Method for producing base oil for lubricant oils
US-9988585-B2 · Jun 5, 2018 · US
US11225616B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11225616-B2 |
| Application number | US-202016920900-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 6, 2020 |
| Priority date | Sep 20, 2019 |
| Publication date | Jan 18, 2022 |
| Grant date | Jan 18, 2022 |
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.
Disclosed is a method of producing a lubricating base oil, including providing a feedstock including a diesel fraction, subjecting the feedstock to catalytic dewaxing, and recovering a lubricating base oil from a product of the catalytic dewaxing. A lubricating base oil produced thereby and a lubricant product including the lubricating base oil are also provided.
Opening claim text (preview).
What is claimed is: 1. A method of producing a lubricating base oil, comprising: providing a feedstock comprising a diesel fraction; subjecting the feedstock to catalytic dewaxing; and recovering a lubricating base oil from a product of the catalytic dewaxing, wherein the feedstock has a specific gravity of 0.81 to 0.87, a kinematic viscosity at 40° C. of 5.0 cSt or less, a kinematic viscosity at 100° C. of 2.0 cSt or less, and a pour point of 5° C. or less, and contains 2.0 wt % or less of each of sulfur and nitrogen. 2. The method of claim 1 , wherein the feedstock has a 10% outflow temperature of 250° C. or less and a 50% outflow temperature of 350° C. or less in a simulated distillation test according to ASTM D2887. 3. The method of claim 1 , wherein an average carbon number of a hydrocarbon molecule in the feedstock is 10 to 25. 4. The method of claim 1 , wherein the feedstock comprises 90 wt % or more of the diesel fraction. 5. The method of claim 1 , wherein the feedstock further comprises a fuel oil fraction that is lighter than the diesel fraction. 6. The method of claim 5 , wherein the fuel oil fraction that is lighter than the diesel fraction is a kerosene fraction. 7. The method of claim 1 , wherein the feedstock comprises unconverted oil in an amount less than 5 wt %. 8. The method of claim 1 , wherein the catalytic dewaxing is performed at a reaction temperature of 250 to 410° C., a reaction pressure of 30 to 200 kg/cm 2 , a liquid hourly space velocity (LHSV) of 0.1 to 3.0 hr −1 , and a hydrogen-to-feedstock volume ratio of 150 to 1000 Nm 3 /m 3 . 9. A lubricating base oil produced by the method of claim 1 , wherein the lubricating base oil has a kinematic viscosity at 40° C. of 9.0 cSt or less, a kinematic viscosity at 100° C. of 2.5 cSt or less, and a pour point of −50° C. or less.
used as base material · CPC title
containing crystalline alumino-silicates, e.g. molecular sieves · CPC title
Resistance to extreme temperature · CPC title
including cracking steps and other hydrotreatment steps · CPC title
Specified values of viscosity or viscosity index · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.