Integration of n-c4/n-c4=/bd separation system for on-purpose butadiene synthesis
US-2015376091-A1 · Dec 31, 2015 · US
US8969645B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-8969645-B2 |
| Application number | US-201213715873-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 14, 2012 |
| Priority date | Dec 14, 2012 |
| Publication date | Mar 3, 2015 |
| Grant date | Mar 3, 2015 |
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.
We provide a process comprising: a. feeding a chlorinated-hydrocarbon and an ionic liquid catalyst to a treatment unit; b. operating the treatment unit at an elevated temperature to produce dechlorinated-hydrocarbon and HCl; and c. collecting the dechlorinated-hydrocarbon, wherein at least 90 wt % of the chlorides are removed. A second process comprises: a. creating an ionic liquid catalyst-rich zone in a distillation unit; b. passing chlorinated-hydrocarbon to the distillation unit; c. operating the unit under conditions causing removal of alkyl chloride to produce dechlorinated-hydrocarbon having a final boiling point close to a first final boiling point. A third process comprises: a. feeding alkylate gasoline blending component and ionic liquid catalyst to a treatment unit; b. operating the treatment unit; and c. collecting a dechlorinated-hydrocarbon, wherein at least 90 wt % of the chlorides have been removed and the dechlorinated-hydrocarbon has a second RON that is close to a first RON.
Opening claim text (preview).
What is claimed is: 1. A process for reducing chloride in a hydrocarbon, comprising: a. feeding a chlorinated-hydrocarbon, comprising greater than 50 up to 5,000 ppmw chlorides, and an ionic liquid catalyst comprising an anhydrous metal halide to a treatment unit; wherein an amount of the ionic liquid catalyst comprising the anhydrous metal halide in the treatment unit is from 20 ppmw to 2 wt %; b. operating the treatment unit under conditions including a temperature from 65.6°…
Chemistry & Metallurgy · mapped topic
Operations & Transport · mapped topic
Chemistry & Metallurgy · mapped topic
Operations & Transport · mapped topic
Operations & Transport · mapped topic
Related publications grouped by family.
Free tools are coming soon. Tell us what you want to track and we'll notify you.
Answers are generated from the same data shown on this page.