Catalyst treatment

Claim 2

A process for the regeneration of a spent olefin ammoxidation catalyst in which at least 20% of the atoms of the active metallic elements in the catalyst are molybdenum atoms which comprises heating the catalyst at a temperature of from 400° to 650° C and at a pressure of from 1.0 to 2.0 kg/cm 2 in an atmosphere comprising from 20 to 45% by volume of steam, the balance being air or a gas inert to the catalyst under the above conditions, for a period of at least one hour.

Claim 3

A process according to claim 1 in which the catalyst is heated at substantially atmospheric pressure.

Claim 4

A process according to claim 1 in which the catalyst is heated at substantially atmospheric pressure in the presence of an air/steam mixture wherein the partial pressure of steam in the mixture is from 200-300 mm.

Claim 5

A process for the regeneration of an olefin ammoxidation catalyst in which at least 40% of the atoms of the active metallic elements in the catalyst are molybdenum atoms which comprises heating the catalyst composition at substantially atmospheric pressure and a temperature of from 500° to 550° C for a period of 1 to 24 hours under an atmosphere consisting of a mixture of air and steam with a partial pressure of steam of from 200 to 300 mm.

Claim 6

A process for the regeneration of an olefin ammoxidation catalyst in which at least 40% of the atoms of the active metallic elements in the catalyst are molybdenum atoms which comprises heating the catalyst composition at substantially atmospheric pressure and a temperature of from 500° to 550° C for a period of 1 to 24 hours under an atmosphere consisting of a mixture of air and steam with a partial pressure of steam of from 200 to 300 mm.

Claim 7

A process for the regeneration of an olefin ammoxidation catalyst composition defined by the following formula: Mo.sub.12 Bi.sub.a Fe.sub.b M.sub.m E.sub.e X.sub.x Z.sub.z O.sub.n where M is an alkali metal, E is an alkaline earth metal, X is phosphorus, arsenic or antimony, Z is cobalt or nickel, a and b are from 0.1 to 12, m is 0.1 to 8, e is from 0 to 8, x is from 0 to 6, z is from 0 to 12 and n is a number determined by the valence requirements of the other elements present, a, b, m, e, x, and z being chosen such that molybdenum provides at least 20% of the atoms of the active metallic element in the catalyst, which process comprises heating the catalyst composition at substantially atmospheric pressure and a temperature of from 500° to 550° C for a period of 1 to 24 hours under an atmosphere consisting of a mixture of air and steam with a partial pressure of steam of from 200 to 300 mm.

Claim 8

A process for the regeneration of an olefin ammoxidation catalyst composition defined by the following formula: Mo.sub.12 Bi.sub.a Fe.sub.b M.sub.m E.sub.e X.sub.x Z.sub.z O.sub.n where M is an alkali metal, E is an alkaline earth metal, X is phosphorus, arsenic or antimony, Z is cobalt or nickel, a and b are from 0.1 to 12, m is 0.1 to 8, e is from 0 to 8, x is from 0 to 6, z is from 0 to 12 and n is a number determined by the valence requirements of the other elements present, a, b, m, e, x, and z being chosen such that molybdenum provides at least 20% of the atoms of the active metallic element in the catalyst, which process comprises heating the catalyst composition at substantially atmospheric pressure and a temperature of from 500° to 550° C for a period of 1 to 24 hours under an atmosphere consisting of a mixture of air and steam with a partial pressure of steam of from 200 to 300 mm.