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CA1153974A Expired / Lapsed CA ⏱️ 0.0 years remaining

Conversion of olefin containing mixtures to gasoline

Assignee: Mobil Oil AS
•
Filing: 1980-12-17
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Granted: 1983-09-20
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Expires: 2000-12-17
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Abstract

Abstract CONVERSION OF OLEFIN CONTAINING MIXTURES TO GASOLINE ABSTRACT Olefin containing mixtures are converted into olefinic gasoline blending stock with an excellent research octane number and in good yield by passage over a catalyst comprising a highly siliceous zeolite having a silica to alumina mole ratio of at least 200 to 1 and a constraint index within the approximate range of 1 to 12.

Inventors

  • 👤 Francis G. Dwyer
  • 👤 William E. Garwood

Bibliographic Details

Application Number —
Jurisdiction CA
Data Source google_patents
Last Synchronized 2026-11-05 02:13
CPC Classifications
B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/70; B01J29/703; B01J29/40; C; C07; C07C; C07C2/00; C07C2529/00; C07C2529/04; C07C2529/06; C07C2529/40; C07C2529/70

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 100 words
An improved process for producing a gasoline fraction having no more than about 20 percent by weight of aromatics, said process comprising contacting a C2-C5 olefin containing mixture with a catalyst comprising a zeolite having a silica to alumina mole ratio of at least 200 to 1 and a constraint index in the approximate range of 1 to 12 at a temperature between 450°F (233°c) and 800°F (427°c), an olefin partial pressure between 0.5 psia (4 k Pa) and 100 psia 689 (k Pa) and a WHSV between 0.1 and 25, and recovering a gasoline fraction containing predominantly higher olefins.
Claim 2
Dependent Claim 100 words
An improved process for producing a gasoline fraction having no more than about 20 percent by weight of aromatics, said process comprising contacting a C2-C5 olefin containing mixture with a catalyst comprising a zeolite having a silica to alumina mole ratio of at least 200 to 1 and a constraint index in the approximate range of 1 to 12 at a temperature between 450°F (233°c) and 800°F (427°c), an olefin partial pressure between 0.5 psia (4 k Pa) and 100 psia 689 (k Pa) and a WHSV between 0.1 and 25, and recovering a gasoline fraction containing predominantly higher olefins.
Claim 3
Dependent Claim 15 words
A process according to Claim 1 wherein said zeolite is ZSM-5, ZSM-11, ZSM-12 or ZSM-48.
Claim 4
Dependent Claim 19 words
A process according to Claim 1 wherein said silica to alumina mole ratio is at least 500 to 1.
Claim 5
Dependent Claim 22 words
A process according to Claim 1, 2 or 3 wherein said silica to alumina mole ratio is at least 1000 to 1.
Claim 6
Dependent Claim 22 words
A process according to Claim 1, 2 or 3 wherein said silica to alumina mole ratio is at least 1400 to 1.
Claim 7
Dependent Claim 22 words
A process according to Claim 1, 2 or 3 wherein said silica to alumina mole ratio is at least 1600 to 1.
Claim 8
Dependent Claim 43 words
A process according to Claim 1, 2 or 3 which is carried out at a temperature between 500°F (260°c) and 700°F (372°c), an olefin partial pressure between 1 psia (7 kPa) and 50 psia (345 kPa) and a WHSV between 0.5 and 15.
Claim 9
Dependent Claim 17 words
A process according to Claim 1, 2 or 3 wherein said zeolite is in the hydrogen form.
Claim 10
Dependent Claim 26 words
A process according to Claim 1, 2 or 3 wherein the gasoline fraction has a research octane number with no added lead of 92 or above.
Claim 11
Dependent Claim 14 words
A process according to Claim 1 wherein said zeolite is incorprated in a matrix.
Claim 12
Dependent Claim 26 words
A process according to Claim 10 wherein the amount of zeolite in said matrix is from 1 wt. % to 95 wt. % of the total.
Claim 13
Dependent Claim 23 words
A process according to Claim 11 wherein the amount of zeolite is from 20 wt. % to 80 wt. % of the total.
Claim 14
Dependent Claim 17 words
A process according to Claim 1, 2 or 3 wherein said catalyst is in the extrudate form.
Claim 15
Dependent Claim 18 words
The process according to Claim 1, 2 or 3 wherein said olefin containing mixture comprises propylene and butylene.

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