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Coke deactivation of Ni and Co catalysts in ethanol steam reforming at mild temperatures in a fluidized bed reactor
ArticleAbstract: The deactivation by coke deposition of Ni and Co catalysts in the steam reforming of ethanol has beePalabras claves:Co catalyst, Coke deactivation, Ethanol steam reforming, hydrogen, Ni catalystAutores:Azkoiti M.J., Bilbao J., Carolina Montero-Calderón, Ereña J., Gayubo A.G., Vicente J.Fuentes:googlescopusComparison of Ni and Co catalysts for ethanol steam reforming in a fluidized bed reactor
ArticleAbstract: A study has been conducted on the steam reforming of ethanol on different Ni and Co catalysts synthePalabras claves:Catalyst deactivation, Cobalt, Ethanol steam reforming, hydrogen, nickelAutores:Bilbao J., Carolina Montero-Calderón, Ereña J., Gayubo A.G., Olazar M., Vicente J.Fuentes:googlescopusAnalysis of ni/la2o3-aal2o3 catalyst deactivation by coke deposition in the ethanol steam reforming
ArticleAbstract: The effect of C-containing byproducts on the deactivation of Ni/La2O3-aAl2O3 catalyst in the steam rPalabras claves:Autores:Bilbao J., Carolina Montero-Calderón, Gayubo A.G., Valle B.Fuentes:googlescopusCatalyst based on sludge derived from wastewater treatment of textile industry
ArticleAbstract: Study of the catalytic properties of residual sludge from effluent treatment plants of two textile iPalabras claves:Autores:Andrés De La Rosa, Carolina Montero-Calderón, Castarieda K., De A.U., Flores D., Katherine Castañeda, Maribel Oña, Ofia M.Fuentes:googlescopusCatalytic cracking of heavy crude oil over iron-based catalyst obtained from galvanic industry wastes
ArticleAbstract: Sewage sludge from the galvanic industry represents a problem to the environment, due to its high mePalabras claves:Catalytic material, Galvanic industry, Sludge, Waste valorizationAutores:Andrés De La Rosa, Carolina Montero-Calderón, Estefanía Villamarin-Barriga, Hugo Solís, Jéssica Canacuán, Pablo Londoño-Larrea, Saldarriaga J.F.Fuentes:scopusEffect of the calcination temperature of Ni/La<inf>2</inf>O<inf>3</inf>-αAl<inf>2</inf>O<inf>3</inf> catalyst on its kinetic behaviour in ethanol steam reforming for H<inf>2</inf> production
Conference ObjectAbstract:Palabras claves:Autores:Bilbao J., Carolina Montero-Calderón, Gayubo A.G., Oar-Arteta L., Valle B.Fuentes:googlescopusKinetic model considering catalyst deactivation for the steam reforming of bio-oil over Ni/La<inf>2</inf>O<inf>3</inf>-ΑAl<inf>2</inf>O<inf>3</inf>
ArticleAbstract: Kinetics of the steam reforming (SR) of bio-oil over a Ni/La2O3-αAl2O3 catalyst is investigated in aPalabras claves:Bio-oil, Deactivation, hydrogen, Kinetic model, Ni catalyst, Steam reformingAutores:Aramburu B., Bilbao J., Carolina Montero-Calderón, Gayubo A.G., Valle B.Fuentes:googlescopusKinetic modelling of dimethyl ether steam reforming over CuFe<inf>2</inf>O<inf>4</inf>/A100H
Conference ObjectAbstract:Palabras claves:Autores:Aguayo A.T., Arandia A., Carolina Montero-Calderón, Gayubo A.G., Oar-Arteta L.Fuentes:googlescopusReaction pathway for ethanol steam reforming on a Ni/SiO<inf>2</inf> catalyst including coke formation
ArticleAbstract: The effect operating conditions (temperature, space time, steam/ethanol molar ratio, ethanol partialPalabras claves:Coke deactivation, Ethanol reforming, Fluidized reactor, hydrogen, Ni/SiO catalyst 2Autores:Azkoiti M.J., Bilbao J., Carolina Montero-Calderón, Ereña J., Gayubo A.G., Vicente J.Fuentes:googlescopusReproducible performance of a Ni/La<inf>2</inf>O<inf>3</inf>–αAl<inf>2</inf>O<inf>3</inf> catalyst in ethanol steam reforming under reaction–regeneration cycles
ArticleAbstract: Equilibration of a Ni/La2O3–αAl2O3 catalyst has been studied with the aim of using it in ethanol stePalabras claves:Deactivation, Ethanol steam reforming, hydrogen, Nickel catalyst, REGENERATIONAutores:Arandia A., Benito P.L., Bilbao J., Carolina Montero-Calderón, Gayubo A.G., Remiro A.Fuentes:googlescopus