Hydroisomerization catalyst, process for producing the same, method of dewaxing hydrocarbon oil, and process for producing lube base oil
US-9518232-B2 · Dec 13, 2016 · US
US9243192B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9243192-B2 |
| Application number | US-201013138064-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 26, 2010 |
| Priority date | Mar 27, 2009 |
| Publication date | Jan 26, 2016 |
| Grant date | Jan 26, 2016 |
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A method for producing aromatic hydrocarbons by bringing a feedstock derived from a fraction containing a light cycle oil produced in a fluid catalytic cracking into contact with a catalyst containing a crystalline aluminosilicate, wherein the proportion of the naphthene content within the feedstock is adjusted so as to be greater than the proportion of the naphthene content in the fraction containing the light cycle oil, and the contact between the feedstock and the catalyst is performed under a pressure within a range from 0.1 MPaG to 1.0 MPaG.
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The invention claimed is: 1. A method for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number, comprising contacting a feedstock derived from a fraction comprising a light cycle oil produced in a fluid catalytic cracking unit with a catalyst comprising a crystalline aluminosilicate in the absence of molecular hydrogen, wherein the feedstock has a 10 volume % distillation temperature of at least 140° C., and a 90 volume % distillation temperature of not more than 360° C., a proportion of a saturated, multi-branched naphthene content in the feedstock is adjusted by mixing the fraction comprising the light cycle oil with a hydrotreated oil or by partially hydrogenating the fraction comprising the light cycle oil so that a proportion of the saturated, multi-branched naphthene content in the feedstock is greater than a proportion of a saturated, multi-branched naphthene content in the fraction comprising the light cycle oil, and the contacting the feedstock with the catalyst is performed under a pressure within a range from 0.1 MPaG to 1.0 MPaG, and a contact time between the feedstock and the catalyst during the contacting the feedstock with the catalyst is within a range from 5 seconds to 300 seconds, and wherein the proportion of the saturated, multi-branched naphthene content in the feedstock is at least 27% by mass. 2. The method for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number according to claim 1 , wherein the proportion of the saturated, multi-branched naphthene content in the feedstock is adjusted by mixing the fraction comprising the light cycle oil with a partially hydrogenated product of the fraction comprising the light cycle oil. 3. The method for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number according to claim 1 , wherein the saturated, multi-branched naphthene comprises mainly naphthene components of 8 or more carbon number. 4. The method for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number according to claim 1 , wherein the catalyst further comprises at least one metal selected from the group consisting of gallium and zinc. 5. The method for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number according to claim 1 , wherein a mass ratio of the naphthene content to a polycyclic aromatic hydrocarbon content in the feedstock is within a range from 0.1 to 5.0.
containing crystalline alumino-silicates, e.g. molecular sieves · CPC title
in the presence of hydrogen from a special source or of a special composition or having been purified by a special treatment · CPC title
containing crystalline alumino-silicates, e.g. molecular sieves {(C10G35/065 takes precedence)} · CPC title
Aromatisation of hydrocarbon oil fractions · CPC title
Aromatics · CPC title
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