US2022315847A1PendingUtilityA1
System and method for producing un-hydrogenated and hydrogenated c9+ compounds
Assignee: SABIC GLOBAL TECHNOLOGIES BVPriority: Jul 15, 2019Filed: Jul 13, 2020Published: Oct 6, 2022
Est. expiryJul 15, 2039(~13 yrs left)· nominal 20-yr term from priority
C10G 69/06C10G 2300/4006C10G 45/44C10G 9/36C10G 45/52C10G 2300/4018C10G 7/00C10G 2300/4012C10G 2400/30C10G 2300/1044C10G 45/48C10G 2400/26
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Claims
Abstract
A system and method for processing pyrolysis gasoline is disclosed. The system and method involves separating a pyrolysis gasoline stream to produce a first stream comprising primarily un-hydrogenated C9+ compounds. The separating of the pyrolysis e gasoline occurs without hydrogenation being carried out on the pyrolysis gasoline before the separating.
Claims
exact text as granted — not AI-modified1 . A method of processing pyrolysis gasoline, the method comprising:
separating a pyrolysis gasoline stream to produce a first stream comprising primarily un-hydrogenated C 9+ compounds.
2 . The method of claim 1 wherein the first stream comprises 98 to 100 wt. % C 9+ compounds.
3 . The method of claim 1 further comprising:
hydrogenating a portion of the first stream to produce a second stream comprising hydrogenated C 9+ hydrogenated compounds.
4 . The method of claim 3 , wherein the hydrogenating of the first portion of the first stream is carried out under reaction conditions comprising a temperature in a range of 100° C. to 200° C., a pressure in a range of 10 bar to 30 bar, a WHSV of 2 h −1 to 8 h −1 , and in the presence of a catalyst comprising Ni/Al 2 O 3 to Pd/Al 2 O 3 .
5 . The method of claim 3 further comprising:
separating the second stream to produce a third stream comprising hydrogenated wash oil and a fourth stream comprising hydrogenated C 9+ residue.
6 . The method of claim 5 wherein third stream comprises 0 to 90 wt. % wash oil and the fourth stream comprises 10 to 100 wt. % hydrogenated C 9+ compounds.
7 . The method of claim 5 , further comprising:
subjecting the third stream to reaction conditions to hydrogenate the third stream.
8 . The method of claim 1 , wherein the separating of the pyrolysis gasoline stream comprises:
distilling the pyrolysis gas stream in a depentanizer column to produce a fifth stream comprising primarily C 4+ compounds and a sixth stream comprising primarily C 6+ compounds.
9 . The method of claim 8 wherein the separating of the pyrolysis gasoline stream further comprises:
distilling the sixth stream in a deoctanizer column to produce a seventh stream comprising primarily C 6 to C 8 compounds and the first stream.
10 . The method of claim 9 comprising:
hydrogenating the seventh stream to produce an eighth stream comprising benzene, toluene, and xylene.
11 . The method of claim 10 , wherein the hydrogenating of the seventh stream is carried out under reaction conditions comprising a temperature in a range of 100° C. to 200° C., a pressure in a range of 10 bar to 30 bar, a WHSV of 2 h −1 to 8 h −1 , and in presence of a catalyst comprising Ni/Al 2 O 3 to Pd/Al 2 O 3 .
12 . The method of claim 8 further comprising:
processing the fifth stream in a stabilizer to produce a ninth stream comprising fuel gas and a tenth stream comprising primarily C 4 and C 5 compounds.
13 . The method of claim 12 further comprising:
hydrogenating the tenth stream to produce an eleventh stream comprising primarily C 4 and C 5 compounds.
14 . The method of claim 13 , wherein the hydrogenating of the tenth stream is carried out under reaction conditions comprising a temperature in a range of 40° C. to 140° C., a pressure in a range of 20 bar to 40 bar, a WHSV of 10 h −1 to 16 h −1 , and in presence of a catalyst comprising Ni/Al 2 O 3 to Pd/Al 2 O 3 .
15 . The method of claim 13 further comprising subjecting the eleventh stream to cracking conditions to form C 2 to C 4 light olefins, LPG, and H 2 .
16 . A method of processing pyrolysis gasoline, the method comprising:
concurrently producing (1) a first stream comprising primarily un-hydrogenated C 9+ compounds and (2) a second stream comprising hydrogenated C 9+ hydrogenated compounds, wherein the producing comprises separating a pyrolysis gasoline stream to produce the first stream comprising primarily un-hydrogenated C 9+ compounds and hydrogenating a portion of the first stream to produce the second stream comprising hydrogenated C 9+ hydrogenated compounds.
17 . The method of claim 16 further comprising:
producing a stream comprising primarily un-hydrogenated C 4+ compounds.
18 . A method of processing pyrolysis gasoline, the method comprising:
separating a pyrolysis gasoline stream to produce a first stream comprising primarily un-hydrogenated C 9+ compounds; hydrogenating a portion of the first stream to produce a second stream comprising hydrogenated C 9+ compounds; separating the second stream to produce a third stream comprising hydrogenated wash oil and a fourth stream comprising hydrogenated C 9+ residue, wherein the separating of the pyrolysis gasoline stream comprises:
distilling the pyrolysis gas stream in a depentanizer column to produce a fifth stream comprising primarily C 4+ compounds and a sixth stream comprising primarily C 6+ compounds;
distilling the sixth stream in a deoctanizer column to produce a seventh stream comprising primarily C 6 to C 8 compounds and the first stream;
processing the fifth stream in a stabilizer to produce a ninth stream comprising fuel gas and a tenth stream comprising primarily C 4 and C 5 compounds; and combining the third stream, the seventh stream, and the tenth stream to form a combined stream and flowing the combined stream to a reactor.
19 . The method of claim 18 , further comprising:
subjecting the combined stream to reaction conditions sufficient to form a reactor effluent.
20 . The method of claim 19 further comprising:
processing the reactor effluent to produce a BTX stream, a stream comprising primarily hydrogenated wash oil, a fuel gas stream and a stream comprising primarily C 5 compounds.Join the waitlist — get patent alerts
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