Dehydrogenation catalyst
The present invention relates to a dehydrogenation catalyst in which a platinum-group metal, an assistant metal, and an alkali metal or alkaline earth metal component are supported on a carrier, wherein the molar ratio of platinum to the assistant metal is 0.5 to 1.49, and the catalyst has an acidity amount of 20 to 150 μmol KOH/g catalyst when it is titrated with KOH. The dehydrogenation catalyst according to the present invention may prevent coke formation from increasing rapidly when the hydrogen/hydrocarbon ratio in a dehydrogenation reaction is reduced, thereby increasing the productivity of the process. Accordingly, it makes it possible to operate the process under a condition in which the hydrogen/hydrocarbon ratio in a dehydrogenation reaction is reduced, thereby improving the economy of the process.
1. A dehydrogenation catalyst comprising:
a platinum-group metal;
an assistant metal; and
an alkali metal or alkaline-earth metal component,
the platinum-group metal, the assistant metal, and the alkali metal or alkaline-earth metal component being supported on a carrier, wherein
a molar ratio of platinum to the assistant metal is 0.5 to 1.49, and
an acidity amount of 20 to 150 μmol KOH/g catalyst is obtained, which is determined by titration of the catalyst with KOH.
2. The dehydrogenation catalyst of claim 1 , wherein the catalyst comprises, based on the total weight of the catalyst, 0.3 to 0.8 wt % of platinum and 0.4 to 0.9 wt % of the alkali metal or alkaline-earth metal.
3. The dehydrogenation catalyst of claim 1 , wherein the catalyst has a bulk density of 0.55 to 0.9 g/cc.
4. The dehydrogenation catalyst of claim 1 , wherein the catalyst has a pill size of 1.2 to 2.5 mm.
5. The dehydrogenation catalyst of claim 1 , wherein the carrier comprises both mesopores having an average pore size of 5 to 100 nm and a total pore volume of 0.05 to 2 cm 3 /g and macropores having an average pore size of 0.1 to 20 μm and a total pore volume of 0.05 to 3 cm 3 /g.
6. The dehydrogenation catalyst of claim 1 , wherein the alkali metal or alkaline-earth metal is one or more selected from the group consisting of calcium, potassium, sodium, magnesium, lithium, strontium, barium, radium, and beryllium.
7. The dehydrogenation catalyst of claim 1 , wherein the assistant metal is one or more selected from the group consisting of tin, germanium, gallium, indium, zinc, and manganese.
8. The dehydrogenation catalyst of claim 1 , wherein the carrier is selected from the group consisting of TiO 2 , SiO 2 , Al 2 O 3 , ZrO 2 , Cr 2 O 3 , Nb 2 O 5 , and mixtures thereof.
9. The dehydrogenation catalyst of claim 8 , wherein the alumina (Al 2 O 3 ) carrier comprises 90% to 100% theta-crystalline phase and 0% to 10% alpha-crystalline phase or gamma-crystalline phase.
10. The dehydrogenation catalyst of claim 1 , wherein the carrier has a specific surface area of 50 to 170 m 2 /g.
11. The dehydrogenation catalyst of claim 1 , wherein the catalyst further comprises one or more halogen components selected from the group consisting of chlorine, phosphorus, and fluorine.
12. A method for dehydrogenating a hydrocarbon, the method comprising bringing the hydrocarbon into contact with a dehydrogenation catalyst set forth in claim 1 .
13. The method of claim 12 , wherein the hydrocarbon is one selected from the group consisting of ethane, propane, n-butane, pentane, hexane, heptane, and octane.