Hydrocarbon Fluids
US-2024010939-A1 · Jan 11, 2024 · US
US9677012B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9677012-B2 |
| Application number | US-201314388548-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 29, 2013 |
| Priority date | Mar 30, 2012 |
| Publication date | Jun 13, 2017 |
| Grant date | Jun 13, 2017 |
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A method for producing a lubricant base oil that has a predetermined boiling point range, the method including a first step of bringing a feedstock containing a first hydrocarbon oil having a boiling point in the above boiling point range and a second hydrocarbon oil having a lower boiling point than the boiling point range into contact with a hydroisomerization catalyst, wherein the catalyst contains a support that includes a zeolite having a one-dimensional porous structure including a 10-membered ring and a binder, and platinum and/or palladium supported on the support.
Opening claim text (preview).
The invention claimed is: 1. A method for producing a lubricant base oil that has a predetermined boiling point range, the method comprising: a first step of, in the presence of hydrogen, bringing a feedstock containing a first hydrocarbon oil having a boiling point in the predetermined boiling point range and a second hydrocarbon oil having a lower boiling point than the predetermined boiling point range into contact with a hydroisomerization catalyst, wherein the catalyst contains a support that includes a zeolite having a one-dimensional porous structure including a 10-membered ring and a binder, and platinum and/or palladium supported on the support, a carbon content of the catalyst is 0.4 to 3.5% by mass, a micropore volume per unit mass of the catalyst is 0.02 to 0.12 cc/g, the zeolite is derived from an ion-exchanged zeolite obtained by ion-exchanging an organic template-containing zeolite that contains an organic template and has a one-dimensional porous structure including a 10-membered ring in a solution containing ammonium ions and/or protons, and a micropore volume per unit mass of the zeolite contained in the catalyst is 0.01 to 0.12 cc/g. 2. The method according to claim 1 , wherein a content of the first hydrocarbon oil in the feedstock is 5 to 60% by volume based on a total amount of feedstock. 3. The method according to claim 1 , wherein the first hydrocarbon oil has a boiling point of at least 520° C. and the second hydrocarbon oil has a boiling point range of 330° C. to less than 520° C. 4. The method according to claim 1 , wherein the first hydrocarbon oil has a boing point range of 470° C. to less than 520° C. and the second hydrocarbon oil has a boiling point range of 330° C. to less than 470° C. 5. The method according to claim 1 , further comprising a second step of obtaining a hydrorefined oil by hydrorefining a dewaxed oil obtained in the first step, and a third step of fractionating a base oil fraction having the boiling point range from the hydrorefined oil.
Specific manufacturing methods for lubricant compositions · CPC title
Noble metals · CPC title
Treatment by methods not otherwise provided for of hydrocarbon oils or fatty oils for lubricating purposes · CPC title
to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins (C10G32/00 takes precedence; improving or increasing the octane number or aromatic content of naphtha C10G35/00) · CPC title
Addition of matrix or binder particles · CPC title
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