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US4599475A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for xylene isomerization using ZSM-23 zeolite

Assignee: Mobil Oil AS
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Filing: 1985-06-19
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Granted: 1986-07-08
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Expires: 2005-06-19
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Abstract

Abstract An improved process is disclosed for the isomerization of xylenes over a zeolite which may contain a platinum group metal. The improvement resides in the use of ZSM-23 zeolite which exhibits enhanced selectivity which inhibits the production of undesired C9+ aromatic transalkylation by-products. ZSM-23 having pores substantially unobstructed by silica, such as that made from a forming mixture containing amorphous precipitated silica as a silica source, has been found to be particularly useful in the process of the present invention.

Inventors

  • 👤 Charles T. Kresge
  • 👤 James C. Vartuli
  • 👤 Michael P. Nicoletti

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 08:37
CPC Classifications
C; C07; C07C; C07C5/00; C07C5/22; C07C5/27; C07C5/2702; C07C5/2708; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/70; B01J29/72; B01J29/74; C07C5/2724; B01J2229/00; B01J2229/10; B01J2229/20; B01J2229/26; B01J2229/30; B01J2229/42; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 72 words
A process for isomerizing an isomerization feed containing an aromatic C 8 mixture of ethylbenzene and xylene by which ethylbenzene and m-xylene conversion is enhanced, said process comprising contacting said feed under conversion conditions with a catalyst comprising ZSM-23 zeolite having a silica to alumina ratio of at least about 12, which zeolite is capable of sorbing greater than about 3 weight percent cyclohexane and greater than about 6.1 weight percent n-hexane.
Claim 2
Dependent Claim 72 words
A process for isomerizing an isomerization feed containing an aromatic C 8 mixture of ethylbenzene and xylene by which ethylbenzene and m-xylene conversion is enhanced, said process comprising contacting said feed under conversion conditions with a catalyst comprising ZSM-23 zeolite having a silica to alumina ratio of at least about 12, which zeolite is capable of sorbing greater than about 3 weight percent cyclohexane and greater than about 6.1 weight percent n-hexane.
Claim 3
Dependent Claim 85 words
A process for isomerizing an isomerization feed containing an aromatic C 8 mixture of ethylbenzene and xylene by which ethylbenzene and m-xylene conversion is enhanced, said process comprising contacting said feed, under conversion conditions with a catalyst comprising ZSM-23 zeolite having a silica to alumina ratio of at least about 12, capable of sorbing greater than about 3 weight percent cyclohexane and greater than about 6.1 weight percent n-hexane, which zeolite is prepared from a forming mixture containing amorphous precipitated silica as a silica source.
Claim 4
Dependent Claim 85 words
A process for isomerizing an isomerization feed containing an aromatic C 8 mixture of ethylbenzene and xylene by which ethylbenzene and m-xylene conversion is enhanced, said process comprising contacting said feed, under conversion conditions with a catalyst comprising ZSM-23 zeolite having a silica to alumina ratio of at least about 12, capable of sorbing greater than about 3 weight percent cyclohexane and greater than about 6.1 weight percent n-hexane, which zeolite is prepared from a forming mixture containing amorphous precipitated silica as a silica source.
Claim 5
Dependent Claim 13 words
The process of claim 2 wherein said zeolite contains a Group VIII metal.
Claim 6
Dependent Claim 12 words
The process of claim 3 wherein said Group VIII metal is platinum.
Claim 7
Dependent Claim 24 words
The process of claim 2 wherein said zeolite is capable of sorbing greater than about 3.5 weight percent cyclohexane and 6.5 weight percent n-hexane.
Claim 8
Dependent Claim 43 words
The process of claim 2 wherein said conversion conditions include a temperature of from about 260° C. to about 538° C., a pressure of about 0 to about 1500 psig and a weight hourly space velocity of between about 0.5 and about 100.
Claim 9
Dependent Claim 17 words
The process of claim 2 wherein said aromatic C 8 mixture contains ethylbenzene, para-xylene, meta-xylene, and ortho-xylene.
Claim 10
Dependent Claim 15 words
The process of claim 2 wherein said zeolite is ZSM-23 predominately in the hydrogen form.
Claim 11
Dependent Claim 36 words
The process of claim 1 wherein said zeolite can sorb n-hexane and cyclohexane at a sorption ratio greater than about 1.5 weight percent n-hexane sorbed/weight percent cyclohexane sorbed at 40 mm partial pressure and room temperature.
Claim 12
Dependent Claim 14 words
The process of claim 9 wherein said sorption ratio is greater than about 2.
Claim 13
Dependent Claim 16 words
The process of claim 9 wherein said sorption ratio ranges between about 2 and about 4.
Claim 14
Dependent Claim 36 words
The process of claim 2 wherein said zeolite can sorb n-hexane and cyclohexane in a sorption ratio greater than about 1.5 weight percent n-hexane sorbed/weight percent cyclohexane sorbed at 40 mm partial pressure and room temperature.
Claim 15
Dependent Claim 14 words
The process of claim 12 wherein said sorption ratio is greater than about 2.
Claim 16
Dependent Claim 16 words
The process of claim 12 wherein said sorption ratio ranges between about 2 and about 4.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-07-07 1990-01-06 1990-07-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-07-07 1994-01-06 1994-07-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-07-07 1998-01-06 1998-07-08 $7700.00 Window Closed / Lapsed

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