Phase Equilibria for extraction processes with designer solvents

dc.contributor.advisorArce Arce, Alberto
dc.contributor.advisorSoto Campos, Ana María
dc.contributor.authorLago García de Dios, Sara
dc.contributor.otherE.T.S. de Enxeñaría. Departamento de Enxeñaría Química
dc.date.accessioned2013-12-27T09:06:05Z
dc.date.available2013-12-27T09:06:05Z
dc.date.issued2013-12-27
dc.description.abstractIn recent years, there has been an increasing concern about the effects of toxic chemicals in the environment. In response to this concern, there is a growing impetus to develop chemical manufacturing processes which can reduce or eliminate the use or generation of hazardous substances. Within this aspect of green chemistry, in this Thesis, Ionic Liquids (ILs) and Deep Eutectic Solvents (DESs) have been tested as greener alternatives in different chemical processes. In a first stage, the capability of using ILs as solvents for citrus essential oil deterpenation by liquid-liquid extraction was investigated. The liquid-liquid equilibria of ternary systems limonene + linalool + IL were determined. Results were analysed in terms of the solute distribution ratio and selectivity, allowing to draw conclusions about the influence of the structure of the ILs in these thermodynamic parameters. Experimental data were correlated by means of the NRTL and UNIQUAC equations. To evaluate the capability of some ILs to act as surfactants in Enhanced Oil Recovery, two of these salts showing surfactant behaviour were tested. Liquid-liquid equilibria of ternary systems water + IL + ndodecane were determined. Winsor Type III systems were found, and the interfacial tensions between phases were measured to prove the ability of these salts to reduce the water – oil interfacial tension. Physical and transport properties of the phases involved, such as density and viscosity, were also experimentally measured. In a last stage, an introductory study on the processing of lignocellulosic biomass with DESs was carried out. Different renewable DESs were prepared from hydrogen bond donor and hydrogen bond acceptor starting materials. Solubility tests of pine wood and wheat straw in these solvents were carried out. From the thermodynamic studies that were carried out in this Thesis, it turns out that designer solvents can be used to develop greener and/or more efficient chemical processes.gl
dc.identifier.urihttp://hdl.handle.net/10347/9570
dc.language.isoenggl
dc.rightsEsta obra atópase baixo unha licenza internacional Creative Commons BY-NC-ND 4.0. Calquera forma de reprodución, distribución, comunicación pública ou transformación desta obra non incluída na licenza Creative Commons BY-NC-ND 4.0 só pode ser realizada coa autorización expresa dos titulares, salvo excepción prevista pola lei. Pode acceder Vde. ao texto completo da licenza nesta ligazón: https://creativecommons.org/licenses/by-nc-nd/4.0/deed.gl
dc.rights.accessRightsopen accessgl
dc.rights.urihttps://creativecommons.org/licenses/by-nc-nd/4.0/deed.gl
dc.subjectExtractiongl
dc.subjectEquilibriumgl
dc.subjectDesigner solventsgl
dc.titlePhase Equilibria for extraction processes with designer solventsgl
dc.typedoctoral thesisgl
dspace.entity.typePublication
relation.isAdvisorOfPublication4dd7270b-22f8-4644-b998-a73d35611e7a
relation.isAdvisorOfPublicationa49ac854-c7ed-48d8-b8d5-f5dae9f9b77a
relation.isAdvisorOfPublication.latestForDiscovery4dd7270b-22f8-4644-b998-a73d35611e7a

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