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US3923882A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of acetic acid

Assignee: Union Carbide Corp
•
Filing: 1974-04-17
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Granted: 1975-12-02
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Expires: 1994-04-17
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Abstract

Abstract A continuous process for the liquid phase oxidation of a hydrocarbon selected from the group consisting of alkanes or alkenes having 3 to 8 carbon atoms or mixtures thereof, said hydrocarbon being straight or branched chain or cyclic, to provide acetic acid comprising A. ADMIXING SAID HYDROCARBON; AN OXYGEN-CONTAINING GAS; INITIALLY A SOLVENT COMPRISING A CARBOXYLIC ACID HAVING 2 TO 4 CARBON ATOMS OR A MIXTURE OF LIQUID PRODUCTS FORMED BY THE PROCESS; A COBALT CATALYST; AND ETHANOL IN A REACTION ZONE WHEREIN THE AMOUNT OF HYDROCARBON IS IN THE RANGE OF ABOUT 5 PERCENT BY WEIGHT TO ABOUT 150 PERCENT BY WEIGHT PROVIDED THAT THERE IS A MOLAR EXCESS OF HYDROCARBON OVER OXYGEN; THE AMOUNT OF COBALT IS IN THE RANGE OF ABOUT 0.03 PERCENT BY WEIGHT TO ABOUT 3 PERCENT BY WEIGHT PROVIDED THAT THE COBALT IS IN THE FORM OF A SALT SOLUBLE IN THE SOLVENT; AND THE AMOUNT OF ETHANOL IS ABOUT 1 PERCENT BY WEIGHT TO ABOUT 20 PERCENT BY WEIGHT, ALL SAID PERCENTAGES BASED ON THE WEIGHT OF THE SOLVENT, AND WHEREIN THE TEMPERATURE IS IN THE RANGE OF ABOUT 80*C to about 150*C; and the total reaction pressure and partial pressure of oxygen are sufficient to maintain the reaction in the liquid phase TO FORM A MIXTURE OF LIQUID PRODUCTS INCLUDING ACETIC ACID; AND B. PASSING THE MIXTURE OF LIQUID PRODUCTS, THE COBALT CATALYST, AND UNREACTED HYDROCARBON FROM STEP (A) INTO A SEPARATION ZONE WHEREIN A PORTION OF THE ACETIC ACID IS SEPARATED AND RECOVERED, AND WHEREIN A PORTION OF THE MIXTURE OF LIQUID PRODUCTS IN SUFFICIENT AMOUNT TO PROVIDE SOLVENT FOR STEP (A), THE COBALT CATALYST, AND THE UNREACTED HYDROCARBON ARE SEPARATED AND RECYCLED TO THE REACTION ZONE.

Inventors

  • 👤 Ben Wilton Kiff

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 20:32
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/16; C07C51/21; C07C51/215

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 79 words
The process defined in claim 1 wherein the amount of butane is in the range of 50 percent by weight to about 125 percent by weight; the amount of cobalt is in the range of about 0.3 percent by weight to about 1.5 percent by weight; the amount of ethanol is in the range of about 1.5 percent by weight to about 8 percent by weight; and the temperature is in the range of about 100* to about 140*C.
Claim 2
Dependent Claim 18 words
The procss defined in claim 2 wherein acetic acid is used as the solvent in the initial cycle.

References Cited (Backward Citations)

US2780654A Cited
US2800506A Cited
US3293292A Cited
US3337620A Cited
US3483250A Cited
US3646128A Cited
US3644512A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-12-01 1979-06-02 1979-12-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-12-01 1983-06-02 1983-12-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-12-01 1987-06-02 1987-12-02 $7700.00 Window Closed / Lapsed

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