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Conversion of olefinic naphtha

Assignee: Mobil Oil AS
•
Filing: 1977-07-25
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Granted: 1978-06-27
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Expires: 1997-07-25
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Abstract

Abstract High severity catalytic conversion of olefinic naphthas which contain diolefins is conducted over special catalysts to yield a product stream which contains little or no non-aromatics boiling in the range of benzene, toluene and xylene. The catalysts are combinations of zinc and a metal of Groups I B and VIII of the Periodic Table with a crystalline aluminosilicate zeolite having a silica/alumina ratio greater than 12 and a constraint index not less than one nor greater than 12.

Inventors

  • 👤 Werner O. Haag
  • 👤 Tracy J. Huang

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 15:05
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/095; B; B01; B01J; B01J29/00; B01J29/04; B01J29/06; B01J29/70; B01J29/7049; B01J29/72; B01J29/74

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 97 words
A process for upgrading of pyrolysis gasoline and other olefinic naphthas which contain olefins which comprises contacting said naphtha at severe conditions of 900° to 1200° F, a pressure of atmospheric to 400 pounds per square inch and weight hourly space velocity of 0.3 to 30 with a catalyst composite of zinc and at least one metal selected from the groups consisting of IB and VIII of the Periodic Table in intimate association with a porous crystalline aluminosilicate zeolite having a silica to alumina ratio of at least 12 and a constraint index between 1 and 12.
Claim 2
Dependent Claim 97 words
A process for upgrading of pyrolysis gasoline and other olefinic naphthas which contain olefins which comprises contacting said naphtha at severe conditions of 900° to 1200° F, a pressure of atmospheric to 400 pounds per square inch and weight hourly space velocity of 0.3 to 30 with a catalyst composite of zinc and at least one metal selected from the groups consisting of IB and VIII of the Periodic Table in intimate association with a porous crystalline aluminosilicate zeolite having a silica to alumina ratio of at least 12 and a constraint index between 1 and 12.
Claim 3
Dependent Claim 26 words
The process of claim 1 conducted at a severity to yield a liquid product fraction containing less than 5% of non-aromatic hydrocarbons boiling above 167° F.
Claim 4
Dependent Claim 25 words
The process of claim 1 conducted at a severity to yield a liquid product containing less than 1% of non-aromatic hydrocarbons boiling above 167° F.
Claim 5
Dependent Claim 23 words
The process of claim 1 conducted at a severity to yield a liquid product containing substantially no non-aromatic hydrocarbons boiling above 167° F.
Claim 6
Dependent Claim 19 words
The process of claim 1 wherein said metal of Group VIII is ruthenium, rhodium, palladium, osmium, iridium or platinum.
Claim 7
Dependent Claim 10 words
The process of claim 5 wherein said metal is palladium.
Claim 8
Dependent Claim 23 words
The process of claim 1 conducted at a temperature not lower than 980° F and weight hourly space velocity not greater than 5.
Claim 9
Dependent Claim 11 words
The process of claim 1 wherein the charge naphtha contains diolefins.

References Cited (Backward Citations)

US3855115A Cited
US3914171A Cited
US3871993A Cited
US3890218A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-06-26 1981-12-26 1982-06-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-06-26 1985-12-26 1986-06-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-06-26 1989-12-26 1990-06-27 $7700.00 Window Closed / Lapsed

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