Partial oxidation catalyst

Claim 2

In a phosphorous-vanadium mixed oxide oxidation catalyst mole ratio P/V being 0.90 to 1.3/1 produced by the process comprising reducing vanadium in the +5 valence state in a substantially anhydrous organic medium to a valence of less than +5 and digesting said reduced vanadium in concentrated phosphoric acid wherein the improvement comprises including a promoter containing a zinc compound in the mole ratio of Zn/V in the range of 0.15 to 0.001/1 in said catalyst during said digesting thereby obtaining a catalyst activated by bringing said catalyst to operating temperature at a rate of 5 to 10° C. per hour.

Claim 3

The phosphorus-vanadium mixed oxide oxidation catalyst according to claim 1 wherein the organic medium is an alcohol, vanadium +5 is present in the compound V 2 0 5 and HC1 is present therein as a reducing agent.

Claim 4

The phosphorus-vanadium mixed oxide oxidation catalyst according to claim 1 wherein in addition to said zinc compound a lithium compound is added during the digesting in an amount of 0.001 to 0.15/1 Li/V mole ratio.

Claim 5

The phosphorous-vanadium mixed oxide oxidation catalyst according to claim 1 wherein in addition to said zinc compound a silicon compound is added during the digesting in an amount of 0.001 to 0.30/1 Si/V mole ratio.

Claim 6

The phosphorous-vanadium mixed oxide oxidation catalyst according to claim 2 wherein the temperature during the education is in the range of 35° to 60° C.

Claim 7

The phosphorus-vanadium mixed oxide oxidation catalyst according to claim 2 wherein the phosphoric acid has a concentration of about 98 to 101% H 3 PO 4 .

Claim 8

The phosphorus-vanadium mixed oxide oxidation catalyst according to claim 5 wherein the temperature during the reduction is in the range of 40° to 55° C.

Claim 9

The phosphorous-vanadium mixed oxide oxidation catalyst according to claim 2 wherein said alcohol is a primary or secondary alcohol.

Claim 10

A substantially anhydrous process for producing improved phosphorus-vanadium mixed oxide oxidation catalysts comprising: admixing a +5 valence vanadium compound with an alcohol, contacting said mixture with gaseous HCl until the valence of vanadium is reduced to less than +5 at a temperature in the range of 35° to 60° C., digesting said reduced vanadium in concentrated phosphoric acid of about 98 to 101% H 3 PO 4 , adding a modifier containing a zinc compound in the mole ratio of Zn/V of 0.15 to 0.001/1 during said digesting, stripping said alcohol from said digested mixture to form a slurry of mixed oxides and alcohol, removing the remaining alcohol under reduced pressure at a temperature in the range of 110° to 170° C., recovering a dried mixed oxide composition and heating said dried mixed oxide composition at a temperature in the range of 200° to 300° C. for a sufficient period to improve the catalytic properties of the composition.

Claim 11

A substantially anhydrous process for producing improved phosphorus-vanadium mixed oxide oxidation catalysts comprising: admixing a +5 valence vanadium compound with an alcohol, contacting said mixture with gaseous HCl until the valence of vanadium is reduced to less than +5 at a temperature in the range of 35° to 60° C., digesting said reduced vanadium in concentrated phosphoric acid of about 98 to 101% H 3 PO 4 , adding a modifier containing a zinc compound in the mole ratio of Zn/V of 0.15 to 0.001/1 during said digesting, stripping said alcohol from said digested mixture to form a slurry of mixed oxides and alcohol, removing the remaining alcohol under reduced pressure at a temperature in the range of 110° to 170° C., recovering a dried mixed oxide composition and heating said dried mixed oxide composition at a temperature in the range of 200° to 300° C. for a sufficient period to improve the catalytic properties of the composition.

Claim 12

The process according to claim 9 wherein said alcohol is a primary or secondary alcohol.

Claim 13

The process according to claim 9 wherein said zinc compound is selected from acetate, carbonate, chloride, bromide, oxide, hydroxide or phosphate.

Claim 14

The process according to claim 8 wherein in addition to said zinc compound a lithium compound is added during the digesting in an amount of 0.001 to 0.15/1 Li/V mole ratio.

Claim 15

The process according to claim 9 wherein in addition to said zinc compound is added during the digesting in a amount of 0.001 to 0.30/1 Si/V mole ratio.

Claim 16

The phosphorus-vanadium mixed oxide oxidation catalyst according to claim 9 wherein said alcohol is a primary or secondary alcohol selected from methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, 2-methyl-1-propanol, 3-methyl-2-butanol, 2,2-dimethyl-1-propanol, 1-hexanol, 4-methyl-1-pentanol, 1-heptanol, 4-methyl-1-hexanol, 4-methyl-1-heptanol, 1,2-ethanediol, glycerol, trimethylolpropane, diethylene glycol or triethylene glycol.

Claim 17

The phosphorus-vanadium mixed oxide oxidation catalyst according to claim 4 wherein said alcohol is 2-methyl-1-propanol.

Claim 18

The phosphorus-vanadium mixed oxide oxidation catalyst according to claim 15 wherein said zinc compound is selected from acetate, carbonate, chloride, bromide, oxide, hydroxide or phosphate.

Claim 19

The phosphorus-vanadium mixed oxide oxidation catalyst according to claim 15 or 16 said zinc compound is zinc chloride.

Claim 20

The process according to claim 10 wherein said primary or secondary alcohol is selected from methanol, ethanol, 1propanol, 2-propanol, 1-butanol, 2-butanol, 2-methyl-1-propanol, 3-methyl-2-butanol, 2,2-dimethyl-1-propanol, 1-hexanol, 4-methyl-1-pentanol, 1-heptanol, 4-methyl-1-hexanol, 4-methyl-1-heptanol, 1,2-ethanediol, glycerol, trimethylolpropane diethylene glycol or triethylene glycol.

Claim 21

The process according to claim 18 wherein the alcohol is 2-methyl-1-propanol.

Claim 22

The process according to claim 19 or 11 wherein said zinc compound is zinc chloride.