Auteur Andrés T. Aguayo
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Documents disponibles écrits par cet auteur (6)
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Sierra, Irene, Auteur ; Erena, Javier, Auteur ; Andrés T. Aguayo, Auteur |A kinetic model has been established for the deactivation of a CuO−ZnO−Al2O3/γ-Al2O3 catalyst in the direct synthesis of dimethyl ether. The model allows calculating the effect of the operating conditions and the evolution of component concentra[...]![]()
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Andrés T. Aguayo, Auteur ; Pedro Castano, Auteur ; Diana Mier, Auteur |The deactivation by coke of a HZSM-5 zeolite catalyst has been studied in the transformation of methanol into hydrocarbons by cofeeding butane (n-butane). This reaction is of interest as an energy-neutral integrated process that enhances the act[...]![]()
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Andrés T. Aguayo, Auteur ; Ana G. Gayubo, Auteur ; Ainara Ateka, Auteur |The joint transformation of methanol and n-butane has been studied under energy-neutral conditions (methanol/n-butane molar ratio of 3/1) on an HZSM-5 zeolite catalyst in order to determine the reactivation kinetics and optimize the process cond[...]![]()
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Diana Mier, Auteur ; Andrés T. Aguayo, Auteur ; Monica Gamero, Auteur |A kinetic model of lumps has been established for n-butane cracking over HZSM-5 zeolitc catalyst (SiO2/ Al2O3 = 30) in the 400-550 °C range, based on the results obtained in a fixed bed reactor (space time, up to 2.4 (g of catalyst) h (mol CH2)-[...]![]()
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Andrés T. Aguayo, Auteur ; Diana Mier, Auteur ; Ana G. Gayubo, Auteur |A kinetic model of seven lumps has been established which allows the quantification of the product distribution (oxygenates, n-butane, C2−C4 olefins, C2−C4 paraffins (without n-butane), C5−C10 fraction, methane) in the transformation of methanol[...]![]()
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Ana G. Gayubo, Auteur ; Beatriz Valle, Auteur ; Andrés T. Aguayo, Auteur |The valorization of crude bio-oil by catalytic transformation into hydrocarbons has been carried out in an online two-step (thermal-catalytic) process. The deposition of pyrolytic lignin, formed by polymerization of biomass-derived products, is [...]


