Olefin Production Process
US-2016347688-A1 · Dec 1, 2016 · US
US2016244385A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016244385-A1 |
| Application number | US-201615143887-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 2, 2016 |
| Priority date | Feb 6, 2013 |
| Publication date | Aug 25, 2016 |
| Grant date | — |
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 feedstream comprising paraxylene and styrene is contacted, in the presence of hydrogen, with a catalyst comprising at least one metal, selected from one or more metals selected from Groups 8-10.
Opening claim text (preview).
1 .- 11 . (canceled) 12 . A process comprising: (i) contacting an aromatic hydrocarbon feedstream comprising benzene and/or toluene with methanol and/or dimethyl ether in the presence of a phosphorus-modified ZSM-5 alkylation catalyst, which has been steamed at a temperature of at least 950° C., to obtain a first product stream comprising greater than about 24 wt % para-xylene and styrene; and (ii) contacting said first product stream comprising greater than about 24 wt % para-xylene and styrene with a hydrogenation catalyst comprising at least one metal selected from Groups 8-10 of the Periodic Table, in the presence of hydrogen, to obtain a second product stream comprising a reduced amount of styrene when compared with said first product stream, wherein less than 0.2 wt % of paraxylene is isomerized by contact with the hydrogenation catalyst. 13 . The process of claim 12 , wherein said second product stream is further characterized as having no detectable levels of styrene, ethylcyclohexane and dimethylcyclohexane, as measured by gas chromatography. 14 . The process of claim 12 , wherein said hydrogenation catalyst further comprises a support selected from Al 2 O 3 , carbon, SiO 2 , TiO 2 , and mixtures thereof. 15 . The process of claim 12 , wherein said metal is selected from Pd, Co, Ni, Ru, and mixtures thereof. 16 . The process of claim 12 , wherein said hydrogenation catalyst further comprises at least one metal or metal compound selected from Ag, Au, In, alkali metals, and alkaline earth metals. 17 . The process of claim 12 , wherein said second product stream contains an increased amount of ethylbenzene relative to said feedstream. 18 . The process of claim 17 , wherein said increased amount of ethylbenzene is equal to the amount of styrene in said first product stream as measured by gas chromatography. 19 . The process of claim 12 , wherein the amount of paraxylene in the first product stream comprises at least 70 wt % based on the total xylene concentration. 20 . The process of claim 12 , wherein the amount of styrene in the first product stream comprises about 0.01 wt % to 2.00 wt %.
by hydrogenation · CPC title
Palladium · CPC title
of non-aromatic carbon-to-carbon double bonds · CPC title
Alumina · CPC title
the non-hydrocarbon is an ether · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.