Abstract:
The present invention relates to a method for manufacturing a cobalt-based catalyst for Fischer-Tropsch synthesis reaction and, more particularly, to a method for manufacturing a cobalt-based catalyst that is represented by Ir-Co/η-Al_2O_3 manufactured by repeatedly impregnating cobalt and iridium in a spherical eta-alumina support, which has many acid points formed thereon, and drying the impregnated product dozens of times, thus supporting the cobalt and iridium at high density in the support. A catalyst manufactured by the manufacturing method according to the present invention increases the conversion rate of carbon monoxide and the selectivity of liquid hydrocarbon when applied to Fischer-Tropsch synthesis reaction.
Abstract:
PURPOSE: Novel metal modified hydrotalcite catalyst for reforming alcohols and a method for producing hydrogen using the same are provided to expand the life of the catalyst without plenty amount of vapor or oxygen. CONSTITUTION: Novel metal modified hydrotalcite catalyst for reforming alcohols immerses Group VIII elements in nickel-based catalyst in the structure of a modified hydrotalcite containing nickel, magnesium, and aluminum. The catalyst for reforming alcohols is represented by chemical formula 1. In chemical formula 1, A is one of Group VIII elements; x is between 0.1 and 5 inclusively; y is between 0.25 and 1 inclusively; and z is between 2 and 2.75 inclusively. The alcohols are C1 to C6 alcohol, C2 to C6 glycol, glycerol, or the mixture of the same.
Abstract:
PURPOSE: Nickel-based hydrotalcite catalyst for modifying the vapor of diesel, a method for manufacturing the same, and a method for manufacturing hydrogen based on the modification of diesel using the same are provided to improve the yield of hydrogen. CONSTITUTION: Nickel-based hydrotalcite catalyst for modifying the vapor of diesel is represented by chemical formula 1. In chemical formula 1, A is one or more alkali earth metal oxides; B is one or more Group 8B precious metal atoms; a is the content of the alkali earth metal in catalyst and is between 0 and 10 weight%; b is the content of the Group 8B precious metal atoms and is between 0 and 10 weight%; either of the alkali earth metal or the Group 8B precious metal atoms is more than or equal to 0 weight%; and x and y are the molar ratio of Ni and Mg; x is between 0.2 and 0.9; and y is between 0.5 and 5.5.