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US4053533A Expired / Lapsed US ⏱️ 0.0 years remaining

Oxidation of acetylenic impurities with copper manganite catalyst

Assignee: Phillips Petroleum Co
•
Filing: 1975-10-15
•
Granted: 1977-10-11
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Expires: 1995-10-15
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Abstract

Abstract Acetylenic compounds are selectively removed from hydrocarbon mixtures containing same by oxidation in the presence of a solid copper-manganese-oxygen catalyst. In one embodiment, acetylenic compounds are selectively removed from a conjugated diene mixture containing same by contacting oxygen and a mixture with a copper manganite catalyst under oxidizing conditions.

Inventors

  • 👤 Lewis E. Drehman
  • 👤 Floyd Farha, Jr.
  • 👤 Arlo J. Moffat

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 18:34
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/148; C07C7/14808; C07C7/14816; D; D21; D21H; D21H17/00; D21H17/20; D21H17/33; D21H17/34

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 82 words
A process for the selective removal of acetylenic contaminants or impurities present in hydrocarbon streams which comprises contacting oxygen and a hydrocarbon-containing mixture contaminated with acetylenic compounds with a catalyst consisting essentially of copper, manganese, and oxygen in which the atomic ratio of copper to manganese varies from about 0.25:1 to about 4:1 under oxidation conditions including a temperature and a mol ratio of oxygen to hydrocarbon sufficient to selectively remove a substantial portion of said acetylenic compounds present in said mixture.
Claim 2
Dependent Claim 82 words
A process for the selective removal of acetylenic contaminants or impurities present in hydrocarbon streams which comprises contacting oxygen and a hydrocarbon-containing mixture contaminated with acetylenic compounds with a catalyst consisting essentially of copper, manganese, and oxygen in which the atomic ratio of copper to manganese varies from about 0.25:1 to about 4:1 under oxidation conditions including a temperature and a mol ratio of oxygen to hydrocarbon sufficient to selectively remove a substantial portion of said acetylenic compounds present in said mixture.
Claim 3
Dependent Claim 44 words
A process according to claim 1 wherein said contacting is effected at a temperature ranging from about 250°-800° F., a reaction pressure ranging from 0.5-500 psig, an oxygen to hydrocarbon mol ratio ranging from 0.01-0.2, and a steam to hydrocarbon mol ratio of 0-100.
Claim 4
Dependent Claim 11 words
A process according to claim 1 wherein the mixture comprises butadiene.
Claim 5
Dependent Claim 28 words
A process according to claim 1 wherein said contacting is effected in the presence of oxygen and steam at a temperature in the range of about 400°-650° F.
Claim 6
Dependent Claim 50 words
A process according to claim 1 wherein said mixture is a butadiene mixture obtained as the effluent from the oxidative dehydrogenation of olefins and the effluent contains oxygen, steam, and 1-acetylenes, as well as butadiene, and the contacting is effected at a temperature in the range of about 400°-650° F.
Claim 7
Dependent Claim 50 words
A process according to claim 1 wherein the catalyst is at least one composition having the formula Cu 3 Mn 2 O 6 , Cu 2 Mn 2 O 5 , CuMnO 2 , CuMn 2 O 3 , CuMn 3 O 4 , and CuMn 2 O 4 .
Claim 8
Dependent Claim 15 words
A process according to claim 1 wherein said catalyst is CuMn 2 O 4 .

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-10-10 1981-04-11 1981-10-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-10-10 1985-04-11 1985-10-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-10-10 1989-04-11 1989-10-11 $7700.00 Window Closed / Lapsed

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