Production of maleic anhydride from four-carbon hydrocarbons using catalysts prepared by hydrothermal techniques

Claim 2

A process for preparing a catalyst comprising the mixed oxides of vanadium and phosphorus, said process comprising the steps of: (a) forming an aqueous oxide slurry of a vanadium compound containing pentavalent vanadium and a mineral acid-free, inorganic reducing agent capable of reducing said pentavalent vanadium to a valence state below +5, wherein said reducing agent is selected from the group consisting of a finely divided metal or a colloidal metal; (b) admixing a phosphorus compound containing pentavalent phosphorus with said aqueous slurry of step (a); (c) heating said aqueous slurry of step (b) at a temperature of at least 120° C. under autogenous pressure so that substantial evaporation of the water in said slurry is prevented; (d) removing the water from the slurry of step (c) to form a dried catalyst; and (e) calcining the dried catalyst at a temperature of 250° C. to 600° C. in the presence of an oxygen-containing gas.

Claim 3

The process of claim 1 wherein said finely divided metal is selected from the group consisting of molybdenum, tungsten, magnesium, aluminum, or nickel.

Claim 4

The process of claim 1 wherein the phosphorus to vanadium atom ratio is 0.1:10 to 10:0.1.

Claim 5

The process of claim 1 wherein the phosphorus to vanadium atom ratio is 0.5:3 to 3:0.5.

Claim 6

The process of claim 1 wherein the compound containing pentavalent vanadium is vanadium pentoxide.

Claim 7

The process of claim 1 wherein the compound containing pentavalent phosphorus is phosphoric acid.

Claim 8

The process of claim 1 wherein the aqueous slurry of step (c) is heated at a temperature of 120° C. to 300° C.

Claim 9

The process of claim 1 wherein the aqueous slurry of step (c) is heated under autogenous pressure of 15 to 1,300 p.s.i.g.

Claim 10

The process of claim 1 wherein the aqueous slurry of step (c) is heated at a temperature of 130° C. to 240° C. under autogenous pressure of 20 to 500 p.s.i.g.

Claim 11

The process of claim 1 wherein the catalyst is prepared in the absence of a hydrogen halide.

Claim 12

The process of claim 1 wherein the catalyst is prepared in the absence of a compound containing trivalent phosphorus.

Claim 13

The process of claim 1 wherein the finely divided metal is tungsten.

Claim 14

The process of claim 1 wherein said colloidal metal is selected from the group consisting of Mo, W, Mg. Al or Ni.

Claim 15

The process of claim 1 wherein the aqueous slurry of step (c) is heated to a temperature of 180° C. to 240° C.

Claim 16

A process for preparing a catalyst comprising the mixed oxides of vanadium and phosphorus, said process comprising the steps of: (a) refluxing an aqueous oxide slurry containing vanadium pentoxide and a mineral acid-free, inorganic reducing agent capable of reducing the vanadium in the vanadium pentoxide to a valence state below +5 to obtain an aqueous slurry containing reduced vanadium, wherein the reducing agent is selected from the group consisting of a finely divided metal or a colloidal metal; (b) admixing phosphoric acid with said aqueous slurry containing reduced vanadium; (c) autoclaving the aqueous slurry of step (b) at a temperature of 120° C. to 250° C. under autogenous pressure of 15 to 1300 p.s.i.g. so as to retain substantially all of the water content in the slurry; (d) removing the water from the slurry of step (c) to form a dried catalyst; and (e) calcining said dried catalyst at a temperature of 250° C. to 600° C. in the presence of an oxygen-containing gas.

Claim 17

A process for preparing a catalyst comprising the mixed oxides of vanadium and phosphorus, said process comprising the steps of: (a) refluxing an aqueous oxide slurry containing vanadium pentoxide and a mineral acid-free, inorganic reducing agent capable of reducing the vanadium in the vanadium pentoxide to a valence state below +5 to obtain an aqueous slurry containing reduced vanadium, wherein the reducing agent is selected from the group consisting of a finely divided metal or a colloidal metal; (b) admixing phosphoric acid with said aqueous slurry containing reduced vanadium; (c) autoclaving the aqueous slurry of step (b) at a temperature of 120° C. to 250° C. under autogenous pressure of 15 to 1300 p.s.i.g. so as to retain substantially all of the water content in the slurry; (d) removing the water from the slurry of step (c) to form a dried catalyst; and (e) calcining said dried catalyst at a temperature of 250° C. to 600° C. in the presence of an oxygen-containing gas.

Claim 18

The process of claim 15 wherein the finely divided metal is tungsten.

Claim 19

The process for preparing a catalyst comprising the mixed oxides of vanadium, phosphorus, and uranium, said process comprising the steps of: (a) forming an aqueous slurry of a vanadium compound containing pentavalent vanadium and a mineral acid-free, inorganic reducing agent capable of reducing said pentavalent vanadium to a valence state below +5, wherein the reducing agent is selected from the group consisting of a finely divided metal or a colloidal metal; (b) admixing a phosphorus compound containing pentavalent phosphorus with said aqueous slurry of step (a); (c) heating said aqueous slurry of step (b) at a temperature of 120° C. under autogenous pressure so that substantial evaporation of the water in said slurry is prevented; (d) removing the water from the slurry of step (c) to form a dried catalyst; and (e) calcining the dried catalyst at a temperature of 250° C. to 600° C. in the presence of an oxygen-containing gas; (f) adding a uranium compound immediately before the addition of the phosphorus compound or after the addition of the phosphorus compound.

Claim 20

The process for preparing a catalyst comprising the mixed oxides of vanadium, phosphorus, and uranium, said process comprising the steps of: (a) forming an aqueous slurry of a vanadium compound containing pentavalent vanadium and a mineral acid-free, inorganic reducing agent capable of reducing said pentavalent vanadium to a valence state below +5, wherein the reducing agent is selected from the group consisting of a finely divided metal or a colloidal metal; (b) admixing a phosphorus compound containing pentavalent phosphorus with said aqueous slurry of step (a); (c) heating said aqueous slurry of step (b) at a temperature of 120° C. under autogenous pressure so that substantial evaporation of the water in said slurry is prevented; (d) removing the water from the slurry of step (c) to form a dried catalyst; and (e) calcining the dried catalyst at a temperature of 250° C. to 600° C. in the presence of an oxygen-containing gas; (f) adding a uranium compound immediately before the addition of the phosphorus compound or after the addition of the phosphorus compound.

Claim 21

The process of claim 17 wherein the catalyst prepared is described by the formula V.sub.a P.sub.b U.sub.c O.sub.x wherein a and b are 1 to 10; c is 0.01 to 5; x is the number of oxygens required to satisfy the valence requirements of the other elements present; and wherein said catalyst optionally contains at least one element selected from the group consisting of tantalum, cerium, chromium, manganese, cobalt, copper, antimony, iron, bismuth, tungsten, molybdenum, alkaline earth metal, an alkali metal, hafnium, zirconium, and thorium.

Claim 22

The process of claim 17 wherein the aqueous slurry of step (c) is heated to a temperature of 180° C. to 240° C.

Claim 23

The process of claim 18 wherein at least one optional promoter is present in the catalyst in an atomic range of 0.01 to 1.

Claim 24

The process of claim 18 wherein a and b are 0.5 to 3.

Claim 25

The process of claim 18 wherein c is 0.1 to 0.5.

Claim 26

The process of claim 18 wherein the optional promoter is selected from the group consisting of Ta, Ce, Mn, Co, Sb, Fe, Bi, W and Mo.

Claim 27

The process of claim 17 wherein the finely divided metal is tungsten in an atomic range of 0.01 to 5.