Process for the production of a gasoline with a low sulfur content
US-9222036-B2 · Dec 29, 2015 · US
US9376353B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9376353-B2 |
| Application number | US-201214355391-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 31, 2012 |
| Priority date | Nov 1, 2011 |
| Publication date | Jun 28, 2016 |
| Grant date | Jun 28, 2016 |
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This invention relates to a method of producing aromatic hydrocarbons and olefin from hydrocarbonaceous oils including large amounts of polycyclic aromatic compounds having two or more rings via partial hydrogenation in the presence of a hydrogenation catalyst and catalytic cracking in the presence of a catalytic cracking catalyst.
Opening claim text (preview).
The invention claimed is: 1. A method of producing an aromatic hydrocarbon and an olefin, comprising: (a) subjecting an oil including a large amount of a polycyclic aromatic compound having two or more rings to partial hydrogenation under reaction conditions of 310˜360° C., 50˜70 atm, and LHSV (Liquid Hourly Space Velocity) of 0.7˜1.0 hr −1 using a hydrogenation catalyst, to obtaining a partially hydrogenated component with one aromatic ring; (b) subjecting the partially hydrogenated component obtained in (a) to catalytic cracking using a catalytic cracking catalyst, to obtain a catalytically cracked component, wherein the catalytic cracking catalyst is provided in the form of a combination of a zeolite molecular sieve having a large pore size of 6.5Å or more and a zeolite molecular sieve having a medium pore size of 5˜6.5Å, and the weight ratio of the zeolite molecular sieve having a large pore size to the zeolite molecular sieve having a medium pore size is 5/95˜95/5; and (c) separating the catalytic cracked component obtained in (b) into (i) benzene, toluene, xylene and a C9+ aromatic hydrocarbon, (ii) an olefin component, and (iii) a residual oil. 2. The method of claim 1 , wherein (a) is performed under reaction conditions of 340˜360° C., 55˜65 atm, and LHSV of 0.7˜1.0 hr −1 . 3. The method of claim 1 , further comprising (d) recycling the (iii) residual oil separated in (c) back to (a).
Catalytic processes {(C07C4/025 takes precedence)} · CPC title
including at least one step of catalytic cracking in the absence of hydrogen · CPC title
C2-C4 olefins · CPC title
Aromatics · CPC title
Aromatics or polyaromatics · CPC title
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