US4101597A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Recovery of p-xylene and benzene from eight carbon atom aromatic fractions
Assignee: Mobil Oil AS
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Filing: 1977-06-23
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Granted: 1978-07-18
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Expires: 1997-06-23
Abstract
Abstract Recovery of valuable components from eight carbon atom (C8) aromatic fractions is enhanced by high temperature processing of C9+ aromatics produced by side reactions during isomerization of a C8 aromatics fraction lean in p-xylene and resulting from separation of that isomer from a mixture of the three xylene isomers and ethyl benzene.
Inventors
- 👤 Lloyd L. Breckenridge
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 21:08
CPC Classifications
C; C07; C07C; C07C15/00; C07C15/02; C07C15/067; C07C15/08; C07C5/00; C07C5/22; C07C5/27; C07C5/2702; C07C5/2724; C07C7/00; C07C7/005; Y; Y10; Y10S; Y10S585/00; Y10S585/8995; Y10S585/905
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
209 words
In a process for recovery of p-xylene from a fresh feed of eight carbon atom alkyl aromatic compounds including ethyl benzene and the three xylene isomers by separating p-xylene from a mixture of said fresh feed with xylene recycle as hereinafter defined, subjecting the mixture depleted of p-xylene to isomerization by contact with hydrogen in the presence of a catalyst consisting essentially of a metal having hydrogenation/dehydrogenation catalyst properties and a crystalline aluminosilicate zeolite having a silica/alumina ratio of at least 12 and a constraint index of about 1 to about 12, separating hydrogen from the isomerate so produced, recycling separated hydrogen to the feed to the isomerization step, separating C 9 + and C 7 - hydrocarbons from the hydrogen free isomerate and adding the remaining C 8 hydrocarbons to said fresh feed as said xylene recycle; the improvement which comprises conducting said isomerization at a temperature of about 550° to 700° F., admixing the separated C 9 + hydrocarbons with hydrogen, contacting the hydrogen/C 9 + mixture with a porous acidic solid catalyst at a temperature of about 750° to 900° F., blending the product of such contacting with said isomerate, and recycling a portion of said separated hydrogen to admixture with said C 9 + hydrocarbons.
Claim 2
Dependent Claim
209 words
In a process for recovery of p-xylene from a fresh feed of eight carbon atom alkyl aromatic compounds including ethyl benzene and the three xylene isomers by separating p-xylene from a mixture of said fresh feed with xylene recycle as hereinafter defined, subjecting the mixture depleted of p-xylene to isomerization by contact with hydrogen in the presence of a catalyst consisting essentially of a metal having hydrogenation/dehydrogenation catalyst properties and a crystalline aluminosilicate zeolite having a silica/alumina ratio of at least 12 and a constraint index of about 1 to about 12, separating hydrogen from the isomerate so produced, recycling separated hydrogen to the feed to the isomerization step, separating C 9 + and C 7 - hydrocarbons from the hydrogen free isomerate and adding the remaining C 8 hydrocarbons to said fresh feed as said xylene recycle; the improvement which comprises conducting said isomerization at a temperature of about 550° to 700° F., admixing the separated C 9 + hydrocarbons with hydrogen, contacting the hydrogen/C 9 + mixture with a porous acidic solid catalyst at a temperature of about 750° to 900° F., blending the product of such contacting with said isomerate, and recycling a portion of said separated hydrogen to admixture with said C 9 + hydrocarbons.
Claim 3
Dependent Claim
31 words
The process of claim 1 wherein toluene is separated from said C 7 - hydrocarbons and added to said C 9 + hydrocarbons for contact with said porous acidic solid catalyst.
Claim 4
Dependent Claim
34 words
The process of claim 1 wherein said porous acidic solid catalyst is a crystalline aluminosilicate zeolite having a silica/alumina ratio of at least 12 and a constraint index of about 1 to about 12.
Claim 5
Dependent Claim
10 words
The process of claim 1 wherein said zeolite is ZSM-5.
Claim 6
Dependent Claim
13 words
The process of claim 3 wherein said porous acidic solid catalyst is ZSM-5.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-07-17 | 1982-01-16 | 1982-07-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-07-17 | 1986-01-16 | 1986-07-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-07-17 | 1990-01-16 | 1990-07-18 | $7700.00 | Window Closed / Lapsed |