Cyclohexane oxidation in the presence of binary catalysts

Claim 2

A process for the preparation of cyclohexanone and cyclohexanol in the weight ratio of from 0.5 to 1.5 ketone to alcohol by contacting a stream comprising liquid cyclohexane with oxygen at each of at least three successive oxidation stages by introducing into each stage a mixture of gases comprising molecular oxygen and inert gas, said oxygen being introduced in an amount in excess of the stoichiometric amount required to react with the cyclohexane, wherein the overall amount of oxygen consumed is not more than 95 mole percent of the amount fed to the stages under the particular conditions of the stages, in the presence of a binary catalyst system comprising chromium and cobalt as compounds which are soluble in cyclohexane at a temperature of from 130° to 180° C. and a pressure of from 60 to 350 psig to produce a first product stream comprising unreacted cyclohexane, cyclohexanone, cyclohexanol, and cyclohexylhydroperoxide; forwarding the first product stream to a deperoxidation operation, wherein the cyclohexylhydroperoxide present in the first product stream is decomposed in the presence of said binary catalyst system, to form additional quantities of cyclohexanone and cyclohexanol, the overall amount of catalyst being in the range of 0.02 to 0.9 ppm chromium and 0.1 to 5 ppm cobalt; and recovering a product consisting essentially of cyclohexanone and cyclohexanol.

Claim 3

The process of claim 1 wherein the weight ratio of cyclohexanone to cyclohexanol is 0.5 to 1.0.

Claim 4

A process for the preparation of cyclohexanone and cyclohexanol in a weight ratio of from 0.5 to 1.5 ketone to alcohol which comprises first oxidizing cyclohexane to produce a first product fluid consisting essentially of unreacted cyclohexane, cyclohexanone, cyclohexanol, and cyclohexylhydroperoxide, the percentage of cyclohexylhydroperoxide to the total of cyclohexanone, cyclohexanol and cyclohexylhydroperoxide being greater than 15% by weight, the first product fluid being substantially free of peroxides other than cyclohexylhydroperoxide, which comprises passing a fluid containing cyclohexane and a cyclohexane soluble cobalt salt in an amount of from 0.1 to 5 ppm of said product fluid downwardly through an oxygen cleanup zone comprising a series of oxygen cleanup stages and an oxidizing zone comprising a series of oxidizing stages at a pressure, measured at the top of the oxygen cleanup zone of 60-350 psig, while countercurrently passing an oxidizing gas containing molecular oxygen upwardly through the zones, the fluid initially passing through each series of oxygen cleanup stages wherein the temperature is maintained in the range of 130°-180° C. and where the oxygen concentration in the upward passing gas leaving the oxygen cleanup zone is reduced to less than four mole percent, the fluid then passing through said series of oxidizing stages operated at a temperature in the range of 140°-170° C. in which the level of oxygen is maintained at a level in excess of the amount of oxygen that will react with the fluid mixture by addition of oxidizing gas, the overall amount of oxygen consumed in the oxidizing zone being not more than 95 mole percent of the amount fed; second reacting the first product fluid containing cyclohexane, cyclohexanol, cyclohexanone and cyclohexylhydroperoxide in the presence of 0.02 to 0.9 ppm chromium and 0.1 to 5 ppm cobalt in a peroxide reactor to produce additional quantities of cyclohexanone and cyclohexanol; followed by recovering a product consisting essentially of cyclohexanone and cyclohexanol.

Claim 5

A process for the preparation of cyclohexanone and cyclohexanol in a weight ratio of from 0.5 to 1.5 ketone to alcohol which comprises first oxidizing cyclohexane to produce a first product fluid consisting essentially of unreacted cyclohexane, cyclohexanone, cyclohexanol, and cyclohexylhydroperoxide, the percentage of cyclohexylhydroperoxide to the total of cyclohexanone, cyclohexanol and cyclohexylhydroperoxide being greater than 15% by weight, the first product fluid being substantially free of peroxides other than cyclohexylhydroperoxide, which comprises passing a fluid containing cyclohexane and a cyclohexane soluble cobalt salt in an amount of from 0.1 to 5 ppm of said product fluid downwardly through an oxygen cleanup zone comprising a series of oxygen cleanup stages and an oxidizing zone comprising a series of oxidizing stages at a pressure, measured at the top of the oxygen cleanup zone of 60-350 psig, while countercurrently passing an oxidizing gas containing molecular oxygen upwardly through the zones, the fluid initially passing through each series of oxygen cleanup stages wherein the temperature is maintained in the range of 130°-180° C. and where the oxygen concentration in the upward passing gas leaving the oxygen cleanup zone is reduced to less than four mole percent, the fluid then passing through said series of oxidizing stages operated at a temperature in the range of 140°-170° C. in which the level of oxygen is maintained at a level in excess of the amount of oxygen that will react with the fluid mixture by addition of oxidizing gas, the overall amount of oxygen consumed in the oxidizing zone being not more than 95 mole percent of the amount fed; second reacting the first product fluid containing cyclohexane, cyclohexanol, cyclohexanone and cyclohexylhydroperoxide in the presence of 0.02 to 0.9 ppm chromium and 0.1 to 5 ppm cobalt in a peroxide reactor to produce additional quantities of cyclohexanone and cyclohexanol; followed by recovering a product consisting essentially of cyclohexanone and cyclohexanol.

Claim 6

The process of claim 3 wherein the ratio of cyclohexanone to cyclohexanol is from 0.5 to 1.0.