Intermetallic Pt2Y bulk nanopowder (2.9 m2 g−1, 28 nm) was chemically synthesized with approachable common chemicals and facilities.
The influence of support materials and preparation methods on CO2 methanation activity was investigated using Ru nanoparticles supported on amorphous ZrO2 (am-ZrO2), crystalline ZrO2 (cr-ZrO2), and SiO2.
Hexagonal boron nitride solid base catalysts were prepared by simple ball-milling at various rotation speeds of a commercial low-surface area boron nitride.
The catalytic hydrodeoxygenation (HDO) of the cyclic five-membered ester gamma-valerolactone (GVL-C5H8O2) on a series of supported metal phosphide and bimetallic phosphide catalysts was studied at 0.5 MPa. Comparison of activities was based on turnover frequencies calculated from surface metal atoms determined from the chemisorption of CO at 50 °C. It was found that catalytic activity followed the order: Ni2P/MCM-41 >> CoP/MCM-41 >> Pd/Al2O3 ≈ MoP/MCM-41 > WP/MCM-41 in mono metallic phosphide catalyst and Ni2P/MCM-41 > NiMo(3:1)P/MCM-41 > NiMo(1:1)P/MCM-41 > NiMo(1:3)P/MCM-41 > MoP/MCM-41 in bimetallic phosphide catalysts. On all catalysts ring opening of the lactone to produce pentanoic acid was the main initial step with subsequent hydrogenation to form pentanal. On Ni2P/MCM-41, CoP/MCM-41 and Pd/Al2O3 this was followed mainly by decarbonylation to produce CO and saturated C4 hydrocarbons. On MoP/MCM-41 and WP/MCM-41 the principal subsequent step was deoxygenation to produce unsaturated C5 hydrocarbons. The bimetallic phosphide catalysts presented performance as pure compounds depending on the metal ratio, but slightly enhanced production of C5 hydrocarbons. A possible reaction network is proposed based on product selectivity.
The catalytic hydrodeoxygenation (HDO) of the cyclic five-membered ester gamma-valerolactone (GVL-C5H8O2) on a series of supported metal phosphide catalysts and a commercial Pd/Al2O3 catalyst was studied at 0.5 MPa.
Several supported transition metal oxides (X/Y, X=WO3, Nb2O5, Y=Al2O3, TiO2, SiO2) were investigated as solid acid catalysts for hydrolysis of dimethyl ether (DME). Among the transition metal oxide catalysts tested, Nb2O5/Al2O3 showed the highest catalytic activity in the temperature range appropriate for DME steam reforming. Using several types of Nb2O5/Al2O3 samples, the effects of Nb2O5 loading amounts and calcination temperature on the catalytic activity were studied to enhance the hydrolysis activity. XRD patterns showed AlNbO4 phase appeared when the calcination temperature was over 800 °C. The BET surface area decreased for the increase in the calcination temperature. For Nb2O5/Al2O3, the acid amount increased consistently with the Nb2O5 loading amounts up to 25 wt%, and it became almost constant for the further increase in the Nb2O5 loadings. 25 wt% Nb2O5/Al2O3 catalyst calcined at 500 °C exhibited the highest catalytic activity for DME hydrolysis, and consequently steam reforming of DME was carried out over the Nb2O5/Al2O3 mixed with Cu/ZnO/Al2O3. It was found that an optimal ratio of Cu/ZnO/Al2O3 to Nb2O5/Al2O3 was 1, which resulted in higher catalytic activity for steam reforming of DME than a mixture of Cu/ZnO/Al2O3 and γ-Al2O3.
Solid Oxide Fuel Cells (SOFC) operating at high temperatures are one of the most efficient electrochemical devices for power generation. For the efficient recovery of exhaust heat from SOFC stacks, external steam reforming of hydrocarbon fuels such as methane is generally employed in commercial SOFC systems. In this study, dry reforming reaction (DR) is proposed as the external reforming because it does not need steam generators and enables to use carbon dioxide as reactant in the anode gas. Supported Ni catalysts have been investigated by using several support materials of different oxygen ion conductivity and basicity. Among the prepared catalysts, Ni/La0.3Sr0.7TiO3-δ (LST) was found to exhibit excellent activity for DR. In order to improve the catalytic activity and tolerance to carbon deposition, post treatment and basic additives were examined for Ni/LST.
As for selective CO methanation over heterogeneous catalysts, numerous investigations of the reaction mechanism and catalyst development are reviewed.