Reactivation of maleic anhydride producing phosphorus-vanadium-oxygen complex oxidation catalysts by treatment with halide containing materials

Claim 2

In a process for the preparation of maleic anhydride from the oxidation of feed materials selected from the group consisting of alkanes, alkenes, or mixtures thereof or aromatics which comprises contacting said feed material and a gas containing molecular oxygen in the vapor phase with a solid catalyst comprising a phosphorus-vanadium-oxygen complex having from about 0.5 to about 5 atoms of phosphorus for each atom of vanadium, wherein the improvement comprises contacting said catalyst complex at reactivating conditions with an effective amount of a reactivating agent selected from the group consisting of: A. molecular halogens; B. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: c(X)n where each X is selected halide and n is an integer from 1 to 4, any remaining radicals being hydrogen; C. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: R(X.sub.1)m where R is alkane, alkene or alkyne of straight or branched structure having at least two carbon atoms and X 1 is independently a primary, secondary or tertiary halide and m is an integer of from 1 to about 20 consistent with the number of carbon atoms of said structure; and D. hydrogen halides; or mixtures thereof to thereby enhance the selectivity of the catalyst for the production of maleic anhydride.

Claim 3

The process of claim 1 further characterized in that said catalyst contains a metal promoter selected from the group consisting of zinc, copper, bismuth, lithium or mixtures thereof.

Claim 4

The process of claim 2 further characterized in that said catalyst contains from about 1 to about 1.5 atoms of phosphorous for each atom of vanadium.

Claim 5

The process of claim 3 further characterized in that the promoter is zinc and is present as from about 0.01 to about 0.3 atoms of zinc for each atom of vanadium.

Claim 6

The process of claim 4 further characterized in that said reactivating agent is selected from the group consisting of CCl 4 , CHCl 3 , CH 2 Cl 2 , HCl, Cl 2 , CH 3 Cl or mixtures thereof.

Claim 7

The process of claim 4 further characterized in that said reactivating agent is CCl 4 .

Claim 8

The process of claim 1 further characterized in that said feed material comprises normal butane, said catalyst contains from about 1 to about 1.5 atoms of phosphorous per atom of vanadium and a zinc metal promoter present as from about 0.01 to about 0.3 atoms of zinc for each atom of vanadium, and said reactivating agent comprises carbon tetrachloride.

Claim 9

The process of claim 1 further characterized in that R has less than 4 carbon atoms and is alkane or alkene and m is an integer of from 1 to about 8 consistent with the number of carbon atoms of said structure, and said hydrogen halide is HCl.

Claim 10

The process of claim 8 further characterized in that said catalyst contains from about 1 to about 1.5 atoms of phosphorous per atom of vanadium and from about 0.01 to about 0.3 atoms of a zinc metal promoter per atom of vanadium.

Claim 11

In a process for the production of maleic anhydride from the oxidation of feed materials selected from the group consisting of alkanes, alkenes or mixtures thereof which comprises contacting said feed materials and a gas containing molecular oxygen in the vapor phase with a solid catalyst comprising a phosphorus -vandadium-oxygen complex, said catalyst complex having from about 0.5 to about 5 atoms of phosphorus for each atom of vanadium, wherein the selectivity of the catalyst for production of maleic anhydride from said feed materials has decreased from a level achieved during earlier catalyst life of said catalyst complex, wherein the improvement comprises contacting said catalyst complex with an effective amount of a reactivating agent selected from the group consisting of: A. molecular halogens; B. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: C(X).sub.n wherein each X is a selected halide and n is an integer from 1 to 4 any remaining radicals being hydrogen; C. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: R(X.sub.1)m where R is alkane, alkene or alkyne of straight or branched structure having at least two carbon atoms, each X 1 is independently a primary, secondary or tertiary halide and m is an integer of from 1 to about 20 consistent with the number of carbon atoms of said structure; and D. hydrogen halides; or mixtures thereof to thereby enhance the selectivity of the catalyst for the production of maleic anhydride.

Claim 12

In a process for the production of maleic anhydride from the oxidation of feed materials selected from the group consisting of alkanes, alkenes or mixtures thereof which comprises contacting said feed materials and a gas containing molecular oxygen in the vapor phase with a solid catalyst comprising a phosphorus -vandadium-oxygen complex, said catalyst complex having from about 0.5 to about 5 atoms of phosphorus for each atom of vanadium, wherein the selectivity of the catalyst for production of maleic anhydride from said feed materials has decreased from a level achieved during earlier catalyst life of said catalyst complex, wherein the improvement comprises contacting said catalyst complex with an effective amount of a reactivating agent selected from the group consisting of: A. molecular halogens; B. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: C(X).sub.n wherein each X is a selected halide and n is an integer from 1 to 4 any remaining radicals being hydrogen; C. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: R(X.sub.1)m where R is alkane, alkene or alkyne of straight or branched structure having at least two carbon atoms, each X 1 is independently a primary, secondary or tertiary halide and m is an integer of from 1 to about 20 consistent with the number of carbon atoms of said structure; and D. hydrogen halides; or mixtures thereof to thereby enhance the selectivity of the catalyst for the production of maleic anhydride.

Claim 13

The process of claim 10 further characterized in that R has less than 4 carbon atoms and is alkane, m is an integer of from 1 to 8 consistent with the number of carbon atoms of said structure and said hydrogen halide is HCl.

Claim 14

The process of claim 10 further characterized in that said feed materials comprise normal butane.

Claim 15

The process of claim 11 further characterized in that said catalyst contains from about 1 to about 1.5 atoms of phosphorous for each atom of vanadium and from about 0.01 to about 0.3 atoms of a zinc promoter per atom of vanadium.

Claim 16

The process of claim 11 further characterized in that said feed materials comprise normal butane, said catalyst contains from about 1 to about 1.5 atoms of phosphorous and from about 0.01 to about 0.3 atoms of a zinc metal promoter for each atom of vanadium.

Claim 17

In a process for the preparation of maleic anhydride which comprises contacting a feed material comprising butane and a gas containing molecular oxygen in the vapor phase with a solid catalyst comprising a phosphorus -vanadium-oxygen complex, said catalyst complex having from about 0.5 to about 5 atoms of phosphorus for each atom of vanadium, wherein the improvement comprises contacting said catalyst complex at reactivating conditions with an effective amount of a reactivating agent containing a material selected from the group consisting of: A. molecular halogens; B. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: C(X).sub.n where each X is a selected halide and n is an integer from 1 to 4 any remaining radicals being hydrogen; C. organic halides represented by the formula: R(X.sub.1).sub.m where R is alkane, alkene or alkyne having from two to three carbon atoms, each X 1 is independently a primary, secondary or tertiary halide and m is an integer of from 1 to about 8 consistent with the number of carbon atoms of said structure: and D. hydrogen halides; or mixtures thereof to thereby enhance the selectivity of the catalyst for the production of maleic anhydride.

Claim 18

In a process for the preparation of maleic anhydride which comprises contacting a feed material comprising butane and a gas containing molecular oxygen in the vapor phase with a solid catalyst comprising a phosphorus -vanadium-oxygen complex, said catalyst complex having from about 0.5 to about 5 atoms of phosphorus for each atom of vanadium, wherein the improvement comprises contacting said catalyst complex at reactivating conditions with an effective amount of a reactivating agent containing a material selected from the group consisting of: A. molecular halogens; B. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: C(X).sub.n where each X is a selected halide and n is an integer from 1 to 4 any remaining radicals being hydrogen; C. organic halides represented by the formula: R(X.sub.1).sub.m where R is alkane, alkene or alkyne having from two to three carbon atoms, each X 1 is independently a primary, secondary or tertiary halide and m is an integer of from 1 to about 8 consistent with the number of carbon atoms of said structure: and D. hydrogen halides; or mixtures thereof to thereby enhance the selectivity of the catalyst for the production of maleic anhydride.

Claim 19

The process of claim 15 further characterized in that said catalyst complex contains a metal promoter selected from the group consisting of zinc, copper, bismuth, lithium or mixtures thereof, the atomic ratio of phosphorous to vanadium being from about 1 to about 1.5.

Claim 20

The process of claim 16 further characterized in that said metal promoter comprises zinc.

Claim 21

The process of claim 16 further characterized in that said reactivating agent comprises carbon tetrachloride.

Claim 22

The process of claim 16 further characterized in that said reactivating conditions include addition of reactivating agent to the feed material.

Claim 23

The process of claim 16 further characterized in that said reactivating conditions include contacting a gaseous stream containing said reactivating agent in the absence of molecular oxygen with said catalyst complex.

Claim 24

The process of claim 16 further characterized in that said reactivating agent is selected from the group consisting of CCl 4 , CHCl 3 , CH 2 Cl 2 , CH 3 Cl, CF 4 , HCl, Cl 2 , trichloroacetic acid and mixtures thereof.

Claim 25

The process of claim 10 further characterized in that said reactivating agent is CCl 4 .

Claim 26

The process of claim 14 further characterized in that said reactivating agent is CCl 4 .

Claim 27

The process of claim 15 further characterized in that said reactivating agent comprises CCl 4 .

Claim 28

The process of claim 15 further characterized in that said reactivating conditions include contacting a gaseous stream containing said reactivating agent in the absence of butane with said catalyst complex.

Claim 29

The process of claim 15 further characterized in that said reactivating conditions include contacting a gaseous stream containing said reactivating agent in the absence of butane and molecular oxygen with said catalyst complex.

Claim 30

In a process for the preparation of maleic anhydride which comprises contacting a feed material comprising butane and a gas containing molecular oxygen in the vapor phase with a solid catalyst comprising a phosphorus-vanadium-oxygen complex, said catalyst complex having from about 0.5 to about 5 atoms of phosphorus for each atom of vanadium wherein the improvement comprises contacting said catalyst complex at reactivating conditions including the absence of feed butane with an effective amount of a reactivating agent containing a material selected from the group consisting of: A. molecular halogens; B. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: C(X).sub.n where each X is a selected halide and n is an integer from 1 to 4 any remaining radicals being hydrogen; C. organic halides represented by the formula: R(X.sub.1).sub.m where R is alkane, alkene or alkyne having from two to three carbon atoms, each X 1 is independently a primary, secondary or tertiary halide and m is an integer of from 1 to about 8 consistent with the number of carbon atoms of said structure; and D. hydrogen halides; or mixtures thereof to thereby enhance the selectivity of the catalyst for the production of maleic anhydride.

Claim 31

In a process for the preparation of maleic anhydride which comprises contacting a feed material comprising butane and a gas containing molecular oxygen in the vapor phase with a solid catalyst comprising a phosphorus-vanadium-oxygen complex, said catalyst complex having from about 0.5 to about 5 atoms of phosphorus for each atom of vanadium wherein the improvement comprises contacting said catalyst complex at reactivating conditions including the absence of feed butane with an effective amount of a reactivating agent containing a material selected from the group consisting of: A. molecular halogens; B. organic halides being in the vapor state above about 250° C. at atmospheric pressure represented by the formula: C(X).sub.n where each X is a selected halide and n is an integer from 1 to 4 any remaining radicals being hydrogen; C. organic halides represented by the formula: R(X.sub.1).sub.m where R is alkane, alkene or alkyne having from two to three carbon atoms, each X 1 is independently a primary, secondary or tertiary halide and m is an integer of from 1 to about 8 consistent with the number of carbon atoms of said structure; and D. hydrogen halides; or mixtures thereof to thereby enhance the selectivity of the catalyst for the production of maleic anhydride.

Claim 32

The process of claim 27 further characterized in that said catalyst complex contains a metal promoter selected from the group consisting of zinc, copper, bismuth, lithium or mixtures thereof, the atomic ratio of phosphorus to vanadium being from about 1 to about 1.5.

Claim 33

The process of claim 28 further characterized in that said metal promoter comprises zinc.

Claim 34

The process of claim 28 further characterized in that said reactivating agent comprises carbon tetrachloride.

Claim 35

The process of claim 27 further characterized in that said reactivating conditions include a temperature of less than about 400° C.

Claim 36

The process of claim 27 further characterized in that said reactivating conditions include a temperature in the range of from about 300° to about 500° C.

Claim 37

The process of claim 32 further characterized in that said reactivating conditions include a steam treatment following contact of said catalyst with reactivating agent.

Claim 38

The process of claim 1 further characterized in that said reactivating conditions include a temperature of less than about 400° C.

Claim 39

The process of claim 1 further characterized in that said reactivating conditions include a temperature in the range of from about 300° to about 500° C.

Claim 40

The process of claim 35 further characterized in that said reactivating conditions include a steam treatment following contact of said catalyst with reactivating agent.

Claim 41

The process of claim 10 further characterized in that said reactivating conditions include a temperature of less than about 400° C.

Claim 42

The process of claim 10 further characterized in that said reactivating conditions include temperature in the range of from about 300° to about 500° C.

Claim 43

The process of claim 38, further characterized in that said reactivating conditions include a steam treatment following contact of said catalyst with reactivating agent.

Claim 44

The process of claim 15 further characterized in that said reactivating conditions include a temperature of less than about 400° C.

Claim 45

The process of claim 15 further characterized in that said reactivating conditions include a temperature in the range of from about 300° to about 500° C.

Claim 46

The process of claim 41 further characterized in that said reactivating conditions include a steam treatment following contact of said catalyst with reactivating agent.

Claim 47

The process of claim 1 further characterized in that said reactivating agent is selected from the group consisting of CCl 4 , CHCl 3 , CH 2 Cl 2 , HCl, Cl 2 , CH 3 Cl or mixtures thereof.

Claim 48

The process of claim 1 further characterized in that said reactivating agent comprises carbon tetrachloride.

Claim 49

The process of claim 12 further characterized in that said reactivating agent is selected from the group consisting of CCl 4 , CHCl 3 , CH 2 Cl 2 , HCl, Cl 2 , CH 3 Cl or mixtures thereof.

Claim 50

The process of claim 17 further characterized in that said reactivating agent is selected from the group consisting of CCl 4 , CHCl 3 , CH 2 Cl 2 , HCl, Cl 2 , CH 3 Cl or mixtures thereof.

Claim 51

The process of claim 29 further characterized in that said reactivating agent is selected from the group consisting of CCl 4 , CHCl 3 , CH 2 Cl 2 , HCl, Cl 2 , CH 3 Cl or mixtures thereof.

Claim 52

The process of claim 29 further characterized in that said reactivating agent comprises carbon tetrachloride.