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US4304657A Expired / Lapsed US ⏱️ 0.0 years remaining

Aromatization process

Assignee: Chevron USA Inc
•
Filing: 1980-07-03
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Granted: 1981-12-08
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Expires: 2000-07-03
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Abstract

Abstract An improved aromatization process is disclosed for upgrading the octane of an aliphatic feedstream, increasing the hydrogen to methane mol ratio of the product and decreasing the C 10 + aromatics production. In the process the feed is diluted with CO, CO 2 or N 2 at a mol ratio in the range of 1:1 to 1:20 of feed to diluent, and passed over a ZSM-5-type of aluminosilicate zeolite catalyst.

Inventors

  • 👤 Stephen J. Miller

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 17:48
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/095

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 107 words
A process for converting a feedstock selected from the group consisting of light straight run naphthas, coker gasolines, FCC gasolines, and pyrolysis gasolines to a product stream comprising aromatic hydrocarbons, hydrogen and methane comprising contacting said feedstock with an aromatization catalyst comprising a zinc HZSM-5 catalyst at a temperature in the range of 340° C. to 815° C. and a pressure in the range from 1 atmosphere to 35 atmospheres in the presence of a diluent essentially free of molecular oxygen, said diluent selected from the group consisting of CO 2 and N 2 at a mol ratio of feedstock to diluent ranging from 1:1 to 1:20.
Claim 2
Dependent Claim 107 words
A process for converting a feedstock selected from the group consisting of light straight run naphthas, coker gasolines, FCC gasolines, and pyrolysis gasolines to a product stream comprising aromatic hydrocarbons, hydrogen and methane comprising contacting said feedstock with an aromatization catalyst comprising a zinc HZSM-5 catalyst at a temperature in the range of 340° C. to 815° C. and a pressure in the range from 1 atmosphere to 35 atmospheres in the presence of a diluent essentially free of molecular oxygen, said diluent selected from the group consisting of CO 2 and N 2 at a mol ratio of feedstock to diluent ranging from 1:1 to 1:20.
Claim 3
Dependent Claim 20 words
A process as recited in claim 1 wherein said mol ratio of feedstock to diluent ranges from 1:5 to 1:10.
Claim 4
Dependent Claim 18 words
A process as recited in claim 1 wherein said mol ratio of feedstock to diluent is approximately 1:6.
Claim 5
Dependent Claim 20 words
A process as recited in claim 1 wherein said temperature is in the range from 480° C. to 540° C.
Claim 6
Dependent Claim 19 words
A process as recited in claim 1 wherein said process is conducted at a pressure of approximately one atmosphere.
Claim 7
Dependent Claim 71 words
A process for converting an aliphatic feedstock to a product stream comprising aromatic hydrocarbons, hydrogen, and methane comprising contacting said feedstock with an aromatization catalyst at a temperature in the range of 340° C. to 815° C. and a pressure in the range from 1 atmosphere to 35 atmospheres, in the presence of a diluent comprising CO 2 at a mol ratio of feedstock to diluent ranging from 1:1 to 1:20.
Claim 8
Dependent Claim 71 words
A process for converting an aliphatic feedstock to a product stream comprising aromatic hydrocarbons, hydrogen, and methane comprising contacting said feedstock with an aromatization catalyst at a temperature in the range of 340° C. to 815° C. and a pressure in the range from 1 atmosphere to 35 atmospheres, in the presence of a diluent comprising CO 2 at a mol ratio of feedstock to diluent ranging from 1:1 to 1:20.
Claim 9
Dependent Claim 16 words
A process as recited in claim 6 wherein said aromatization catalyst comprises a zinc HZSM-5 catalyst.
Claim 10
Dependent Claim 16 words
A process as recited in claim 6, wherein the diluent consists essentially of CO 2 .
Claim 11
Dependent Claim 14 words
A process as recited in claim 1, wherein the diluent is CO 2 .

References Cited (Backward Citations)

US3775501A Cited
US4035285A Cited
US4090949A Cited
US4157356A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-12-07 1985-06-08 1985-12-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-12-07 1989-06-08 1989-12-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-12-07 1993-06-08 1993-12-08 $7700.00 Window Closed / Lapsed

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