978 resultados para heterogeneous catalysis


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This PhD work deals with problems of synthetic organic chemistry with particular attention to the development of environmentally friendly processes. In particular, new synthetic strategies have been studied based on the use of low cost heterogeneous catalysts, non-toxic reagents and mild operating conditions that do not involve, when possible, the use of solvents. The catalysts examined are both basic and acids, commercial or prepared by hetereogenization of homogeneous catalysts synthesized by tethering or impregnation. In particular it will be discussed the catalytic activity of oxides (Al2O3 and TiO2), supported sulphonic acids and hydrotalcites for the reactions of selective monoesterificazion of dicarboxylic acids, dehydrogenation of butane in gas phase, esterification of levulinic acid, Friedel-Craft acylations, C-C and C-P coupling. The use of these materials has allowed the development of simple processes with low environmental impact. The operating conditions are in fact mild and reaction times short. The selectivity for the desired products is in all reported cases very high and the catalysts can be recycled maintaining their optimum performances.

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Catalytically active heterogeneous catalysts have been prepared via microwave deposition of iron oxide nanoparticles (0.5–1.2 wt%) on MCM-41 type silica materials with different morphologies (particles, helical and spheres). This methodology leads to iron oxide nanoparticles composed by a mixture of FeO and Fe2O3 species, being the Fe(II)/Fe(III) peak ratio near to 1.11 by XPS. DRUV spectroscopy indicates the presence of tetrahedral coordinated Fe3+ in the silica framework of the three catalysts as well as some extraframework iron species in the catalysts with particle and sphere-like morphologies. The loading of the nanoparticles does neither affect the mesopore arrangement nor the textural properties of the silica supports, as indicated by SAXS and nitrogen adsorption/desorption isotherms. A detailed investigation of the morphology of the supports in various microwave-assisted catalyzed processes shows that helical mesostructures provide optimum catalytic activities and improved reusabilities in the microwave-assisted redox (selective oxidation of benzyl alcohol) catalyzed process probably due to a combination of lower particle size and higher acidity in comparison with the supports with particle and sphere morphology.

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Copper-impregnated magnetite is a versatile heterogeneous catalytic system for the synthesis of 1,3-diynes by the homocoupling of terminal alkynes. This catalyst does not require the use of pressurized oxygen as the oxidant and it does not need a solvent or harsh conditions to give the expected products. Moreover, the catalyst can be removed from the reaction medium simply by using a magnet. The reaction occurs at the lowest copper loading reported for any heterogeneous catalyst.

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Catalysts consisting of cobalt and nickel impregnated on magnetite have been prepared, characterized and used for the hydroacylation reaction of different azodicarboxylate compounds with aldehydes, using nearly stoichiometric amounts of both reagents in only 3 h. Furthermore, this reaction has been conducted with the smallest amount of catalyst. The cobalt catalyst is stable enough to be removed by magnetic decantation and recycled ten-fold without any detrimental effect on the results.

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Reactive, but not a reactant. Heterogeneous catalysts play an unseen role in many of today's processes and products. With the increasing emphasis on sustainability in both products and processes, this handbook is the first to combine the hot topics of heterogeneous catalysis and clean technology. It focuses on the development of heterogeneous catalysts for use in clean chemical synthesis, dealing with how modern spectroscopic techniques can aid the design of catalysts for use in liquid phase reactions, their application in industrially important chemistries - including selective oxidation, hydrogenation, solid acid- and base-catalyzed processes - as well as the role of process intensification and use of renewable resources in improving the sustainability of chemical processes. With its emphasis on applications, this book is of high interest to those working in the industry.

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Metal–organic frameworks, or MOFs, have emerged as a new class of porous materials made by linking metal and organic units. The easy preparation, structural and functional tunability, ultrahigh porosity, and enormous surface areas of MOFs have led to them becoming one of the fastest growing fields in chemistry. MOFs have potential applications in numerous areas such as clean energy, adsorption and separation processes, biomedicine, and sensing. One of the most promising areas of research with MOFs is heterogeneous catalysis. This thesis describes the design and synthesis of new, carboxylate-based MOFs for use as catalysts. These materials have been characterized using diffraction, spectroscopy, adsorption, and imaging techniques. The thesis has focused on preparing highly-stable MOFs for catalysis, using post-synthetic methods to modify the properties of these crystals, and applying a combination of characterization techniques to probe these complex materials. In the first part of this thesis, several new vanadium MOFs have been presented. The synthesis of MIL-88B(V), MIL-101(V), and MIL-47 were studied using ex situ techniques to gain insight into the synthesis–structure relationships. The properties of these materials have also been studied. In the second part, the use of MOFs as supports for metallic nanoparticles has been investigated. These materials, Pd@MIL-101–NH2(Cr) and Pd@MIL-88B–NH2(Cr), were used as catalysts for Suzuki–Miyaura and oxidation reactions, respectively. The effect of the base on the catalytic activity, crystallinity, porosity, and palladium distribution of Pd@MIL-101–NH2(Cr) was studied. In the final part, the introduction of transition-metal complexes into MOFs through different synthesis routes has been described. A ruthenium complex was grafted onto an aluminium MOF, MOF-253, and an iridium metallolinker was introduced into a zirconium MOF, UiO-68–2CH3. These materials were used as catalysts for alcohol oxidation and allylic alcohol isomerization, respectively.

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We applied small-angle neutron scattering (SANS) and ultra small-angle neutron scattering (USANS) to monitor evolution of the CO2 adsorption in porous silica as a function of CO2 pressure and temperature in pores of different sizes. The range of pressures (0 < P < 345 bar) and temperatures (T=18 OC, 35 OC and 60 OC) corresponded to subcritical, near critical and supercritical conditions of bulk fluid. We observed that the adsorption behavior of CO2 is fundamentally different in large and small pores with the sizes D > 100 Å and D < 30 Å, respectively. Scattering data from large pores indicate formation of a dense adsorbed film of CO2 on pore walls with the liquid-like density (ρCO2)ads≈0.8 g/cm3. The adsorbed film coexists with unadsorbed fluid in the inner pore volume. The density of unadsorbed fluid in large pores is temperature and pressure dependent: it is initially lower than (ρCO2)ads and gradually approaches it with pressure. In small pores compressed CO2 gas completely fills the pore volume. At the lowest pressures of the order of 10 bar and T=18 OC, the fluid density in smallest pores available in the matrix with D ~ 10 Å exceeds bulk fluid density by a factor of ~ 8. As pressure increases, progressively larger pores become filled with the condensed CO2. Fluid densification is only observed in pores with sizes less than ~ 25 – 30 Å. As the density of the invading fluid reaches (ρCO2)bulk~ 0.8 g/cm3, pores of all sizes become uniformly filled with CO2 and the confinement effects disappear. At higher densities the fluid in small pores appears to follow the equation of state of bulk CO2 although there is an indication that the fluid density in the inner volume of large pores may exceed the density of the adsorbed layer. The equivalent internal pressure (Pint) in the smallest pores exceeds the external pressure (Pext) by a factor of ~ 5 for both sub- and supercritical CO2. Pint gradually approaches Pext as D → 25 – 30 Å and is independent of temperature in the studied range of 18 OC ≤ T ≤ 60 OC. The obtained results demonstrate certain similarity as well as differences between adsorption of subcritical and supercritical CO2 in disordered porous silica. High pressure small angle scattering experiments open new opportunities for in situ studies of the fluid adsorption in porous media of interest to CO2 sequestration, energy storage, and heterogeneous catalysis.

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A rapid electrochemical method based on using a clean hydrogen-bubble template to form a bimetallic porous honeycomb Cu/Pd structure has been investigated. The addition of palladium salt to a copper-plating bath under conditions of vigorous hydrogen evolution was found to influence the pore size and bulk concentration of copper and palladium in the honeycomb bimetallic structure. The surface was characterised by X-ray photoelectron spectroscopy, which revealed that the surface of honeycomb Cu/Pd was found to be rich with a Cu/Pd alloy. The inclusion of palladium in the bimetallic structure not only influenced the pore size, but also modified the dendritic nature of the internal wall structure of the parent copper material into small nanometre-sized crystallites. The chemical composition of the bimetallic structure and substantial morphology changes were found to significantly influence the surface-enhanced Raman spectroscopic response for immobilised rhodamine B and the hydrogen-evolution reaction. The ability to create free-standing films of this honeycomb material may also have many advantages in the areas of gas- and liquid-phase heterogeneous catalysis.

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The formation of readily recoverable and reusable organic semiconducting Cu- and AgTCNQ (TCNQ=7,7,8,8-tetracyanoquinodimethane) microstructures decorated with Pt and Pd metallic nanoparticles is described for the effective reduction of CrVI ions in aqueous solution at room temperature using both formic acid and an environmentally friendly thiosulfate reductant. The M-TCNQ (M=metal) materials were formed by electrocrystallisation onto a glassy carbon surface followed by galvanic replacement in the presence of H2PtCl6 or PdCl2 to form the composite material. It was found that loading of the surface with nanoparticles could easily be controlled by changing the metal salt concentration. Significantly, the M-TCNQ substrates facilitated the formation of well-isolated metal nanoparticles on their surfaces under appropriate galvanic replacement conditions. The semiconductor–metal nanoparticle combination was also found to be critical to the catalyst performance, wherein the best-performing material was CuTCNQ modified by well-isolated Pt nanoparticles with both formic acid and thiosulfate ions as the reductant.

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Fluid–solid interactions in natural and engineered porous solids underlie a variety of technological processes, including geological storage of anthropogenic greenhouse gases, enhanced coal bed methane recovery, membrane separation, and heterogeneous catalysis. The size, distribution and interconnectivity of pores, the chemical and physical properties of the solid and fluid phases collectively dictate how fluid molecules migrate into and through the micro- and meso-porous media, adsorb and ultimately react with the solid surfaces. Due to the high penetration power and relatively short wavelength of neutrons, smallangle neutron scattering (SANS) as well as ultra small-angle scattering (USANS) techniques are ideally suited for assessing the phase behavior of confined fluids under pressure as well as for evaluating the total porosity in engineered and natural porous systems including coal. Here we demonstrate that SANS and USANS can be also used for determining the fraction of the pore volume that is actually accessible to fluids as a function of pore sizes and study the fraction of inaccessible pores as a function of pore size in three coals from the Illinois Basin (USA) and Bowen Basin (Australia). Experiments were performed at CO2 and methane pressures up to 780 bar, including pressures corresponding to zero average contrast condition (ZAC), which is the pressure where no scattering from the accessible pores occurs. Scattering curves at the ZAC were compared with the scattering from same coals under vacuum and analysed using a newly developed approach that shows that the volume fraction of accessible pores in these coals varies between �90% in the macropore region to �30% in the mesopore region and the variation is distinctive for each of the examined coals. The developed methodology may be also applied for assessing the volume of accessible pores in other natural underground formations of interest for CO2 sequestration, such as saline aquifers as well as for estimating closed porosity in engineered porous solids of technological importance.

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Electrocatalysis is a core field of interfacial science because it involves enhancement of reaction rates as in the case of heterogeneous catalysis, with an additional control through the variation of electrode potential. Electrocatalytic rates are influenced by the electrode potential either directly or indirectly. Because of increasing significance of green chemistry and clean energy with an intimate relationship between heterogeneous electrocatalysis and electrochemical energy conversion (batteries and fuel cells), the field of electrocatalysis has grown rapidly. In this article, basic concepts of electrode kinetics to assess electrocatalysis, and catalytic aspects of a few important electrochemical reactions are reviewed.

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Devido ao efeito estufa, a produção de hidrogênio a partir da reação de reforma do bioetanol tem se tornado um assunto de grande interesse em catálise heterogênea. Os catalisadores à base de Pt são empregados nos processos de purificação de H2 e também em eletrocatalisadores das células a combustível do tipo membrana polimérica (PEMFC). O hidrogênio obtido a partir da reforma do etanol contém como contaminante o acetaldeído e pequenas quantidades de CO. Assim, pode-se prever que muitas reações podem ocorrer na presença de catalisadores de Pt durante o processo de purificação do H2 e mesmo no próprio eletrocatalisador. Desta forma, este trabalho tem como objetivo descrever o comportamento do acetaldeído na presença de catalisadores de Pt. Para tanto foram preparados dois catalisadores, Pt/SiO2 e Pt/USY, contendo 1,5% de metal em ambos. Também foi estudado um eletrocatalisador (comercial) de Pt suportado em carvão (Pt/C). Os catalisadores foram caracterizados através das técnicas de análise textural, difração de raios X (DRX), quimissorção de H2, reação de desidrogenação do ciclohexano, espectroscopia no infravermelho de piridina adsorvida, dessorção a temperatura programada de n-butilamina (TPD de n-butilamina), dessorção a temperatura programada de CO2 (TPD-CO2), análise termogravimétrica, microscopia eletrônica de varredura (MEV) e espectroscopia de dispersão de energia (EDS). Os testes catalíticos foram realizados entre as temperaturas de 50 e 350 C em corrente contendo acetaldeído, H2 e N2. Foi observado que as propriedades ácido-básicas dos suportes promovem as reações de condensação com formação de éter etílico e acetato de etila. O acetaldeído em catalisadores de Pt sofre quebra das ligações C-C e C=O. A primeira ocorre em uma ampla faixa de temperaturas, enquanto a segunda apenas em temperaturas abaixo de 200 C. A quebra da ligação C-C produz metano e CO. Já a quebra da ligação C=O gera carbono residual nos catalisadores, assim como espécies oxigênio, que por sua vez são capazes de eliminar o CO da superfície dos catalisadores. Nota-se que o tipo de suporte utilizado influencia na distribuição de produtos, principalmente a baixas temperaturas. Além disso, constatou-se que a descarbonilação não é uma reação sensível à estrutura do catalisador. Verificou-se também a presença de resíduos sobre os catalisadores, possivelmente oriundos não somente da quebra da ligação C=O, mas também de reações de polimerização

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O biodiesel é definido como um mono alquil éster de ácidos graxos de cadeia longa derivado de fontes renováveis tais como óleos vegetais e gorduras animais. Sua importância esta associada ao uso como um combustível alternativo para motores do ciclo Diesel podendo ser utilizado puro ou em misturas com o diesel representando economia de petróleo e menor poluição ambiental. Em geral é obtido por meio da reação de transesterificação na qual os triacilgliceróis, principais constituintes dos óleos e gorduras reagem com álcool, em presença de um catalisador ácido ou básico, produzindo ésteres de ácidos graxos e glicerol. A transesterificação pode ser conduzida por catálise homogênea ou heterogênea. O grande desafio da indústria é otimizar o processo a fim de alcançar um produto e uma rota de produção tecnologicamente eficiente e ambientalmente correta. O objetivo desta pesquisa foi estudar a síntese do biodiesel utilizando o processo de transesterificação do óleo de girassol por catálises homogênea e heterogênea. Foram realizadas reações de transesterificação via rotas metílica e etílica, empregando como catalisador homogêneo alcóxido de potássio e como catalisador heterogêneo a resina comercial de troca iônica Amberlyst 26

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La Ciencia y Tecnología de Materiales tiene el reto permanente de desarrollar y mejorar materiales multifuncionales y respetuosos con el medio ambiente. En este sentido, los materiales de tipo MOF (Metal-Organic Framework) están siendo objeto de un gran interés, ya que las redes sólidas de coordinación (especialmente, las porosas) presentan aplicaciones en campos en los que la sociedad manifiesta una demanda creciente de ciencia y tecnología, como el almacenamiento y transporte de energía, la captura de gases con efecto invernadero, la catálisis heterogénea y la liberación controlada de fármacos, entre otros. En este contexto, el presente trabajo se planteó con el objetivo de desarrollar nuevos materiales de tipo MOF basados en metaloporfirinas, al objeto de mimetizar las funciones que desempeñan las mismas en los sistemas biológicos, con el fin de reproducirlas en el estado sólido. Para ello, se han escogido biometales como el hierro y el cobalto: característicos de estos sistemas, de bajo coste y medioambientalmente respetuosos. Por otra parte, las porfirinas seleccionadas han sido las siguientes: TPP (meso-tetra-4-fenilporfirina), TCPP (meso-tetra-4-carboxifenilporfirina) y TPPS (meso-tetra-4-sulfonatofenilporfirina). Estas tres moléculas conforman un conjunto de ligandos que difieren ligeramente en sus grupos funcionales. Asimismo, en ocasiones, se ha utilizado un ligando secundario dipiridínico (4,4´-bipiridina) que ha actuado como espaciador. El diseño de las síntesis se ha centrado tanto en las combinaciones adecuadas de metales y ligandos como en la selección de las técnicas de síntesis. Así, se han obtenido cinco nuevos compuestos, que se han sintetizado en condiciones solvotermales suaves o mediante radiación microondas. La caracterización preliminar de los mismos se ha llevado a cabo mediante análisis cuantitativo, espectroscopia infrarroja y Raman, difracción y fluorescencia de rayos X y medidas de densidad. El estudio estructural se ha realizado mediante difractometría de rayos X y el estudio térmico se ha llevado a cabo mediante termogravimetría y termodifractometría. En los casos en que ha resultado procedente, también se han caracterizado los compuestos mediante espectroscopia ultravioleta-visible (UV-Vis), Mössbauer y resonancia paramagnética electrónica (EPR) y mediante medidas de la susceptibilidad magnética. Asimismo, ocasionalmente, se han realizado cálculos mecano-cuánticos basados en la teoría del funcional de la densidad (DFT) y medidas catalíticas. El primero de los cinco compuestos obtenidos, de fórmula [FeTCPP], es quiral y destaca por ser la tercera estructura 2D publicada basada en esta porfirina. La formación de este compuesto está condicionada por la oxidación de los iones de hierro y por la existencia de grupos carboxílicos en la porfirina. Por otra parte, con la participación del espaciador 4,4´-bipiridina (bipy) se han obtenido tres redes 1D. Así, la estructura cristalina del compuesto ([FeTPPbipy]•)n se explica mediante la formación de radicales neutros que se estabilizan en un empaquetamiento que permite la formación de enlaces entre los grupos fenílicos de distintas cadenas. La formación de estos enlaces queda corroborada por la existencia de significativas interacciones antiferromagnéticas. Por otra parte, en el compuesto [CoTPP(bipy)]•([CoTPP])0.22•(TPP)0.78, la disposición de las cadenas deja grandes huecos en la red que se ocupan con porfirinas tanto coordinadas como sin coordinar. El tercero de estos compuestos 1D presenta la fórmula [CoTPPS0.5(bipy)(H2O)2]•6H2O y destaca porque la extensión de las cadenas se produce por la alternancia de dos tipos de octaedros de CoII. La naturaleza de los grupos sulfonato de la porfirina TPPS es determinante para comprender la intrincada red de enlaces de hidrógeno de este compuesto, que propician la formación de una red interpenetrada caracterizada por su gran estabilidad térmica (hasta los 370ºC). Finalmente, con la porfirina TCPP se ha obtenido un segundo compuesto de fórmula -O-[FeTCPP]2•nDMF (n≈ 16; DMF = dimetilformamida). El mismo presenta grandes cavidades (47% de porosidad) que diluyen la matriz magnética, caracterizada por fuertes interacciones antiferromagnéticas intradiméricas. Todo ello revela una inusual estructura superhiperfina, observada por espectroscopia EPR. El trabajo que se recoge en esta memoria constituye, por lo tanto, un “viaje” de mayor a menor dimensionalidad en las estructuras cristalinas. La guía de este viaje ha sido la búsqueda de propiedades catalíticas en sistemas heterogéneos. Así, el [CoTPP(bipy)]•([CoTPP])0.22•(TPP)0.78 obedece el enfoque de inmovilizar o anclar el catalizador en los huecos de la red. Sin embargo, la estrategia alternativa seguida para el compuesto m-O-[FeTCPP]2•nDMF (es decir, que el propio MOF actúe de catalizador) es la que ha aportado mejores y más prometedores resultados en lo que a catálisis heterogénea se refiere.