Preparation method of hydrogenated petroleum resin

Patent metadata

Field	Value
Publication number	US-12173109-B2
Application number	US-202017615885-A
Country	US
Kind code	B2
Filing date	Jun 2, 2020
Priority date	Jun 3, 2019
Publication date	Dec 24, 2024
Grant date	Dec 24, 2024

Abstract

The invention relates to a method for preparing hydrogenated petroleum resin. More specifically, the invention relates to a method for preparing hydrogenated petroleum resin having aromaticity of 10% or more and exhibiting excellent color and thermal stability, through a hydrogenation reaction in a slurry reactor, using a selective hydrogenation catalyst having excellent selectivity to olefinic double bonds in petroleum resin.

First claim

The invention claimed is:

1. A method for preparing hydrogenated petroleum resin comprising the steps of:
introducing a selective hydrogenation catalyst and hydrogen gas in a mixture of petroleum resin and a solvent and conducting a hydrogenation reaction,
wherein the selective hydrogenation catalyst is a supported catalyst in which nickel and sulfur are supported on a carrier, and comprises nickel in the content of 40 to 80 wt %, based on the total weight of the selective hydrogenation catalyst, and
the hydrogenated petroleum resin has aromaticity of 10 to 15%, APHA value measured according to ASTM D1209 of 10 to 20, and color number measured with Gardner color scale after aging at 180° C. for 72 hours of 13 to 15.

2. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the mole ratio of sulfur to 1 mole of nickel is 0.03 to 0.5.

3. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the carrier comprises silica, alumina, magnesia or a mixture thereof.

4. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the carrier is comprised in an amount of 10 to 50 wt % based on the total weight of the selective hydrogenation catalyst.

5. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the selective hydrogenation catalyst is used in the amount of 0.2 to 10 parts by weight, based on 100 parts by weight of the petroleum resin.

6. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein one or more hydrogenation catalysts selected from the group consisting of a selective hydrogenation catalyst comprising nickel and copper; a selective hydrogenation catalyst comprising noble metal; and a non-selective hydrogenation catalyst of nickel metal are further added during the hydrogenation reaction.

7. The method for preparing hydrogenated petroleum resin according to claim 6 , wherein the one or more hydrogenation catalysts are comprised in an amount of 0.1 to 10 parts by weight, based on 1 part by weight of the selective hydrogenation catalyst which is the supported catalyst in which nickel and sulfur are supported on the carrier, and comprises nickel in the content of 40 to 80 wt %, based on the total weight of the selective hydrogenation catalyst.

8. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the solvent is a hydrocarbon-based solvent selected from the group consisting of pentane, hexane, heptane, nonane, decane, cyclohexane, methylcyclohexane, benzene, toluene, xylene, and a mixture thereof.

9. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the solvent is used in an amount of 40 to 80 parts by weight, based on 100 parts by weight of the petroleum resin.

10. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the hydrogenation reaction is conducted in a slurry reactor.

11. The method for preparing hydrogenated petroleum resin according to claim 10 , wherein the slurry reactor is an autoclave type reactor equipped with a stirrer or a loop type reactor circulating and mixing reaction fluid.

12. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the hydrogenation reaction is conducted at a temperature of 150 to 250° C., and a pressure of 20 to 100 bar.

13. The method for preparing hydrogenated petroleum resin according to claim 1 , wherein the hydrogenation reaction is conducted while continuously introducing hydrogen gas so as to maintain reaction pressure during the reaction.

14. Hydrogenated petroleum resin prepared by the method according to claim 1 , having aromaticity of 10 to 15%, APHA value measured according to ASTM D1209 of 10 to 20, and color number measured with Gardner color scale after aging at 180° C. for 72 hours of 13 to 15.

15. A pressure sensitive adhesive comprising the hydrogenated petroleum resin according to claim 14 .

16. An adhesive comprising the hydrogenated petroleum resin according to claim 14 .

Assignees

• Hanwha Solutions Corp

Inventors

• Seo Sangho
• Han Keedo
• Seong Pilje
• Shin Dong Il
• Jeon Bong Sik

Classifications

• B01J2235/05

  Nuclear magnetic resonance [NMR] · CPC title

• B01J35/45

  Nanoparticles · CPC title

• B01J35/393

  Metal or metal oxide crystallite size · CPC title

• B01J35/40

  characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title

• C09J145/00

  Adhesives based on homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic system; Adhesives based on derivatives of such polymers (based on polymers of cyclic esters of polyfunctional acids C09J131/00; based on polymers of cyclic anhydrides or imides C09J135/00) · CPC title