A process for conversion of hydrocarbons
US-2019211277-A1 · Jul 11, 2019 · US
US9328299B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9328299-B2 |
| Application number | US-201414271399-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 6, 2014 |
| Priority date | Jun 4, 2013 |
| Publication date | May 3, 2016 |
| Grant date | May 3, 2016 |
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 increasing the yields of light olefins and the yields of aromatics from a hydrocarbon stream is presented. The process includes a first separation to direct the light components that are not reformable to a cracking unit, with the remainder passed to a second separation unit. The second separation unit extracts normal components from the hydrocarbon stream to pass to the cracking unit. The resulting hydrocarbon stream with reduced light ends and reduced normals is passed to a reforming unit.
Opening claim text (preview).
The invention claimed is: 1. A process for producing light olefins, comprising: passing a straight run naphtha stream to a first separation column to generate a first light stream comprising methylcyclopentane, and C 5− hydrocarbons and a first heavy stream comprising cyclohexane, and C7+ heavier hydrocarbons; passing the first heavy stream to a hydrotreating unit to remove sulfur and other catalyst poisonous impurities to generate a treated heavy stream; passing the treated heavy stream to a second separation unit to generate an extract stream comprising heavier normal paraffins and a raffinate stream comprising cyclohexane and non-normal hydrocarbons; passing the extract stream, the first light stream to a cracking unit to generate light olefins; and passing the raffinate stream and a cracker heavy stream from a heavy cracking unit to a catalytic reforming unit to produce a product with an increased amount of aromatics. 2. The process of claim 1 wherein the cracking unit is a catalytic cracking unit. 3. The process of claim 1 wherein the cracking unit is a steam cracking unit. 4. The process of claim 1 wherein the second separation unit is an adsorption separation unit.
Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one other conversion process (C10G67/00 takes precedence) · CPC title
including a sorption process as the refining step in the absence of hydrogen · CPC title
Treatment of hydrocarbon oils by at least one hydrotreatment process and at least one process for refining in the absence of hydrogen only · CPC title
processes also including other conversion steps · CPC title
only thermal cracking steps · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.