Process and Catalyst for Resin Hydrogenation

US2016159941A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016159941-A1
Application numberUS-201414904793-A
CountryUS
Kind codeA1
Filing dateJul 17, 2014
Priority dateJul 17, 2013
Publication dateJun 9, 2016
Grant date

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  1. Title

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  2. Abstract

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  4. Key dates

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  5. First independent claim

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Abstract

Official abstract text for this publication.

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

Opening claim text (preview).

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 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 . 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. 6 . The catalyst according to claim 5 , wherein the catalyst has a pore volume between 2 and 60 nm of at least 0.35 ml/g of catalyst. 7 . 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 copercipitated material; and treating the washed recovered copercipitated 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. %; a cobalt content, calculated as Co, of 0.25-4 wt. % based on the weight of the reduced catalyst. 8 . The process according to claim 7 , wherein said catalyst has a cobalt content, calculated as Co, of 0.25-1.5 wt. %, based on the weight of the reduced catalyst. 9 . The process according to claims 7 , wherein said catalyst has a pore volume between 2 and 60 nm of at least 0.35 ml/g of catalyst. 10 . (canceled) 11 . The process according to claim 3 , wherein said catalyst has a pore volume between 10 and 60 nm of at least 0.20 ml/g of catalyst. 12 . 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. 13 . The catalyst according to claim 6 , wherein the catalyst has a pore volume preferably between 10 and 60 nm of at least 0.20 ml/g of the catalyst. 14 . The process according claims 9 , wherein said catalyst has a pore volume between 10 and 60 nm of at least 0.20 ml/g of catalyst.

Assignees

Inventors

Classifications

  • Constitutive chemical elements of heterogeneous catalysts · CPC title

  • with gases containing free hydrogen · CPC title

  • Protection of catalysts, e.g. by coating · CPC title

  • Nickel · CPC title

  • Precipitation; Co-precipitation · CPC title

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What does patent US2016159941A1 cover?
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 catalys…
Who is the assignee on this patent?
Basf Corp
What technology area does this patent fall under?
Primary CPC classification C08F8/04. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Jun 09 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).