A supported metal catalyst in which an electric conductivity is enhanced. The supported metal catalyst includes a support powder; and metal fine particles supported by the support powder. The support powder is an aggregate of support fine particles; the support fine particles are provided with a chained portion structured by a plurality of crystallites being fusion-bonded to form a chain; the support fine particles are structured with a metal oxide; and the supported amount of metal fine particles per unit area of the surface area of the support powder calculated based on sphere approximation is 3.4 to 13.7 (mg/m.sup.2).

Oxidative dehydrogenation catalysts for converting lower paraffins to alkenes such as ethane to ethylene when prepared as an agglomeration, for example extruded with supports comprising slurries of Nb.sub.2O.sub.5.

Oxidative dehydrogenation catalysts for converting lower paraffins to alkenes such as ethane to ethylene when prepared as an agglomeration, for example extruded with supports comprising slurries of Nb.sub.2O.sub.5.

The present disclosure refers to increasing the catalytic efficiency of Weyl semimetals by subjecting Weyl semimetals to an external magnetic field of greater than 0 T, for example greater than 0.1 T. In a preferred embodiment of the present disclosure the Weyl semimetal is selected from the group consisting of NbP, TaP, NbAs and TaAs.

The present disclosure refers to increasing the catalytic efficiency of Weyl semimetals by subjecting Weyl semimetals to an external magnetic field of greater than 0 T, for example greater than 0.1 T. In a preferred embodiment of the present disclosure the Weyl semimetal is selected from the group consisting of NbP, TaP, NbAs and TaAs.

A catalytic distillation process, which when operated under vacuum conditions, makes possible the facilitation of peroxyacid chemistry under intrinsically safe conditions with superior efficiency compared to conventional technology. In particular, the process can be used for the production of performic acid (PFA) created from the chemical reaction of formic acid and hydrogen peroxide, while contacting one or more kinds of heterogeneous catalysts, immobilized in one or more regions of the reactor (i.e. within reaction zones within the column). Aqueous hydrogen peroxide and formic acid feed streams are directed to the catalytic distillation column. The products are separated from the reactants in situ from the distillation action within the column The process is made efficient by utilizing moisture tolerant catalyst materials which facilitate the chemical conversion of the reactants operating at or near stoichiometric amount and by operating the catalytic distillation reactor at or near 100% conversion and at an optimal reflux ratio which prevents the accumulation of water in the system while maximizing external mass transfer rates, catalyst wetting efficiency and energy efficiency.

A catalytic distillation process, which when operated under vacuum conditions, makes possible the facilitation of peroxyacid chemistry under intrinsically safe conditions with superior efficiency compared to conventional technology. In particular, the process can be used for the production of performic acid (PFA) created from the chemical reaction of formic acid and hydrogen peroxide, while contacting one or more kinds of heterogeneous catalysts, immobilized in one or more regions of the reactor (i.e. within reaction zones within the column). Aqueous hydrogen peroxide and formic acid feed streams are directed to the catalytic distillation column. The products are separated from the reactants in situ from the distillation action within the column The process is made efficient by utilizing moisture tolerant catalyst materials which facilitate the chemical conversion of the reactants operating at or near stoichiometric amount and by operating the catalytic distillation reactor at or near 100% conversion and at an optimal reflux ratio which prevents the accumulation of water in the system while maximizing external mass transfer rates, catalyst wetting efficiency and energy efficiency.

Provided is a method of preparing an intermetallic catalyst. The method includes form core-shell particles including a transition metal oxide coating layer by irradiating ultrasonic waves to a precursor mixture solution including a noble metal precursor, a transition metal precursor, and a carrier to; forming intermetallic particles including a transition metal oxide coating layer by annealing the core-shell particles; and removing the transition metal oxide coating layer from the intermetallic particles.

A catalyst comprising a barium niobate-based cubic perovskite structure where, Mg and Ca has been used to dope the niobium sites along with Fe, Ni, Co, Y, and Pr.

A catalyst comprising a barium niobate-based cubic perovskite structure where, Mg and Ca has been used to dope the niobium sites along with Fe, Ni, Co, Y, and Pr.