José Cambra - Academia.edu (original) (raw)
Papers by José Cambra
Chemical Engineering Journal, 2014
Fuel Science and Technology International
Conventional HDS-catalysts consist of Co and Mo supported on Y-Al2O3. The addition of Zn as a sec... more Conventional HDS-catalysts consist of Co and Mo supported on Y-Al2O3. The addition of Zn as a second promoter or the alumina acidification with F increase the catalitye activity in HDS of commercial feeds (Fierro et al., 1984; Boorman et al., 1984). In this paper the combined effect of both Zn and F incorporation is discussed. A series of Zn-Co-Mo catalysts
International Journal of Hydrogen Energy
ChemInform, 1993
ABSTRACT ChemInform is a weekly Abstracting Service, delivering concise information at a glance t... more ABSTRACT ChemInform is a weekly Abstracting Service, delivering concise information at a glance that was extracted from about 100 leading journals. To access a ChemInform Abstract of an article which was published elsewhere, please select a “Full Text” option. The original article is trackable via the “References” option.
Bulletin des Sociétés Chimiques Belges, 1995
Bulletin des Sociétés Chimiques Belges, 1991
Studies in Surface Science and Catalysis, 1997
... and P. Grange, editors 567 Hydrocracking activity of NiMo - USY zeolite hydrotreating catalys... more ... and P. Grange, editors 567 Hydrocracking activity of NiMo - USY zeolite hydrotreating catalysts B. Egla'', JF Cambra'', B. Guemez^ PL Arias'', B. Paweiec^ and ... In previous works [4-6] the HDS and HDN activities of Ni, Mo and MoNi zeolite supported catalysts were studied, and a ...
Economic Effects of Biofuel Production, 2011
Waste and Biomass Valorization, 2010
Topics in Catalysis, 2014
Topics in Catalysis, 2008
Process Safety and Environmental Protection, 2013
ABSTRACT Waelz oxide is a zinc and lead concentrate pyrometallurgically derived from electric arc... more ABSTRACT Waelz oxide is a zinc and lead concentrate pyrometallurgically derived from electric arc furnace dust. There are clear incentives to leaching and purify this oxide to produce liquors that can be electrowinned to obtain recycled metallic zinc. This study is focused on this electrolytic zinc production from previously obtained sulphuric liquor. This liquor was obtained from double leached Waelz oxide (DLWO) throughout a hydrometallurgical process. The electrolytic liquor, after the corresponding leaching and purification stages, contains around 49 kg/m3. This liquor was fed to an electrowinning process where platinum or lead anodes and aluminium cathodes were used. After optimizing the different electrowinning critical parameters, and working at these optimal conditions, almost 88 secondary zinc kg were precipitated per each initial DLWO tonne in one-through process. The zinc purity was higher than 99.5%. After some mass balance calculations, it can be concluded that, optimizing the process configuration through internal recycling, around 210 Zn kg/DLWO t with purity near to 100% could be achieved.
Minerals Engineering, 2010
Journal of Molecular Catalysis A: Chemical, 2013
Journal of Membrane Science, 2012
ABSTRACT A PdCu membrane was characterised and then tested in complex hydrogen containing streams... more ABSTRACT A PdCu membrane was characterised and then tested in complex hydrogen containing streams from methane oxidation and reforming processes. The hydrogen permeance and stability of the PdCu membrane, prepared by electroless plating, was analysed in pure hydrogen and by thermal cycling in inert and hydrogen atmospheres. This membrane was then placed in a membrane module, into which the product gases from a catalytic reactor were fed. Methane catalytic partial oxidation (CPO) and wet-CPO were performed in the catalytic reactor. Firstly, process feed pressure and sweep gas flow were optimised and, finally, the effect of mixture compounds (CO, CO2, CH4 and H2O) on membrane behaviour was analysed. Changes in the composition of the mixture fed into the membrane module had only little influence on membrane performance during the 30 h of operation. Around 60% of the hydrogen produced in the catalytic reactor was separated in the membrane module, operating at 673 K, 3.5 bar(g) feed pressure and 550 NmL/min of sweep gas. The membrane was characterised using SEM and XRD.
Journal of Materials Science, 2013
Chemical Engineering Journal, 2014
Fuel Science and Technology International
Conventional HDS-catalysts consist of Co and Mo supported on Y-Al2O3. The addition of Zn as a sec... more Conventional HDS-catalysts consist of Co and Mo supported on Y-Al2O3. The addition of Zn as a second promoter or the alumina acidification with F increase the catalitye activity in HDS of commercial feeds (Fierro et al., 1984; Boorman et al., 1984). In this paper the combined effect of both Zn and F incorporation is discussed. A series of Zn-Co-Mo catalysts
International Journal of Hydrogen Energy
ChemInform, 1993
ABSTRACT ChemInform is a weekly Abstracting Service, delivering concise information at a glance t... more ABSTRACT ChemInform is a weekly Abstracting Service, delivering concise information at a glance that was extracted from about 100 leading journals. To access a ChemInform Abstract of an article which was published elsewhere, please select a “Full Text” option. The original article is trackable via the “References” option.
Bulletin des Sociétés Chimiques Belges, 1995
Bulletin des Sociétés Chimiques Belges, 1991
Studies in Surface Science and Catalysis, 1997
... and P. Grange, editors 567 Hydrocracking activity of NiMo - USY zeolite hydrotreating catalys... more ... and P. Grange, editors 567 Hydrocracking activity of NiMo - USY zeolite hydrotreating catalysts B. Egla'', JF Cambra'', B. Guemez^ PL Arias'', B. Paweiec^ and ... In previous works [4-6] the HDS and HDN activities of Ni, Mo and MoNi zeolite supported catalysts were studied, and a ...
Economic Effects of Biofuel Production, 2011
Waste and Biomass Valorization, 2010
Topics in Catalysis, 2014
Topics in Catalysis, 2008
Process Safety and Environmental Protection, 2013
ABSTRACT Waelz oxide is a zinc and lead concentrate pyrometallurgically derived from electric arc... more ABSTRACT Waelz oxide is a zinc and lead concentrate pyrometallurgically derived from electric arc furnace dust. There are clear incentives to leaching and purify this oxide to produce liquors that can be electrowinned to obtain recycled metallic zinc. This study is focused on this electrolytic zinc production from previously obtained sulphuric liquor. This liquor was obtained from double leached Waelz oxide (DLWO) throughout a hydrometallurgical process. The electrolytic liquor, after the corresponding leaching and purification stages, contains around 49 kg/m3. This liquor was fed to an electrowinning process where platinum or lead anodes and aluminium cathodes were used. After optimizing the different electrowinning critical parameters, and working at these optimal conditions, almost 88 secondary zinc kg were precipitated per each initial DLWO tonne in one-through process. The zinc purity was higher than 99.5%. After some mass balance calculations, it can be concluded that, optimizing the process configuration through internal recycling, around 210 Zn kg/DLWO t with purity near to 100% could be achieved.
Minerals Engineering, 2010
Journal of Molecular Catalysis A: Chemical, 2013
Journal of Membrane Science, 2012
ABSTRACT A PdCu membrane was characterised and then tested in complex hydrogen containing streams... more ABSTRACT A PdCu membrane was characterised and then tested in complex hydrogen containing streams from methane oxidation and reforming processes. The hydrogen permeance and stability of the PdCu membrane, prepared by electroless plating, was analysed in pure hydrogen and by thermal cycling in inert and hydrogen atmospheres. This membrane was then placed in a membrane module, into which the product gases from a catalytic reactor were fed. Methane catalytic partial oxidation (CPO) and wet-CPO were performed in the catalytic reactor. Firstly, process feed pressure and sweep gas flow were optimised and, finally, the effect of mixture compounds (CO, CO2, CH4 and H2O) on membrane behaviour was analysed. Changes in the composition of the mixture fed into the membrane module had only little influence on membrane performance during the 30 h of operation. Around 60% of the hydrogen produced in the catalytic reactor was separated in the membrane module, operating at 673 K, 3.5 bar(g) feed pressure and 550 NmL/min of sweep gas. The membrane was characterised using SEM and XRD.
Journal of Materials Science, 2013