Catalyst for producing monocyclic aromatic hydrocarbons, and method for producing monocyclic aromatic hydrocarbons

US9809507B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9809507-B2
Application numberUS-201414467707-A
CountryUS
Kind codeB2
Filing dateAug 25, 2014
Priority dateJun 30, 2009
Publication dateNov 7, 2017
Grant dateNov 7, 2017

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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Abstract

Official abstract text for this publication.

A catalyst for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., wherein the catalyst contains a crystalline aluminosilicate, gallium and/or zinc, and phosphorus, and the amount of phosphorus supported on the crystalline aluminosilicate is within a range from 0.1 to 1.9% by mass based on the mass of the crystalline aluminosilicate; and a method for producing monocyclic aromatic hydrocarbons, the method involving bringing a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., into contact with the above-mentioned catalyst for producing monocyclic aromatic hydrocarbons.

First claim

Opening claim text (preview).

The invention claimed is: 1. A method for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number, the method comprising bringing a feedstock oil containing polycyclic aromatic hydrocarbons and having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil containing polycyclic aromatic hydrocarbons and having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., into contact with a catalyst comprising a medium pore size zeolite, gallium and/or zinc, and phosphorus, wherein the amount of phosphorus supported on the medium pore size zeolite is within a range from 0.1 to 1.9% by mass based on the mass of the medium pore size zeolite. 2. The method according to claim 1 , wherein a cracked gas oil produced in a fluid catalytic cracking is used as the feedstock oil. 3. The method according to claim 1 , wherein the feedstock oil is brought into contact with the catalyst in a fluidized bed reactor. 4. The method according to claim 1 , wherein the medium pore size zeolite is a pentasil-type zeolite. 5. The method according to claim 1 , wherein the medium pore size zeolite is an MFI-type zeolite. 6. A method for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number, the method comprising bringing a feedstock oil containing polycyclic aromatic hydrocarbons and having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil containing polycyclic aromatic hydrocarbons and having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., into contact with a catalyst comprising a medium pore size zeolite, gallium and/or zinc, and phosphorus, wherein the amount of phosphorus is within a range from 0.1 to 5.0% by mass based on the mass of the catalyst. 7. The method according to claim 6 , wherein a cracked gas oil produced in a fluid catalytic cracking is used as the feedstock oil. 8. The method according to claim 6 , wherein the feedstock oil is brought into contact with the catalyst in a fluidized bed reactor. 9. The method according to claim 6 , wherein the medium pore size zeolite is a pentasil-type zeolite. 10. The method according to claim 6 , wherein the medium pore size zeolite is an MFI-type zeolite.

Assignees

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Classifications

  • Aromatics · CPC title

  • Kerosene having a boiling range of about 180 - 230 °C · CPC title

  • Diesel having a boiling range of about 230 - 330 °C · CPC title

  • Oil well production fluids · CPC title

  • Aromatisation of hydrocarbon oil fractions · CPC title

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What does patent US9809507B2 cover?
A catalyst for producing monocyclic aromatic hydrocarbons of 6 to 8 carbon number from a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and an end point temperature of not more than 400° C., or a feedstock oil having a 10 volume % distillation temperature of at least 140° C. and a 90 volume % distillation temperature of not more than 360° C., wherein the catalys…
Who is the assignee on this patent?
Jx Nippon Oil & Energy Corp
What technology area does this patent fall under?
Primary CPC classification B01J29/405. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Nov 07 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).