Search results for "Phase behaviour"

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Transesterification of rapeseed oil over acid resins promoted by supercritical carbon dioxide

2011

The methanolysis of rapeseed oil catalyzed by commercial styrene-divinylbenzene macroporous acid resins was performed in a batch reactor at 100-140 °C and 10-46 MPa to study the effect of supercritical carbon dioxide (scCO2) on the performances of the process. Reaction temperatures of 120-140 °C were necessary to obtain high enough yields of fatty acid methyl esters. Upon addition of scCO2 faster transesterification kinetics was obtained also at the lowest investigated operating pressure (10-11 MPa), working in two fluid phase systems. Experiments performed changing the reaction time indicated that most of the esters were formed during the first 3 h. When the pressure was increased at 38-46…

General Chemical EngineeringMethanolysiKineticsBatch reactorOperating pressurePolymeric acidHeterogeneous catalysisCatalysiCatalysisHeterogeneous catalysiIon exchange resinSupercritical carbon dioxideOrganic chemistryFatty acid methyl esterRapeseed oilEsterPhysical and Theoretical ChemistryVegetable oils Supercritical fluid extractionIon-exchange resinStyreneReaction systemReaction timeBiodieselFluid phasiTwo-fluid Batch reactorSupercritical carbon dioxideEsterificationChemistryReaction kineticTransesterificationSettore ING-IND/27 - Chimica Industriale E TecnologicaFatty acidCondensed Matter PhysicsPhase behaviourTransesterificationCarbon dioxideReaction temperatureMacroporouStyrene-divinylbenzeneBiodieselEnhancement effectIon exchangeThe Journal of Supercritical Fluids
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