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