Hydrogenation reaction catalyst and preparation method therefor

1. A hydrogenation reaction catalyst for petroleum resin; comprising nickel, a promoter, and a carrier,

wherein the promoter comprises copper and sulfur,

the carrier is at least one selected from the group consisting of silica and alumina,

the nickel has an average crystal size of 1 nm to 10 nm and the hydrogenation reaction catalyst has an average particle size of 1 μm to 20 μm,

a content of the nickel is in a range of 62 parts by weight to 65 parts by weight based on 100 parts by weight of the hydrogenation reaction catalyst,

a content of the copper is in a range of 0.8 parts by weight to 1 parts by weight based on 100 parts by weight of the hydrogenation reaction catalyst,

a mole ratio of the sulfur to the nickel is in a range of 0.02:1 to 0.2:1,

a content of the sulfur is in a range of 2.2 parts by weight to 2.9 parts by weight based on 100 parts by weight of the hydrogenation reaction catalyst,

the catalyst is to selectively hydrogenate an olefin by changing a relative hydrogenation rate of the olefin and an aromatic group during a hydrogenation reaction of an unsaturated hydrocarbon compound containing the aromatic group of the petroleum resin, and

the aromatic/olefin hydrogenation ratio is 0.3-0.8.

2. The hydrogenation reaction catalyst of claim 1 , wherein a hydrogen adsorption amount per weight of the nickel is in a range of 0.01 mmol-H 2 /g-Ni to 0.5 mmol-H 2 /g-Ni.

3. A method for preparing the hydrogenation reaction catalyst according to claim 1 , the method comprising:

(a) producing a primary solution by dissolving nickel, copper compound, and a carrier powder in distilled water;

(b) adding the primary solution to a precipitation vessel and stirring and heating the primary solution to 50° C. to 120° C.;

(c) producing a secondary solution by injecting a solution containing a pH regulator and sulfur into the heated primary solution for 30 minutes to 2 hours, and forming a precipitate on which Ni is supported through precipitation;

(d) producing a dried product by washing, filtering, and heating the precipitate at 100° C. to 200° C. for 5 hours to 24 hours; and

(e) producing a reduced product by reducing the dried product in a hydrogen atmosphere at a temperature of 200° C. to 500° C.

4. The method of claim 3 , further comprising, in the step (d), calcining the dried product in an air atmosphere at a temperature of 200° C. to 500° C.

5. The method of claim 3 , further comprising, in the step (e), producing a powder catalyst by passivating the reduced product with a nitrogen mixed gas containing 0.1% to 20% oxygen.

6. The method of claim 3 , wherein the precipitation is performed at a pH of 7 to 9.

7. A hydrogenation method characterized by selectively hydrogenating an olefin of an unsaturated hydrocarbon compound containing an aromatic group by using the hydrogenation reaction catalyst prepared according to claim 3 .

8. A selectively hydrogenated petroleum resin prepared by the hydrogenation method according to claim 7 .

9. The selectively hydrogenated petroleum resin of claim 8 , wherein the petroleum resin has an APHA value of 30 or less.