Pevaporation is a method for separating volatile components from liquid mixtures at ambient temperatures. The paint processing industry uses Hansen solubility parameters (HSP) to indicate polymer solubility. The potential of this method to predict solvent-polymer affinity was investigated for screening potential membrane materials for the pervaporation of a model solution containing linalool and linalyl acetate (major components of lavender essential oil), in ethanol. Published HSP values were collated for various polymers, and statistically analysed to determine variations in HSP values for polymer species. An investigation of published research into pervaporation of organic/organic binary solutions separated by homogeneous membranes indicated that the solvent whose HSP value was closest to that of the polymer would preferentially permeate. This relationship did not always hold for halogenated solvents or aqueous/organic solutions. Conflicting literature regarding the relationship between solvent uptake by polymers and HSP relative energy differences was resolved using a logarithmic relationship between these two parameters. The following membranes were selected, using their HSP to indicate their potential to interact with lavender oil components: Polyamide (PA: 26.9 micro;m), Polycarbonate (PC: 20.5 micro;m), Poly(ether imide) (PEI: 29.2 micro;m), Poly(ether sulphone) (PES: 27.6 micro;m), Polyethylene (HDPE: 10 micro;m, LDPE: 13-30 micro;m), Polyimide (PI: 30.0 micro;m), Poly(methyl methacrylate) (PMMA: 50 micro;m), Polypropylene (PP: 15.9 micro;m), and Poly(tetrafluoro ethylene) (PTFE: 26.7 micro;m). The HSP (dispersive, polar hydrogen bonding components) for each membrane were calculated using the mean value obtained from swelling experiments, group contribution (calculated using Hoftyzer-Van Krevelen, Hoy and Beerbower methods), refractive indices (dispersive component), dielectric constants (polar component), and published HSP values. Pervaporation experiments investigated the effect of membrane thickness, process temperature, permeate pressure, impinging jet heights, feed flow rates and concentrations, and pre-soaking the membrane; on flow rate and selectivity in a polyethylene membrane. Membrane thickness was the dominant factor in membrane selectivity; the thinnest membranes (11.3-14.8 micro;m) had much poorer selectivity than membranes gt;24.7 micro;m. Temperatures between 22-34ordm;C, permeate pressure lt;10 kPa, impinging jet heights between 0.36-3.36 mm, feed flow rates between 541-1328 mL/min and concentrations between 1.78-6.01 % v/v of linalool and linalyl acetate in ethanol did not significantly affect selectivity. Flow rates increased with operating temperature, permeate pressure, and impinging jet heights. However, feed flow rate and concentration had no effect on membrane flux rate. Pre-soaking the membrane reduced the time to reach steady-state. Selected membranes were further investigated under standard operating conditions (permeate temperature 30ordm;C, permeate pressure lt;10 kPa, impinging jet height 1.36 mm, feed flow rate 804 mL/min and feed concentration of 5% v/v of linalool and linalyl acetate in ethanol). PMMA completely disintegrated in feed solution, and PC was too brittle to make an effective homogeneous membrane. PA, PC, PEI and PTFE had the highest efficiency (selectivity x flow rate) in their homogeneous form. However, PEI, PI and PTFE had the greatest selectivity, thus further trials should be done to improve stability and flow rates through these membranes. Pervaporation selectivity did not always follow trends predicted by HSP. Although polymers such as PA, PEI, PES, and PI preferentially permeated linalool as predicted, PC, PP and PTFE did not preferentially permeate linalyl acetate. This may have been due to the difference in size and diffusivity of these molecules (linalyl acetate, the larger molecule, did not follow the sorption selectivity predictions), or reliability of literature HSP values and those calculated by group contribution. This research shows that HSP is a good screening method for pervaporation membranes, especially where the molecules being separated are of comparable size. Polymers that have HSP close to the desired component and not to other components tend to have the best selectivity and flux characteristics. However, diffusion is an important factor, and is not completely accounted for by HSP. Recommendations for further research include: carrying out pervaporation analyses of selected polymers using pure lavender essential oil; modifying polymers to form asymmetric or composite membranes with improved permeation characteristics; and potential use of thin channel inverse gas chromatography to determine a more accurate HSP which includes diffusivity.

La presente tesis estudia el desarrollo de tecnologías de separación y recuperación de aromas. Se busca obtener dos clases distintas de productos, concentrados aromáticos y bebidas parcialmente desalcoholizadas. En ambos productos se requiere una alta calidad aromática.Distintos casos de estudio se han seleccionado:i) La separación concentración del 2,4-decadienoato de etilo, aroma impacto de la pera, y ii) la separación-concentración del trans-2-hexen-1-ol, aroma impacto de los arándanos. En ambos casos, se tratan corrientes acuosas de la etapa de concentración de zumos en la indsutria. Para el estudio de la separación /concentración del aroma de pera se aplica adsorción en Carbón Activo Granular y Destilación con Membranas a Vacío, y para el aroma del arándano se selecciona la Pervaporación. Para todos estos casos se analiza el rendimiento del proceso y se desarrolla el modelo matemático obteniéndose sus principales parámetros de transporte.iii) La reducción del contenido de etanol en vino mediante Destilación Osmótica. Se ha desarrollado el modelo matemático que describe el transporte del etanol y los compuestos aromáticos. La validación del modelo y el análisis sensorial se llevaron a cabo mediante vino real. / The thesis document deals with the development of technologies for the separation and recovery of aromatic compounds. Two different kind of products are sought, aroma concentrates from fruit juices and partially de-alcoholised beverages. On both products high aromatic quality is required.Several cases of study have been selected: i) The separation of separation-concentration of ethyl E-2, Z-4-decadienoato, pear impact aroma compound, and ii) separation-concentration of E-2-hexen-1-ol, bilberries impact aroma compound. In both cases, aqueous streams to be treated in the industry would come from the juice concentration stage. The study of the separation and concentration of the pear aroma compound was made by using Adsorption onto Granular Activated Carbon and Vacuum Membrane Distillation, and for the bilberry aroma compound, Pervaporation was selected. For all of these cases of study, the performance analysis and mathematical modeling have been performed and the main transport parameters.iii) The reduction of the alcohol content of wine by Osmotic Distillation. A mathematical model describing both the ethanol and aroma compounds transport was developed. Model validation and sensorial analysis on real wine were made.