Abstract:
PURPOSE: A catalyst for the Fischer-Tropsch process and a manufacturing method thereof are provided to accelerate the carbide forming reaction to increase the generation of hydrocarbon with a long chain like wax, and to be able to have the similar activity to the catalysts manufactured by co-precipitation by reducing the catalyst under the condition that synthetic gas (CO+H2) exists at a relatively low temperature of 350-400deg.C. CONSTITUTION: A catalyst for the Fischer-Tropsch process includes an iron compound as an active material, sodium and sodium hydroxide as co-catalyst, and a carrier. A manufacturing method of the catalyst for the Fischer-Tropsch process comprises the following steps: a step of removing moisture and foreign substances attached on the surface of the carrier by plasticizing the carrier; a step of stirring the plasticized carrier under the nitrogen atmosphere; a step of manufacturing a melted and dipped carrier by adding sodium and sodium hydroxide in the stirred carrier; a step of dipping an iron precursor and a copper precursor in the melted and dipped carrier; and a step of drying and plasticizing the carrier in which an iron precursor and a copper precursor are dipped.
Abstract:
PURPOSE: A manufacturing method for a metal- or metal oxide-supported catalyst using a melt-infiltration process with a metal hydrate salt and a metal- or metal oxide-supported catalyst thereof are provided to easily and quickly mass produce the metal- or metal oxide-supported catalyst by using a nitrate hydrate metal salt or a chloride hydrate metal salt with a low melting point. CONSTITUTION: A manufacturing method for a metal- or metal oxide-supported catalyst using a melt-infiltration process with a metal hydrate salt comprises the following steps: The metal hydrate salt is mixed with a metal substrate with a porous structure. After the mixing process, the mixture is melted at the melting point of the metal hydrate salt such that the metal hydrate salt infiltrates into the substrate. The metal hydrate salt infiltrated in the supporter is plasticized at a high temperature and chagrined to nanoparticles. The metal hydrate salt has a melting point within 35 - 120 deg. C. [Reference numerals] (a) Step of mixing metal hydrate salt and a support; (b) Step of carrying by melting impregnation; (c) Step of nanoparticulation by plasticizing