O objetivo desta pesquisa foi estudar a formação de partículas de licopeno em pó de colágeno hidrolisado (CH) comercial usando CO2 supercrítico (CO2-SC). O estudo consistiu em três etapas: a medida de solubilidade do CH em CO2-SC por método estático para conhecer a afinidade do CH pelo CO2, a formação de partículas de misturas físicas compostas de diferentes proporções de CH/licopeno (4:1, 6:1, 8:1 e 10:1) através de processamento em uma autoclave com CO2-SC a 140 bar e 50 °C em agitação de 1.250 rpm por 45 min para definir a proporção de CH/licopeno, e o estudo do efeito de outras condições de CO2-SC (150 bar e 50 °C, 150 bar e 60 °C, 250 bar e 50 °C, 250 bar e 60 °C) na formação de partículas de licopeno em CH para identificar a melhor condição de CO2-SC. As partículas resultantes foram caracterizadas com relação à sua morfologia por microscopia eletrônica de varredura, distribuição de tamanho por difração a laser, comportamento térmico por calorimetria diferencial de varredura, estrutura química por espectroscopia de infravermelho de transformada de Fourier, liberação de carga, e estrutura física interna das partículas por microscopia de laser confocal para conhecer o mecanismo de formação das partículas pelo processamento com CO2-SC. Os resultados indicaram que o CH é pouco solúvel em CO2-SC, motivo pelo qual não há potencial para processos de micronização supercrítica relacionados à solubilidade do biomaterial carreador em CO2-SC. No estudo de proporções de CH/licopeno foi observado que o processo com CO2-SC a 140 bar e 50 °C permite a obtenção de partículas de licopeno em CH na forma de pó de coloração vermelha com intensidade dependente da quantidade de licopeno inicial, sem mudanças importantes na estrutura física porosa do CH, e um aumento de tamanho das partículas. Recomenda-se a proporção 10:1 de CH/licopeno, pois nela se evidenciou menor aglomeração de partículas e formação de fissuras na superfície das partículas que facilitam a incorporação do licopeno em CH seguindo um mecanismo de impregnação supercrítica propiciado pela sorção de CO2 e arraste simultâneo de licopeno ao interior da estrutura física das partículas de CH. Na exploração de outras condições de CO2-SC, na temperatura de 60 °C (150/250 bar) obteve-se uma massa de aparência viscoelástica sem utilidade para a formação de partículas. Entanto, na temperatura de 50 °C foi observado que as partículas de licopeno em CH formadas com CO2-SC a 150 bar, quando comparadas com as formadas com CO2-SC a 250 bar, evidenciaram formação de fissuras que resultaram na melhor dispersão e maior carga de licopeno na estrutura interna do CH. Além disso, as análises do comportamento térmico e o espectro de infravermelho destas partículas evidenciaram a formação de interações eletrostáticas entre o licopeno e o CH favorecidas pelo processamento com CO2-SC. Assim, conclui-se que o processamento com CO2-SC a 140/150 bar e 50 °C poderia ser utilizada para o design de partículas de licopeno impregnadas em CH, gerando um ingrediente com possível ampla atividade funcional pela atividade biológica do CH em tecidos conjuntivos e pela atividade antioxidante do licopeno. / The objective of this research was to study the formation of lycopene particles in commercial powder of hydrolyzed collagen (HC) using supercritical CO2 (SC-CO2). The study consisted of three steps: the solubility measurement of HC in SC-CO2 by static method to know the affinity of HC by CO2, the formation of particles of physical mixtures composed of different ratios of HC/lycopene (4:1, 6:1, 8:1 and 10:1) by autoclaving with SC-CO2 at 140 bar and 50 °C under stirring at 1,250 rpm for 45 min to define the HC/lycopene ratio, and the study of the effect of other conditions of SC-CO2 (150 bar and 50 °C, 150 bar and 60 °C, 250 bar and 50 °C, 250 bar and 60 °C) in the particle formation of lycopene in HC to identify the best SC-CO2 condition. The resulting particles were characterized with respect to their morphology by scanning electron microscopy, size distribution by laser diffraction, thermal behavior by differential scanning calorimetry, chemical structure by Fourier transform infrared spectroscopy, charge release, and physical structure of the particles by confocal laser microscopy to know the mechanism of particle formation by SC-CO2 processing. The results indicated that HC is poorly soluble in SC-CO2 and therefore has no potential for supercritical micronization processes related to the solubility of the biomaterial in SC-CO2. In the study of ratios of HC/lycopene it was observed that the process with SC-CO2 at 140 bar and 50 °C allowed to obtain lycopene particles in HC with powder appearance of red color with intensity depending on the amount of initial lycopene, without important changes in the porous physical structure of HC, and an increase in particle size. It is recommended a 10:1 ratio of HC/lycopene, since this ratio showed less particle agglomeration, and formation of fissures on the surface of the particles facilitating the incorporation of lycopene into HC following a mechanism of supercritical impregnation propitiated by CO2 sorption and simultaneous drag of lycopene to the interior of the physical structure of the HC particles. In the exploration of other conditions of SC-CO2, at 60 °C (150/250 bar) a mass of viscoelastic appearance was obtained without utility for the formation of particles. However, at 50 °C was observed that the lycopene particles in HC formed with SC-CO2 at 150 bar, when compared with the particles formed with SC-CO2 at 250 bar evidenced the formation of fissures, which had positive influence in the dispersion and charge of lycopene in the internal structure of HC. In addition, analyzes of the thermal behavior and the infrared spectrum of these particles evidenced the formation of electrostatic interactions between lycopene and HC favored by SC-CO2 processing. Thus, it can be concluded that SC-CO2 processing at 140/150 bar and 50 °C could be used for the design of lycopene particles impregnated in HC, producing an ingredient with possible broad functional activity due to the biological activity of HC in connective tissues and the antioxidant activity of lycopene.

O objetivo desta pesquisa foi estudar a formação de partículas de licopeno em pó de colágeno hidrolisado (CH) comercial usando CO2 supercrítico (CO2-SC). O estudo consistiu em três etapas: a medida de solubilidade do CH em CO2-SC por método estático para conhecer a afinidade do CH pelo CO2, a formação de partículas de misturas físicas compostas de diferentes proporções de CH/licopeno (4:1, 6:1, 8:1 e 10:1) através de processamento em uma autoclave com CO2-SC a 140 bar e 50 °C em agitação de 1.250 rpm por 45 min para definir a proporção de CH/licopeno, e o estudo do efeito de outras condições de CO2-SC (150 bar e 50 °C, 150 bar e 60 °C, 250 bar e 50 °C, 250 bar e 60 °C) na formação de partículas de licopeno em CH para identificar a melhor condição de CO2-SC. As partículas resultantes foram caracterizadas com relação à sua morfologia por microscopia eletrônica de varredura, distribuição de tamanho por difração a laser, comportamento térmico por calorimetria diferencial de varredura, estrutura química por espectroscopia de infravermelho de transformada de Fourier, liberação de carga, e estrutura física interna das partículas por microscopia de laser confocal para conhecer o mecanismo de formação das partículas pelo processamento com CO2-SC. Os resultados indicaram que o CH é pouco solúvel em CO2-SC, motivo pelo qual não há potencial para processos de micronização supercrítica relacionados à solubilidade do biomaterial carreador em CO2-SC. No estudo de proporções de CH/licopeno foi observado que o processo com CO2-SC a 140 bar e 50 °C permite a obtenção de partículas de licopeno em CH na forma de pó de coloração vermelha com intensidade dependente da quantidade de licopeno inicial, sem mudanças importantes na estrutura física porosa do CH, e um aumento de tamanho das partículas. Recomenda-se a proporção 10:1 de CH/licopeno, pois nela se evidenciou menor aglomeração de partículas e formação de fissuras na superfície das partículas que facilitam a incorporação do licopeno em CH seguindo um mecanismo de impregnação supercrítica propiciado pela sorção de CO2 e arraste simultâneo de licopeno ao interior da estrutura física das partículas de CH. Na exploração de outras condições de CO2-SC, na temperatura de 60 °C (150/250 bar) obteve-se uma massa de aparência viscoelástica sem utilidade para a formação de partículas. Entanto, na temperatura de 50 °C foi observado que as partículas de licopeno em CH formadas com CO2-SC a 150 bar, quando comparadas com as formadas com CO2-SC a 250 bar, evidenciaram formação de fissuras que resultaram na melhor dispersão e maior carga de licopeno na estrutura interna do CH. Além disso, as análises do comportamento térmico e o espectro de infravermelho destas partículas evidenciaram a formação de interações eletrostáticas entre o licopeno e o CH favorecidas pelo processamento com CO2-SC. Assim, conclui-se que o processamento com CO2-SC a 140/150 bar e 50 °C poderia ser utilizada para o design de partículas de licopeno impregnadas em CH, gerando um ingrediente com possível ampla atividade funcional pela atividade biológica do CH em tecidos conjuntivos e pela atividade antioxidante do licopeno. / The objective of this research was to study the formation of lycopene particles in commercial powder of hydrolyzed collagen (HC) using supercritical CO2 (SC-CO2). The study consisted of three steps: the solubility measurement of HC in SC-CO2 by static method to know the affinity of HC by CO2, the formation of particles of physical mixtures composed of different ratios of HC/lycopene (4:1, 6:1, 8:1 and 10:1) by autoclaving with SC-CO2 at 140 bar and 50 °C under stirring at 1,250 rpm for 45 min to define the HC/lycopene ratio, and the study of the effect of other conditions of SC-CO2 (150 bar and 50 °C, 150 bar and 60 °C, 250 bar and 50 °C, 250 bar and 60 °C) in the particle formation of lycopene in HC to identify the best SC-CO2 condition. The resulting particles were characterized with respect to their morphology by scanning electron microscopy, size distribution by laser diffraction, thermal behavior by differential scanning calorimetry, chemical structure by Fourier transform infrared spectroscopy, charge release, and physical structure of the particles by confocal laser microscopy to know the mechanism of particle formation by SC-CO2 processing. The results indicated that HC is poorly soluble in SC-CO2 and therefore has no potential for supercritical micronization processes related to the solubility of the biomaterial in SC-CO2. In the study of ratios of HC/lycopene it was observed that the process with SC-CO2 at 140 bar and 50 °C allowed to obtain lycopene particles in HC with powder appearance of red color with intensity depending on the amount of initial lycopene, without important changes in the porous physical structure of HC, and an increase in particle size. It is recommended a 10:1 ratio of HC/lycopene, since this ratio showed less particle agglomeration, and formation of fissures on the surface of the particles facilitating the incorporation of lycopene into HC following a mechanism of supercritical impregnation propitiated by CO2 sorption and simultaneous drag of lycopene to the interior of the physical structure of the HC particles. In the exploration of other conditions of SC-CO2, at 60 °C (150/250 bar) a mass of viscoelastic appearance was obtained without utility for the formation of particles. However, at 50 °C was observed that the lycopene particles in HC formed with SC-CO2 at 150 bar, when compared with the particles formed with SC-CO2 at 250 bar evidenced the formation of fissures, which had positive influence in the dispersion and charge of lycopene in the internal structure of HC. In addition, analyzes of the thermal behavior and the infrared spectrum of these particles evidenced the formation of electrostatic interactions between lycopene and HC favored by SC-CO2 processing. Thus, it can be concluded that SC-CO2 processing at 140/150 bar and 50 °C could be used for the design of lycopene particles impregnated in HC, producing an ingredient with possible broad functional activity due to the biological activity of HC in connective tissues and the antioxidant activity of lycopene.

Le procédé d’imprégnation en milieu supercritique est une alternative « propre » à l’imprégnation par voie liquide. Entre autres applications, les procédés d’imprégnation peuvent être utilisés pour l’élaboration de systèmes de délivrance de médicaments appliqués aux domaines pharmaceutique et médical. Cette étude porte sur l’élaboration de systèmes de délivrance de médicaments en utilisant l'imprégnation supercritique des principes actifs sur deux types de supports : des matrices polymériques (lentilles intraoculaires) et des matrices poreuses (silices mésoporeuses). Dans le premier cas, des lentilles polymériques intraoculaires (IOLs), utilisées pour la chirurgie de la cataracte, ont été imprégnées par des principes actifs : un anti-inflammatoire (Dexaméthasone 21-phosphate disodium: DXP) et un antibiotique (Ciprofloxacine: CIP). Plus particulièrement, deux types de lentilles ont été étudiés : des IOLs rigides à base de PMMA et des IOLs souples à base de P-HEMA. Les expériences d'imprégnation supercritique ont été effectuées en mode batch et les taux d'imprégnation ont été déterminés par des études de cinétique de relargage des principes actifs. L’influence des conditions opératoires sur l’efficacité de l’imprégnation a été étudiée en réalisant des expériences d’imprégnation préliminaires suivies par des plans d’expériences par la suite. Dans le second cas, une silice mésoporeuse a été utilisée comme support d’imprégnation pour un médicament faiblement hydrosoluble (Fénofibrate), afin d’augmenter sa cinétique de dissolution. L’imprégnation supercritique a été effectuée avec le CO2 pur en faisant varier la pression et le taux de dépressurisation (rapide et lent). / Supercritical impregnation is an attractive “clean” alternative to conventional impregnation processes using generally liquid organic solvents. Among other applications, the impregnation process can be used for the development of controlled drug delivery systems applied to the pharmaceutical and medical fields. This work focuses on the preparation of controlled drug delivery systems using supercritical impregnation of drugs in two kinds of impregnation supports: polymeric matrices (intraocular lenses) and porous supports (mesoporous silica). Firstly, the supercritical impregnation of polymeric intraocular lenses (IOLs), used in cataract surgery, by an anti-inflammatory drug (Dexamethasone 21-phosphate disodium: DXP) and an antibiotic (Ciprofloxacin: CIP), is studied. More particularly, two polymeric IOLs were tested: rigid intraocular lenses made from derivative of PMMA and foldable intraocular lenses made from derivative of P-HEMA. Supercritical impregnations were carried out in a batch mode and the impregnation yields were determined through drug release kinetics studies in a solution simulating the aqueous humor. The influence of operating conditions on impregnation was studied by performing preliminary impregnation experiments followed by experimental designs. The second part of this work deals with the loading of a poorly water-soluble drug (Fenofibrate) in a mesoporous silica for improving drug dissolution kinetics. Supercritical impregnations were carried out with pure CO2 at different pressures (100 to 200 bar) and depressurization rates (rapid and slow).

À l’heure où l’intégration des enjeux environnementaux dans le développement de procédés éco-efficients joue un rôle essentiel dans le moteur de l’innovation responsable, la chimie verte est devenue l’un des sujets de préoccupation majeure. Ainsi, le développement de nouveaux procédés éco-respectueux pour la production d’ingrédients naturels issus de matières premières végétales renouvelables est devenu une démarche incontournable dans le modèle de recherche. L’objectif de cette thèse a consisté au développement d’une stratégie d’éco-valorisation innovante employant les fluides sub/supercritiques pour l’extraction, la caractérisation, la production et l’imprégnation sur support cosmétique de produits naturels d’origine végétale. Pour cela, nous avons utilisé comme modèle végétal : les graines oléagineuses de la plante Kniphofia uvaria, sélectionnée pour des applications cosmétiques grâce à ses propriétés bioactives antioxydantes et anti-âge. Dans un premier temps, le développement de méthodes complémentaires en SFC ainsi que le développement du couplage SFC-MS a été réalisé à l’aide de la source APCI afin d’identifier les molécules responsables des activités bioactives des graines de Kniphofia uvaria. Ainsi, le développement d’un système hybride (U)HPLC/SFC-HRMS a été réalisé afin de mettre en place ce couplage. Des optimisations en termes de proportion et nature de solvant make-up ainsi qu’un travail au niveau des paramètres SFC et MS ont été faits afin de d’améliorer la sensibilité et la spécificité des analyses lipidiques. Dans un second temps, nous nous sommes attachés au développement d’une stratégie d’enrichissement en composés bioactifs à l’aide des méthodes : SFE et CPC. Ainsi, en SFE, des optimisations en termes de température, pression, nature/proportions de co-solvant dans le fluide ont été réalisées alors qu’en CPC, des optimisations au niveau de l’injection ont été faites. Des conditions optimales pour le fractionnement sélectif des anthraquinones et des triglycérides ont été déterminées en SFE et CPC. Dans un dernier temps, ce travail a consisté à développer un couplage en-ligne pour extraire et imprégner sélectivement sur silice cosmétique : les anthraquinones. Le développement et l’optimisation de ce procédé en-ligne ont été réalisés à l’échelle du laboratoire et ont démontré la faisabilité de ce couplage ainsi qu’un intérêt certain pour l’obtention de produits naturels sous une première forme galénique, destinée à une future incorporation dans la formulation de cosmétiques. / Nowadays, green chemistry is a great challenge. It seeks innovation in the development of eco-efficient processes. The production of natural products from renewable materials by these new environmentally friendly processes is more and more used. The aim of this Ph.D thesis is to develop an eco-valuation strategy to extract, characterize, produce and impregnate natural products onto a cosmetic support using sub/supercritical fluids. Consequently, we used oleaginous plant seeds from Kniphofia uvaria as a plant model, which was selected for its interesting cosmetic properties such as antioxidant or anti-ageing. Firstly, the SFC-MS hyphenation with the APCI as an ionization source was developed to screen bioactive molecules; responsible of cosmetic properties. This coupling was performed by the hybrid combination of (U)HPLC/SFC-HRMS. Various optimizations in terms of the solvent make-up (nature and proportion), modulation with SFC and MS parameters were carried out in order to improve sensitivity and selectivity of lipid analysis. Secondly, an enrichment strategy to concentrate bioactive compounds in the final extract was developed by SFE and CPC. Thus, in SFE, experimental parameters (temperature, pressure, nature/proportion of the modifier in the CO2 fluid) were optimized while in CPC, the injection optimization was realized. Methods for the selective fractionation of anthraquinones and triglycerides were obtained in CPC and SFE. Finally, an on-line sub/supercritical extraction-impregnation process was developed to extract and for simultaneously impregnating anthraquinones onto a cosmetic silica. Development and optimization of this process was realized on a laboratory scale. Consequently, this study demonstrated the feasibility of this concept and it presents a great interest to provide natural products as a galenic form, which could be used in the cosmetic formulation.