Conselho Nacional de Desenvolvimento Científico e Tecnológico / A biossorção é o termo aplicado à tecnologia de adsorção de íons metálicos em solução, por meio de materiais de natureza biológica inativa, comparável à adsorção utilizando-se adsorventes convencionais. A biossorção depende da temperatura, pH, concentração inicial do íon metálico, e tipo de biosorvente. O objetivo principal dessa dissertação é estudar e comparar os processos de adsorção de cobre iônico a partir de soluções aquosas utilizando Sargassum sp., alginato de cálcio úmido e desidratado e carvão ativo em pó e granular, em regime de batelada e contínuo. O alginato de cálcio foi preparado através de uma solução 4% (m/v) de alginato de sódio gotejada em solução 37% (m/v) de cloreto de cálcio dihidratado. O alginato de cálcio apresentou uma umidade de 89% após secagem em estufa a 100C por 24 horas. Os parâmetros da biossorção foram fixados em: a dose de adsorventes de 2 g/L; a temperatura em 30C; pH da solução em 5,0; e velocidade de rotação da chapa rotatória em 150 rpm. Para os estudos de cinética e equilíbrio, os ensaios foram feitos em regime de batelada. Nos ensaios cinéticos para duas concentrações medias (0,16 e 3,15 mmol/L) variou-se o tempo de contato (1 a 120 min) para se atingir o equilíbrio. Nos ensaios de equilíbrio variou-se as concentrações (0,16 a 15,72 mmol/L) utilizando o tempo de equilíbrio determinado nos ensaios cinéticos. Foram utilizadas duas modelagens cinéticas (a de pseudo-primeira ordem e a de segunda ordem) e duas modelagens do equilíbrio (Langmuir e Freundlich). O modelo cinético de segunda ordem ajustou melhor os resultados. O tempo de equilíbrio para adsorção do cobre foi de 60 minutos para Sargassum sp. e pellets de alginatos de cálcio úmido e desidratado. Para os carvões ativos os tempos de equilíbrio para a adsorção do cobre foram mais rápidos, mas a capacidade de remoção do cobre foram muito baixas. Com base nos resultados desfavoráveis obtidos para os carvões ativos eles foram descartados para se prosseguir com os ensaios de equilíbrio. A isoterma de Freundlich melhor ajusta os dados experimentais para Sargassum sp. e alginato de cálcio úmido. A capacidade de adsorção máxima calculada pelo modelo de Freundlich: na concentração de equilíbrio de 11,66 0,06 mmol/L foi de 1,97 0,07 mmol/g para Sargassum sp.; e na concentração de equilíbrio de 12,12 0,03 mmol/L foi de 1,69 0,04 mmol/g para alginato de cálcio úmido. O processo de biossorção em regime contínuo, com alturas de leito variável de 10 a 40 cm, teve melhor desempenho com a altura de 40 cm. Em regime de batelada, o desempenho da Sargassum sp. foi superior ao dos alginatos de cálcio (úmido melhor que o desidratado), que por sua vez foram superiores ao desempenho dos carvões ativos em pó e granular (em pó melhor que o granular). O sistema contínuo com concentração inicial de cobre de 8,5 mmol/L deve ser operado com altura de leito igual ou superior a 40 cm, ou com sistemas multicolunas para soluções mais concentradas / Biosorption is the term applied to the adsorption technology of metallic ions in solution than through materials of inactive biological nature. Its close to adsorption using conventional adsorbents. Biosorption depends on temperature, pH, initial concentration of metal ion and type of biosorbents. The main objective of this dissertation is to study and compare the adsorption of copper ions from aqueous solution in batch and continuous system using Sargassum sp.; wet and dehydrated calcium alginate; powder and granular activated carbon. Calcium alginate was prepared by 4% w/v sodium alginate solution dropwise into 37% w/v calcium chloride dehydrate. Calcium alginate presented 89% of moisture after dry in an oven at 100C for 24 hours. Biosorption parameters were set as follow: dose of adsorbent 2 g/L; temperature at 30C, pH at 5.0, and stirring speed of the rotating plate at 150 rpm. For the kinetic and equilibrium studies, the tests were done in a batch system. In kinetic assays for two concentrations (0.16 and 3.15 mmol/L) was varied contact time (1-120 min) to reach equilibrium. In equilibrium assays were varied concentrations (0.16 to 15.72 mmol/L) using the time determined in kinetic experiments. It was used two kinetic modeling (the pseudo-first-order and second-order) and two equilibrium modeling (Langmuir and Freundlich). The second-order kinetic model better fitted the results. The equilibrium time for adsorption of copper was 60 minutes for Sargassum sp. and wet and dehydrated calcium alginate pellets. For the activated carbon, equilibrium times for the adsorption of copper were obtained faster, but the capacity of copper removal were extremely low. Based on the unfavorable results obtained for the activated carbon they were discharged to proceed with tests of equilibrium. The Freundlich isotherm fitted the experimental data for Sargassum sp. and wet calcium alginate. The maximum adsorption capacity calculated using Freundlich model: at equilibrium concentration of 11.66 0.06 mmol/L was 1.97 0.07 mmol/g for Sargassum sp. and at equilibrium concentration of 12.12 0.03 mmol/L was 1.69 0.04 mmol/g for wet calcium alginate. Biosorption in a continuous system, with bed heights from 10 to 40 cm, had the best performance with a height of 40 cm. In a batch system, the performance of Sargassum sp. was higher than calcium alginate (wet rather than dehydrated), which in turn were higher than the performance of powder and granular active carbon (powder better than granular). The continuous system with initial copper concentration of 8.5 mmol/L, must be operated with a bed height equal or greater 40 cm, or with multicolumn systems for more concentrated solutions

La possibilité d’administrer des formes sèches orales est encore de nos jours un enjeu dans certaines spécialités médicales telles que la pédiatrie, la neurologie ou la gériatrie. Les mini-comprimés orodispersibles présentent un intérêt majeur pour répondre à cette problématique.L’objectif de ce travail est d’étudier les différents phénomènes qui régissent la conception de cette forme pharmaceutique par compression directe.Trois axes de recherche ont été fixés pour la réalisation de ce travail : - Premièrement, étudier les paramètres de formulation et de fabrication des mini-comprimés orodispersibles.- Deuxièmement, améliorer notre compréhension des phénomènes qui régissent la désintégration de ces comprimés au travers de l’étude du comportement de l’excipient clé de la désintégration : le super-désintégrant.- Enfin, développer un matériau à base d’acide alginique et d’alginate de calcium ayant pour fonction d’accélérer la désintégration des mini-comprimés orodispersibles.Les résultats obtenus permettent d’orienter les choix des différents excipients et les paramètres techniques pour la fabrication de cette forme. D’autre part, ils mettent en évidence le besoin de définir des spécifications et des techniques de caractérisation qui lui sont dédiées. Les résultats obtenus lors de l’étude du comportement des super-désintégrants au moment de leur hydratation, soulignent l’importance de la capacité de conduction de l’eau des super-désintégrants dans le mécanisme de désintégration des mini-comprimés orodispersibles. Enfin, les résultats des travaux réalisés pour l’obtention de matériaux super-désintégrants à base d’acide alginique permettent d’établir de premières orientations à suivre dans leurs modes de production.Les différentes conclusions issues des travaux menés lors de cette thèse permettront de valoriser cette forme pharmaceutique innovante et d’en favoriser de nouveaux développements. / Patient acceptability of a medical product is a key aspect in the development of medicines. Oral administration of dry forms presents still several limitations in some medical specialties such as pediatrics, neurology or geriatrics. Orodispersible Mini Tablets (ODMTs) have been described as a potential solution to these drawbacks.In this thesis, the different parameters governing the design of these pharmaceutical forms by direct compression have been studied.Three main lines of research have been followed to carry out this work:- Firstly, the different parameters of formulation and manufacture of orodispersible mini tablets were evaluated.- Secondly, the behavior of different commercial super disintegrants, key excipents in the disintegrating action, was studied in order to improve our understanding of the phenomena governing the disintegration mechanisms of the ODMTs.- Finally, various alginate-based materials were developed and its function as super disintegrants in orodispersible mini tablets was tested.The obtained results can be used as indicatives in the choice of excipient and the technical parameters for an effective manufacture of OMDTs. Moreover, they have highlighted the need to continue defining specifications and characterization techniques dedicated to further development of OMDTs. The results obtained during the hydration studies (swelling ratio, swelling force and water uptake) of the super disintegrants underline the importance of wicking in the disintegration mechanism of the ODMT.Finally, the prepared alginate-based materials have shown to present interesting mechanical properties for the development of effective and available super disintegrants for direct compression.The choice of suitable super disintegrants for ODMTs formulation requires extensive knowledge of their properties for promoting the breakout of the tablet and of their interaction with both, water and the various materials constituting the tablet. Thus, the knowledge gained in this thesis on super disintegrant functionality will promote the appropriate development of this innovative pharmaceutical form.

This study aims to investigate the possibility of using calcium-alginate as a coagulant in low turbidity waters. Jar tests were initially performed with synthetically prepared turbid waters to investigate the effect of alginate and calcium concentrations, alginate&rsquo / s molecular weight, rapid mixing time and speed (schedule), initial pH and alkalinity of synthetic water on turbidity removal efficiency of calcium-alginate system step by step. Alum as a coagulant was then used in jar tests conducted with synthetic water to compare with calcium-alginate in terms of its turbidity removal efficiency and produced sludge properties. Finally, raw water acquired from water treatment plant was tested for treatability by using calcium-alginate based on previously determined optimum parameters via jar tests. Experiments of calcium-alginate system with synthetic water showed that calcium was a key parameter in coagulation and high molecular weight alginate performed better in turbidity removal. Significant improvements in turbidity removal were observed when mixing schedules were rearranged / especially in case of increasing rapid mixing time following calcium dosing. Calcium-alginate system neither was notably affected by pH or alkalinity nor did significantly change the pH or alkalinity of the medium. Alum worked well in turbidity removal with additional adjustments of pH and alkalinity, however / alum produced higher quantities of sludge than calcium-alginate system. &ldquo / Raw water&ldquo / experiments with calcium-alginate did not result in desired level of turbidity removals due to the excessively different characteristics of this water compared to the synthetically prepared turbid water.

Coagulation and flocculation processes are important parts of water and wastewater treatment. Coagulation or destabilization of colloidal suspensions results in aggregation of colloidal particles by physical and chemical processes. Flocculation results in the formation of larger and settleable structures by bridging. Alginate, a polysaccharide obtained from marine brown algae, produces a gel structure when mixed with calcium ions, which is expected to be a potential coagulant in water treatment. This study aims to determine the use of calcium alginate as a potential coagulant during water treatment and determine its capabilities and deficiencies in coagulation processes. The study was conducted on turbid water samples prepared in the laboratory and those taken from the inlet of Ankara ivedik Water Treatment Plant (IWTP) by running typical jar tests. The main experimental variables were initial alginate and calcium doses, initial turbidity of water samples and the order with which the two chemicals are dosed. The main criteria investigated to check the success of the system was the final turbidity values and the turbidity removal capacity of calcium- alginate. Experiments were conducted on three different laboratory &ndash / prepared turbid water samples and on the raw water taken from the inlet point of Ankara ivedik Drinking Water Treatment Plant (IWTP). These were prepared as high (150 NTU) medium (80 NTU) and low (10 NTU) turbidity samples. The calcium concentrations tested varied between 30 and 200 mg/L and alginate concentrations tested varied between 0.04 to 40 mg/L. Depending on the initial turbidity and initial calcium concentration of water sample the results depict that calcium alginate could be used as an effective coagulant for high (150 NTU) and medium (80 NTU) turbidity water sample especially at the calcium doses of 120 and 160 mg/L for low alginate concentration doses like 0.4 mg/L. The final turbidity met both the requirements of Drinking Water Standards applied in Turkey and Europe. Generally, the higher the initial turbidity was, the higher the turbidity removal efficiency achieved, even with very low alginic acid concentration. As the initial turbidity decreased, initial concentration of calcium required for the effective coagulation processes decreased. However, for low (10 NTU) turbidity water samples the system did not work properlyHowever, for low turbidity water samples, the turbidity removal efficiency decreased, and it was difficult to meet the limits.

Les biofilms sont des communautés de microorganismes incorporés dans une matrice exo-polymérique complexe. Ils sont reconnus pour jouer un rôle important comme barrière de diffusion dans les systèmes environnementaux et la santé humaine, donnant lieu à une résistance accrue aux antibiotiques et aux désinfectants. Comme le transfert de masse dans un biofilm est principalement dû à la diffusion moléculaire, il est primordial de comprendre les principaux paramètres influençant les flux de diffusion. Dans ce travail, nous avons étudié un biofilm de Pseudomonas fluorescens et deux hydrogels modèles (agarose et alginate) pour lesquels l’autodiffusion (mouvement Brownien) et les coefficients de diffusion mutuels ont été quantifiés. La spectroscopie par corrélation de fluorescence a été utilisée pour mesurer les coefficients d'autodiffusion dans une volume confocal de ca. 1 m3 dans les gels ou les biofilms, tandis que les mesures de diffusion mutuelle ont été faites par cellule de diffusion. En outre, la voltamétrie sur microélectrode a été utilisée pour évaluer le potentiel de Donnan des gels afin de déterminer son impact sur la diffusion. Pour l'hydrogel d'agarose, les observations combinées d'une diminution du coefficient d’autodiffusion et de l’augmentation de la diffusion mutuelle pour une force ionique décroissante ont été attribuées au potentiel de Donnan du gel. Des mesures de l'effet Donnan (différence de -30 mV entre des forces ioniques de 10-4 et 10-1 M) et l'accumulation correspondante d’ions dans l'hydrogel (augmentation d’un facteur de 13 par rapport à la solution) ont indiqué que les interactions électrostatiques peuvent fortement influencer le flux de diffusion de cations, même dans un hydrogel faiblement chargé tel que l'agarose. Curieusement, pour un gel plus chargé comme l'alginate de calcium, la variation de la force ionique et du pH n'a donné lieu qu'à de légères variations de la diffusion de sondes chargées dans l'hydrogel. Ces résultats suggèrent qu’en influençant la diffusion du soluté, l'effet direct des cations sur la structure du gel (compression et/ou gonflement induits) était beaucoup plus efficace que l'effet Donnan. De même, pour un biofilm bactérien, les coefficients d'autodiffusion étaient pratiquement constants sur toute une gamme de force ionique (10-4-10-1 M), aussi bien pour des petits solutés chargés négativement ou positivement (le rapport du coefficient d’autodiffusion dans biofilm sur celui dans la solution, Db/Dw ≈ 85 %) que pour des nanoparticules (Db/Dw≈ 50 %), suggérant que l'effet d'obstruction des biofilms l’emporte sur l'effet de charge. Les résultats de cette étude ont montré que parmi les divers facteurs majeurs qui affectent la diffusion dans un biofilm environnemental oligotrophe (exclusion stérique, interactions électrostatiques et hydrophobes), les effets d'obstruction semblent être les plus importants lorsque l'on tente de comprendre la diffusion du soluté. Alors que les effets de charge ne semblaient pas être importants pour l'autodiffusion de substrats chargés dans l'hydrogel d'alginate ou dans le biofilm bactérien, ils ont joué un rôle clé dans la compréhension de la diffusion à travers l’agarose. L’ensemble de ces résultats devraient être très utiles pour l'évaluation de la biodisponibilité des contaminants traces et des nanoparticules dans l'environnement. / Biofilms are primarily communities of microorganisms embedded in a complex exopolymer matrix. They are thought to play an important role as diffusive barriers in environmental systems and human health, resulting in increased resistance to disinfectants and antibiotics. Since mass transport in a biofilm is primarily due to molecular diffusion, it is critical to understand the main parameters influencing diffusive fluxes in a biofilm. In this thesis, a Pseudomonas fluorescens biofilm and two model hydrogels, (agarose and calcium alginate), were investigated. Both self-diffusion (Brownian motion) and mutual diffusion coefficients were quantified. Fluorescence correlation spectroscopy was used to measure the self-diffusion coefficients in a ca. 1 m3 confocal volume in the gels or biofilms, whereas a diffusion cell setup was employed for mutual diffusion measurements. In addition, microelectrode voltammetry was used to evaluate Donnan potential of the gels in order to determine its impact on diffusion. For the agarose hydrogel, the combined observations of a decreasing self-diffusion coefficient coupled with increasing mutual diffusion as a function of a decreasing ionic strength have been attributed to the gel’s Donnan potential. Measurements of the Donnan effect (difference of -30 mV between ionic strengths of 10-4 and 10-1 M) and the corresponding accumulation of ions in the hydrogel (13x enhancement with respect to the bulk solution) indicated that electrostatic interactions can strongly influence the diffusive flux of cations, even in a weakly charged hydrogel, such as agarose. Somewhat surprisingly, for a more highly charged gel such as calcium alginate, varying ionic strength and pH resulted in only small changes to the diffusion of charged probes in the hydrogel. These results suggested that the direct effect of the cations on gel structure (due to an induced swelling or compression) was much more effective than the Donnan effect when influencing solute diffusion. Similarly, for a bacterial biofilm, self-diffusion coefficients were virtually constant across a range of examined ionic strengths (10-4-10-1 M) for both negatively and positively charged small solutes (Db/Dw≈85%) and nanoparticles (Db/Dw≈50%), suggesting that the obstruction effect of the biofilms again overwhelmed the charge effect. The results of this work indicated that among the various major factors affecting diffusion in an oligotrophic environmental biofilm (steric exclusion, hydrophobic and electrostatic interactions), obstruction effects appeared to be the most important when attempting to understand the solute diffusion. While charge effects did not appear to be important to the self-diffusion of charged substrates in the alginate hydrogel or bacterial biofilm, they were key to understanding diffusion through another gel, with numerous biomedical and environmental applications, i.e. agarose. These results should be extremely useful when evaluating the bioavailability of the trace contaminants and nanoparticles in the environment.

Les biofilms sont des communautés de microorganismes incorporés dans une matrice exo-polymérique complexe. Ils sont reconnus pour jouer un rôle important comme barrière de diffusion dans les systèmes environnementaux et la santé humaine, donnant lieu à une résistance accrue aux antibiotiques et aux désinfectants. Comme le transfert de masse dans un biofilm est principalement dû à la diffusion moléculaire, il est primordial de comprendre les principaux paramètres influençant les flux de diffusion. Dans ce travail, nous avons étudié un biofilm de Pseudomonas fluorescens et deux hydrogels modèles (agarose et alginate) pour lesquels l’autodiffusion (mouvement Brownien) et les coefficients de diffusion mutuels ont été quantifiés. La spectroscopie par corrélation de fluorescence a été utilisée pour mesurer les coefficients d'autodiffusion dans une volume confocal de ca. 1 m3 dans les gels ou les biofilms, tandis que les mesures de diffusion mutuelle ont été faites par cellule de diffusion. En outre, la voltamétrie sur microélectrode a été utilisée pour évaluer le potentiel de Donnan des gels afin de déterminer son impact sur la diffusion. Pour l'hydrogel d'agarose, les observations combinées d'une diminution du coefficient d’autodiffusion et de l’augmentation de la diffusion mutuelle pour une force ionique décroissante ont été attribuées au potentiel de Donnan du gel. Des mesures de l'effet Donnan (différence de -30 mV entre des forces ioniques de 10-4 et 10-1 M) et l'accumulation correspondante d’ions dans l'hydrogel (augmentation d’un facteur de 13 par rapport à la solution) ont indiqué que les interactions électrostatiques peuvent fortement influencer le flux de diffusion de cations, même dans un hydrogel faiblement chargé tel que l'agarose. Curieusement, pour un gel plus chargé comme l'alginate de calcium, la variation de la force ionique et du pH n'a donné lieu qu'à de légères variations de la diffusion de sondes chargées dans l'hydrogel. Ces résultats suggèrent qu’en influençant la diffusion du soluté, l'effet direct des cations sur la structure du gel (compression et/ou gonflement induits) était beaucoup plus efficace que l'effet Donnan. De même, pour un biofilm bactérien, les coefficients d'autodiffusion étaient pratiquement constants sur toute une gamme de force ionique (10-4-10-1 M), aussi bien pour des petits solutés chargés négativement ou positivement (le rapport du coefficient d’autodiffusion dans biofilm sur celui dans la solution, Db/Dw ≈ 85 %) que pour des nanoparticules (Db/Dw≈ 50 %), suggérant que l'effet d'obstruction des biofilms l’emporte sur l'effet de charge. Les résultats de cette étude ont montré que parmi les divers facteurs majeurs qui affectent la diffusion dans un biofilm environnemental oligotrophe (exclusion stérique, interactions électrostatiques et hydrophobes), les effets d'obstruction semblent être les plus importants lorsque l'on tente de comprendre la diffusion du soluté. Alors que les effets de charge ne semblaient pas être importants pour l'autodiffusion de substrats chargés dans l'hydrogel d'alginate ou dans le biofilm bactérien, ils ont joué un rôle clé dans la compréhension de la diffusion à travers l’agarose. L’ensemble de ces résultats devraient être très utiles pour l'évaluation de la biodisponibilité des contaminants traces et des nanoparticules dans l'environnement. / Biofilms are primarily communities of microorganisms embedded in a complex exopolymer matrix. They are thought to play an important role as diffusive barriers in environmental systems and human health, resulting in increased resistance to disinfectants and antibiotics. Since mass transport in a biofilm is primarily due to molecular diffusion, it is critical to understand the main parameters influencing diffusive fluxes in a biofilm. In this thesis, a Pseudomonas fluorescens biofilm and two model hydrogels, (agarose and calcium alginate), were investigated. Both self-diffusion (Brownian motion) and mutual diffusion coefficients were quantified. Fluorescence correlation spectroscopy was used to measure the self-diffusion coefficients in a ca. 1 m3 confocal volume in the gels or biofilms, whereas a diffusion cell setup was employed for mutual diffusion measurements. In addition, microelectrode voltammetry was used to evaluate Donnan potential of the gels in order to determine its impact on diffusion. For the agarose hydrogel, the combined observations of a decreasing self-diffusion coefficient coupled with increasing mutual diffusion as a function of a decreasing ionic strength have been attributed to the gel’s Donnan potential. Measurements of the Donnan effect (difference of -30 mV between ionic strengths of 10-4 and 10-1 M) and the corresponding accumulation of ions in the hydrogel (13x enhancement with respect to the bulk solution) indicated that electrostatic interactions can strongly influence the diffusive flux of cations, even in a weakly charged hydrogel, such as agarose. Somewhat surprisingly, for a more highly charged gel such as calcium alginate, varying ionic strength and pH resulted in only small changes to the diffusion of charged probes in the hydrogel. These results suggested that the direct effect of the cations on gel structure (due to an induced swelling or compression) was much more effective than the Donnan effect when influencing solute diffusion. Similarly, for a bacterial biofilm, self-diffusion coefficients were virtually constant across a range of examined ionic strengths (10-4-10-1 M) for both negatively and positively charged small solutes (Db/Dw≈85%) and nanoparticles (Db/Dw≈50%), suggesting that the obstruction effect of the biofilms again overwhelmed the charge effect. The results of this work indicated that among the various major factors affecting diffusion in an oligotrophic environmental biofilm (steric exclusion, hydrophobic and electrostatic interactions), obstruction effects appeared to be the most important when attempting to understand the solute diffusion. While charge effects did not appear to be important to the self-diffusion of charged substrates in the alginate hydrogel or bacterial biofilm, they were key to understanding diffusion through another gel, with numerous biomedical and environmental applications, i.e. agarose. These results should be extremely useful when evaluating the bioavailability of the trace contaminants and nanoparticles in the environment.

La adsorció sobre carbó actiu és un tractament habitual para a l'eliminació de metalls contaminants d'afluents aquosos. Amb la finalitat de reduir el cost dels tractament actuals s'està estudiant la utilització d'adsorbents de baix cost com a substituts dels sorbents convencionals que s'utilitzen usualment en els tractaments d'aigües. En aquesta tesi s'ha avaluat la possibilitat d'aprofitar diversos residus vegetals procedents de processos agrícoles o residus industrials, com a sorbents per a l'eliminació de metalls de solucions aquoses. En concret, el treball s'ha centrat en assolir dos grans objectius, primer de tot, conèixer la possibilitat d'utilitzar el pinyol d'oliva com a adsorbent de metalls divalents de solucions aquoses, com són el Cd(II), Cu(II), Ni(II) i Pb(II), i en segon lloc, avaluar la utilització de quatre residus vegetals (escorça de yohimbe, rapa de raïm, suro i pinyol d'oliva) per a l'extracció de Cr(VI) de solucions aquoses i utilitzar el residu vegetal més apropiat com a base per tal d'obtenir un nou sorbent, amb més bona morfologia per ser utilitzat en sistemes d'eliminació de Cr(VI) en continu. Les dades cinètiques d'adsorció es van tractar amb el model cinètic de pseudo-segon ordre, amb el que es van determinar la velocitat inicial d'adsorció dels metalls. Els models d'isotermes d'equilibri de Langmuir i Freundlich es van utilitzar per descriure els equilibris d'adsorció i calcular els paràmetres de les isotermes. En els assajos amb mescles binàries de metalls, els resultats es van tractar amb el model ampliat de Langmuir.En aquest treball s'ha determinat, primerament, que el pinyol d'oliva és un bon sorbent dels metalls divalents estudiats. S'ha determinat que l'adsorció dels metalls varia amb el pH de la solució i que la presència de sals en la solució provoca una davallada en l'adsorció. També es va determinar la competència en l'adsorció entre els metalls al realitzar assajos en mescles binàries.Amb els estudis d'extracció de Cr(VI) amb els quatre materials s'ha determinat que aquests vegetals poden adsorbir el Cr(VI) en solució, tot i que la rapa i la yohimbe són els materials que presenten unes capacitats d'adsorció més elevades. Les anàlisis amb espectroscòpia electrònica de Raig-X realitzats en la rapa de raïm i la yohimbe en contacte amb Cr(VI) varen demostrar la presència del metall en els dos estats d'oxidació, Cr(VI) i Cr(III), evidenciant la participació del mecanisme de reducció de Cr(VI) en l'adsorció del metall sobre els materials.Amb l'encapsulació de la rapa de raïm es va incrementar significativament la capacitat d'adsorció del metall respecta a la seva utilització en la forma original. Les dades experimentals es van tractar amb un model de difusió i es va determinar el coeficient de difusió en l'adsorció en el sorbent amb diferent percentatge de rapa en l'interior.Finalment s'han realitzat estudis preliminars d'adsorció de crom hexavalent en continu utilitzant columnes de petites dimensions farcides amb el sorbent format per boles de rapa encapsulada en alginat càlcic. En aquests assajos s'ha determinat l'efecte en l'adsorció de metall de diversos paràmetres d'operació, com la concentració inicial de metall, el cabal i l'alçada de llit. El model de transferència de matèria i difusió en columna emprat pel tractament de les dades experimentals va mostrar l'efecte de la concentració inicial i del cabal en els coeficients de difusió i transferència de matèria. El model BDST no va predir correctament el temps de servei en els diferents paràmetres d'operació experimentats a causa de la complexitat del procés d'adsorció. Amb aquests assajos preliminars s'han establert les bases de l'adsorció de Cr(VI) amb el nou sorbent en sistemes en continu amb la finalitat de realitzar estudis posteriors d'eliminació del metall en columnes de majors dimensions. / Adsorption with activated carbon is a usual treatment to remove metals from wastewater. In order to reduce the cost of the treatment, several studies have been carried out to evaluate the use of low cost sorbents as an alternative to conventional sorbents used in wastewater treatment. In this work, the use of different vegetable wastes from agricultural or industrial processes has been evaluated as sorbents for metal removal from aqueous solutions. The aim of this work was to study first, the usefulness of olive stones as a sorbent for divalent metals such as Cd(II), Cu(II), Ni(II) and Pb(II) from aqueous solutions and then the use of four vegetable wastes (yohimbe bark, grape stalks, cork and olive stones) for the removal of Cr(VI) from aqueous solutions. The vegetable waste powder was encapsulated in calcium alginate to obtain spherical gel beads that were used in continuous flow process for Cr(VI) removal.In all sorption experiments, kinetic data were modeled by the pseudo-second order kinetic equation and determine the constants sorption rates. Langmuir and Freundlich model isotherms were use to describe sorption equilibrium data and to obtain the isotherm parameters. In binary mixtures, the extended Langmuir isotherm model was used. The results showed that olive stones are a good sorbent for studied divalent metal. Metal uptake was pH dependent and the presence of salts in solution provokes a decrease in metal uptake. A clear competence between metals to be adsorbed on the waste was observed in metal binary mixtures. Although results obtained in Cr(VI) removal studies show that the four studied wastes can adsorb Cr(VI), grape stalks and yohimbe bark wastes showed the best chromium sorption capacity. X-Ray Photoelectron Spectroscopy analysis on grape stalks and yohimbe chromium loaded samples put into evidence that both Cr(VI) and Cr(III) were sorbed on wastes surface indicating that Cr(VI) sorption process involves a redox reaction. The gel beads obtained when encapsulating grape stalks in calcium alginate showed a significant increase in Cr(VI) sorption capacity compared to the original grape stalks waste. A diffusion model was used to analyze the experimental data and to determine the diffusion coefficient for Cr(VI) sorption by beads containing different percentage of grape stalks encapsulated in calcium alginate. Finally, preliminary studies of Cr(VI) removal in continuous flow using the beads containing grape stalks powder gel in laboratory columns have been carried out. The effect of operating parameters such as feed metal concentration, flow rate and bed depth was studied. The mass transfer and diffusion model used to describe column data showed the effect of feed metal concentration and flow rate in both, diffusion and mass transfer coefficients, respectively. The bed depth service time model (BDST) failed in predicting the service time when changing operating parameters due to the complexity of the sorption process. With these preliminary column experiments we established the basis for Cr(VI) sorption by the proposed sorbent in continuous flow process for further development of the process to be used in higher scale columns.