Despite comprehensive studies addressing the chemical kinetics of butanol isomers, relevant uncertainties associated with the emissions of relevant pollutants persists. Also, a lack of chemistry knowledge of processes designed to produce biofuels limits their implementation at industrial scales. Therefore, the first objective of this thesis was to use cutting-edge kinetic theories to calculate rate constants of propen-2-ol, 1-pronenol, and vinyl alcohol keto-enol tautomerizations, which account for the production of the harmful carbonyl species. The second objective was to use the predictive capabilities of dynamic theories to reveal new chemistry of syngas oxy-combustion in supercritical CO2 and complexities of the zeolite dealumination, two processes involved in coal and biomass conversion. Rate constants computations considered transition state theory with variational effects, tunneling correction, and multistructural torsional anharmonicity. The study also included pressure effects by using and improving the system-specific quantum Rice-Ramsperger-Kassel/modified strong collision model. The atomistic simulations used ReaxFF force fields in hydrogen/oxygen/carbon monoxide/ carbon dioxide mixtures to represent the syngas system and an MFI zeolite with different water loading to model the dealumination. The results show that the studied assisted tautomerizations have much lower energy barriers than the unimolecular process. However, the “catalytic” effect is efficient only if the partner molecule is at high concentrations. Pressure effects are pronounced in the chemically activated tautomerizations, and the improved algorithm to compute pressure-dependent rate constants overcomes the initial difficulties associated with its application to C3 or larger molecules at temperatures above 800-1000 K. Reactive molecular dynamics simulations revealed the role of CO2 as an initiator in the syngas oxy-combustion and a new step involving the formation of formic acid. Those simulations for the zeolite dealumination process also showed that proton transfer, framework flexibility, and aluminum dislodging mediated by silicon reactions are complex dynamic phenomena determining the process. These aspects complement the dealumination theory uncovered so far and establish new paths in the study of water-zeolite interactions. Overall, the rate constants computed in this work reduce relevant uncertainties in the chemical kinetic mechanisms of alcohol oxidation, and the molecular dynamics simulations broaden the chemical knowledge of processes aimed at the utilization of alternative energy resources.

[ES] Las zeolitas son catalizadores ampliamente utilizados en una gran variedad de procesos químicos, por lo que la optimización de sus propiedades físico-químicas es fundamental para mejorar su aplicación en procesos de interés industrial y medioambiental. En la presente tesis doctoral se proponen diversas metodologías de síntesis directa y post-sintéticas con el fin de controlar aspectos importantes de estos materiales desde la escala microscópica hasta la molecular y atómica, así como su implicación directa en su aplicación como catalizadores y/o materiales conductores. En un primer objetivo, se estudia la influencia del tamaño de cristal y la estructura zeolítica en la transformación selectiva de CO2 hacia productos de interés como olefinas y aromáticos cuando se combina con un catalizador de hierro dopado con potasio. Por un lado, la estructura zeolítica tipo MFI (poro medio) permite maximizar la formación de productos aromáticos, mientras que las zeolitas tipo CHA (poro pequeño) y beta (poro grande) favorecen la formación de olefinas ligeras en distinta proporción. La utilización de las zeolitas ácidas nanocristalinas permite incrementar la formación de olefinas ligeras y aumentar el tiempo de vida de los catalizadores bifuncionales. Asimismo, se estudia el efecto del confinamiento a nivel molecular de diferentes estructuras zeolíticas de poro pequeño con distinto tipo de cavidad para la reacción de metanol a olefinas (MTO), pudiéndose correlacionar la selectividad hacia distintas olefinas ligeras con un parámetro teórico que depende de las dimensiones y la forma de las cavidades de los materiales microporosos. En segundo lugar, se estudia la estabilización de distintas especies metálicas en posiciones extra-red de los materiales zeolíticos, controlando su formación desde átomos individuales a clústeres y/o nanopartículas. La estructura de la zeolita CHA permite encapsular nanopartículas de Pt en el interior de sus cavidades, que son activas y estables para la reacción de oxidación de CO incluso tras tratamientos de envejecimiento a elevadas temperaturas. Por otro lado, se racionaliza la formación de nanopartículas de germanio dispersas en distintas matrices zeolíticas híbridas aprovechando la labilidad del germanio en la red cristalina de las mismas para su aplicación como materiales conductores. Se realiza una optimización de dichos materiales híbridos orgánicos-inorgánicos basados en nanopartículas de Ge mediante diversos tratamientos post-sintéticos, maximizando la dispersión de las nanopartículas y la formación de especies carbonosas para, finalmente, evaluar sus propiedades como materiales conductores. En último lugar, se utiliza esa labilidad del Ge en posiciones cristalinas de las zeolitas como estrategia para controlar a escala atómica la incorporación selectiva de distintos heteroátomos (Si y Sn). La síntesis de la estructura ITT con poros extra-grandes está limitada a bajas relaciones de Si/Ge, presentando por tanto una limitada estabilidad hidrotermal. Por ello, se lleva a cabo una sustitución isomórfica de átomos de Ge por átomos de Si, mejorando la estabilidad hidrotermal de dicho material para su aplicación en la reacción de craqueo catalítico de un gasoil de vacío, posibilitando su regeneración, y obteniendo similar selectividad a diésel y más propileno que con la muestra de origen. Por otro lado, se incorpora selectivamente Sn en la estructura BEC (polimorfo C de la zeolita beta) mediante tratamientos post-sintéticos en los defectos estructurales generados tras la eliminación de átomos de Ge, favoreciéndose la formación de sitios "abiertos" de Sn, que han demostrado ser más activos para reacciones de moléculas oxigenadas en comparación a los sitios "cerrados" de Sn. Las ventajas catalíticas del material Sn-BEC sintetizado se demuestran en la reacción Meerwein-Ponndorf-Verley-Oppenauer (MPVO), obteniéndose mayores velocidades de reacción por sitio de Sn "abierto" que con la zeolita Sn-beta(F) convencional. / [CA] Les zeolites són catalitzadors àmpliament utilitzats en una gran varietat de processos químics, per la qual cosa l'optimització de les seues propietats fisicoquímiques és fonamental per a millorar la seua aplicació en processos d'interès industrial i mediambiental. En la present tesi doctoral es proposen diverses metodologies de síntesi directa i post-sintètiques amb la finalitat de controlar aspectes importants d'aquests materials des de l'escala microscòpica fins a la molecular i atòmica, així com la seua implicació directa en la seua aplicació com a catalitzadors i/o materials conductors. Com a primer objectiu, s'estudia la influència de la grandària de cristall i l'estructura zeolítica en la transformació selectiva de CO¿ cap a productes d'interès com a olefines i aromàtics quan es combina amb un catalitzador de ferro dopat amb potassi. D'una banda, l'estructura zeolítica tipus MFI (porus mitjà) permet maximitzar la formació de productes aromàtics, mentre que les zeolites tipus CHA (porus xicotet) i beta (porus gran) afavoreixen la formació d'olefines lleugeres en diferent proporció. La utilització de les zeolites àcides nanocristalines permet incrementar la formació d'olefines lleugeres i augmentar el temps de vida dels catalitzadors bifuncionals. Així mateix, s'estudia l'efecte del confinament a nivell molecular de diferents estructures zeolítiques de porus xicotet amb diferent tipus de cavitat per a la reacció de metanol a olefines (MTO), podent-se correlacionar la selectivitat cap a diferents olefines lleugeres amb un paràmetre teòric que depèn de les dimensions i la forma de les cavitats dels materials microporosos. En segon lloc, s'estudia l'estabilització de diferents espècies metàl·liques en posicions extra-xarxa dels materials zeolítics, controlant la seua formació des d'àtoms individuals a clústers i/o nanopartícules. L'estructura de la zeolita CHA permet encapsular nanopartícules de Pt a l'interior de les seues cavitats, actives i estables per a la reacció d'oxidació de CO fins i tot després de tractaments d'envelliment a elevades temperatures. D'altra banda, es racionalitza la formació de nanopartícules de germani disperses en diferents matrius zeolítiques híbrides aprofitant la labilitat del germani en la xarxa cristal·lina de les mateixes per a la seua aplicació com a materials conductors. Es realitza una optimització d'aquests materials híbrids orgànics-inorgànics basats en nanopartícules de Ge mitjançant diversos tractaments post-sintètics, maximitzant la dispersió de les nanopartícules i la formació d'espècies carbonoses per a, finalment, avaluar les seues propietats com a materials conductors. En últim lloc, s'utilitza eixa labilitat del Ge en posicions cristal·lines de les zeolites com a estratègia per a controlar a escala atòmica la incorporació selectiva de diferents heteroàtoms (Si i Sn). La síntesi de l'estructura ITT amb porus extra-grans està limitada a baixes relacions de Si/Ge, presentant per tant una limitada estabilitat hidrotermal. Per això, es du a terme una substitució isomòrfica d'àtoms de Ge per àtoms de Si, millorant l'estabilitat hidrotermal d'aquest material per a la seua aplicació en la reacció de craqueig catalític d'un gasoil de buit, possibilitant la seua regeneració i obtenint una selectivitat similar a dièsel i més propilè que amb la mostra d'origen. D'altra banda, s'incorpora selectivament Sn en l'estructura BEC (polimorf C de la zeolita beta) mitjançant tractaments post-sintètics als defectes estructurals generats després de l'eliminació d'àtoms de Ge, afavorint-se la formació de llocs "oberts" de Sn, que han demostrat ser més actius per a reaccions de molècules oxigenades en comparació als llocs "tancats" de Sn. Els avantatges catalítics del material Sn-BEC sintetitzat es demostren a la reacció Meerwein-Ponndorf-Verley-Oppenauer (MPVO), obtenint-se majors velocitats de reacció per lloc de Sn "obert" que amb la zeolita Sn-beta(F) convencional. / [EN] Zeolites are catalysts used in many chemical processes of industrial and environmental interest. The optimization of the physicochemical properties of these materials is essential to improve their efficiency and attractiveness to current and future technologies. This doctoral thesis aimed to control relevant aspects of the zeolites at the microscopic, molecular, and atomic scale that have a direct effect on their application as catalysts and conductive materials. With this in mind, several methodologies for the direct synthesis of zeolites and several post-synthetic treatments were proposed. Firstly, the influence of crystal size and zeolitic structure on the selective transformation of CO2 towards products of interest such as olefins and aromatics is studied when combined with an iron catalyst doped with potassium. On the one hand, the MFI-type zeolitic structure (medium pore) allows the formation of aromatic products to be maximized. Meanwhile, the CHA (small pore) and BEA (large pore) zeolites favour the production of light olefins in different proportions. The use of nanocrystalline acid zeolites allows to increase the production of light olefins and increases the lifetime of the bifunctional catalysts. Likewise, the effect of confinement at the molecular level of different small-pore zeolitic structures with different types of cavities for the reaction of methanol to olefins (MTO) is studied. Using a theoretical parameter, it was finally possible to correlate the selectivity towards different light olefins with the type of cavities in the microporous materials. Secondly, the stabilization of different metallic species in extra-framework positions of the zeolitic materials is studied by controlling the formation from the individual atoms towards clusters and/or nanoparticles. The structure of the CHA zeolite allows Pt nanoparticles to be encapsulated inside its cavities, which continues being active and stable for the CO oxidation reaction even after aging treatments at high temperatures. On the other hand, the formation of germanium nanoparticles dispersed in different hybrid zeolitic matrices is rationalized by taking advantage of the lability of germanium in their crystalline framework for their application as conductive materials. The optimization of these hybrid organic-inorganic materials based on Ge nanoparticles is carried out through various post-synthetic treatments by maximizing the dispersion of the nanoparticles and the formation of carbonaceous species to evaluate their properties as conductive materials. Finally, the mentioned lability of Ge in crystalline positions is used as a strategy to control the selective incorporation of different heteroatoms (Si and Sn) at the atomic scale. The fact that the synthesis of the ITT structure with extra-large pores is limited to low Si/Ge ratios leads to reduced hydrothermal stability. Therefore, an isomorphic substitution of Ge atoms with Si atoms is carried out. It improved the hydrothermal stability of the material to be applied in the catalytic cracking of a vacuum gasoil, enabling its regeneration. Moreover, the modified material presents similar selectivity to diesel and yields more propylene as compared to the original sample. Also, Sn is selectively incorporated into the BEC structure (polymorph C of beta zeolite) through post-synthetic treatments in the structural defects generated after the elimination of Ge atoms, favouring the formation of "open" Sn sites. It has been shown that this kind of site is more active for reactions involving oxygenated molecules compared to the "closed" sites of Sn. The catalytic advantages of the synthesized Sn-BEC material are demonstrated in the Meerwein-Ponndorf-Verley-Oppenauer (MPVO) reaction. Higher reaction rates per "open" Sn site than with the conventional Sn-beta(F) zeolite were obtained. / Rodríguez Fernández, A. (2024). Diseño racional de materiales zeolíticos: efectos de confinamiento y control de centros metálicos en posiciones de red y extra-red en aplicaciones de interés [Tesis doctoral]. Universitat Politècnica de València. https://doi.org/10.4995/Thesis/10251/202870

Comparative studies over micro-/mesoporous Cu-containing zeolites ZSM-5 prepared by top-down treatment involving NaOH, TPAOH or mixture of NaOH/TPAOH (tetrapropylammonium hydroxide) were conducted. The results of the catalytic data revealed the highest activity of the Cu-ZSM-5 catalyst both in the absence and presence of water vapor. The physico-chemical characterization (diffuse reflectance UV-Vis (DR UV-Vis), Fourier transform infrared (FT-IR) spectroscopy, electron paramagnetic resonance (EPR) spectroscopy, temperature-programmed desorption of NOx (TPD-NOx), and microkinetic modeling) results indicated that the microporous structure of ZSM-5 effectively stabilized isolated Cu ion monomers. Besides the attempts targeted to the modification of the textural properties of the parent ZSM-5, in the next approach, we studied the effect of the co-presence of sodium and copper cations in the microporous H-ZSM-5. The presence of co-cation promoted the evolution of [Cu–O–Cu]2+ dimers that bind NOx strongly with the desorption energy barrier of least 80 kJ mol−1. Water presence in the gas phase significantly decreases the rate of ammonia oxidation, while the reaction rates and activation energies of NH3-SCR remain unaffected.

A systematic silylation approach using mono-, di-, and trichlorosilanes with different alkyl chain lengths was employed to enhance the hydrothermal stability of zeolite Y. DRIFT spectra of the silylated zeolites indicate that the attachment of the silanes takes place at surface silanol groups. Regarding hydrothermal stability under aqueous-phase processing (APP) conditions, i.e., pH ≈ 2, 473 K and autogenous pressure, the selective silylation of the zeolite surface usingmonochlorosilanes has no considerable influence. By using trichlorosilanes, the hydrothermal stability of zeolite Y can be improved significantly as proven by a stability test in an aqueous solution of 0.2M levulinic acid (LA) and 0.6M formic acid (FA) at 473 K. However, the silylationwith trichlorosilanes results in a significant loss of total specific pore volume and total specific surface area, e.g., 0.35 cm3 g−1 and 507m2 g−1 for the silylated zeolite Y functionalized with n-octadecyltrichlorosilane compared to 0.51 cm3 g−1 and 788 m2 g−1 for the parent zeolite Y. The hydrogenation of LA to g-valerolactone (GVL) was conducted over 3 wt.-% Pt on zeolite Y (3PtY) silylated with either n-octadecyltrichlorosilane or methyltrichlorosilane using different reducing agents, e.g., FA or H2. While in the stability test an enhanced hydrothermal stability was found for zeolite Y silylated with n-octadecyltrichlorosilane, its stability in the hydrogenation of LA was far less pronounced. Only by applying an excess amount of methyltrichlorosilane, i.e., 10 mmol per 1 g of zeolite Y, presumably resulting in a high degree of polymerization among the silanes, a recognizable improvement of the stability of the 3 PtY catalyst could be achieved. Nonetheless, the pore blockage found for zeolite Y silylated with an excess amount of methyltrichlorosilane was reflected in a drastically lower GVL yield at 493 K using FA as reducing agent, i.e., 12 vs. 34% for 3PtY after 24 h.

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Catalytic pyrolysis technology is one of the thermochemical platforms used to produce high quality bio-oil and chemicals from biomass feedstocks. In the catalytic pyrolysis process, the biomass is rapidly heated under inert atmosphere in the presence of an acid catalyst or zeolite to promote deoxygenation and cracking of the primary vapors into hydrocarbons and small oxygenates. This dissertation examines the utilization of conventional fluid catalytic cracking (FCC) catalyst in the fractional catalytic pyrolysis of hybrid poplar wood. The influence of Y-zeolite content, steam treatment, addition of ZSM-5 additive, process conditions (temperature, weight hourly space velocity (WHSV) and vapor residence time) and recycling of the non-condensable gases (NCG) on the product distribution and the quality of the bio-oil were investigated. The first part of the study demonstrates the influence of catalytic property of FCC catalyst on the product distribution and quality of the bio-oil. It was found that FCC catalyst with higher Y-zeolite content produces higher coke yield and lower organic liquid fraction (OLF). Conversely, FCC catalyst with lower Y-zeolite content results in lower coke yield and higher OLF. The results showed that higher Y-zeolite content extensively cracks dehydrated products from cellulose decomposition and demethoxylates phenolic compounds from lignin degradation. The Y-zeolite promoted both deoxygenation and coke forming reactions due to its high catalytic activity and large pore size. Higher Y-zeolite content increased the quality of the bio-oil with respect to higher heating value (HHV), pH, density, and viscosity. The steam treatment at 732 oC and 788 oC decreased the total BET surface area of the FCC catalyst. The findings suggest that steam treatment reduces the coking tendency of the FCC catalyst and enhances the yield of the OLF. Analysis of the bio-oils showed that the steamed FCC catalyst produces bio-oil with lower viscosity and density. Gas chromatography and 13C-NMR spectrometry suggest that steam treatment affect the catalyst selectivity in the formation of CO, CO2, H2, CH4, C2-C5 hydrocarbons and aromatic hydrocarbons. The addition of ZSM-5 additive to the FCC catalyst was found to alter the characteristic/functionality of the catalytic medium. The product slate showed decrease in coke yield and increase in OLF with increase in ZSM-5 additive. The FCC/ZSM-5 additive hybrid catalysts produced bio-oils with relatively lower viscosity and higher pH value. The formation of CO2, CH4, and H2 decreased whilst C5 and aromatic hydrocarbons increased with increase in ZSM-5 additive level. The second part of the work assesses the effect of operating conditions on the catalytic pyrolysis process. The response surface methodology study showed reaction temperature to be the most influential statistically significant independent variable on char/coke yield, concentration of non-condensable gases, carbon content, oxygen content, pH and viscosity of the bio-oils. The WHSV was the most important statistically significant independent variable that affects the yield of organic liquid and water. Adequate and statistically significant models were generated for the prediction of the responses with the exception of viscosity. Recycling of the NCG in the process was found to potentially increase the liquid yield and decrease char/coke yield. The experiments with the model fluidizing gases showed that CO/N2, CO2/N2, CO/CO2/N2 and H2/N2 increase the liquid yield and CO2/N2 decrease char/coke yield. The results showed that recycling of NCG increases the higher heating value and the pH of the bio-oil as well as decreases the viscosity and density. The concept of recycling the NCG in the catalytic cracking of biomass vapors with FCC catalyst improved the overall process. The evaluation of the reactivity of conventional FCC catalyst towards bio-based molecules provide essential direction for FCC catalyst formulation and design for the production of high quality bio-oils from catalytic pyrolysis of biomass. / Ph. D.

Les interactions lumière-matière dans les mileux moléculaires et bio-moléculaires peuvent mener à des processus complexes où les polarisations des champs optiques se couplent aux assemblages de dipoles de transitions moléculaires. La manipulation des polarisations des champs optiques en microscopie de uorescence peut en particulier donner accès à des modi cations nes d'arrangements moléculaires. Dans ce travail de thèse nous introduisons une méthode basée sur la variation continue d'un état de polarisation d'excitation complémentée par une analyse polarisée, appliquée à la microscopie de uorescence multi-photons. La uorescence à deux photons polarimétrique permet d'accéder à une information statique quantitative sur la forme et l'orientation de la distribution orientationnelle moléculaire dans des membranes lipidiques articielles, dans des cellules ou sur des composés molécluaires co-cristallins qui peuvent être fortement hétérogènes. La uorescence à trois photons polarimétrique apporte de plus un diagnostique de cristallinité dans des cristaux de protéines, avec une forte sensibilité à leur structure et symétrie. L'implémentation expérimentale de cette technique requiert de quantier les distortions de polarisation provenant du montage expérimental et de l'échantillon lui-même, qui sont nement analysés.