133 research outputs found

    Mesoporous sulfonic acid silicas for pyrolysis bio-oil upgrading via acetic acid esterification

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    Propylsulfonic acid derivatised SBA-15 catalysts have been prepared by post modification of SBA-15 with mercaptopropyltrimethoxysilane (MPTMS) for the upgrading of a model pyrolysis bio-oil via acetic acid esterification with benzyl alcohol in toluene. Acetic acid conversion and the rate of benzyl acetate production was proportional to the PrSO3H surface coverage, reaching a maximum for a saturation adlayer. Turnover frequencies for esterification increase with sulfonic acid surface density, suggesting a cooperative effect of adjacent PrSO3H groups. Maximal acetic acid conversion was attained under acid-rich conditions with aromatic alcohols, outperforming Amberlyst or USY zeolites, with additional excellent water tolerance

    Preparation of Glycerol Carbonate Esters by using Hybrid Nafion-Silica Catalyst

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    Glycerol carbonate esters (GCEs), which are valuable biomass-deriv. compds., have been prepd. through the direct esterification of glycerol carbonate and long org. acids with different chain lengths, in the absence of solvent, and with heterogeneous catalysts, including acidic-org. resins, zeolites, and hybrid org.-inorg. acids. The best results, in terms of activity and selectivity towards GCEs, were obtained using a Nafion-silica composite. A full reaction scheme has been established, and it has been demonstrated that an undesired competing reaction results in the generation of glycerol and esters derived from a secondary hydrolysis of the endocyclic ester group, which is attributed to water formed during the esterification reaction. The influence of temp., substrate ratio, catalyst-to-substrate ratio, and the use of solvent has been studied and, under optimized reaction conditions and with the adequate catalyst, it was possible to achieve 95 % selectivity for the desired product at 98 % conversion. It was demonstrated that the reaction rate decreased as the no. of carbon atoms in the linear alkyl chain of the carboxylic acid increased for both p-toluenesulfonic acid and Nafion-silica nanocomposite (Nafion SAC-13) catalysts. After fitting the exptl. data to a mechanistically based kinetic model, the reaction kinetic parameters for Nafion SAC-13 catalysis were detd. and compared for reactions involving different carboxylic acids. A kinetic study showed that the reduced reactivity of carboxylic acids with increasing chain lengths could be explained by inductive as well as steric effects.The authors wish to acknowledge the Spanish Science and Innovation Ministry (Consolider Ingenio 2010, CTQ-2011-27550 and MULTICAT CSD2009-00050 projects) and the Generalitat Valenciana (Prometeo program) for their financial support. S.M. thanks the Ministerio de Educacion for a FPI fellowship.Climent Olmedo, MJ.; Corma CanĂłs, A.; Iborra Chornet, S.; MartĂ­nez Silvestre, S.; Velty ., A. (2013). Preparation of Glycerol Carbonate Esters by using Hybrid Nafion-Silica Catalyst. ChemSusChem. 6(7):1224-1234. doi:10.1002/cssc.201300146S1224123467BUDRONI, G., & CORMA, A. (2008). Gold and gold–platinum as active and selective catalyst for biomass conversion: Synthesis of Îł-butyrolactone and one-pot synthesis of pyrrolidone. Journal of Catalysis, 257(2), 403-408. doi:10.1016/j.jcat.2008.05.031Climent, M. J., Corma, A., & Iborra, S. (2011). Converting carbohydrates to bulk chemicals and fine chemicals over heterogeneous catalysts. Green Chemistry, 13(3), 520. doi:10.1039/c0gc00639dCorma, A., Iborra, S., & Velty, A. (2007). Chemical Routes for the Transformation of Biomass into Chemicals. Chemical Reviews, 107(6), 2411-2502. doi:10.1021/cr050989dMĂ€ki‐Arvela, P., Holmbom, B., Salmi, T., & Murzin, D. Y. (2007). Recent Progress in Synthesis of Fine and Specialty Chemicals from Wood and Other Biomass by Heterogeneous Catalytic Processes. Catalysis Reviews, 49(3), 197-340. doi:10.1080/01614940701313127Arias, K. S., Al-Resayes, S. I., Climent, M. J., Corma, A., & Iborra, S. (2013). From Biomass to Chemicals: Synthesis of Precursors of Biodegradable Surfactants from 5-Hydroxymethylfurfural. ChemSusChem, 6(1), 123-131. doi:10.1002/cssc.201200513Biodiesel Production 2004Vicente, G., Martı́nez, M., & Aracil, J. (2004). Integrated biodiesel production: a comparison of different homogeneous catalysts systems. Bioresource Technology, 92(3), 297-305. doi:10.1016/j.biortech.2003.08.014Behr, A., Eilting, J., Irawadi, K., Leschinski, J., & Lindner, F. (2008). Improved utilisation of renewable resources: New important derivatives of glycerol. Green Chem., 10(1), 13-30. doi:10.1039/b710561dPagliaro, M., Ciriminna, R., Kimura, H., Rossi, M., & Della Pina, C. (2007). Von Glycerin zu höherwertigen Produkten. Angewandte Chemie, 119(24), 4516-4522. doi:10.1002/ange.200604694Pagliaro, M., Ciriminna, R., Kimura, H., Rossi, M., & Della Pina, C. (2007). From Glycerol to Value-Added Products. Angewandte Chemie International Edition, 46(24), 4434-4440. doi:10.1002/anie.200604694Climent, M. J., Corma, A., De Frutos, P., Iborra, S., Noy, M., Velty, A., & ConcepciĂłn, P. (2010). Chemicals from biomass: Synthesis of glycerol carbonate by transesterification and carbonylation with urea with hydrotalcite catalysts. The role of acid–base pairs. 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    On the influence of Si:Al ratio and hierarchical porosity of FAU zeolites in solid acid catalysed esterification pretreatment of bio-oil

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    A family of faujasite (FAU) zeolites with different Si:Al ratio, and/or hierarchical porosity introduced via post-synthetic alkaline desilication treatment, have been evaluated as solid acid catalysts for esterification pretreatments of pyrolysis bio-oil components. Acetic acid esterification with aliphatic and aromatic alcohols including methanol, anisyl alcohol, benzyl alcohol, p-cresol and n-butanol was first selected as a model reaction to identify the optimum zeolite properties. Materials were fully characterised using N2 porosimetry, ICP, XRD, XPS, FT-IR, pyridine adsorption, NH3 TPD, In-situ ATR and inverse gas chromatography (IGC). IGC demonstrates that the surface polarity and hence hydrophobicity of FAU decreases with increased Si:Al ratio. Despite possessing a higher acid site loading and acetic acid adsorption capacity, high Al-content FAU possess weaker acidity than more siliceous catalysts. Esterification activity increases with acid strength and decreasing surface polarity following the order FAU30>FAU6>FAU2.6. The introduction of mesoporosity through synthesis of a hierarchical HFAU30 material further enhances esterification activity through improved acid site accessibility and hydrophobicity. Methanol was the most reactive alcohol for esterification, and evaluated with HFAU30 for the pretreatment of a real pyrolysis bio-oil, reducing the acid content by 76% under mild conditions

    Divalent Metal Vinylphosphonate Layered Materials: Compositional Variability, Structural Peculiarities, Dehydration Behavior, and Photoluminescent Properties

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    A family of M-VP (M = Ni, Co, Cd, Mn, Zn, Fe, Cu, Pb; VP = vinylphosphonate) and M-PVP (M = Co, Cd; PVP = phenylvinylphosphonate) materials have been synthesized by hydrothermal methods and characterized by FTIR, elemental analysis, and thermogravimetric analysis (TGA). Their structures were determined either by single crystal X-ray crystallography or from laboratory X-ray powder diffraction data. The crystal structure of some M-VP and M-PVP materials is two-dimensional (2D) layered, with the organic groups (vinyl or phenylvinyl) protruding into the interlamellar space. However, the Pb-VP and Cu-VP materials show dramatically different structural features. The porous, three-dimensional (3D) structure of Pb-VP contains the Pb center in a pentagonal pyramid. A Cu-VP variant of the common 2D layered structure shows a very peculiar structure. The structure of the material is 2D with the layers based upon three crystallographically distinct Cu atoms; an octahedrally coordinated Cu2+ atom, a square planar Cu2+ atom and a Cu+ atom. The latter has an unusual co-ordination environment as it is 3-coordinated to two oxygen atoms with the third bond across the double bond of the vinyl group. Metal-coordinated water loss was studied by TGA and thermodiffractometry. The rehydration of the anhydrous phases to give the initial phase takes place rapidly for Cd-PVP but it takes several days for Co-PVP. The M-VP materials exhibit variable dehydration-rehydration behavior, with most of them losing crystallinity during the process.Proyecto nacional MAT2010-15175 (MICINN, España

    Some Aspects of Lithification In Chalk

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    Chalk is affected by different diagenetic processes in comparison with other carbonate rocks. Commonly observed lithification processes are pressure-solution and reprecipitation and neomorphism. The first process is divisible into: (a) spot-welding or welding; (b) overgrowth; (c) stylolitization and cementation. Further, pressure-solution and reprecipitation is dependent on (a) geostatic pressure and (b) the ratio of Mg/Ca in the pore fluid. Overgrowth of calcite cement is controlled by the size and shape of the biogenic crystals. Neomorphism is also important in diagenesis. Neomorphic process dominates when pressure-solution process is ineffective. Organic and insoluble residue content dictate neomorphism. In conclusion, pressure-solution or neomorphism or a combination of both accounts for various modes of lithification observed in chalk
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