Process and catalyst for resin hydrogenation

Patent metadata

Field	Value
Publication number	US-9644044-B2
Application number	US-201414904793-A
Country	US
Kind code	B2
Filing date	Jul 17, 2014
Priority date	Jul 17, 2013
Publication date	May 9, 2017
Grant date	May 9, 2017

Abstract

The invention is in the field of catalysis. More specifically, the invention pertains to catalytic hydrogenation processes and catalysts used therein. According to the invention there is provided a process for the hydrogenation of hydrocarbon resins, in particular hydrocarbon resin feeds with a relatively high sulfur content using a cobalt promoted nickel on silica/alumina catalyst, the catalyst per se, and the process of preparing said catalyst.

First claim

The invention claimed is:

1. A process for hydrogenation of a hydrocarbon resin feed containing one or more sulfur compounds, the process comprising:
contacting said hydrocarbon resin feed with hydrogen in the presence of a catalyst,
wherein said catalyst is a cobalt promoted supported nickel on silica and alumina catalyst, said cobalt promoted catalyst having
a nickel content, calculated as Ni of 45 to 85 wt. %;
a silicon content, calculated as SiO 2 , of 13.75-45 wt. %; and
an aluminum content, calculated as Al 2 O 3 , of 1-15 wt. %,

based on the weight of the reduced catalyst.

2. The process according to claim 1 , wherein said catalyst has a cobalt content, calculated as Co, of 0.25-12 wt. %, based on the weight of the reduced catalyst.

3. The process according to claim 1 , wherein said catalyst has a pore volume in pores with a size between 2 and 60 nm of at least 0.35 ml/g of catalyst.

4. The process according to claim 1 , wherein the one or more sulfur compound content of the hydrocarbon resin is more than 40 ppm, calculated as sulfur, based on the weight of the hydrocarbon resin feed.

5. The process according to claim 3 , wherein said catalyst has a pore volume in pores with a size between 10 and 60 nm of at least 0.20 ml/g of catalyst.

6. The process according to claim 4 , wherein the one or more sulfur compound content of the hydrocarbon resin is more than 100 ppm, calculated as sulfur, based on the weight of the hydrocarbon resin feed.

7. A cobalt promoted supported nickel on silica and alumina catalyst, wherein said catalyst comprises:
a nickel content, calculated as Ni of 45 to 85 wt. %;
a silicon content, calculated as SiO 2 , of 13.75-45 wt. %;
an aluminum content, calculated as Al 2 O 3 , of 1-15 wt. %; and
a cobalt content, calculated as Co, of 0.25-1.5 wt. %,

based on the weight of the reduced catalyst.

8. The catalyst according to claim 7 , wherein the catalyst has a pore volume in pores with a size between 2 and 60 nm of at least 0.35 ml/g of catalyst.

9. The catalyst according to claim 8 , wherein the catalyst has a pore volume in pores with a size between 10 and 60 nm of at least 0.20 ml/g of the catalyst.

10. A process for preparing a cobalt promoted supported nickel on silica and alumina catalyst, said process comprises:
coprecipitating one or more nickel salts, cobalt salts, aluminum salts and one or more silicon compounds at a pH-value of 7.0-9.0,
recovering the coprecipitated material from the precipitation liquid,
washing the recovered coprecipitated material; and
treating the washed recovered coprecipitated material to produce said catalyst,
wherein said catalyst comprises:
a nickel content, calculated as Ni of 45 to 85 wt. %;
a silicon content, calculated as SiO 2 , of 13.75-45 wt. %;
an aluminum content, calculated as Al 2 O 3 , of 1-15 wt. %; and
a cobalt content, calculated as Co, of 0.25-4 wt. %

based on the weight of the catalyst.

11. The process according to claim 10 , wherein said catalyst has a cobalt content, calculated as Co, of 0.25-1.5 wt. %, based on the weight of the catalyst.

12. The process according to claim 10 , wherein said catalyst has a pore volume between 2 and 60 nm of at least 0.35 ml/g of catalyst.

13. The process according claim 12 , wherein said catalyst has a pore volume in pores with a size between 10 and 60 nm of at least 0.20 ml/g of catalyst.

Assignees

• Basf Corp

Inventors

• Sandee Albertus Jacobus
• Chintada Jogesh
• Terörde Robert Johan Andreas Maria

Classifications

• B01J23/755

  Nickel · CPC title

• B01J37/03

  Precipitation; Co-precipitation · CPC title

• B01J2523/00

  Constitutive chemical elements of heterogeneous catalysts · CPC title

• B01J37/06

  Washing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• C10G45/06

  containing nickel or cobalt metal, or compounds thereof · CPC title