"Water behavior in pure silicalite and Dealuminated Zeolite Y (DAY), two highly hydrophobic zeolites, was investigated at different temperatures in the range 100-600 K by molecular dynamics simulations. The Compass forcefield was used to carry out the study. A full flexibility of water molecules and of the zeolite framework was considered. The results show that water behavior is more complex in silicalite than in zeolite DAY. Three different activation energies for water diffusion were obtained in silicalite in the range 250-600 K compared to two for DAY. The values of these activation energies are discussed in detail and are related to the hydrogen bond‘s strength and the zeolite structure. Moreover, from the radial distribution functions (rdfs), it is shown that water mostly exists in the gas phase at room temperature in silicalite whereas liquid water is observed in DAY in agreement with previous experimental observations. The self-diffusion coefficients of water and the rdfs are obtained as a function of temperature in order to explain the behavior differences of water in the two all-silica zeolites. The loading influence on the self-diffusion coefficients is also investigated for both crystals. The results are compared with previous experimental and theoretical studies."

Cinzas oriundas da combustão de carvão são resíduos produzidos no processo de geração de energia em termoelétricas. Esses resíduos industriais podem ser aproveitados como matéria prima para síntese de zeólitas, as quais são materiais aluminossilicatos porosos com importantes aplicações, como adsorventes no tratamento de efluentes líquidos. Nesse contexto, o objetivo deste trabalho foi sintetizar zeólitas a partir de três diferentes cinzas de carvão e utilizá-las na remoção de corante violeta cristal em soluções aquosas via processo de adsorção. Para isso, foram sintetizadas zeólitas denominadas ZP, ZF e ZFD a partir de três diferentes cinzas de carvão, sendo elas, respectivamente: cinzas de carvão de combustão em leito pulverizado, de combustão em planta piloto de leito fluidizado e de combustão em planta piloto de leito fluidizado utilizando processo de dessulfuração interna. A síntese foi feita pelo método hidrotérmico, utilizando NaOH 3 mol L-1 como agente mineralizante, relação líquido/sólido (L/S) igual a 6 e tempo de reação de 24 h a 100 °C. Os materiais obtidos foram submetidos à caracterização física, química e morfológica, nas quais foi observada a formação de três diferentes fases zeolíticas (zeólitas P, X e sodalita) nas amostras ZF e ZFD, e uma única fase (zeólita P) na amostra ZP. Os valores de área superficial BET encontrados foram de 17, 35 e 40 m2 g-1 para as zeólitas ZP, ZFD e ZF, respectivamente, com tamanho de poros na faixa de 3 a 4 nm para os três materiais. Os valores de capacidade de troca catiônica (CTC) ficaram entre 2,07 e 2,85 meq NH4 + g-1. Posteriormente foram realizados ensaios de adsorção do corante em que foi avaliada a influência do pH, tempo de contato e concentração de sólido adsorvente. Ainda, foram construídas isotermas de adsorção para esses sistemas e os modelos de isotermas de Langmuir, Freundlich e BET modificado foram ajustados aos dados experimentais. Os resultados mostraram que a maior eficiência foi obtida pela zeólita ZF, alcançando máxima remoção de corante de 85 % nos estudos do efeito do tempo de contato, e as melhores condições experimentais obtidas foram de 60 min e 15 g L-1 de concentração de sólido adsorvente. O modelo de isotermas que melhor se ajustou aos dados experimentais foi BET modificado, com R2 = 0,9894. A síntese de zeólita a partir de cinzas de carvão mostrou potencial na produção de um adsorvente alternativo para remoção do corante violeta cristal de águas contaminadas, contribuindo também para a diminuição do impacto ambiental das atividades de combustão de carvão. / Ashes from coal combustion are waste produced in the process of power generation in thermoelectric. These industrial wastes can be used as raw material for zeolite synthesis, which are porous aluminosilicate with important applications, such as adsorbents in the treatment of liquid effluents. The objective of this study was to synthesize zeolites from three different coal ash and apply it in crystal violet dye adsorption processes in aqueous solution. Thereunto, zeolites called ZP, ZF e ZFD were synthesized from the three different coal ashes, as so, respectively: coal ashes from powdered bed combustion, from combustion in a fluidized bed pilot plant and from combustion in a fluidized bed pilot plant with internal desulphurization. The synthesis was carried by hydrothermal method, using NaOH 3 mol L-1 as the mineralizing agent, the liquid/solid ratio (L/S) equal to 6 and 24 hours reaction time at 100 ° C. The materials were subjected to physical, chemical and morphological characterization and it was observed the formation of three different zeolite phases (zeolites P, X and sodalite) in the sample ZF and ZFD, and a single phase (zeolite P) in ZP sample. The BET surface area values were 17, 35 and 40 m2 g-1 to ZP, ZFD and ZF zeolites, respectively, with pore size in the range of 3 to 4 nm for all three materials. The values of cation exchange capacity (CEC) were between 2.07 and 2.85 meq NH4 + g-1. Subsequently, adsorption tests were carried out in which it was evaluated the influence of pH, contact time and adsorbent solid concentration. Still, adsorption isotherms were built for these systems and isotherm models of Langmuir, Freundlich and modified BET were fitted to experimental data. The results showed that the highest efficiency was obtained by zeolite ZF, achieving maximum dye removal of 85 % in the studies of contact time effects, and the best experimental conditions were 60 min and adsorbent solid concentration of 15 g L-1. The BET isotherm model was found to be the best fit to experimental data, with R2 = 0.9894. The zeolite synthesis from coal ash has shown potential in the production of an alternative adsorbent to remove the crystal violet dye from contaminated water, also contributing to reducing the environmental impact of coal combustion activities.

Cinzas de carvão mineral são resíduos gerados em grandes quantidades nas usinas termelétricas. Este é um dos resíduos de maior geração no Brasil, aproximadamente 1,7 milhões de toneladas por ano. A disposição muitas vezes irregular deste resíduo pode causar problemas de ordem ambiental, como contaminação de águas subterrâneas, do solo e desequilíbrio de sistemas ecológicos. Uma possibilidade de uso para estas cinzas é a síntese de zeólitas, que são minerais aluminossilicatos microporosos com propriedades interessantes para uso na indústria. Neste trabalho, estudou-se a síntese de zeólitas a partir de cinzas volantes visando à sua aplicação em dessulfuração de gases. A síntese foi realizada pelo método hidrotérmico, utilizando solução alcalina de KOH e relação solução/sólido de 2 mL g-1. As variáveis estudadas foram temperatura (100 e 150 °C), concentração da solução alcalina (3 e 5 mol L-1) e tempo de reação (8, 24, 48 e 72 h). Os produtos obtidos e as cinzas precursoras foram caracterizados quanto à composição química (FRX), mineralógica (DRX), morfológica (MEV), área específica (BET) e capacidade de troca catiônica (CTC). A partir da determinação das estruturas cristalinas (DRX) foi possível identificar a formação das zeólitas merlinoíta e perlialita em algumas das condições investigadas. O maior valor de área específica BET foi de 102,42 m2 g-1, nas condições de síntese de 150 °C, 5 mol L-1 e 72 h, representando um aumento de 30 vezes em relação à área das cinzas. Os valores de capacidade de troca catiônica ficaram entre 0,71 e 2,02 meq NH4+ g-1 para as diferentes condições estudadas. Com as amostras que apresentaram os melhores resultados nas caracterizações foram realizados testes de dessulfuração e seu desempenho foi comparado com as cinzas precursoras, carvão ativado e zeólita comercial. Foram construídas curvas de ruptura e isotermas de adsorção para esses sistemas. As zeólitas sintetizadas a partir das cinzas apresentaram maiores valores de adsorção máxima. A zeólita que apresentou melhor resultado de adsorção foi a sintetizada nas condições de 150 °C, 5 mol L-1 e 72 h de tempo de reação, sendo esta também a que apresentou maior valor de área específica. Sendo assim, a síntese de zeólitas a partir de cinzas de carvão, geradas no próprio processo de combustão em usinas térmicas, mostra-se como uma potencial aplicação no sentido de que estas podem ser utilizadas na própria usina para adsorção do SO2 gerado durante a combustão. / Coal ash is a waste generated in large quantities in the power plants. This is one of the wastes generated in larger quantities in Brazil, approximately 1.7 million tons per year. The often irregular disposal of this waste can cause environmental problems, such as contamination of groundwater, soil and imbalance of ecological systems. One possibility for using ashes is the synthesis of zeolites, which are microporous aluminosilicate minerals with interesting properties for use in industry. In this work, the synthesis of zeolites from fly ash was studied, aiming its application for gas desulfurization. The synthesis was performed by the hydrothermal method using an alkaline solution of KOH and a solution/solid ratio of 2 mL g-1. The variables temperature (100 and 150 °C), alkaline solution concentration (3 and 5 mol L-1) and reaction time (8, 24, 48 and 72 hours) were studied. The products obtained and the precursory ashes were characterized by its chemical composition (FRX), mineralogical (XRD), morphological (SEM), specific surface area (BET) and cation exchange capacity (CEC). From the determination of the crystalline structures (XRD) it was possible to identify the formation of the merlinoite and perlialite zeolites for some of the investigated conditions. The highest BET surface area was 102.42 m2 g-1 under the synthesis conditions of 150 °C, 5 mol L-1 and 72 hours. This value represented an increase of 30 times in the surface area comparing to the ash. The cation exchange capacity values varied between 0.71 and 2.02 meq NH4+ g-1 for the different conditions studied. Desulfurization tests were carried out for the samples that showed the best characterization results and its performance was compared with the precursor ash, activated carbon and commercial zeolite. Rupture curves and adsorption isotherms were constructed for these systems. The zeolites synthesized from ash showed higher values of maximum adsorption. The zeolite that showed the best adsorption result was synthesized at the conditions of 150 °C, 5 mol L-1 and 72 hours of reaction time, which also had the highest surface area value. Thus, the synthesis of zeolites from coal ash, generated in the combustion process in thermal plants, is shown as a potential application in the sense that these can be used in the plant to adsorb SO2 generated during combustion.

Lewis acidic zeolites are silica-based, crystalline microporous materials containing tetravalent heteroatoms (M4+=Ti, Sn, Zr, Hf) substituted in framework locations, and have been reported to catalyze a wide range of reactions involving oxygenates and hydrocarbons. The synthetic protocols used to prepare Lewis acid zeolites determine the structures of the active sites and the reaction pockets that confine them, which in turn influences reactivity, product selectivity, and catalyst stability. Specifically, aqueous-phase reactions of biomass-derived molecules, such as glucose isomerization, are sensitive to the hydrophobicity of confining environments, leading to changes in turnover rates. As a result, precise evaluation of the structure and behavior of reaction environments and confined active sites among catalysts of varying provenance or treatment history requires quantitative descriptions of active Lewis acid site densities, of densities of surface functional groups that determine the polarity of microporous confining environments, and of the kinetic behavior of these catalytic materials.<div><br></div><div>Methods for quantifying Lewis acid sites and silanol defects are developed here by analyzing infrared (IR) spectra collected after Lewis base (CD3CN, pyridine) titrations of Lewis acidic zeolite surfaces and are compared to vapor-phase methanol and water adsorption isotherms. Additionally, IR spectra collected under ex situ (flowing vapor-phase water) and in situ (aqueous-phase, 373 K, 0-50 wt% glucose) conditions are used to compare co-adsorbed water densities and structures within hydrophobic (low silanol density) and hydrophilic (high silanol density) confining environments within M-Beta zeolites. Under reaction conditions relevant for sugar conversion in aqueous media (353-398 K, 1-50 wt% glucose), hydrophilic reaction pockets stabilize liquid-like extended water structures within microporous environments, while hydrophobic channels stabilize vapor-phase water at lower intraporous water densities. Higher aqueous-phase glucose isomerization rates (368-383 K, 1-50 wt% glucose, per kinetically relevant active site) are observed on hydrophobic Ti-Beta (~6-12x, per Lewis acidic Ti) and Sn-Beta (~50x, per Lewis acidic Sn in open configuration) zeolites over their hydrophilic analogs. Higher turnover rates on hydrophobic M-Beta zeolites reflect the absence of an extended, hydrogen-bonded network of waters, which entropically destabilizes kinetically relevant hydride shift transition states by reducing the flexibility of their primary solvation spheres. These findings suggest catalyst design strategies to minimize the generation of silanol groups within confining reaction environments would lead to increases in turnover rates.<br></div><div><br></div><div>The methods derived herein can be applied to understanding the role of the confining environment and the associated co-adsorbed water on zeolitic materials of different topology and Lewis acid site identity. For example, the transient formation of silanol defects under aqueous-phase operating conditions is primarily responsible for the deactivation of Sn-Beta catalysts observed during aqueous-phase glucose isomerization. Further, quantifying the role of the confining environment geometry and hydrophobicity on aqueous-phase glucose isomerization rates can be used as guidance for catalyst design to increase reaction rates and selectivities toward specific isomerization products. These findings show that both the active site identity and its confining environment, which vary with zeolite topology and micropore polarity, combine to influence reactivity, selectivity and stability for aqueous-phase glucose isomerization catalysis.<br></div>

In the first part, the mechanisms for the dissociation of TPA are studied under three types of conditions. The unimolecular dissociation is initiated by the breaking of either the N-Calpha and Calpha -Cbeta bonds and leads to many complicated processes. Within the confined space inside neutral zeolite channels, the diffusion of H radicals enhances a cycle of reactions, which accounts for the experimental observation of dipropylamine and monopropylamine. In the presence of an acidic site, the dissociation of TPA goes through catalyzed successive steps to produce ammonia and propylene molecules. / In the last part, two distinct paths are proposed to investigate the carbon nanotube growth mechanism using benzene as the growth seed and propylene as carbon resource. There is an incremental aromatization process, involving both alkylation and dehydrogenation, that leads to linked aromatic rings to form either (3,3) tube or (4,2) tube. Two paths are identified, one via toluene and the other via cumene. The cumene path is more favorable as the barrier is significant lower. / In the second part, A T5 cluster model is used to investigate mechanisms of propylene aromatization to benzene, which involves chemisorption, dimerization, cyclization and dehydrogenation. Propylene can be chemisorbed to form two distinct products, n-propoxide and i-propoxide, which can further be dimerizated to form longer chain olefins 1-hexene and 2-hexene (from n-propoxide), and 4-methyl-1-pentene and 4-methyl-2-penetene (from i-propoxide). Initiated by H2 elimination, these dimerization products can further go through cyclization process to generated either 6-member ring cyclohexene or 5-member ring methyl-cyclopentene. Catalyzed by zeolite, cyclohexene can directly dehydrogenate to form benzene whereas methyl-cyclopentene can dehydrogenate to form fulven, an isomer to benzene. Under acidic zeolite environment, a fulvene can readily be transformed to the thermodynamically more stable benzene. / The growth mechanisms of mono-sized and parallel-aligned single wall carbon nanotube (CNT) in the microporous channels of AlPO4-5 are investigated by density functional theory calculations. Detailed mechanisms are proposed for the decomposition of TPA, the formation of aromatic ring, and the growth of carbon nanotubes. / Liu, Jianwen. / Adviser: Zhifeng Liu. / Source: Dissertation Abstracts International, Volume: 70-09, Section: B, page: . / Thesis submitted in: December 2008. / Thesis (Ph.D.)--Chinese University of Hong Kong, 2009. / Includes bibliographical references (leaves 98-99). / Electronic reproduction. Hong Kong : Chinese University of Hong Kong, [2012] System requirements: Adobe Acrobat Reader. Available via World Wide Web. / Electronic reproduction. [Ann Arbor, MI] : ProQuest Information and Learning, [200-] System requirements: Adobe Acrobat Reader. Available via World Wide Web. / Abstracts in English and Chinese. / School code: 1307.

Complex reaction kinetics of the solid acid alkylation of isobutane with butenes over a proton-exchanged Y-zeolite has been modeled at the elementary step level. Starting with a computer algorithm that generated the reaction network based on the fundamentals of the carbenium ion chemistry, the formation of over 100+ product species has been modeled in order to gain understanding of the underlying phenomena leading to rapid catalyst deactivation and product selectivity shifts observed in experimental runs. An experimental investigation of the solid acid alkylation process was carried out in a fixed bed catalytic reactor operating with an excess of isobutane under isothermal conditions at moderate temperatures (353-393 K) in liquid phase. Experimental data varying with run-time for a set of butene space-times and reaction temperatures were collected for parameter estimation purposes. A kinetic model was formulated in terms of rate expressions at the elementary step level including a rigorous modeling of deactivation through site coverage. The single event concept was applied to each rate coefficient at the elementary step level to achieve a significant reduction in the number of model parameters. Based on the identification of structural changes leading to the creation or destruction of symmetry axes and chiral centers in an elementary step, formulae have been developed for the calculation of the number of single events. The Evans-Polanyi relationship and the concept of stabilization energy were introduced to account for energy levels in surface-bonded carbenium ions. A novel functional dependency of the stabilization energy with the nature of the carbenium ion and the carbon number was proposed to account for energy effects from the acid sites on the catalyst. Further reductions in the number of parameters and simplification of the equations for the transient pseudohomogeneous one-dimensional plug-flow model of the reactor were achieved by means of thermodynamic constraints. Altogether, the single event concept, the Evans-Polanyi relationship, the stabilization energy approach and the thermodynamic constraints led to a set of 14 parameters necessary for a complete description of solid acid alkylation at the elementary step level.

Poröse Sol-Gel-Materialien finden in vielen Bereichen Anwendung bzw. sind Gegenstand der aktuellen Forschung. Zu diesen Bereichen zählen sowohl klassische Anwendungen, wie z. B. die Verwendung als Katalysator, Molekularsieb oder Trockenmittel, als auch nichtklassische Anwendungen, wie z. B. der Einsatz als Kontrastmittel in der Magnet-Resonanz-Tomographie oder in Form von dünnen Zeolithfilmen als Isolatoren in Mikrochips. Auch für den Einsatz in der Photonik werden poröse Materialien in Betracht gezogen, wie die Entwicklung des Zeolith-Farbstoff-Lasers zeigt. Mikroporöse Zeolithe können generell über einfache Ionenaustauschreaktionen mit Lanthanoidionen in lumineszente Materialien umgewandelt werden. Neben der Erzeugung eines lumineszenten Materials, dessen Lumineszenzeigenschaften charakterisiert werden müssen, bietet die Nutzung von Lanthanoidionen die Möglichkeit diese Ionen als Sonde zur Charakterisierung der Ion-Wirt-Wechselwirkungen zu funktionalisieren, was z. B. in Bezug auf die Anwendung als Katalysator von großer Bedeutung ist. Dabei werden die einzigartigen Lumineszenzeigenschaften der Lanthanoidionen, in diesem Fall von Europium(III) und Terbium(III), genutzt. In dieser Arbeit wurden Lanthanoid-dotierte mikroporöse Zeolithe, mikroporös-mesoporöse Hybridmaterialien und mesoporöse Silikate hinsichtlich ihrer Lumineszenzeigenschaften und ihrer Wechselwirkung des Wirtsmaterials mit den Lanthanoidionen mittels zeitaufgelöster Lumineszenzspektroskopie untersucht. Zeitaufgelöste Emissionsspektren (TRES) liefern dabei sowohl Informationen in der Wellenlängen- als auch in der Zeitdomäne. Erstmalig wurden die TRES mittels einer umfangreichen Auswertemethodik behandelt. Neben der Anpassung des Abklingverhaltens mit einer diskreten Zahl von Exponentialfunktionen, wurden unterstützend auch Abklingzeitverteilungsanalysen durchgeführt. Zeitaufgelöste flächennormierte Emissionsspektren (TRANES), eine Erweiterung der normalen TRES, konnten erstmals zur Bestimmung der Zahl der emittierenden Lanthanoidspezies in porösen Materialien genutzt werden. Durch die Berechnung der Decayassoziierten Spektren (DAS) konnten den Lanthanoidspezies die entsprechenden Lumineszenzspektren zugeordnet werden. Zusätzlich konnte, speziell im Fall der Europium-Lumineszenz, durch Kombination von zeitlicher und spektraler Information das zeitabhängige Asymmetrieverhältnis R und die spektrale Evolution des 5D0-7F0-Übergangs mit der Zeit t untersucht und somit wesentliche Informationen über die Verteilung der Europiumionen im Wirtsmaterial erhalten werden. Über die Abklingzeit und das Asymmetrieverhältnis R konnten Rückschlüsse auf die Zahl der OH-Oszillatoren in der ersten Koordinationssphäre und die Symmetrie der Koordinationsumgebung gezogen werden. Für die mikroporösen und mikroporös-mesoporösen Materialien wurden verschiedene Lanthanoidspezies, im Regelfall zwei, gefunden, welche entsprechend der beschriebenen Methoden charakterisiert wurden. Diese Lanthanoidspezies konnten Positionen in den Materialien zugeordnet werden, die sich im tief Inneren des Porensystems oder auf bzw. nahe der äußeren Oberfläche oder in den Mesoporen befinden. Erstere Spezies ist aufgrund ihrer Position im Material gut vor Feuchtigkeitseinflüssen geschützt, was sich deutlich in entsprechend langen Lumineszenzabklingzeiten äußert. Zusätzlich ist diese Europiumspezies durch unsymmetrische Koordinationsumgebung charakterisiert, was auf einen signifikanten Anteil an Koordination der Lanthanoidionen durch die Sauerstoffatome im Wirtsgitter zurückzuführen ist. Ionen, die sich nahe oder auf der äußeren Oberfläche befinden, sind dagegen für Feuchtigkeit zugänglicher, was in kürzeren Lumineszenzabklingzeiten und einer symmetrischeren Koordinationsumgebung resultiert. Der Anteil von Wassermolekülen in der ersten Koordinationssphäre ist hier deutlich größer, als bei den Ionen, die sich tiefer im Porensystem befinden und entspricht in vielen Fällen der Koordinationszahl eines vollständig hydratisierten Lanthanoidions. Auch der Einfluss von Oberflächenmodifikationen auf die Speziesverteilung und das Verhalten der Materialien gegenüber Feuchtigkeit wurde untersucht. Dabei gelang es den Einfluss der Feuchtigkeit auf die Lumineszenzeigenschaften und die Speziesverteilung durch die Oberflächenmodifikation zu verringern und die Lumineszenzeigenschaften teilweise zu konservieren. Im Fall der mesoporösen Silikamonolithe wurde auch eine heterogene Verteilung der Lanthanoidionen im Porensystem gefunden. Hier wechselwirkt ein Teil der Ionen mit der Porenwand, während sich die restlichen Ionen in der wäßrigen Phase innerhalb des Porensystems aufhalten. Das Aufbringen von Oberflächenmodifikationen führte zu einer Wechselwirkung der Ionen mit diesen Oberflächenmodifikationen, was sich in Abhängigkeit von der Oberflächenbeladung in den enstprechenden Lumineszenzeigenschaften niederschlug. / Porous sol-gel materials are suitable for many applications and subject to ongoing research activities. This includes classical applications, e.g. as catalyst, molecular sieve or drying agent, as well as non-classical applications, e.g. as contrast agent in magnetic resonance tomography or in the form of thin zeolite films as isolators in microchips. The interest in porous materials also covers photonic applications as shown by the development of the zeolite-dye-microlaser. Zeolites, which belong to the subfamily of microporous materials, can be converted into luminescent materials using simple ion-exchange procedures. In addition to the creation of a luminescent material, which luminescence properties have to be characterized, the incorporation of lanthanide ions offers the possibility to use these ions as a luminescent probe for the characterization of the ion-host interactions. This is particularly interesting concerning the application of porous materials as catalysts. Therefor, the unique luminescence properties of the lanthanide ions europium(III) and terbium(III) are used. In this work lanthanide-doped microporous zeolites, microporous-mesoporous hybrid materials and mesoporous silicates were investigeted regarding their luminescence properties and the ion-host-interactions using time-resolved luminescence spectroscopy. Thereby, time-resolved emission spectra (TRES) provide information in the wavelength and time domain. For the analysis of the TRES a broad set of analytic methods was applied and thus a corresponding “toolbox“ developed. Fitting of the luminescence decays was performed with a discrete number of exponentials and supported by luminescence decay times distributions. Time-resolved area normalized emission spectra (TRANES), an advancement of TRES, could be used for the determination of the number of emissive lanthanide species in porous materials for the first time. Calculation of the decay-associated spectra (DAS) allowed the correlation of spectral information with luminescence decay times and thus delivered the luminescence spectra of the different europium species. For europium(III) we could use in addition the time-dependent asymmetry ratio and spectral evolution of the 5D0-7F0-transition with time to obtain further information about the distribution of the lanthanide ions in the host material. Luminescence decay times and spectra allowed conclusions on the number of OH-oscillators in and the symmetry of the first coordination sphere. For the microporous and microporous-mesoporous materials were found different lanthanide species, which were characterized by the above mentioned methods. These lanthanide species can be found on different positions in the host material. One position is located deep in the pore system. Here, lanthanide ions are hardly accessible for water and mainly coordinated by framework oxygens. This results in long luminescence decay times and distorted coordination spheres. The second position can be found near or on the outer surface or in the mesopores. Lanthanide ions located here, are easily accessible for water and thus show shorter luminescence decay times and a more symmetrical coordination sphere, which is mostly made up by water molecules. Another investigated aspect was the influence of surface modifications on the luminescence behavior of the lanthanide ions inside the material. Here we could show, that surface modifications hydrophobize the material and thus are able to protect the lanthanide ions from water, which is important for the conservation of the luminescence properties. Concerning the mesoporous silicates, again a heterogeneous distribution of the lanthanide ions in the pore system was found. A part of the lanthanide ions interacts with the pore wall, while the other part is located in the aqueous phase inside the pores. Surface modification led to a interaction of the lanthanide ions with the modification. This was reflected in the luminescence properties depending on the structure of the modification and the surface loading.

Microporous materials have a wide range of important applications in separation, gas adsorption, ion-exchange and catalysis. Open-framework germanates are a family of microporous compounds and are of particular interest. This thesis focuses on the synthesis and characterization of new open-framework germanates as well as introducing the transition-metal nickel into germanate structures. One new microporous germanosilicate, SU-78 and four new open-framework germanates, SU-74, SU-75, SU-69 and SU-76 have been obtained by using organic molecules as structure directing agents (SDAs). The incorporation of nickel and organic SDAs in the synthesis resulted in five novel nickel germanates, SUT-1, SUT-2, SUT-3, SUT-4 and SUT-5, in which nickel complexes act either as framework-forming components or as structure directing agents. The general synthesis route is described and the variables that affect the synthesis products are summarized. Different techniques applied on the characterization of chemical and physical properties of the products are also introduced. / <p>At the time of the doctoral defense, the following papers were unpublished and had a status as follows: Paper 1: Submitted. Paper 2: Submitted. Paper 3: Submitted. Paper 5: Manuscript.</p>

Novel open-framework germanates and open low-dimensional structures were synthesized and characterized. Their crystal structures were solved by single crystal X-ray diffraction or X-ray powder diffraction combined with other techniques. Although related open-framework materials, such as zeolites, are of interest for the ability to selectively accommodate guest species in their rings, pores and channels, germanates are primarily of interest for their unique structural properties. Compared to aluminosilicate-based zeolites, germanium oxides readily form frameworks with extra-large rings and low framework density. The formation of elegant germanate architectures is attributed to the unique Ge-O bond geometries compared to Si-O, and the tendency to form large clusters. This thesis is to serve as an introduction to germanate synthesis, structures and characterization. Structures are categorized in accordance to their building units; the Ge7X19 (Ge7), Ge9X25-26 (Ge9) and Ge10X28 (Ge10) (X = O, OH, or F) clusters. Structure determination techniques as well as the characterization techniques used to examine the properties of the materials are presented. While most of the discussed techniques have routinely been used to study crystalline open-frameworks, we introduce the use of infrared spectroscopy for the identification of cluster types, valuable for structure determination by X-ray powder diffraction. Structures and properties of the novel materials ASU-21, SU-62, SU-63, SU-64, SU-65, SU-66, SU-71, SU-72, SU-73, SU-74, SU-75 and SU-JU-14 are described and put into context with previously known structures. The novel structures are all built of the Ge7, Ge9 or Ge10 clusters, and vary from a framework with novel topology to the first open zero-dimensional germanate cavities built of such clusters. / <p>At the time of the doctoral defense, the following papers were unpublished and had a status as follows: Paper 2: Submitted. Paper 3: Manuscript. Paper 4: Submitted. Paper 6: Submitted. Paper 7: Manuscript. Paper 8. Manuscript. Paper 10: Unpublished book chapter.</p><p> </p>

Zeolites are a well-known class of crystalline oxide materials with tunable compositions and nanoporous structures, and have been used extensively in catalysis, adsorption, and ion exchange. The zeolite MFI is one of the well-studied zeolites because it has a pore size and structure suitable for separation or chemical conversion of many industrially important molecules. Modification of zeolite structures with organic groups offers a potential new way to change their properties of zeolites, beyond the manipulation of the zeolite framework structure and composition. The main goals of this thesis research are to study the organic-modification of the MFI pore structure, and to assess the effects of such modification on the adsorption and transport properties of zeolite MFI sorbents and membranes. In this work, the internal pore structure of MFI zeolite particles and membranes has been modified by direct covalent condensation or chemical complexation of different organic molecules with the silanol defect sites existing in the MFI structure. The organic molecules used for pore modification are 1-butanol, 1-hexanol, 3-amino-1-propanol, 1-propaneamine, 1,3-diaminopropane, 2-[(2-aminoethyl)amino]ethanol, and benzenemethanol. TGA/DSC and 13C/29Si NMR characterizations indicated that the functional groups were chemically bound to the zeolite framework, and that the loading was commensurate with the concentration of internal silanol defects. Gas adsorption isotherms of CO2, CH4, and N2 on the modified zeolite materials show a range of properties different from that of the bare MFI zeolite. The MFI/3-amino-1-propanol, MFI/2-[(2-aminoethyl)amino]ethanol, and MFI/benzenemethanol materials showed the largest differences from bare MFI. These properties were qualitatively explained by the known affinity of amino- and hydroxyl groups for CO2, and of the phenyl group for CH4. The combined influence of adsorption and diffusion changes due to modification can be studied by measuring permeation of different gases on modified MFI membranes. To study these effects, I synthesized MFI membranes with [h0h] out-of-plane orientation on α-alumina supports. The membranes were modified by the same procedures as used for MFI particles and with 1-butanol, 3-amino-1-propanol, 2-[(2-aminoethyl)amino]ethanol, and benzenemethanol. The existence of functional groups in the pores of the zeolite was confirmed by PA-FTIR measurements. Permeation measurements of H2, N2, CO2, CH4, and SF6, were performed at room temperature before and after modification. Permeation of n-butane, and i-butane were measured before and after modification with 1-butanol. For all of the studied gases, gas permeances decreased by 1-2 orders of magnitude compared to bare MFI membranes for modified membranes. This is a strong indication that the organic species in the MFI framework are interacting with or blocking the gas molecule transport through the MFI pores. A detailed fundamental study of the CO2 adsorption mechanism in modified zeolites is necessary to gain a better understating of the adsorption and permeation behavior of such materials. Towards this end, an in situ FTIR study was performe.For the organic molecules with only one functional group (1-butanol, benzenemethanol, and 1-propaneamine), physical adsorption was found - as intuitively expected - to be the only observed mode of attachment of CO2 to the modified zeolite material. Even in the case of MFI modified with 1,3-diaminopropane, only physical adsorption is seen. This is explained by the isolated nature of the amine groups in the material, due to which only a single amine group can interact with a CO2 molecule. On the other hand, chemisorbed CO2 species are clearly observed on bare MFI, and on MFI modified with 3-amino-1-propanol or 2-[(2-aminoethyl)amino]ethanol. Specifically, these are carbonate-like species that arise from the chemisorption of CO2 to the silanol group in bare MFI and the alcohol groups of the modifying molecule. The possibility of significant contributions from external surface silanol groups in adsorbing CO2 chemisorbed species was ruled out by a comparative examination of the FTIR spectra of 10 μm and 900 nm MFI particles modified with 2-[(2-aminoethyl)amino]ethanol.