The gas-phase maleic anhydride hydrogenation was studied at 170 °C and 1 bar using Ni/SiO2–Al2O3 catalysts varying metal loading. The maximum γ-butyrolactone selectivity was reached for a 10 wt% nickel load. On the basis of temperature programmed experiments, it is proposed that new active sites in selective succinic anhydride hydrogenolysis are formed when Ni loads are higher than 8 wt%Fil: Meyer, Camilo Ignacio. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico - CONICET - Santa Fe. Instituto de Investigaciones en Catálisis y Petroquímica; Argentina;Fil: Regenhardt, Silvina Andrea. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico - CONICET - Santa Fe. Institu...
Supported metal catalysts are widely used in industrial processes, and the particle size of the acti...
The hydrogenolysis of n-heptane over 2%, 4%, 6% and 8% Ni / Al2 O3 was studied in a flow reactor usi...
Not only catalyst composition, but also temperature, pressure and H2/C4 ratio play important roles i...
The gas phase hydrogenation of maleic anhydride to obtain γ-butyrolactone was studied using Ni suppo...
The gas phase hydrogenation of maleic anhydride (MA) to succinic anhydride (SA) and the subsequent h...
The gas-phase hydrogenation of maleic anhydride over Ni catalysts supported on SiO2 and SiO2-Al2O3, ...
The gas-phase hydrogenation of maleic anhydride was studied using Cu and/or Ni based catalysts, supp...
Se estudió la hidrogenación de anhídrido maleico en fase gas empleando catalizadores de Cu y/o Ni, s...
The proper selection of transition metals and support is pivotal to the design of active and selecti...
This thesis presents my efforts in the design and development of novel ceria (CeO2)-supported Ni-bas...
Pt-based catalysts, supported on Al2O3, SiO2 and SiO2-Al2O3, were prepared by incipient wetness imp...
The rational design of catalyst is vital in the hydrogenation of maleic anhydride (MA) to chemicals,...
In this work, the deactivation of a Cu(10%)/SiO2 catalyst in the gas-phase hydrogenation of maleic a...
The rational design of catalyst is vital i...
A series of Sc-doped ZrO2 supports, with Sc2O3 content in the range of 0 to 7.5% (mol/mol), were pre...
Supported metal catalysts are widely used in industrial processes, and the particle size of the acti...
The hydrogenolysis of n-heptane over 2%, 4%, 6% and 8% Ni / Al2 O3 was studied in a flow reactor usi...
Not only catalyst composition, but also temperature, pressure and H2/C4 ratio play important roles i...
The gas phase hydrogenation of maleic anhydride to obtain γ-butyrolactone was studied using Ni suppo...
The gas phase hydrogenation of maleic anhydride (MA) to succinic anhydride (SA) and the subsequent h...
The gas-phase hydrogenation of maleic anhydride over Ni catalysts supported on SiO2 and SiO2-Al2O3, ...
The gas-phase hydrogenation of maleic anhydride was studied using Cu and/or Ni based catalysts, supp...
Se estudió la hidrogenación de anhídrido maleico en fase gas empleando catalizadores de Cu y/o Ni, s...
The proper selection of transition metals and support is pivotal to the design of active and selecti...
This thesis presents my efforts in the design and development of novel ceria (CeO2)-supported Ni-bas...
Pt-based catalysts, supported on Al2O3, SiO2 and SiO2-Al2O3, were prepared by incipient wetness imp...
The rational design of catalyst is vital in the hydrogenation of maleic anhydride (MA) to chemicals,...
In this work, the deactivation of a Cu(10%)/SiO2 catalyst in the gas-phase hydrogenation of maleic a...
The rational design of catalyst is vital i...
A series of Sc-doped ZrO2 supports, with Sc2O3 content in the range of 0 to 7.5% (mol/mol), were pre...
Supported metal catalysts are widely used in industrial processes, and the particle size of the acti...
The hydrogenolysis of n-heptane over 2%, 4%, 6% and 8% Ni / Al2 O3 was studied in a flow reactor usi...
Not only catalyst composition, but also temperature, pressure and H2/C4 ratio play important roles i...