Toluene methylation with transalkylation of heavy aromatics

US9783462B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9783462-B2
Application numberUS-201314022643-A
CountryUS
Kind codeB2
Filing dateSep 10, 2013
Priority dateSep 10, 2013
Publication dateOct 10, 2017
Grant dateOct 10, 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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  6. CPC / IPC classifications

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Abstract

Official abstract text for this publication.

A method of producing a purified mixed xylene comprising: introducing toluene and methanol to an alkylation reactor ( 32 ); reacting the toluene and the methanol in the alkylation reactor ( 32 ) to form a hydrocarbon stream ( 22 ) comprising a first mixed xylene, wherein the alkylation reactor ( 32 ) comprises an alkylation catalyst; separating the hydrocarbon stream ( 22 ) into a toluene stream ( 24 ) and a separated C 8+ stream ( 14 ); introducing the toluene stream ( 24 ) to a transalkylation reactor ( 38 ) with a transalkylation catalyst to produce a transalkylated stream ( 17 ) comprising a second mixed xylene; adding the transalkylated stream ( 17 ) to the hydrocarbon stream ( 22 ); and separating a C 8 product stream ( 19 ) comprising the purified mixed xylene from the separated C 8+ stream ( 14 ).

First claim

Opening claim text (preview).

We claim: 1. A method of producing a purified mixed xylene comprising: introducing a toluene stream ( 3 ) and methanol to an alkylation reactor ( 32 ), wherein the toluene stream comprises toluene and 1 wt % to 30 wt % of C 9= aromatics, based upon a total weight of the toluene stream; reacting the toluene and the methanol in the alkylation reactor ( 32 ) to form a hydrocarbon stream ( 22 ) comprising a first mixed xylene, wherein the alkylation reactor ( 32 ) comprises an alkylation catalyst that comprises a phosphorus containing, medium pore, pentasil zeolite having a silica/alumina ratio of greater than or equal to 200; separating the hydrocarbon stream ( 22 ) into a toluene stream ( 24 ) and a separated C 8+ stream ( 14 ); introducing the toluene stream ( 24 ) to a transalkylation reactor ( 38 ) with a transalkylation catalyst to produce a transalkylated stream ( 17 ) comprising a second mixed xylene; adding the transalkylated stream ( 17 ) to the hydrocarbon stream ( 22 ); and separating a C 8 product stream ( 19 ) comprising the purified mixed xylene from the separated C 8+ stream ( 14 ). 2. The method of claim 1 , wherein the phosphorus is present in an amount of 0.01 to 0.15 g per gram of zeolite. 3. The method of claim 1 , wherein the toluene stream ( 3 ) comprises 5 wt % to 30 wt % of C 9+ aromatics. 4. The method of claim 3 , wherein the toluene stream ( 3 ) comprises 10 wt % to 30 wt % of C 9+ aromatics. 5. The method of claim 1 , wherein greater than or equal to 0.05 g of C 9+ aromatics per gram of toluene converted is produced in the alkylation reactor ( 32 ). 6. The method of claim 1 , wherein the purified mixed xylene comprises greater than or equal to 85 wt % p-xylene based on the total amount of mixed xylene. 7. The method of claim 1 , wherein the reacting the toluene and the methanol is carried out under conditions such that a selectivity for para-xylene of greater than or equal to 80 mol % is achieved. 8. The method of claim 1 , wherein the reacting the toluene and the methanol is carried out under conditions such that a selectivity for para-xylene of less than or equal to 75 mol % is achieved. 9. The method of claim 1 , further comprising separating the C 8+ stream ( 14 ) in a xylene column ( 39 ) into the C 8 product stream ( 19 ) and a separated C 9+ stream ( 18 ). 10. The method of claim 9 , further comprising separating the separated C 9+ stream ( 18 ) in a C 9 separation column ( 40 ) into a C 9 stream ( 20 ) and a C 10+ stream ( 21 ); and introducing the C 9 stream ( 20 ) to the transalkylation reactor ( 38 ). 11. The method of claim 1 , further comprising introducing a C 9+ stream ( 16 ) to the transalkylation reactor ( 38 ).

Assignees

Inventors

Classifications

  • of only one hydrocarbon · CPC title

  • of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11 · CPC title

  • Xylenes · CPC title

  • C07C2/864Primary

    the non-hydrocarbon is an alcohol · CPC title

  • C07C2/66Primary

    Catalytic processes · CPC title

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What does patent US9783462B2 cover?
A method of producing a purified mixed xylene comprising: introducing toluene and methanol to an alkylation reactor ( 32 ); reacting the toluene and the methanol in the alkylation reactor ( 32 ) to form a hydrocarbon stream ( 22 ) comprising a first mixed xylene, wherein the alkylation reactor ( 32 ) comprises an alkylation catalyst; separating the hydrocarbon stream ( 22 ) into a toluene strea…
Who is the assignee on this patent?
Saudi Basic Ind Corp
What technology area does this patent fall under?
Primary CPC classification C07C2/864. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Oct 10 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).