Upgrading sugar-alcohol derived gas oil in a gas oil hydrocracker
US-2015376514-A1 · Dec 31, 2015 · US
US9732287B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9732287-B2 |
| Application number | US-201414222829-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 24, 2014 |
| Priority date | Oct 1, 2008 |
| Publication date | Aug 15, 2017 |
| Grant date | Aug 15, 2017 |
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 to manufacture a base stock, comprising hydrocracking, separating, and dewaxing, wherein the base stock has a ratio of Noack volatility to CCS VIS at −25° C. multiplied by 100 from 0.15 to 0.40. We also provide a base stock made by a process, and a base oil manufacturing plant that produces the base stock.
Opening claim text (preview).
What is claimed is: 1. A process to manufacture a base stock, comprising: a. hydrocracking a heavy hydrocarbon feedstock in a hydrocracking zone, wherein the operating conditions in the hydrocracking zone are selected to convert vacuum gas oil to a product slate containing greater than 20 wt % of a waxy intermediate fraction; b. separating the waxy intermediate fraction into a lower boiling fraction and a higher boiling fraction; c. dewaxing the higher boiling fraction under conditions whereby the dewaxed higher boiling fraction has: i. a first boiling range from 730 to 1000° F. (388 to 538° C.), ii. a first VI from 105 to 120, iii. a first CCS VIS at −25° C. from 2500 to 4500 mPa·s, and iv. a ratio of a first Noack volatility to the first CCS VIS at −25° C. multiplied by 100 from 0.15 to 0.40; and d. dewaxing the lower boiling fraction under conditions whereby the dewaxed lower boiling fraction has: i. an additional boiling range from 700 to 925° F. (371 to 496° C.), ii. an additional VI from 105 to 115, iii. an additional Noack volatility less than 18 wt %, and iv. a ratio of the additional Noack volatility to an additional CC VIS at −25° C. multiplied by 100 from 0.80 to 1.55, and wherein the dewaxing is hydroisomerization dewaxing which is performed at a total pressure of between about 2000 to 3000 psig. 2. The process of claim 1 , wherein the higher boiling fraction is a bottoms fraction.
used as base material · CPC title
Distillation range · CPC title
Extraction of unsaturated hydrocarbons · CPC title
Specified values of viscosity or viscosity index · CPC title
Noack Volatility · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.