Oligomerization of Alpha Olefins Using Metallocene-SSA Catalyst Systems and Use of the Resultant Polyalphaolefins to Prepare Lubricant Blends
US-2016264493-A1 · Sep 15, 2016 · US
US10549269B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10549269-B2 |
| Application number | US-201715494176-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 21, 2017 |
| Priority date | Oct 31, 2014 |
| Publication date | Feb 4, 2020 |
| Grant date | Feb 4, 2020 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A process for the manufacture of a catalyst comprising a fluorinated metal oxide is provided. A catalyst comprising a fluorinated metal oxide is provided. A catalytic hydrogenation process is also provided.
Opening claim text (preview).
The invention claimed is: 1. A hydrogenation catalyst comprising a fluorinated metal oxide, wherein an atomic percentage of fluorine (F) contained in the fluorinated metal oxide is equal to or greater than 3 atom %, and wherein the fluorinated metal oxide is a fluorinated ternary metal oxide consisting essentially of Cu, Zn, Zr, O, and F. 2. The hydrogenation catalyst according to claim 1 , wherein the fluorinated ternary metal oxide has a BET (Brunner-Emmet-Teller) value from 30 to 150 m 2 /g. 3. The hydrogenation catalyst according to claim 2 , wherein the BET (Brunner-Emmet-Teller) value is at least about 40 m 2 /g and equal to or less than 130 m 2 /g. 4. The hydrogenation catalyst according to claim 1 , wherein the atomic percentage is in a range from 6 atom % to 14 atom %. 5. The hydrogenation catalyst according to claim 1 , wherein the fluorinated ternary metal oxide comprises a metal oxide system selected from the group consisting of: Cu/ZnO/ZrO 2 and CuO/ZnO/ZrO 2 . 6. The hydrogenation catalyst according to claim 5 , wherein the metal oxide system is CuO/ZnO/ZrO 2 . 7. The hydrogenation catalyst according to claim 1 further comprising a layer of ionic liquid. 8. A hydrogenation catalyst comprising a fluorinated metal oxide, wherein an atomic percentage of fluorine contained in the fluorinated metal oxide is equal to or greater than 3 atom %, and further comprising a layer of ionic liquid.
using catalysts, e.g. selective catalysts · CPC title
characterised by the catalyst used · CPC title
with alkaline earth metals, magnesium, beryllium, zinc, cadmium or mercury · CPC title
containing copper, silver, gold, or compounds thereof · CPC title
Fluorides · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.