In dieser Arbeit ein neues bioanalytisches Konzept untersucht, das nanoskalige Zeolith-Imidazolat-Frameworks (ZIFs) als Marker für antikörperbasierte Analysemethoden einsetzt, einschließlich Enzyme-Linked-Immunosorbent-Assay (ELISA) und Lateral Flow Immunoassay (LFIA). Der Vorteil von ZIFs als Marker gegenüber etablierten Materialien ist ihre vielseitige, einfache und kostengünstige Synthese. Dazu gehört die Möglichkeit, niedermolekulare Substanzen für zusätzliche Sensorzwecke zu verkapseln und für eine hohe Selektivität stabil an Biomakromoleküle zu konjugieren. Als modellhafter Zielanalyt von Relevanz wurden Phthalat-Acylester (PAEs) ausgewählt. Die Relevanz des Nachweises von PAEs ergibt sich aus ihren Eigenschaften als endokrin wirksame Chemikalien (EDCs) und krebserregend. In Kombination mit der Tatsache, dass PAEs aufgrund ihrer Verwendung als Weichmacher in Kindergeschirr, Spielzeug, Trinkflaschen und anderen Produkten auf Polyvinylchlorid-Basis in der Umwelt reichlich vorhanden sind, zeigt, wie wichtig der routinemäßige Nachweis von PAEs in Trinkwasser oder Lebensmitteln ist. / This work explores a new bioanalytical concept that employs nanosized Zeolite Imidazolate Frameworks (ZIFs) particles as labels for antibody-based analytical methods, including enzyme-linked immunosorbent assay (ELISA) and lateral flow immunoassay (LFIA). The advantage of ZIFs as labels over established materials is their versatile, facile, and cheap synthesis. This includes the ability to encapsulate low molecular weight substances for additional sensing purposes and for stable conjugation to biomacromolecules for high selectivity. As a model target analyte of relevance Phthalate acyl esters (PAEs) have been selected. The relevance of the detection of PAEs is due to their properties as endocrine disrupting chemicals (EDCs) and carcinogenic. Combined with PAEs being abundant on the environment because of their use as plasticizers in plastic-made tableware for children, toys, drinking bottles and other polyvinylchloride-based products, shows the importance or their routine detection of drinking water or foods being so critical.

Mixed matrix membranes (MMMs) have gained importance because they combine the desirable properties of the polymers and the organic/inorganic filler materials and they may have a very big potential. In this study polyethersulfone (PES) was used as polymeric material, and Zeolitic Imidazolate Framework-8 (ZIF-8) was used as porous filler material, and 2-hydroxy 5-methyl aniline(HMA), was used as a third component in membrane formulation. In this study, ZIF-8 crystals were synthesized with varying particle sizes, and a novel recycling methodology was developed to improve the efficiency of ZIF-8 production. ZIF-8 nano-crystals were synthesized by a 1-hour stirring method at room temperature and characterized by X-ray diffractometer, scanning electron microscopy (SEM), transmission electron microscopy (TEM), dynamic light scattering (DLS) and thermal gravimetric analysis (TGA). In order to investigate the effect of ZIF-8 loading on the membrane performance, different types of membranes were prepared with varying amounts of ZIF-8 between 10-60% (w/w). Moreover, ternary mixed matrix membranes were synthesized consisting of different amounts of ZIF-8 between 10-30% (w/w) and HMA 1-10% (w/w). Gas transport properties of the membranes were investigated by single gas permeation experiments of H2, CO2 and CH4 at 3 bar feed pressure. In order to investigate the effect of feed pressure on the gas transport properties of the membranes, single gas experiments were conducted on 3, 6, 8, 10 and 12 bar feed pressures. Moreover, binary gas permeation experiments of CO2/CH4 pair were conducted through selected membranes at 3 bar and 12 bar feed pressures. In addition to gas permeation experiments, the morphology and thermal characteristics of the membranes were characterized by SEM, TGA and differential scanning calorimetry (DSC) analysis. The incorporation of ZIF-8 crystals into continuous PES matrix resulted in high performance gas separation membranes. The permeabilities of all studied gases increased with ZIF-8 loading while the ideal selectivities showed a slight decrease compared to neat PES membrane. Highly reproducible and repeatable results were obtained up to 30 % w/w ZIF-8 loading, while membrane formulation reproducibility was decreased for higher ZIF-8 contents (&gt / 30 w/w %). Addition of HMA improved the gas separation performances of the binary membranes significantly by decreasing permeabilities and increasing ideal selectivities. PES/ZIF-8(%20)/HMA(%7) membrane has the best separation performance for all gases among the ternary membranes. When 7 w/w % HMA was added to PES/ZIF-8(%20) membrane, H2 permeability decreased from 26.3 to 13.7 barrer, while H2/CH4 ideal selectivity increased from 61.8 to 103.7. Increasing feed pressures appreciably increased the separation performances of all membranes. While the H2 permeability is pressure independent, the CO2 and CH4 permeabilities were reduced with increasing feed pressures and the highest selectivity improvement was observed in H2/CH4 pair for all membrane compositions. For instance, when the feed pressure was increased from 3 bar to 12 bar, the percentage improvements in ideal selectivities through PES/ZIF-8(%10)/HMA(%4) membrane were calculated as 26, 69, 113 % for the H2/CO2, CO2/CH4 and H2/CH4 gas pairs / respectively. This results show that working at higher feed pressures will be more advantageous for separation of the studied gas pairs. The ideal selectivities and the separation factors were equal to each other for all membrane compositions both for 3 and 12 bar operating pressures.

Distillation and absorption columns offer significant energy demands for future development in the petrochemical and fine chemical industries. Membranes and adsorbents are attractive alternatives to these classical separation units due to lower operating cost and easy device fabrication; however, membranes possess an upper limit in separation performance that results in a trade-off between selectivity (purity) and permeability (productivity) for the target gas product, and adsorbents require the need to be water-resistant to natural gas streams in order to withstand typical gas compositions. Composite membranes, or mixed-matrix membranes, are an appealing alternative to pure polymeric membrane materials by use of a molecular sieve “filler” phase which has higher separation performance than the pure polymer. In this thesis, the structure-property-processing relationships for a new class of molecular sieves known as zeolitic imidazolate frameworks (ZIFs) are investigated for their use as the filler phase in composite membranes or as adsorbents. These materials show robust chemical and thermal stability and are a promising class of molecular sieves for acid gas (CO₂/CH₄) separations. The synthesis of mixed-linker ZIFs is first investigated. It is shown that the organic linker composition in these materials is controllable without changing the crystal structure or significantly altering the thermal decomposition properties. There are observable changes in the adsorption properties, determined by nitrogen physisorption, that depend on the overall linker composition. The results suggest the proposed synthesis route facilitates a tunable process to control either the adsorption or diffusion properties depending on the linker composition. The structure-property-processing relationship for a specific ZIF, ZIF-8, is then investigated to determine the proper processing conditions necessary for fabricating defect-free composite membranes. The effect of ultrasonication shows an unexpected coarsening of ZIF-8 nanoparticles that grow with increased sonication time, but the structural integrity is shown to be maintained after sonication by using X-ray diffraction, Pair Distribution Function analysis, and nitrogen physisorption. The permeation properties of composite membranes revealed that intense ultrasonication is necessary to fabricate defect-free membranes for CO₂/CH₄ gas separations. Finally, the separation properties of mixed-linker ZIFs is investigated by using adsorption studies of CO₂ and CH₄ and using composite membranes with differing linker compositions. Adsorption properties of mixed-linker ZIFs reveal that these materials possess tunable surface properties, and a selectivity enhancement of six fold over ZIF-8 is observed with mixed-linker ZIFs without changing the crystal structure. Gas permeation studies of composite membranes reveal that the separation properties of mixed-linker ZIFs are different from their parent frameworks. By proper selection of mixed-linker ZIFs, there is an overall improvement of separation properties in the composite membranes when compared to ZIF-8.

The overall focus of this thesis is on the development and understanding of nanoporous layered silicates and membranes, particularly for potential applications in gas separations. Nanoporous layered materials are a rapidly growing area of interest, and include materials such as layered zeolites, porous layered oxides, layered aluminophosphates, and porous graphenes. They possess unique transport properties that may be advantageous for membrane and thin film applications. These materials also have very different chemistry from 3-D porous materials due to the existence of a large, chemically active, external surface area. This feature also necessitates the development of innovative strategies to process these materials into membranes and thin films with high performance.

The oil is of vital importance to society due to its derivatives with large employment in economic activities and especially its use as an energy source. The economic and social expansion of the country in recent decades, it requires significant development of our infrastructure, especially in the energy sector. The oil that is positioned as the energy source worldwide leader showed marked increase in the average international price over the past years. In this adverse scenario, improvements in the process of refining the oil representing the large-scale gains for society. The present research study is to evaluate the characteristics of efficiency of catalysis of zeolites ZSM-12 for use as additives for lowcost production of heterogeneous microporous catalysts for catalytic cracking of step (FCC), allowing further reductions in the cost of refining oil. The zeolites are crystalline aluminosilicates, which, in its acid form, playing the role of the main active component of FCC catalysts. In our study the zeolite ZSM-12 (zeolite Socony Mobil) a zeolite synthesized with high SiO2/Al2O3 ratio that presents a structure formed by pores dimensional elliptical opening 12 containing tetrahedral SiO4 (or AlO4) with diameter of 5.5 x 5.9 Å. The results were very promising for the SiO2/Al2O3 ratio assessed, with high conversion and selectivity (mainly the C1 and C3), pointing to ZSM-12 that potential low cost of zeolitic additive for FCC catalysts. / O Petróleo é de vital importância para a sociedade devido aos seus derivados com largo emprego nas atividades econômicas e principalmente sua utilização como fonte energética. A expansão econômica e social do país, nas últimas décadas, vem exigindo importante desenvolvimento da nossa infra-estrutura, notadamente no setor de energia. O petróleo que se posiciona como a fonte de energia líder mundial, apresentou acentuada oscilação do preço médio internacional ao longo dos últimos anos, atingindo no segundo semestre do ano de 2008 o maior preço já praticado desde os primórdios da indústria petrolífera. Neste cenário adverso, melhorias no processo de refino do petróleo representam ganhos em larga escala para sociedade. O presente trabalho de pesquisa teve como finalidade avaliar as características de eficiência de catálise de zeólitas ZSM-12 (Zeolite Socony Mobil) para serem utilizadas como aditivos de baixo custo para produção de catalisadores heterogêneos microporosos para a etapa de craqueamento catalítico (FCC), possibilitando futuras reduções no custo de refino do petróleo. As zeólitas são aluminossilicatos cristalinos, que, na sua forma ácida, desempenham o papel de principal componente ativo dos catalisadores de FCC. A zeólita ZSM-12 apresenta uma estrutura formada por poros unidimensionais de abertura elíptica contendo 12 tetraedros SiO4 (ou AlO4), com diâmetro de 5,5 x 5,9 Å. Nos experimentos foram utilizadas amostras de ZSM- 12 de razões SiO2/Al2O3 de 50, 80, 100 e 150, e foi possível observar que quanto maior a cristalinidade da amostra (verificada por difração de raios-X) maior a conversão durante o craqueamento. A região de máximo de conversão ocorre aproximadamente na razão SiO2/Al2O3 de 80 a 100 e intervalos de tempo entre 0 e 20 minutos. Os resultados mostraram-se bastante promissores para as razões SiO2/Al2O3 avaliadas, apresentando alta conversão e seletividade (principalmente ao C1 e C3), apontando a ZSM-12 como potencial aditivo zeolítico de baixo custo para catalisadores de FCC.

L'objectif de cette thèse était d'évaluer quelques Metal-Organic Frameworks (MOFs), choisis en fonction de leur taille de pores, de leur volume poreux et de leur stabilité thermique, en adsorption et séparation des hydrocarbures. Pour étudier le comportement général des MOFs nous avons choisi des MOFs avec des centres métalliques insaturés, des MOFs à charpente anionique et des ZIFs neutres et avons étudié leur sélectivité en séparation de trois familles d'hydrocarbures, à savoir alcanes, alcènes, aromatiques. Les MOFs à centre métallique insaturé se comportent généralement comme des zéolithes polaires, les ZIFs comme des zéolithes apolaires et/ou comme des tamis moléculaires. Les adsorbants les plus prometteurs sont testés sur des séparations d'intérêt industriel telles que la séparation des isomères de xylène, la séparation des paraffines linéaires, monobranchées et di-branchées et l'adsorption sélective du thiophène en vu de l'évaluation de ces adsorbants en désulfuration des essences.

Ce travail s'inscrit dans le cadre de la protection de l'environnement et s'intéresse spécifiquement à la dépollution d'effluents aqueux en vue de piéger d'une part les anions nitrate et/ou phosphate, responsables du phénomène d'eutrophisation, mais également le toluène, hydrocarbure couramment rencontré dans les effluents aqueux urbains et industriels ou les eaux naturelles. Le piégeage de ces polluants a été effectué sur des matériaux zéolithiques. Une grande partie des expérimentations utilise un matériau potentiellement efficace pour le piégeage des trois polluants cités plus haut, à savoir la SMZ ("Surfactant-Modified Zeolite"), classiquement préparée à partir d'une zéolithe naturelle, la clinoptilolite, et d'un tensioactif, le bromure d'hexadecyltriméthylammonium (HDTMA+). En piégeage d'ions nitrate, d'autres SMZ, réalisées à partir de zéolithes synthétiques (LTA, FAU) et diverses espèces organiques tensioactives ou non se montrent moins performantes que la SMZ classique, à l'exception d'un nouveau matériau préparé à partir de nanofeuillets de zéolithe MFI et modifié avec l'ion HDTMA+ (SMZN). Pour le piégeage des ions phosphate, les performances de la SMZ classique ont été comparées à celles de plusieurs zéolithes calciques. Enfin, le piégeage de toluène a été expérimenté sur quatre matériaux, la SMZ classique, un charbon actif et deux zéolithes hydrophobes, la silicalite-1 et la zéolithe bêta. Les expérimentations de piégeage ont été réalisées en système fermé ou en système ouvert. L'influence de la concentration initiale en polluants, du rapport liquide/solide, du débit de filtration, de la présence de compétiteurs et du temps de contact a été examinée. / This work concerns the environmental protection, specifically the treatment of aqueous effluents. Effluents containing nitrate and/or phosphate anions, responsible for the eutrophication phenomenon, and also toluene, which is commonly found in urban and industrial flows and natural waters, were specifically studied. The removal of these pollutants was performed on zeolitic materials. A large part of the experiments use a material potentially efficient to remove the three pollutants mentioned above, namely the SMZ ("Surfactant-Modified Zeolite"), conventionally prepared from a natural zeolite, clinoptilolite, and a surfactant, hexadecyltrimethylammonium bromide (HDTMA+). For nitrate removal, other SMZ, prepared from synthetic zeolites (LTA, FAU) and various organic species (surfactant or not) were less efficient than conventional SMZ except a new material prepared from zeolite MFI nanosheets and modified with HDTMA+ ion. The efficiency of the conventional SMZ for the phosphate ions uptake was compared with those of several calcic zeolites. Finally, removal of toluene was performed on four materials, conventional SMZ, an activated carbon and two hydrophobic zeolites, namely silicalite-1 and beta zeolite. Uptake experiments were conducted in batch-wise and fixed-bed column systems, the second representing a more realistic simulation of dynamic field condition The influence of the initial pollutant concentration, the liquid/solid ratio, the filtration rate, the presence of competitive species and the contact time was examined.

L'objectif de cette thèse était d’évaluer quelques Metal-Organic Frameworks (MOFs), choisis en fonction de leur taille de pores, de leur volume poreux et de leur stabilité thermique, en adsorption et séparation des hydrocarbures. Pour étudier le comportement général des MOFs nous avons choisi des MOFs avec des centres métalliques insaturés, des MOFs à charpente anionique et des ZIFs neutres et avons étudié leur sélectivité en séparation de trois familles d'hydrocarbures, à savoir alcanes, alcènes, aromatiques. Les MOFs à centre métallique insaturé se comportent généralement comme des zéolithes polaires, les ZIFs comme des zéolithes apolaires et/ou comme des tamis moléculaires. Les adsorbants les plus prometteurs sont testés sur des séparations d’intérêt industriel telles que la séparation des isomères de xylène, la séparation des paraffines linéaires, monobranchées et di-branchées et l’adsorption sélective du thiophène en vu de l’évaluation de ces adsorbants en désulfuration des essences. / The aim of this thesis was to evaluate several Metal Organic Frameworks (MOFs), selected based on criteria of pore size, pore volume and thermal stability, in adsorption and separation of hydrocarbons. For studying the general behavior of MOFs in hydrocarbon adsorption, we have chosen MOFs with open metal sites, MOFs with anionic frameworks and neutral ZIFs. The MOFs with open metal sites behave similar to polar zeolites, the ZIFs behave like apolar zeolites and/or like molecular sieves. Finally we selected the most interesting MOFs and tested them in several separations with industrial interest: xylene isomers, paraffin isomers and selective adsorption of thiophene for the purpose of fuel desulfuration.

Ce travail de thèse inclut deux parties : i) l'étude fondamentale de la formation de cristaux zéolithiques ; et ii) la préparation de massifs zéolithiques de taille centimétriques à porosité interparticulaire contrôlée. La première partie de ce travail est donc consacrée à l'étude de l'effet de la microstructure (propriétés physiques et texturales) et de la composition chimique du gel sur la vitesse de nucléation et la taille des cristaux formés. Les résultats de cette étude se résument par le rôle important que joue la composition du gel (plus particulièrement sa concentration en hydroxyde de cation alcalin) sur le degré de polymérisation des particules du gel, la détermination de sa microstructure et par conséquent sur la vitesse de nucléation des zéolithes et la taille des cristaux. Les connaissances acquises dans la première partie ont été utilisées dans le développement du deuxième objective. Notamment, la préparation de massifs zéolithiques de taille centimétrique de types structuraux *BEA et MFI. Le contrôle post-synthèse de la porosité interparticulaire de ces massifs était essentiel pour leur utilisation dans des applications bien précises. A cette fin, une méthode en deux étapes, comportant un assemblage de nanocristaux de zéolithes préformés (en présence ou en absence d'un liant) puis un traitement de croissance secondaire pour l'élimination de la porosité interparticulaire, a été mise en œuvre. Plusieurs traitements de croissance secondaire furent évalués selon le type de zéolithe étudié. Une attention particulière fut accordée à l'étude de l'évolution du liant au cours des processus de préparation et de calcination des massifs zéolithiques. / The present study includes two parts: i) fundamental study of zeolite nucleation-crystal growth mechanism; and ii) preparation of zeolite bodies with controlled interparticle porosity.Thus the first part of the present work deals with the study of the effect of physico-chemical characteristics of initial hydrogel on the nucleation and crystal growth kinetics of zeolite crystals. The obtained data revealed that the concentration of alkali metal hydroxide in the initial system controls the rate of polymerization of the aluminosilicate species, the size of initial gel particles, and the textural properties of the gel. Consequently, the following reaction was to great extent predetermined by the events taking place during mixing the initial reactants.The second part of this work was targeted at the preparation of centimeter-sized zeolite bodies of *BEA- and MFI-type with reduced to minimum inter-particle porosity. A preparation method consisting in assembling of zeolite nanocrystals (with or without a binder) was developed and further optimized. The preformed bodies were subjected to a hydrothermal treatrnent in a fresh zeolite synthesis solution in order to till up the inter-particle porosity. Depending onthe zeolite type, different methods of secondary growth treatrnents were employed. A particular attention has been paid on the study of the binder evolution during the calcination and secondary growth processes.

This master’s thesis was conducted at the Department of Nanotechnology and Functional Materials at Ångström Laboratory as part of an on-going project to develop hybrid nanocomposites from Cladophora cellulose and a sub-type of metal-organic frameworks; zeolitic imidazolate frameworks (ZIFs). By utilizing a state-of-the-art interfacial synthesis approach, in-situ growth of ZIF particles on the cellulose could be achieved. TEMPO-mediated oxidation was diligently used to achieve cellulose nanofibers with carboxylate groups on their surfaces. These were ion-exchanged to promote growth of ZIF particles in a nanocellulose solution and lastly, metal ions and organic linkers which the ZIFs are composed of were added to the surface functionalized and ion-exchanged nanocellulose solution to promote ZIF growth. By vacuum filtration, mechanical pressing and furnace drying; freestanding nanopapers were obtained. A core-shell morphology between the nanocellulose and ZIF crystals was desired and by adjusting the metal ion concentration, a change in morphologies was expected. The nanocomposites were investigated with several relevant analytical tools to confirm presence, attachment and in-situ growth of ZIF crystal particles upon the surface of the fine nanocellulose fibers. Both the CNF@ZIF-67 and CNF@ZIF-8 nanocomposites were successfully prepared as nanopapers with superior surface areas and thermal properties compared to pure TEMPO-oxidized cellulose nanopapers. The CNF@ZIFs showcased hierarchical porosities, stemming from the micro- and mesoporous ZIFs and nanocellulose, respectively. Also, it was demonstrated that CNF@ZIF-8 selectively adsorbed CO2 over N2. Partial formation of core-shell structure could be obtained, although a relationship between increased metal ions and ZIF particle morphology could not wholly be observed.