996 resultados para basic sites


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Exploring advanced materials for efficient capture and separation of CO2 is important for CO2 reduction and fuel purification. In this study, we have carried out first-principles density functional theory calculations to investigate CO2, N2, CH4, and H2 adsorption on the amphoteric regioselective B80 fullerene. Based on our calculations, we find that CO2 molecules form strong interactions with the basic sites of the B80 by Lewis acid–base interactions, while there are only weak bindings between the other three gases (N2, CH4, and H2) and the B80 adsorbent. The study also provides insight into the reaction mechanism of capture and separation of CO2 using the electron deficient B80 fullerene.

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Photoacoustic spectroscopy has been employed to estimate quantitatively the acid sites on oxide catalysts. The technique involves the measurement of the ratio of intensities of absorption bands due to conjugate bases and acids of indicators adsorbed on the catalyst surface as a function of the amount of added n-butylamine. Basic sites in sodium-impregnated alumina samples have been examined by adsorbing phenolphthalein on these surfaces.

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Photoacoustic spectroscopy has been employed to estimate quantitatively the acid sites on oxide catalysts. The technique involves the measurement of the ratio of intensities of absorption bands due to conjugate bases and acids of indicators adsorbed on the catalyst surface as a function of the amount of added n-butylamine. Basic sites in sodium-impregnated alumina samples have been examined by adsorbing phenolphthalein on these surfaces.

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Photoacoustic spectroscopy has been employed to study the electronic spectra of a variety of solids. The systems studied include powders of intensely coloured dyes, amorphous chalcogenides and oxide gels besides polycrystalline samples of several oxide materials. Surface sensitivity of the technique has been examined by study of dye adsorption on oxide surfaces and determination of surface areas of active oxides. Acidic and basic sites on catalyst surfaces have also been estimated by this technique.

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Coordination-driven self-assembly of 3-(5-(pyridin-3-yl)-1H-1,2,4-triazol-3-yl)pyridine (L) was investigated with 90 degrees cis-blocked Pd(II) acceptors and tetratopic Pd(NO3)(2). Although the ligand is capable of binding in several different conformations (acting as a ditopic donor through the pyridyl nitrogens), the experimental results (including X-ray structures) showed that it adopts a particular conformation when it binds with 90 degrees cis-blocked Pd(II) acceptors (two available sites) to yield 2 + 2] self-assembled macrocycles. On the other hand, with Pd(NO3)(2) (where four available sites are present) a different conformer of the same donor was selectively bound to form a molecular cubic cage. The experimental findings were corroborated well with the density functional theory (B3LYP) calculations. The tetratopic Pd(NO3)(2) yielded a 6 + 12] self-assembled Pd6L12 molecular cube, which contains a potential void occupied by nitrate and perchlorate ions. Being a triazole based ligand, the free space inside the cage is enriched with several sp(2) hybridised nitrogen atoms with lone pairs of electrons to act as Lewis basic sites. Knoevenagel condensation reactions of several aromatic aldehydes with active methylene compounds were successfully performed in reasonably high yields in the presence of the cage.

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Resumen: Se propone utilizar un óxido como el Cr2O3 como catalizador ya que se ha determinado anteriormente, en la primera etapa de esta investigación, (“Estudio comparativo de la retención de SO2 sobre óxidos de metales de transición soportados en alúmina”), que la retención de SO2 sobre su superficie es un proceso de quimisorción con formación de especies sulfito superficiales sobre sitios básicos y un proceso de óxido reducción del ión metálico. Apoya este mecanismo el hecho de que la cantidad de SO2 adsorbido es función de la temperatura. La mayor eficiencia del Cr2O3 puede explicarse en base a sus propiedades superficiales, lo cual ha sido utilizado en la segunda etapa de reacción de reducción, ya que se ha completado la etapa inicial de quimisorción. En la segunda etapa de esta investigación (“Estudio de la reacción de reducción de SO2 con CH4 a altas temperaturas sobre catalizador de Cr2O3 soportado en alúmina”), se apuntó al estudio de un nuevo tipo de sinergia entre propiedades ácido-base y propiedades redox en una misma superficie. Esta tercera etapa apuntó a determinar la influencia que tiene el O2 en este proceso, ya que el O2 se encuentra presente en las chimeneas industriales en las condiciones de reacción entre el SO2 y el CH4, y produce modificaciones en los parámetros de reacción. Se experimentó con diferentes masas de catalizador y flujos de los distintos gases, y se estudió la influencia de la presencia de oxígeno en la reacción y particularmente con diferentes flujos del mismo, y la posibilidad de regeneración del catalizador.

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Resumen: Se propone utilizar un óxido como el Cr2O3 como catalizador ya que se ha determinado anteriormente, en la primera etapa de esta investigación, (“Estudio comparativo de la retención de SO2 sobre óxidos de metales de transición soportados en alúmina”), que la retención de SO2 sobre su superficie es un proceso de quimisorción con formación de especies sulfito superficiales sobre sitios básicos y un proceso de óxido reducción del ión metálico. Apoya este mecanismo el hecho de que la cantidad de SO2 adsorbido es función de la temperatura. La mayor eficiencia del Cr2O3 puede explicarse en base a sus propiedades superficiales, lo cual ha sido utilizado en la segunda etapa de reacción de reducción, ya que se ha completado la etapa inicial de quimisorción. En la segunda etapa de esta investigación (“Estudio de la reacción de reducción de SO2 con CH4 a altas temperaturas sobre catalizador de Cr2O3 soportado en alúmina”), se apuntó al estudio de un nuevo tipo de sinergia entre propiedades ácido-base y propiedades redox en una misma superficie. La tercera etapa apuntó a determinar la influencia que tiene el O2 en este proceso, ya que el O2 se encuentra presente en las chimeneas industriales en las condiciones de reacción entre el SO2 y el CH4, y produce modificaciones en los parámetros de reacción. Se experimentó con diferentes masas de catalizador y flujos de los distintos gases, y se estudió la influencia de la presencia de oxígeno en la reacción y particularmente con diferentes flujos del mismo, y la posibilidad de regeneración del catalizador.En esta cuarta y última etapa se están estudiando los cambios que se producen en la reacción al pasar de escala laboratorio a planta piloto utilizando una columna de mayor diámetro construída en metal. A través de los datos experimentales se está estudiando, en conjunto con el INIFTA, la presencia de especies sulfito y sulfato sobre la superficie del soporte. Adicionalmente, por medio del programa VASP (Vienna Ab-initio Simulation Package), se analiza la interacción entre los reactivos gaseosos y el soporte.

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Nos últimos anos, a busca por fontes de energia renováveis e o desenvolvimento de novas tecnologias para a produção de biocombustíveis têm sido objeto de intensa investigação. O biodiesel é um combustível biodegradável, derivado de fontes renováveis e é obtido em escala industrial principalmente através da reação de transesterificação de óleos vegetais e/ou gorduras animais com metanol na presença de catalisadores homogêneos, como NaOH. Entretanto, a utilização de catalisadores heterogêneos tem sido sugerida por diversos autores, por apresentar vantagens como a eliminação dos problemas de separação e purificação dos produtos obtidos. No presente trabalho foi investigada a produção de biodiesel a partir da transesterificação do óleo de soja com metanol utilizando óxidos mistos de Zn e Al como catalisadores sólidos básicos. A influência das variáveis: temperatura, concentração de catalisador e relação molar metanol/óleo de soja na produção de biodiesel foi avaliada. Os catalisadores preparados apresentaram predominantemente sítios básicos e foram ativos frente à reação estudada, sendo os resultados mais promissores apresentados pelo óxido misto com relação molar Al/(Al+Zn)=0,50, obtido por tratamento térmico à 450C, que apresentou rendimentos em ésteres metílicos de até 98,5% sob condições específicas. A metodologia da superfície de resposta foi utilizada visando estabelecer as condições ótimas para maximizar o rendimento em ésteres metílicos, tendo sido encontradas a temperatura de 165oC e a concentração de catalisador de 5,8% m/m em relação massa de óleo, no caso da relação molar metanol/óleo de soja limitada em 15. Essa limitação teve como objetivo garantir um processo viável em escala comercial

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The coupling selectivity was greatly enhanced by adding Li to La2O3, compared with the single La2O3. The O2- species was found on the Li/La2O3 but not on the single La2O3. In low-temperature desorption, ethane desorbed from the Li/La2O3 but was not detected with the single La2O3. It is considered that the addition of Li gave rise to some basic sites which are favorable for the coupling reaction.

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Five hydrotalcites with Mg/Al molar ratio range of 3-15 were prepared. The structure and basicity of Mg-Al mixed oxides (Mg(Al)O) transformed from hydrotalcites were investigated by TPD, XPS, XRD, FT-IR and NMR techniques. The results of elemental analysis and XPS indicate that Al is enriched in the surface regions of Mg(Al)O, and its amount increases with the Mg/Al molar ratio and, the calcination temperature. Al-27-MAS-NMR results show that Al exists in two chemical environments: tetrahedral aluminium (Al(t)) and octahedral aluminium (Al(o)) in Mg(AI)O. The amount of Al(t) increases with the Mg/Al molar ratio and the calcination temperature. It is assumed that Al(t) may be mainly from the surface Al. Temperature-programmed desorption (TPD) of CO2 shows that the number of basic sites of Mg(Al)O samples increases with the Mg/Al molar ratio, and the maximum number of basic sites is obtained for hydrotalcite calcined at 773 K. Infrared spectra of adsorbed CO2 and B(OCH3)(3) reveal that there are two kinds of basic sites: weak basic OH- sites and strong basic O2- sites on the Mg(AI)O samples, the base strength depends on the Mg/Al molar ratio and calcination temperature.

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Natural dolomitic rock has been investigated in the transesterification of C-4 and C-8 triglycerides and olive oil with a view to determining its viability as a solid base catalyst for use in biodiesel synthesis. XRD reveals that the dolomitic rock comprised 77% dolomite and 23% magnesian calcite. The generation of basic sites requires calcination at 900 degrees C, which increases the surface area and transforms the mineral into MgO nanocrystallites dispersed over CaO particles. Calcined dolomitic rock exhibits high activity towards the liquid phase transesterification of glyceryl tributyrate and trioctanoate, and even olive oil, with methanol for biodiesel production.

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The changes in surface acidity/basicity and catalytic activity of cerium oxide due to surface modification by sulphate ion have been investigated. Electron donor properties of both the modified and unmodified oxides have been studied using electron acceptors of various electron affinity values, viz. 7,7,8,8-tetracyanoquinodimethane, 2,3,5,6-tetrachloro--l, 4-benzoquinone. p-dinitrobenzene and m-dinitrobenzene in order to find out whether the increase in acidity on suphation is due to the generation of new acidic sites or they are formed at the expense of some of the basic sites. The surface acidity/basicity has been determined using a set of Hammett indicators. The data have been correlated with the catalytic activity of the oxides for esterification of acetic acid using l-butanol, reduction of cyclohexanone with 2- propanol and oxidation of cyclohexanol using benzophenone.

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A comparative study on the anisole methylation with methanol over lanthanum-promoted Sn02 catalyst and its sulfate-doped analogue is presented. A maximum 2.6-xylenol selectivity of 82% was achieved at 400 degreeC under optimized conditions at an anisole conversion of 65% over lanthanum-promoted Sn02 catalyst. The sulfate modification resulted in the dealkylation of anisole to phenol followed by several unselective side reactions due to the creation of strong acid sites. The activity of lanthanum-modified tin oxide catalysts in the selective formation of 2.6-xylenol is ascribed to the presence of weak Lewis acid sites and comparatively stronger basic sites.

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Various compositions of chromium manganese ferrospinels were tested as catalysts for the vapour phase alkylation of aniline with methanol. The samples were prepared by room temperature co-precipitation technique and characterized by various physico-chemical methods. The acidity–basicity determination revealed that the samples possess greater amount of basic sites than acidic sites. All the ferrite samples proved to be selective and active for N-monoalkylation of aniline leading to N-methyl aniline; Cr0.6Mn0.4Fe2O4, Cr0.8Mn0.2Fe2O4 and CrFe2O4 exhibited cent percent selectivity for N-methyl aniline. Neither C-alkylated products nor any other side products were detected for all catalyst samples. The catalytic activity of the samples studied in this reaction is related to their acid–base properties and also on the cation distribution. Under the optimized reaction conditions all the systems showed constant activity for a long duration.

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Ferrospinels of nickel, cobalt and copper and their sulphated analogues were prepared by the room temperature coprecipitation route to yield samples with high surface areas. The intrinsic acidity among the ferrites was found to decrease in the order: cobalt> nickel> copper. Sulphation caused an increase in the number of weak and medium strong acid sites, whereas the strong acid sites were left unaffected. Electron donor studies revealed that copper ferrite has both the highest proportion of strong sites and the lowest proportion of weak basic sites. All the ferrite samples proved to be good catalysts for the benzoy lation of toluene with benzoyl chloride. copper and cobalt ferrites being much more active than nickel ferrite. The catalytic activity for benzoylation was not much influenced by sulphation, but it increased remarkably with calcination temperature of the catalyst. Surface Lewis acid sites, provided by the octahedral cations on the spinel surface, are suggested to be responsible for the catalytic activity for the benzoylation reaction.