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US4111986A Expired / Lapsed US ⏱️ 0.0 years remaining

Butane oxidation to acetic acid

Assignee: BP Corp North America Inc
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Filing: 1977-04-19
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Granted: 1978-09-05
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Expires: 1997-04-19
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Abstract

Abstract Oxidizing butane to acetic acid which comprises contacting a sufficient concentration of an oxygen-containing gas with normal butane in the presence of catalyst consisting essentially of bromine and cobalt to initiate a self-sustaining exothermic reaction.

Inventors

  • 👤 Wilford J. Zimmerschied

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 13:15
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/16; C07C51/21; C07C51/215

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 70 words
The process of oxidizing butane to acetic acid which comprises contacting a sufficient concentration of an oxygen-containing gas with normal liquid butane in the presence of a dissolved catalyst consisting essentially of bromine and cobalt in a solvent medium comprising acetic acid to initiate a self-sustaining exothermic reaction, wherein each 100 grams of butane is contacted with oxygen at a rate of at least 5 liters of oxygen per hour.
Claim 2
Dependent Claim 70 words
The process of oxidizing butane to acetic acid which comprises contacting a sufficient concentration of an oxygen-containing gas with normal liquid butane in the presence of a dissolved catalyst consisting essentially of bromine and cobalt in a solvent medium comprising acetic acid to initiate a self-sustaining exothermic reaction, wherein each 100 grams of butane is contacted with oxygen at a rate of at least 5 liters of oxygen per hour.
Claim 3
Dependent Claim 29 words
The process of claim 1 wherein an oxygen containing gas is injected below the surface of the reaction medium at a rate sufficient to initiate a self-sustaining exothermic reaction.
Claim 4
Dependent Claim 34 words
The process of claim 2 wherein the catalyst components are present in a concentration of from about 1 to 50 milliequivalents of cobalt and 2 to 500 milliequivalents of bromine per mole of butane.
Claim 5
Dependent Claim 11 words
The process of claim 3 wherein said catalyst is cobaltous bromide.
Claim 6
Dependent Claim 33 words
The process of claim 1 wherein each 100 grams of butane is contacted with oxygen at a rate of at least 10 liters of oxygen per hour to initiate said self-sustaining exothermic reaction.
Claim 7
Dependent Claim 28 words
The process of claim 5 wherein an oxygen-containing gas is injected below the surface of the reaction medium at a rate sufficient to initiate a self-sustaining exothermic reaction.
Claim 8
Dependent Claim 34 words
The process of claim 6 wherein the catalyst components are present in a concentration of from about 1 to 50 milliequivalents of cobalt and 2 to 500 milliequivalents of bromine per mole of butane.

References Cited (Backward Citations)

US3247249A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-09-04 1982-03-06 1982-09-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-09-04 1986-03-06 1986-09-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-09-04 1990-03-06 1990-09-05 $7700.00 Window Closed / Lapsed

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