Abstract: Catalysts for hydrogenation of CO2 to dimethyl ether. These catalysts comprise 0.1-10 wt % per total catalyst weight of a catalytic material containing Pd (e.g. metallic palladium), 0.05-5 wt % per total catalyst weight of a promoter containing Ca (e.g. metallic calcium), as well as 85-99 wt % of CeO2 as a catalyst support. Methods of preparing and characterizing the catalysts as well as processes for catalyzing the hydrogenation of CO2 to dimethyl ether and other byproducts such as methanol, carbon monoxide, and methane portrayed by reactant conversion, product selectivity, and catalyst stability are disclosed.

Abstract: Catalysts for hydrogenation of CO2 to dimethyl ether. These catalysts comprise 0.1-10 wt % per total catalyst weight of a catalytic material containing Pd (e.g. metallic palladium), 0.05-5 wt % per total catalyst weight of a promoter containing Ca (e.g. metallic calcium), as well as 85-99 wt % of CeO2 as a catalyst support. Methods of preparing and characterizing the catalysts as well as processes for catalyzing the hydrogenation of CO2 to dimethyl ether and other byproducts such as methanol, carbon monoxide, and methane portrayed by reactant conversion., product selectivity, and catalyst stability are disclosed.

Abstract: A vanadium oxide catalyst supported on a cerium oxide and zirconium oxide composite core is described. The catalyst comprises 0.1-3 wt % vanadium oxide relative to the total catalyst weight, and the catalyst is in the form of microparticles having diameters of 5-80 ?m. A method using a wetness impregnation technique to produce the catalyst is described. The use of the catalyst in the partial oxidation of methanol to produce formaldehyde is specified, along with the catalyst's stability for reaction periods of 50 or more hours. A method of regenerating the catalyst for multiple reactions is also described.

Abstract: A catalyst composition for methanol partial oxidation for hydrogen production includes a zinc metal supported on a reducible porous oxide carrier. The zinc metal can vary from about 0.1 wt. % to about 30 wt. % of the catalyst composition. The catalyst composition can be used to produce hydrogen from methanol at high yield and with a low selectivity towards carbon monoxide (CO) production. The reducible porous oxide carrier includes a mechanical mixture of CeO2 and ZrO2.

Abstract: A method of producing dimethyl ether involving contacting methanol with a catalyst in the presence of oxygen in a reactor to form the dimethyl ether. The catalyst comprises manganese on a cerium oxide catalyst support, wherein a weight ratio of manganese to the cerium oxide catalyst support is in the range of 0.005 to 0.5. Further, a method of manufacturing the catalyst, including mixing cerium oxide (CeO2) with a solution comprising manganese salt and a solvent, evaporating the solvent, followed by drying and calcining to form a catalyst which comprises manganese on a cerium oxide catalyst support, wherein a weight ratio of manganese to the cerium oxide catalyst support is in the range of 0.005 to 0.5.

Abstract: A catalyst of vanadium oxide supported on cerium oxide and zirconium oxide is specified. The catalyst comprises 0.1-10 wt % vanadium oxide relative to the total catalyst weight, and the catalyst is in the form of microparticles. A method using a wetness impregnation technique to produce the catalyst is described. The use of the catalyst in the oxidative dehydration of methanol to produce dimethyl ether is specified, along with the catalyst's stability for reaction periods of 50 or more hours.

Abstract: A method of producing dimethyl ether involving contacting methanol with a catalyst in the presence of oxygen in a reactor to form the dimethyl ether. The catalyst comprises manganese on a cerium oxide catalyst support, wherein a weight ratio of manganese to the cerium oxide catalyst support is in the range of 0.005 to 0.5. Further, a method of manufacturing the catalyst, including mixing cerium oxide (CeO2) with a solution comprising manganese salt and a solvent, evaporating the solvent, followed by drying and calcining to form a catalyst which comprises manganese on a cerium oxide catalyst support, wherein a weight ratio of manganese to the cerium oxide catalyst support is in the range of 0.005 to 0.5.

Abstract: A catalyst composition for methanol partial oxidation for hydrogen production includes a zinc metal supported on a reducible porous oxide carrier. The zinc metal can vary from about 0.1 wt. % to about 30 wt. % of the catalyst composition. The catalyst composition can be used to produce hydrogen from methanol at high yield and with a low selectivity towards carbon monoxide (CO) production. The reducible porous oxide carrier includes a mechanical mixture of CeO2 and ZrO2.