Afin de limiter les rejets de polluants dans l’atmosphère par les véhicules, les normes Euro ont été mises en place en Europe à partir des années 1990. Ces normes sont de plus en plus strictes. Par exemple, pour les cas des poids lourds, le maximum d’émission des NOx a été divisé par cinq lors du passage Euro V (2009) à Euro VI (2014). Parallèlement à cela, certaines flottes captives de poids lourds roulent au 100 % biodiesel. Or, ce carburant contient des minéraux (Na, K, P) qui peuvent interagir avec la ligne de dépollution des gaz d’échappement.Dans ces travaux, l’étude a porté sur l’impact de Na et P déposés séparément ou simultanément sur des catalyseurs de réduction catalytique sélective des oxydes d’azote par l’ammoniac (NH3-SCR) à base de zéolithe Ferrierite (FER) contenant du cuivre.En mettant en relation les activités catalytiques en NH3-SCR et les différentes caractérisations mises en œuvre avant et après ajout des minéraux, il a été conclu que l’ajout de sodium entrainait une perte d’activité à basse température (< 300 °C) liée à l’empoisonnement des sites acides du catalyseur, et que la perte d’activité à haute température (> 450 °C) est liée à la formation de CuO. Cette formation de CuO est due à un échange entre le cuivre et le sodium lors de l’empoisonnement par voie aqueuse. Pour l’empoisonnement au phosphore, la désactivation à basse température (< 300 °C) apparait liée à une interaction entre le cuivre et le phosphore. Cette interaction entraine une augmentation de la température de réduction du cuivre. L’ajout simultané de sodium et phosphore entraine une désactivation des catalyseurs plutôt similaire à celle du phosphore qu’à celle du sodium. / In order to decrease the air pollution due to vehicles, European legislation have been implemented since the 90’s. The European norm are stricter. For example, the NOx emissions limit for trucks were divided by five between Euro V (2009) and Euro VI (2014). In parallel, some trucks use exclusively 100 % biodiesel. Unfortunately, biodiesel contains some minerals (Na, K, P) with can interact with the exhaust gas post-treatment system.This work presents the impact of Na and/or P deposits on Selective Catalytic Reduction catalysts with dedicated to the NH3-SCR process, based on copper/Ferrierite (FER).By combining the results of NH3-SCR catalytic activity and characterisations before and after adding minerals, the main parameters of deactivation were highlighted. Sodium deactivation at low temperature (< 300 °C) is due to the decrease of acidity. The deactivation at high temperature (> 450 °C) is due to the formation of copper oxide when sodium was added in water. This formation of CuO results of an exchange of Na and Cu in the exchange positions of the zeolite. Phosphorous addition mainly leads to a catalytic deactivation at low temperature (< 300 °C), the deactivation seems to be link to Cu-P interaction. This interaction leads to the increase of the reduction temperature of copper. Overall, the simultaneous addition of sodium and phosphorous leads to a decrease of catalytic activity similar to the one with phosphorous alone.

As indústrias lançam diversos poluentes no meio ambiente. Dentre os poluentes destacam-se os elementos tóxicos presentes em efluentes líquidos por acarretarem alto risco potencial à saúde humana e ao meio ambiente. Os efluentes podem ser tratados por materiais adsorventes, os quais podem ser provindos de resíduos industriais. Uma forma de contribuir significativamente na sustentabilidade de uma indústria é a transformação de um de seus resíduos em sub-produto de valor agregado para aplicação no tratamento de seus efluentes líquidos como adsorvente de baixo custo. O objetivo deste trabalho foi sintetizar, e caracterizar zeólitas de cinzas de carvão e avaliar sua aplicação como material adsorvente no tratamento de efluente. Os materiais zeolíticos derivados de três tipos diferentes de cinzas de carvão (cinzas manga, cinzas ciclone e cinzas pesadas) geradas na usina termelétrica de Figueira-PR foram usados para tratar o lixiviado do aterro de cinzas de carvão da mesma usina. As seguintes características das zeólitas foram determinadas: composição mineralógica, composição química, teor de carbono total, análise morfológica, área superficial específica, capacidade de troca catiônica (CTC), perda ao fogo, pH, condutividade e densidade aparente. A fase zeolítica formada foi do tipo sodalita com as três amostras usadas como matéria prima após ativação hidrotérmica alcalina. O material zeolítico de cinzas manga apresentou a menor relação SiO2/Al2O3 (1,46), maior CTC (2,36 meq g-1) e área superficial específica (69,5 m2 g-1) e, consequentemente, maior capacidade de remoção dos íons do efluente. As concentrações de As e Cr estavam acima do padrão de lançamento de efluentes. As três amostras de materiais zeolíticos apresentaram uma remoção significativa de Ni, Cd, Zn e Co na dose de 10 g.L-1. Os materiais zeolíticos das cinzas manga e ciclone foram eficientes para reduzir a concentração de As abaixo do limite imposto pela legislação, enquanto a remoção do Cr não foi efetiva com nenhum dos materiais. Na segunda etapa do trabalho, as zeólitas foram modificadas com o surfactante brometo de hexadeciltrimetilamônio (HTDMA-Br) em concentrações de 1,8 e 20 mmol L-1. A modificação das zeólitas não melhorou a eficiência de remoção do As. A remoção do Cr usando a amostra de zeólita de cinzas manga modificada com HDTMA-Br 20 mmol L-1 resultou em uma concentração final muito próxima ao limite permitido pela legislação. / The industries release various types of pollutants into to the environment. Among these pollutants are the liquid effluents containing toxic elements, they carry a high potential risk to human health and the environment. Some effluents can be treated by adsorbent materials, which can be made from industrial waste. One way to contribute significantly to the sustainability of an industry is to transform one of its residues into a value-added by-product and use in the treatment of its own liquid effluents as a low cost adsorbent. The objective of this estudy was to synthesize and characterize coal ash zeolites and evaluate their application as adsorbent material in the treatment of effluent. Zeolite materials derived from three different types of coal ash (fly ashes, cyclone ashes and heavy ashes) generated at the Figueira-PR thermoelectric plant were used to treat leachate from the coal ash landfill of the same plant. The following zeolite characteristics were determined: mineralogical composition, chemical composition, total carbon content, morphological analysis, specific surface area, cation exchange capacity (CTC), fire loss, pH, conductivity and bulk density. The zeolite phase formed with the three samples used as raw material after alkaline hydrothermal activation was sodalite. The zeolite material from fly ash had the lowest SiO2/Al2O3 ratio (1.46), higher CTC (2.36 meq g-1) and specific surface area (69.5 m2 g-1) and, consequently, greater effluent removal capacity. The As and Cr concentrations were above the effluent discharge standard. The three samples of zeolitic materials showed a significant removal of Ni, Cd, Zn and Co in the dose of 10 g L-1. The zeolite materials from fly and cyclone ash were efficient to reduce As concentrations below the limit imposed by legislation, while removal of Cr was not effective with any of the materials. In the second stage of the study, the zeolites were modified with the surfactant hexadecyltrimethylammonium bromide (HTDMA-Br) in concentrations of 1.8 and 20 mmol.L-1. The zeolite removal efficiency of As did not improve after its modification. Removal of Cr using the 20 mmol.L-1 modified HDTMA-Br modified fly ash zeolite sample resulted in a final concentration very close to the limit allowed by the legislation.

Thesis (Master of Engineering in Chemical Engineering)--Cape Peninsula University of Technology, 2018. / Zeolites have found applications as heterogeneous or solid catalyst in the petrochemical and refining industries. Zeolite ZSM-5 in particular is a highly siliceous solid catalyst with a porous network that consists of medium pore structure (pore openings 5-5.5 A). The solid catalyst (ZSM-5) is well known for its high temperature stability and strong acidity, which makes it an established catalyst used for different petrochemical processes such as Methanol-To-Gasoline (MTG), isomerisation, disproportionation, and cracking. Unlike in the past, the synthesis of zeolite ZSM-5 from other sources that contains silica (Si) and alumina (Al) with the addition of a template (TPBr) as a structure-directing agent is eminent. Its synthesis can be achievable from coal fly ash that is a waste material and a cheap source of Si and Al. Coal fly ash is a waste material that is produced during the combustion of coal to generate electricity. The elemental composition of coal fly ash consists of mostly SiO2 and Al2O3 together with other significant and trace elements. Zeolite ZSM-5 catalyst synthesised from coal fly ash by previous authors required an excessive amount of additional source of silica even though the XRD spectra still show the presence of quartz and mullite phase in the final products. These phases prevented the use of fly ash (solid) as a precursor to synthesise zeolite ZSM-5 products. However, the synthesis of high purity zeolite ZSM-5 products by extracting silica and alumina from South African fly ash and then using it with small amounts of fumed silica was investigated This aim was achieved by fusing fly ash (FA) with sodium hydroxide (NaOH) under hydrothermal condition set at 550 oC for 1 hour 30 minutes. The quartz and mullite phase observed by previous authors was digested by the fusion process. Thereafter, the treatment of fused fly ash filtrate (FFAF) with concentrated H2SO4 (98-99%), precipitated silica and removed Al that therefore increased the Si/Al ratio from 1.97 in fly ash (FA) to 9.5 in the silica extract (named fused fly ash extract). This route was designed to improve the quality of the final products and reduced the amount of fumed silica added to the synthesis mixture prior to hydrothermal synthesis. In this line of investigation, the process of adding fumed silica to the hydrothermal gel was optimised. H-FF1 with a Si/Al ratio of 9.5 was synthesised using the silica extract without the addition of fumed silica. Its XRD, SEM and relative crystallinity results proved that H-FF1 was inactive and hence was not further characterised and utilised in the conversion of methanol to hydrocarbons (MTH). Purer phase zeolite ZSM-5 products (H-FF2 and H-FF3) that were synthesised from silica extract with the addition of small amounts of fumed silica were characterised and successfully used in the methanol to hydrocarbons (MTH) reaction. The synthesised ZSM-5 products had different Si/Al ratio, different morphology, crystal size, BET surface area, and relative crystallinity as well as different trends in the MTH reaction. It was also observed that H-FF2 and H-FF3 (pure phase) solid catalyst deactivated faster than the commercial H-ZSM-5 in the MTH reaction. However, the MTH conversion over H-FF2 competed with that of the commercial H-ZSM-5 within 3 hours of time on stream (TOS) but later deactivated at a faster rate. This was caused by the large crystal size and reduced BET surface area of H-FF2 when compared to the commercial H-ZSM-5. However, H-FF2 performed better than H-FF3 on stream (MTH reaction) due to its smaller crystal size and higher BET. This study has successfully utilised a route that synthesised high purity zeolite ZSM-5 products from the South African fused fly ash extract (FFAE) with the addition of small amounts of fumed silica. The properties of the synthesised zeolite ZSM-5 products (H-FF2 and H-FF3) were similar to that of the commercial H-ZSM-5 as well as active in the MTH reaction. This promoted the utilisation of a waste material (coal fly ash) to synthesise highly siliceous zeolite ZSM-5 products that avoided the presence of mineral phases from fly ash in the final products.

Afin de répondre aux problématiques écologique et économique du traitement des Matériaux Contenant de l’Amiante (MCA), un procédé complet permettant de traiter de manière optimale ces déchets a été proposé. Pour cela, trois types de déchets ont d’abord été analysés par plusieurs techniques de caractérisation complémentaires (diffraction des rayons X, microscopie électronique à balayage, infrarouge et RMN du solide). Ces analyses ont permis l’identification des différentes phases présentes au sein des déchets. Cette identification est nécessaire, car elle permet d’adapter de manière optimale le procédé de destruction au déchet. La première étape de ce procédé est le traitement en température des MCA dans une solution d’acide nitrique. Elle permet la dissolution de la matrice du déchet et la dénaturation des fibres de chrysotile qui sont présentes dans 95 % des déchets amiantés. Deux phases sont alors récupérées à l’issue de ce traitement : une phase solide composée de silice pure et une phase liquide contenant, notamment, du calcium, du magnésium et du fer. Si les déchets contiennent des fibres de type amphibole (5 % des MCA) ils sont ensuite traités par voie hydrothermale dans un autoclave contenant une solution de soude. Cette étape mène à la dissolution complète du déchet. Une solution basique contenant du silicium est ainsi récupérée. Différentes voies de valorisations ont été développées. Les ions présents dans la solution acide sont récupérés par précipitation sélective des hydroxydes. Une autre voie consiste à synthétiser une zéolithe à partir de la silice pure et de la solution basique. Les isothermes d’adsorption de cette dernière ont été tracés afin de déterminer sa capacité d’adsorption de certains cations métalliques polluants. Pour terminer, une étude fondamentale a été menée sur les nanotubes de silice obtenus avec le traitement de fibres d’amiante pures et différentes applications de ces nanotubes de silice ont été évoquées. / To answer the ecological and economic problems of the treatment of Materials Containing Asbestos (MCA), a complete process allowing to handle in an optimal way these waste was proposed. For that purpose, three types of waste were analyzed by several complementary techniques of characterization (X-rays diffraction, Scanning Electron Microscopy, infrared and NMR spectroscopy). These analyses allowed the identification of the present various phases within waste. This identification is necessary, because it allows to adapt in the optimal way for the destruction of the waste. The first stage of the process is a treatment in temperature of the MCA in a solution of nitric acid leading to the dissolution of the matrix of the waste and the denaturation of the fibers of chrysotile which are present in 95 % of MCA. Two phases are then got back at the end of this treatment: a solid phase of pure silica and a liquid phase containing, in particular, calcium, magnesium and iron ions. If previous waste contains fibers of amphibole type (5 % of the MCA) they are then treated through a hydrothermal process in an autoclave containing a solution of soda. This stage leads to the complete dissolution of the waste. The basic solution containing some silicon is so got back. Various ways of valuations were then developed. The present ions in the acid solution are chemically sorted out by a selective precipitation of hydroxides. Another way consists in synthesizing a zeolite from the pure silica coming from the acid treatment and from the basic solution after hydrothermal treatment. The isotherms of adsorption of this synthesized zeolite were established to determine its capacity of adsorption of certain polluting metallic cations. To finish, a fundamental study was led on the nanotubes of silica obtained after the acid treatment of pure asbestos fibers and diverse applications of these nanotubes of silica were evoked.

Les zéolithes sont des aluminosilicates cristallins possédant une microporosité organisée et régulière de taille moléculaire. Les zéolithes ZSM-5 sont largement employées dans l’industrie comme catalyseurs acides mais leur application commerciale requiert des objets de taille millimétrique pour leur résistance mécanique, pour diminuer la perte de charge dans les réacteurs et pour diluer l’acidité de la zéolithe, principalement par ajout de liant, peptisant... La mise en forme est l’étape clé dans le processus d’industrialisation d’un catalyseur car les additifs peuvent modifier les propriétés intrinsèques de la zéolithe après mise en forme. Les objectifs de la thèse sont donc d’identifier et de rationaliser les conséquences physico-chimiques de la mise en forme sur les propriétés des zéolithes en étudiant l’accessibilité, la concentration et la force de leurs sites acides, ainsi que de décrire la nature de l’interface zéolithe/liant. Pour cela, une approche multi-techniques a été mise en œuvre. Elle combine des mises en forme modèles, tout en faisant varier la nature du liant et de la zéolithe ZSM-5, des caractérisations texturales, spectroscopiques (infra-rouge, RMN) et de microscopies, de l’acidité (adsorption-désorption de molécules sondes suivies par analyses thermiques et spectroscopiques), et tests catalytiques modèles. La caractérisation des propriétés des zéolithes utilisées dans cette étude (de différentes tailles de cristaux et de différents rapports Si/Al) a été menée préalablement à celles des matériaux mis en forme. Les grands cristaux de zéolithes se sont révélés plus acides mais moins actifs en catalyse. Une partie des Al des petits cristaux forment des aluminols dont l’acidité est plus faible que celle des sites pontés. De plus, l’ensemble des sites pontés ne contribue pas à la réaction catalytique, seule une partie du cristal est efficace. Durant ce travail, deux types de liants ont été utilisés : l’alumine et la silice qui sont largement employées dans l’industrie. Le but a été de mettre en évidence, dans un premier temps, les effets de la mise en forme sur une zéolithe et un liant donné puis d’estimer l’impact de la nature de la zéolithe (taille de cristal et rapport Si/Al). Pour le liant de type alumine, un bouchage partiel de la microporosité est suspecté indépendamment de la taille des cristaux et du rapport Si/Al de la zéolithe. Un phénomène d’alumination de la structure de la zéolithe par création de sites pontés a été mis en évidence. Pour le liant de type silice, le paramètre critique à prendre en considération lors de la mise en forme est sa teneur en cations sodium. Le phénomène d’échange ionique a été mis en évidence, les propriétés acides et catalytiques des catalyseurs s’effondrent mais de manière réversible. Cet effet augmente quand la taille des cristaux de zéolithes diminue et quand le rapport Si/Al augmente / Zeolites are crystalline and microporous aluminosilicates with an ordered and regular structure of molecular dimension. ZSM-5 zeolites are widely used in the industry as acid catalysts but their commercial application requires millimeter-sized bodies for mechanical strength and dilution of the zeolite acidity mainly, by addition of binder, peptizer... Shaping of zeolite is the key step of the process for the industrialization of a catalyst because the additives may modify the intrinsic properties of zeolites after shaping. The aims of this PhD thesis are to identify and rationalize the physico-chemical impacts of shaping on the zeolite properties by studying the accessibility, the concentration and the strength of acid sites, as well as to describe the zeolite/binder interface. To do this, a multi-technical approach was set up. It combines model shaped materials, by varying the type of binder and ZSM-5 zeolite, textural, spectroscopic (IR, NMR) and acid characterizations, microscopy and catalytic testing. The characterization of zeolites used in this study (various crystal sizes and Si/Al ratios) was carried out prior of those of shaped materials. Large crystals have been shown more acid but less active in catalysis. Some of Al of the small crystals form aluminols whose acidity is weaker than that of bridging sites. Moreover, all the bridging sites do not contribute to the catalytic reaction, only a part of the crystal is efficient. During this work, two types of binders were used: alumina and silica which are widely used in the industry. The strategy was to highlight, in a first step, the shaping impacts on a ZSM-5 and a given binder and then, to estimate the impact of the zeolite nature (crystal size and Si/Al ratio). For the alumina-type binder, a partial pore blocking is suspected, independently of the crystal size and the Si/Al ratios. A phenomenon of alumination of the zeolite structure was found. For the silica-type binder, the critical parameter is the content of sodium cations inside the binder before the shaping. An ion exchange phenomenon was highlighted and the acid and catalytic properties of the materials collapse but in a reversible way. This impact increases when the crystal size decreases and when the Si/Al ratio increases

The current study investigated application of natural adsorbents in brine treatment. Brines are hypersaline waters generated in power stations and mining industries rich in Mg2+, K+, Ca2+, Na+, SO4 2- , Cl- and traces of heavy metals, thus there is a need for these brines to be treated to recover potable water and remove problematic elements. Natural adsorbents have been successfully used in waste water treatment because of their high surface area and high adsorptive properties when they are conditioned with acid or base. The investigation of pH showed that natural adsorbents did not perform well at low pH of 4 and 6. The adsorbents were able to work efficiently at the natural pH of 8.52 of the brine solution. These results show that natural adsorbents hold great potential to remove cationic major components and selected heavy metal species from industrial brine wastewater. Heterogeneity of natural adsorbents samples, even when they have the same origin, could be a problem when wastewater treatment systems utilizing natural clinoptilolite and bentonite are planned to be developed. Therefore, it is very important to characterize the reserves fully in order to make them attractive in developing treatment technologies.

Zeolites are crystalline inorganic solids that are industrially used for adsorption, ion exchange and catalysis. As catalysts, they have been particularly successful in the hydrocarbon processing industry due to their unique activities and selectivities. Zeolites are mainly used in acid catalyzed reactions, but their catalytic functionality can be diversified through the incorporation of elements that are traditionally not part of their framework. The incorporation of various elements has been studied in recent decades resulting in zeolites with potential to perform different chemistries or improve catalytic performance in existing ones. However, many of these investigations have been conducted under conditions that do not necessarily represent realistic scenarios for industrial implementation. The main objective of this dissertation was to study the single and simultaneous framework incorporation of tin, boron, germanium and aluminum in MFI zeolites under synthesis conditions that are more in line with industrial preparations. These include the use of mixtures in alkaline media with high concentration of precursor species. The interest on tin resides on its potential for Lewis acid catalysis, while boron and germanium have potential for modulating acid strength and enhancing catalytic properties respectively. Three specific systems were studied: MFI zeolites with simultaneous incorporation of germanium and aluminum (i.e. Ge-Al-MFI zeolites), MFI zeolites with simultaneous incorporation of germanium and boron (i.e. B-Ge-MFI zeolites), and MFI zeolites with single incorporation of tin (i.e. Sn-MFI zeolites). Systematic synthesis experiments were coupled with extensive analytical characterization in order to assess how element incorporation and zeolite physicochemical properties are affected by synthesis conditions. In addition, the catalytic activity of Sn-MFI zeolites for the hydroxylation of phenol was studied. The general conclusion from this work is that framework incorporation of these elements is highly influenced by pH, mixture composition and the presence of sodium cations. Sodium cations are commonly included in industrial preparations through the use of sodium hydroxide, but they were found to negatively affect framework incorporation due to a tendency to form stable extra-framework impurities with the heteroatoms, especially germanium and tin. pH and mixture composition are particularly influential in controlling germanium and boron incorporation, while the incorporation of tin, its coordination environment and catalytic performance were found to depend on synthesis conditions as well as post-synthesis treatments.

Crosslinkable mixed matrix membranes represent an attractive technology that promises both outstanding separation properties and swelling resistance for the purification of natural gas. This approach relies upon dispersal of a CO2/CH4 size-discriminating zeolite in a crosslinkable polymer, which is resistant to CO2 swelling when crosslinked. The resulting membrane has the potential to separate CO2 from CH4 more effectively than traditional pure polymer membranes, while also providing needed membrane stability in the presence of aggressive CO2-contaminated natural gas streams. Control studies are conducted using the pure crosslinkable polymer to observe the separation properties and swelling resistance. Initial crosslinkable mixed matrix membrane experiments are then performed and result in an increase in membrane productivity, instead of the expected increase in selectivity. Traditionally, this is caused by material incompatibility at the polymer/zeolite interface, so the crosslinkable mixed matrix membranes are characterized to examine this issue. During the material characterization, a new non-ideal transport phenomenon is discovered in the zeolite phase. A model is developed to better understand the transport and predict subsequent experimental results. Once the independent materials are proven to be viable, crosslinkable mixed matrix membranes that show enhancements in both efficiency and productivity and exhibit stability in the presence of aggressive CO2 feeds are created.

Mixed matrix membranes offer an attractive route to the development of high performance and efficiency membranes required for demanding gas separations. Such membranes combine the advantageous processing characteristics of polymers with the excellent separation productivity and efficiency of molecular sieving materials. This research explores the development of mixed matrix membranes, namely in the form of asymmetric hollow fiber membranes using zeolites as the molecular sieving phase and commercially available high performance polymers as the continuous matrix. Lack of adhesion between the typically hydrophobic polymer and the hydrophilic native zeolite surface is a major hurdle impeding the development of mixed matrix membranes. Silane coupling agents have been used successfully to graft polymer chains to the surface of the zeolite to increase compatibility with the bulk polymer in dense films. However, transitioning from a dense film to an asymmetric structure typically involves significant processing changes, the most important among them being the use of phase separation to form the asymmetric porous structure. During the phase separation, it is believed that hydrophilic sieves can act as nucleating agents for the hydrophilic polymer lean phase. Such nucleation tendencies are believed to lead to the formation of gaps between the polymer and sieve resulting in poor mixed matrix performance. This research focuses on defining procedures and parameters to form successful mixed matrix hollow fiber membranes. The first part of this dissertation describes dope mixing procedures and unsuccessful results obtained using a silane coupling agent to enhance polymer-zeolite adhesion. The next section follows the development of a highly successful surface modification technique, discovered by the author, employing the use of a Grignard reagent. As a test case, two zeolites of different silicon-to-aluminum ratios are successfully modified and used to develop mixed matrix membranes with greatly increased gas separation efficiencies. The broad applicability of the surface treatment is also demonstrated by the successful incorporation of the modified zeolites in a second polymer matrix. The final section of the work describes the novel occurrence of large defects (macrovoids) caused by the presence of large zeolite particles proposing a particle size effect in the formation of such defects.

Nanoporous materials have attracted tremendous interest, investment and effort in research and development due to their potential applications in various areas such as membranes, catalysis, sensors, delivery, and micro devices. Controlling a nanoporous material’s microstructure is of great interest due to the strong influence on efficiency and performance. For particles, microstructure refers to particle size, shape, surface morphology, and composition. When discussing thin films, microstructure includes film thickness, crystal orientation and grain boundaries. In this respect, we focus to develop novel methods for the synthesis and characterization of nanoporous materials and their films, which are capable of controlling the microstructure of material. This dissertation is composed of two main sections and each explores the fabrication of a different nanoporous material: 1) A simple fabrication method for producing oriented MFI zeolite membranes with controlled thickness, orientation, and grain boundary; 2) A microfluidic synthesis of ordered mesoporous silica particles with controllable size, shape, surface morphology, and composition. The first section of this dissertation demonstrates a simple and commercially viable method termed the micro-tiles-and-mortar method to make continuous b-oriented MFI membranes with controlled membrane microstructure. This simple method allows for control of the thickness of the membrane by using plate-like seed crystals with different thicknesses along the b-axis (0.5 μm to 2.0 μm), as well as to manipulate the density and structure of grain boundaries. Microstructural effects of silicalite-1 membranes on the gas separation are investigated by measuring the permeation and separation for xylene isomers. In the second section of this dissertation, a new synthesis method for the ordered mesoporous silica particles with controllable microstructure is demonstrated. This novel method combines a microfluidic emulsification technique and nonaqueous inorganic synthesis with a diffusion-induced self-assembly (DISA). The systematic control of the particle microstructure such as size, shape, and surface morphology is shown by adjusting microfluidic conditions.