La spéciation colloïdale des éléments traces métalliques (Cu, Pb et Cd) a été étudiée dans l'estuaire de la Penzé (Manche Occidentale, Bretagne) lors du cycle saisonnier. Cette étude a été réalisée afin de mieux comprendre les mécanismes responsables du transfert des métaux entre les différentes fractions (particulaire, colloïdale et réellement dissoute) lors du mélange des eaux. Deux techniques ont été utilisées : (i) l'ultrafiltration permettant le fractionnement en 7 fractions de taille différente et (ii) la chronopotentiométrie pour la détermination de la teneur en métal dans les différentes fractions. L'ultrafiltration a été choisie car c'est une méthode non destructive et de mise en oeuvre simple et peu coûteuse. Les limites de détection de la chronopotentiométrie ont été améliorées de façon à pouvoir doser les métaux dans les différentes fractions. Nos résultats ont montré une présence particulièrement importante des métaux (Cu, Pb, Cd) dans la fraction colloïdale. Si le Cd est trouvé dans la partie plutôt basse du spectre de taille colloïdal (<50 kDa), le Pb est par contre préférentiellement associé à des composés de haut poids moléculaire (>300 kDa). Quant au Cu, il présente une distribution intermédiaire. Lors du cycle saisonnier, deux phénomènes majeurs ont été identifiés : (i) une forte mobilisation des substances humiques depuis les sols du bassin versant à l'automne et (ii) la dégradation du matériel organique particulaire dans le compartiment benthique au printemps. Ces processus affectent non seulement la répartition colloïdale des éléments étudiés mais jouent également un rôle important dans les quantités et les formes transférées vers la zone côtière.

Les technologies à membranes sont en plein développement ; toutefois, les problèmes de colmatage limitent cette expansion. Les acides humiques présents dans les eaux naturelles induisent des chutes de production des membranes et sont à l'origine de fortes diminutions des durées de vie des matériaux filtrants. L'objectif principal de ce travail a été de développer une approche originale du colmatage de membranes basses pression d'ultrafiltration (UF). L'originalité de ce travail est de proposer plusieurs outils d'autopsie de membranes à deux échelles, l'une macroscopique (par des mesures de perméabilité hydraulique, dont sont déduites les résistances de colmatage et l'indice de colmatage MFI-UF) et l'autre microscopique (par la détermination de la dimension fractale des particules d'acides humiques et leurs agrégats déposés à la surface de la membrane). En utilisant une combinaison de ces outils macroscopiques, microscopiques et in situ, nous avons développé une nouvelle méthodologie pour l'analyse d'un gâteau d'acides humiques sur une membrane et ainsi permis d'évaluer plus finement que jusqu'ici la nature, les mécanismes, et les conséquences du colmatage de membranes basses pression. Cette méthode a été appliquée aux fibres creuses (vierge et colmaté par l'eau de surface naturelle), combinées avec l'autopsie de membrane. De plus, un nouvel appareillage semi-automatique de la mesure du potentiel d'écoulement, mise au point par nos soins, a permis de réaliser des investigations à l'intérieur de la structure de la membrane afin d'y déceler le cas échéant la présence de matière organiques naturelles (MON). La dernière partie est consacrée à une étude du prétraitement d'une solution d'acides humiques en présence de.bentonite modifiée (dénommée mont-Al-CTAB) afin de tenter de limiter le colmatage par les MON. La méthode de prétraitement employant la bentonite s'est avérée efficace en réduisant la résistance totale du gâteau d'acides humiques, en particulier en provoquant la diminution de la dimension fractale du gâteau formé en présence de bentonite.

Les propriétés complexantes de deux polymères, l'un d'origine biologique (le chitosane) l'autre synthétique (la polyethyleneimine, PEI), ont été mises à profit pour fixer des ions métalliques, au premier rang desquels le mercure. Le procédé de couplage complexation-ultrafiltration permet dans des conditions expérimentales optimisées, d'atteindre des taux de rétention supérieurs à 95 %. Si l'efficacité du chitosane est fortement contrôlée par le pH : rétention négligeable à pH inférieur à 4, et optimale à pH proche de 5,5 ; dans le cas de la PEI, l'influence du pH est moins marqué. La rétention du mercure a été testée dans des solutions binaires (Ni, Zn, Pb et Cu). Les deux macroligands montrent une nette préférence pour le mercure vis-à-vis de métaux tels que Zn, Ni et Pb. Le modèle de filtration sur gâteau se révèle logiquement le plus approprié pour modéliser le colmatage dans le cas de ces expériences menées sur une cellule d'ultrafiltration statique.

In the production of biodiesel via the transesterification of vegetable oils, purification to international standards is challenging. A key measure of biodiesel quality is the level of free glycerol in the biodiesel. In order to remove glycerol from fatty acid methyl ester (FAME or biodiesel), a membrane separation setup was tested. The main objective of this thesis was to develop a membrane process for the separation of free glycerol dispersed in FAME after completion of the transesterification reaction and to investigate the effect of different factors on glycerol removal. These factors included membrane pore size, pressure, temperature, and methanol, soap and water content. First, a study of the effect of different materials present in the transesterification reaction, such as water, soap, and methanol, on the final free glycerol separation was performed using a modified polyacrylonitrile (PAN) membrane, with 100 kD (ultrafiltration) molecular weight cut off for all runs at 25°C. Results showed low concentrations of water had a considerable effect in removing glycerol from the FAME. The mechanism of separation of free glycerol from FAME was due to the removal of an ultrafine dispersed glycerol-rich phase present in the untreated (or raw) FAME. The size of the droplets and the free glycerol separation both increased with increasing water content of the FAME. Next, three types of polymeric membranes in the ultrafiltration range with different molecular weight cut off, were tested at three fixed operating pressures and three operating temperatures (0, 5 and 25oC) to remove the free glycerol from a biodiesel reactor effluent. The ASTM standard for free glycerol concentration was met for the experiments performed at 25°C. The results of this study indicate that glycerol could be separated from raw FAME to meet ASTM and EN standards at methanol feed concentrations of up to 3 mass%. The process was demonstrated to rely on the formation of a dynamic polar layer on the membrane surface. Ceramic membranes of different pore sizes (0.05 µm (ultrafiltration (UF) range) and 0.2 µm (microfiltration (MF) range)) were used to treat raw FAME directly using the membrane separation set up at temperatures of 0, 5 and 25°C. The results were encouraging for the 0.05 µm pore size membrane at the highest temperature (25°C). The effect of temperature on glycerol removal was evident from its relation with the concentration factor (CF). Higher temperatures promoted the achievement of the appropriate CF value sooner for faster separation. Membrane pore size was also found to affect separation performance. A subsequent study revealed the effect of different variables on the size of the glycerol droplets using dynamic light scattering (DLS). A key parameter in the use of membrane separation technology is the size of the glycerol droplets and the influence of other components such as water, methanol and soaps on that droplet size. The effect of water, methanol, soap and glycerol on the size of suspended glycerol droplets in FAME was studied using a 3-level Box-Behnken experimental design technique. Standard statistical analysis techniques revealed the significant effect of water and glycerol on increasing droplet size while methanol and soap served to reduce the droplet size. Finally, a study on the effect of trans-membrane pressure (TMP) at different water concentrations in the FAME phase on glycerol removal using UF (0.03 µm pore size, polyethersulfone (PES)) and MF (0.1 and 0.22 µm pore sizes, PES) membranes at 25, 40 and 60°C was performed. Results showed that running at 25°C for the two membrane types produced the best results for glycerol removal and exceeded the ASTM and EN standards. An enhancement of glycerol removal was found by adding small amounts of water up to the maximum solubility limit in biodiesel. An increase in temperature resulted in an increase in the solubility of water in the FAME and less effective glycerol removal. Application of cake filtration theory and a gel layer model showed that the gel layer on the membrane surface is not compressible and the specific cake resistance and gel layer concentration decrease with increasing temperature. An approximate value for the limiting (steady-state) flux was reported and it was found that the highest fluxes were obtained at the lowest initial water concentrations at fixed temperatures. In conclusion, dispersed glycerol can be successfully removed from raw FAME (untreated FAME) using a membrane separation system to meet the ASTM biodiesel fuel standards. The addition of water close to the solubility limit to the FAME mixture enables the formation of larger glycerol droplets and makes the separation of these droplets straightforward.

In the production of biodiesel via the transesterification of vegetable oils, purification to international standards is challenging. A key measure of biodiesel quality is the level of free glycerol in the biodiesel. In order to remove glycerol from fatty acid methyl ester (FAME or biodiesel), a membrane separation setup was tested. The main objective of this thesis was to develop a membrane process for the separation of free glycerol dispersed in FAME after completion of the transesterification reaction and to investigate the effect of different factors on glycerol removal. These factors included membrane pore size, pressure, temperature, and methanol, soap and water content. First, a study of the effect of different materials present in the transesterification reaction, such as water, soap, and methanol, on the final free glycerol separation was performed using a modified polyacrylonitrile (PAN) membrane, with 100 kD (ultrafiltration) molecular weight cut off for all runs at 25°C. Results showed low concentrations of water had a considerable effect in removing glycerol from the FAME. The mechanism of separation of free glycerol from FAME was due to the removal of an ultrafine dispersed glycerol-rich phase present in the untreated (or raw) FAME. The size of the droplets and the free glycerol separation both increased with increasing water content of the FAME. Next, three types of polymeric membranes in the ultrafiltration range with different molecular weight cut off, were tested at three fixed operating pressures and three operating temperatures (0, 5 and 25oC) to remove the free glycerol from a biodiesel reactor effluent. The ASTM standard for free glycerol concentration was met for the experiments performed at 25°C. The results of this study indicate that glycerol could be separated from raw FAME to meet ASTM and EN standards at methanol feed concentrations of up to 3 mass%. The process was demonstrated to rely on the formation of a dynamic polar layer on the membrane surface. Ceramic membranes of different pore sizes (0.05 µm (ultrafiltration (UF) range) and 0.2 µm (microfiltration (MF) range)) were used to treat raw FAME directly using the membrane separation set up at temperatures of 0, 5 and 25°C. The results were encouraging for the 0.05 µm pore size membrane at the highest temperature (25°C). The effect of temperature on glycerol removal was evident from its relation with the concentration factor (CF). Higher temperatures promoted the achievement of the appropriate CF value sooner for faster separation. Membrane pore size was also found to affect separation performance. A subsequent study revealed the effect of different variables on the size of the glycerol droplets using dynamic light scattering (DLS). A key parameter in the use of membrane separation technology is the size of the glycerol droplets and the influence of other components such as water, methanol and soaps on that droplet size. The effect of water, methanol, soap and glycerol on the size of suspended glycerol droplets in FAME was studied using a 3-level Box-Behnken experimental design technique. Standard statistical analysis techniques revealed the significant effect of water and glycerol on increasing droplet size while methanol and soap served to reduce the droplet size. Finally, a study on the effect of trans-membrane pressure (TMP) at different water concentrations in the FAME phase on glycerol removal using UF (0.03 µm pore size, polyethersulfone (PES)) and MF (0.1 and 0.22 µm pore sizes, PES) membranes at 25, 40 and 60°C was performed. Results showed that running at 25°C for the two membrane types produced the best results for glycerol removal and exceeded the ASTM and EN standards. An enhancement of glycerol removal was found by adding small amounts of water up to the maximum solubility limit in biodiesel. An increase in temperature resulted in an increase in the solubility of water in the FAME and less effective glycerol removal. Application of cake filtration theory and a gel layer model showed that the gel layer on the membrane surface is not compressible and the specific cake resistance and gel layer concentration decrease with increasing temperature. An approximate value for the limiting (steady-state) flux was reported and it was found that the highest fluxes were obtained at the lowest initial water concentrations at fixed temperatures. In conclusion, dispersed glycerol can be successfully removed from raw FAME (untreated FAME) using a membrane separation system to meet the ASTM biodiesel fuel standards. The addition of water close to the solubility limit to the FAME mixture enables the formation of larger glycerol droplets and makes the separation of these droplets straightforward.

An investigation was conducted focusing on how NOM affects coagulation in a United States south eastern coastal surface water. Current water treatment practice at Savannah Water I and D was investigated to determine the efficacy of NOM removal using existing coagulation methods. A robust assessment of alum and ferric sulfate for use as coagulants in the removal of disinfection byproduct (DBP) precursor material was conducted using composite water created from sample sites within the SWID watershed. Both coagulants were optimized for the removal of NOM. Pragmatic methods of NOM size analysis and its reactivity with chlorine was investigated. UF membranes were used in conjunction with a permeation coefficient model (PCM) to determine an apparent molecular weight distribution of NOM present in the watershed. Individual size classes were assessed for their potential to form trihalomethanes (THMs) upon chlorination. Coagulation using alum and ferric sulfate was assessed to determine removal efficiency of individual NOM size classes under various coagulation scenarios. Finally, UV254 absorbance (UVA) was assessed to determine its potential use as an indicator of DOC concentration in raw and treated water at SWID. Additionally, an investigation into the relationship between specific UVA (SUVA) and THM formation potential (THM-FP) was conducted.

In this study, resolution of racemic mandelic acid by enyzme enhanced ultrafiltration (EEUF) was studied. In order to develop a methodology, bovine serum albumin (BSA) was used as a model protein for polymer enhanced ultrafiltration (PEUF) experiments and the enzyme S-mandelate dehydrogenase was used for EEUF experiments. To be used for enzyme enhanced ultrafiltration experiments, the gene which is responsible from the production of S-mandelate dehydrogenase was isolated from Pseudomonas putida, expressed in Escherichia coli and the recombinant enzyme was produced. For PEUF experiments, effects of pH and ligand ratio were investigated. Total retention of mandelic acid increased with decrease in pH and total retention of mandelic acid reached to a maximum value of 74.4% at pH 4.3. For EEUF experiments, pH and ligand ratio effect on total retention, enantiomeric excess, enantioselectivity were investigated. Although apoenzyme was tried to be obtained by diafiltration and conversion was tried to be prevented, conversion occured especially at high pH values. To create the apoenzyme effect, three methods were studied. Enzyme conversion was prevented by sodium sulfite inhibition but enzyme did not retain mandelic acid. By oxygen saturation of enzyme, conversion was prevented, binding was achieved but enzyme showed no enantioselectivity. When the enzyme was diafiltrated at pH 10.0, total mandelic acid retention, enantiomeric excess and enantioselectivity reached to 77.2%, 38.9%, 2.27, respectively and the enzyme selectivity was reversed as R-selective.

Kidney bean proteins and peptides can be developed to serve as an important ingredient for the formulation of high quality foods or therapeutic products that may positively impact on body function and human health. The main goal of this thesis was to determine the in vitro structural and functional characteristics of major proteins and enzymatic protein hydrolysate of red kidney bean (Phaseolus vulgaris). Selective aammonium sulfate precipitation of the kidney bean proteins yielded 88% globulin and 7% albumin.The globulin and albumin are glycoproteins that contained ~4% and 45% carbohydrate contents, respectively. Physicochemical and functional characteristics of the globulin fraction, such as, gelation concentration, foam stability, emulsion capacity, and emulsion stability were superior to those of albumin. Reducing SDS-PAGE revealed vicilin with molecular weight of ~45 kDa as the major globulin in kidney beans. Circular dichroism spectroscopy of the purified vicilin showed reductions in α-helix, and β-pleated sheet conformations upon addition of NaCl or changes in pH. Likewise, the tertiary structures as observed from the near-UV CD spectra were also changed by shifts in pH conditions and NaCl addition. Far UV-CD showed increased β-sheet content up till 60oC from room temperature, but a steady loss in the tertiary structure as temperature was further increased; however, β-sheet structure was still detectable at 80oC. Differential scanning calorimetry thermograms showed a prominent endothermic peak with denaturation temperature at around 90oC, attributed to thermal denaturation of vicilin. Alcalase hydrolysis of kidney bean globulin produced multifunctional peptides that showed potential antihypertensive properties because of the in vitro inhibition of activities of renin and angiotensin I converting enzyme as well as the antioxidant properties. The <1 and 5-10 kDa peptide fractions exhibited highest (p<0.05) renin inhibition and the ability to scavenge 2, 2-Diphenyl-1-picrylhydrazyl free radical, inhibit peroxidation of linoleic acid and reduce Fe3+ to Fe2+. Based on this study, incorporation of kidney bean globulin as an ingredient may be useful for the manufacture of high quality food products. Likewise, the kidney bean protein hydrolysates, especially the <1 kDa fraction represent a potential source of bioactive peptides for the formulation of functional foods and nutraceuticals.

Ce mémoire est essentiellement consacré à la synthèse électrochimique et à la caractérisation structurale de matériaux composites d'électrode nanostructurés du type polymère fonctionnalisé contenant une dispersion homogène de nanoparticules d'oxydes de ruthénium ou d'iridium, ainsi qu'à l'étude de leurs propriétés électrocatalytiques vis-à-vis de l'oxydation en milieu aqueux de l'arsenic(III) en arsenic(V). La combinaison de l'oxydation électrocatalytique de l'arsenic(III) avec la technique d'ultrafiltration LPR (Liquid phase Polymer-assisted Retention) nous a permis de confirmer tout l'intérêt de cette approche combinée pour éliminer l'arsenic. Dans ce processus, les matériaux nanocomposites à base d'oxyde d'iridium ont montré les propriétés les plus intéressantes, car ils sont capables de catalyser l'oxydation de l'arsénite en milieu neutre et à des potentiels peu positifs. Enfin, les matériaux d'électrode nanostructurés à base d'oxyde d'iridium sont également efficaces pour l'oxydation catalytique à 4 électrons de l'eau en dioxygène et présentent donc un fort intérêt potentiel dans le contexte de la réaction de dissociation de l'eau. Mots clés : oxyde de ruthénium, oxyde d'iridium, nanocomposite, électrocatalyse, arsenic, ultrafiltration, oxydation de l'eau

In the production of biodiesel via the transesterification of vegetable oils, purification to international standards is challenging. A key measure of biodiesel quality is the level of free glycerol in the biodiesel. In order to remove glycerol from fatty acid methyl ester (FAME or biodiesel), a membrane separation setup was tested. The main objective of this thesis was to develop a membrane process for the separation of free glycerol dispersed in FAME after completion of the transesterification reaction and to investigate the effect of different factors on glycerol removal. These factors included membrane pore size, pressure, temperature, and methanol, soap and water content. First, a study of the effect of different materials present in the transesterification reaction, such as water, soap, and methanol, on the final free glycerol separation was performed using a modified polyacrylonitrile (PAN) membrane, with 100 kD (ultrafiltration) molecular weight cut off for all runs at 25°C. Results showed low concentrations of water had a considerable effect in removing glycerol from the FAME. The mechanism of separation of free glycerol from FAME was due to the removal of an ultrafine dispersed glycerol-rich phase present in the untreated (or raw) FAME. The size of the droplets and the free glycerol separation both increased with increasing water content of the FAME. Next, three types of polymeric membranes in the ultrafiltration range with different molecular weight cut off, were tested at three fixed operating pressures and three operating temperatures (0, 5 and 25oC) to remove the free glycerol from a biodiesel reactor effluent. The ASTM standard for free glycerol concentration was met for the experiments performed at 25°C. The results of this study indicate that glycerol could be separated from raw FAME to meet ASTM and EN standards at methanol feed concentrations of up to 3 mass%. The process was demonstrated to rely on the formation of a dynamic polar layer on the membrane surface. Ceramic membranes of different pore sizes (0.05 µm (ultrafiltration (UF) range) and 0.2 µm (microfiltration (MF) range)) were used to treat raw FAME directly using the membrane separation set up at temperatures of 0, 5 and 25°C. The results were encouraging for the 0.05 µm pore size membrane at the highest temperature (25°C). The effect of temperature on glycerol removal was evident from its relation with the concentration factor (CF). Higher temperatures promoted the achievement of the appropriate CF value sooner for faster separation. Membrane pore size was also found to affect separation performance. A subsequent study revealed the effect of different variables on the size of the glycerol droplets using dynamic light scattering (DLS). A key parameter in the use of membrane separation technology is the size of the glycerol droplets and the influence of other components such as water, methanol and soaps on that droplet size. The effect of water, methanol, soap and glycerol on the size of suspended glycerol droplets in FAME was studied using a 3-level Box-Behnken experimental design technique. Standard statistical analysis techniques revealed the significant effect of water and glycerol on increasing droplet size while methanol and soap served to reduce the droplet size. Finally, a study on the effect of trans-membrane pressure (TMP) at different water concentrations in the FAME phase on glycerol removal using UF (0.03 µm pore size, polyethersulfone (PES)) and MF (0.1 and 0.22 µm pore sizes, PES) membranes at 25, 40 and 60°C was performed. Results showed that running at 25°C for the two membrane types produced the best results for glycerol removal and exceeded the ASTM and EN standards. An enhancement of glycerol removal was found by adding small amounts of water up to the maximum solubility limit in biodiesel. An increase in temperature resulted in an increase in the solubility of water in the FAME and less effective glycerol removal. Application of cake filtration theory and a gel layer model showed that the gel layer on the membrane surface is not compressible and the specific cake resistance and gel layer concentration decrease with increasing temperature. An approximate value for the limiting (steady-state) flux was reported and it was found that the highest fluxes were obtained at the lowest initial water concentrations at fixed temperatures. In conclusion, dispersed glycerol can be successfully removed from raw FAME (untreated FAME) using a membrane separation system to meet the ASTM biodiesel fuel standards. The addition of water close to the solubility limit to the FAME mixture enables the formation of larger glycerol droplets and makes the separation of these droplets straightforward.