Method for producing hydrogenated conjugated diene polymer
US-2015368387-A1 · Dec 24, 2015 · US
US2016159941A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016159941-A1 |
| Application number | US-201414904793-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 17, 2014 |
| Priority date | Jul 17, 2013 |
| Publication date | Jun 9, 2016 |
| Grant date | — |
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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.
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.
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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