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.
ジメチルエーテル(DME)の水和反応の酸触媒として,担持遷移金属酸化物(X/Y,X=WO3,Nb2O5,Y=Al2O3,TiO2,SiO2)を検討した。DME水蒸気改質反応に適した温度域で,Nb2O5/Al2O3触媒は検討した担持遷移金属酸化物触媒の中で最も高いDME水和反応活性を示した。このNb2O5/Al2O3触媒において,Nb2O5担持量や焼成温度を変えて触媒を調製し,水和反応活性の向上を検討した。焼成温度の影響として,800 °Cを超える温度で焼成すると新しい結晶相AlNbO4が現れた。また,BET表面積は焼成温度の上昇で単調に低下した。Nb2O5担持量の影響については,25 wt%までは担持量の増加とともに酸量が増加し,さらに担持量を増加しても酸量はほぼ一定であった。500 °Cで焼成した25 wt% Nb2O5/Al2O3触媒が最もDME水和反応活性が高く,この触媒をCu/ZnO/Al2O3触媒と混合してDME水蒸気改質反応に使用した。Cu/ZnO/Al2O3触媒のNb2O5/Al2O3触媒に対する混合比は,重量比で1が最適であることが分かり,酸触媒のγ-Al2O3と混合した場合よりもDME水蒸気改質反応活性が高いことが分かった。
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.