Process for the Production of Xylenes
US-2015376086-A1 · Dec 31, 2015 · US
US9783462B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9783462-B2 |
| Application number | US-201314022643-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 10, 2013 |
| Priority date | Sep 10, 2013 |
| Publication date | Oct 10, 2017 |
| Grant date | Oct 10, 2017 |
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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 ).
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 ).
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