초록

Alkanes are oxidised to oxygenates such as carboxylic acids with molecular oxygen employing a two component catalyst system which uses a liganded heavy metal compound and a mixed metal oxide.

대표청구항 ▼

The invention claimed is: 1. A process for the oxidation of C1 to C5 alkanes comprising contacting the alkane with oxygen in the presence of a two component catalyst system said system comprising a first component which comprises a ligand co-ordinated heavy metal, where the heavy metal is selected

The invention claimed is: 1. A process for the oxidation of C1 to C5 alkanes comprising contacting the alkane with oxygen in the presence of a two component catalyst system said system comprising a first component which comprises a ligand co-ordinated heavy metal, where the heavy metal is selected from palladium, platinum, osmium, rhenium, indium, rhodium, ruthenium and gold and mixtures thereof, and the ligand is selected from N,N,N,N-tetramethylethylenediamine, bipyridine, 2,6-bis[1-2,6-di-I-propylphenyl-imino)ethyl]pyridine, 2,2161,211 terpyridine and 1,2 bis (dimethyl phosphino) ethane and mixtures thereof; and a second component which comprises a mixed metal oxide, where the mixed metal oxide comprises a calcined composition of Moa, Vb, Gac, Pdd, Nbe, and Xf, wherein X=at least one element selected from the group consisting of La, Te, Ge, Zn, Si, In and W; a is 1; b is 0.01 to 0.9; c is >0 to 0.2; d is 0.0000001 to 0.2; e is >0 to 0.2; and f is >0 to 0.5. 2. A process according to claim 1 in which the reaction is performed in the gas phase. 3. A process according to claim 1 in which the reaction is perfonned in the liquid phase which may be solution or slurry. 4. A process according to claim 1 in which the oxygen containing product is molecular oxygen provided as air. 5. A process according to claim 1 in which the reaction is perfonned at a temperature in the range 150째 C. to 450째 C. 6. A process according claim 1 in which the two componcnt catalyst system used in the present invention is a mixed catalyst system. 7. A process according to claim 1 in which the catalyst system comprises two separate catalysts and the alkane is initially exposed to die liganded heavy metal component. 8. A process according to claim 1 performed in a single reactor with a stacked bed catalyst wherein the alkane first passes through the bed of the liganded heavy metal component and then through the bed of the mixed metal oxide catalyst together with the oxygen source. 9. A process according to claim 8 in which the oxygen source is fed into the reactor together with the alkane. 10. A process according to claim 8 in which some or all of the oxygen is introduced into the reactor towards or at the end of the bed or the liganded heavy metal component. 11. A process according to claim 1 in which the ligand is selected from bidentate and tridentate heteroatom containing ligands. 12. A process according to claim 1 in which the tiganded heavy metal components of the catalyst system is employed on a support. 13. A process according to claim 12 in which the support is selected from alumina, silica, titania, zirconia and mixed metal oxides. 14. A process according to claim 1 in which the two component catalyst system is prepared by reacting supported metal oxides selected from the aroup consisting of oxides of manganese, iron and cobalt with the liganded heavy-metal compounds. 15. A process according to claim 1 in which the mixed metal oxide exhibits the following five main diffraction peaks at specific diffraction angles 2θ in the x-ray diffraction pattern of the mixed metal oxide (as measured by using Cu-Kα ray as the X-ray source). X-ray lattice plane Diffraction angle 2θ Spacing (짹0.3) medium (A) Relative intensity 22.1 4.02 100 28.2 3.16 20-150 36.2 2.48 5-60 45.2 2.00 2-40 50.0 1.82 2-40. 16. A process according to claim 1 in which the liganded heavy metal is present in an amount such that the finished supported catalyst contains greater than 0.005 wt % and less than 2 wt % heavy metal in the finished catalyst. 17. A process according to claim 1 in which the alkane is propane. 18. A process according to claim 17 in which the soPrce of the propane is a gas stream which contains at least three volume percent of propane or a mixture of propylene and propane and less than thirty vohune percent of C1 or C5 alkanes. 19. A process according to claim 17 in which the gas stream also contains more than five volume percent of diluents selected from nitrogen, argon, carbon dioxide and water in the form of steam and mixtures thereof. 20. A process according to claim 17 in which the reaction mixture contains one mole of propane, 0.01 to 2.0 moles of molecular oxygen either as pure oxygen or in the form of air, and zero to 4.0 moles of water in the fonn of steam. 21. A process according to claim 1 in which the oxygen source comprises purified oxygen, air or oxygen-enriched air. 22. A process according to claim 1 in which the ratio of alicane to oxygen is in the range of 1/5 to 5/1. 23. A process according to claim 1 in which the reaction is affected in the presence of one or more diluents selected from the group consisting of argon, nitrogen and steam. 24. A process according to claim 23 in which the ratio of propane to diluents is in the range of 1/5-1/1. 25. A process according to claim 1 in which the water vapour or steam is used as a reaction diluent and as a heat moderator for the reaction. 26. A process according to claim 1 in which the gaseous components of the reaction mixture are uniformly admixed prior to being introduced into the reaction zone. 27. A process according to claim 1 in which the gaseous components are preheated individually or after being admixed, prior to being introduced into the reaction zone. 28. A process according to claim 1 in which the reaction zone has a pressure of from 1 to 50 bar, a temperature of from about 150째 C. to about 450째 C., and the contact time between the reaction mixture and the catalyst is from about 0.01 second to 100 seconds, at a space hourly velocity of from about 50 to about 50,000 h-1. 29. A process according to claim 1 in which the process is carried out in a single stage with all the oxygen and reactants being supplied as a single feed with non-reacted initial reactants being recycled. 30. A process according to claim 1 in which a multiple stage addition of oxygen or hydrocarbon to the reactor is used. 31. A process according to claim 1 in which recycling of un-reacted gases with purge mode is applied. 32. A process according to claim 1 comprising oxidizing C1-C5 alkanes to produce carboxylic acids. 33. A process for the oxidation of C1 to C5 alkanes comprising contacting the alkane with oxygen in the presence of a two component catalyst system said system comprising a first component which comprises a ligand co-ordinated heavy metal, where the heavy metal is selected from palladium, platinum, osmium, rhenium, indium, rhodium, ruthenium and gold and mixtures thereof, and the ligand is selected from N,N,N,N-tetramethylethylenediamine, bipyridine, 2,6-bis[1-2,6-di-I-propylphenyl-imino)ethyl]pyridine, 2,2161,211 terpyridine and 1,2 bis (dimethyl phosphino) ethane and mixtures thereof; and a second component which comprises a mixed metal oxide, where the mixed metal oxide comprises Mo, V, Te, O and X wherein X is at least one element selected from the group consisting of niobium, tantalum, tungsten, titanium, alumium, zirconium, chromium, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, platinum, antimony, bismuth, boron, indium, and cerium. 34. A process according to claim 33 in which the mixed metal oxide exhibits the following five main diffraction peaks at specific diffraction angles 2θ in the x-ray diffraction pattern of the i-nixed metal oxide (as measured by using Cu-Kα ray as the X-ray source). X-ray lattice plane Diffraction angle 2θ Spacing (짹0.3) medium (A) Relative intensity 22.1 4.02 100 28.2 3.16 20-150 36.2 2.48 5-60 45.2 2.00 2-40 50.0 1.82 2-40. 35. A process according to claim 33 in which the reaction zone has a pressure of from 1 to 50 bar, a temperature of from about 150째 C. to about 450째 C., and the contact time between the reaction mixture and the catalyst is from about 0.01 second to 100 seconds, at a space hourly velocity of from about 50 to about 50,000 h-1. 36. A process according to claim 33 performed in a single reactor with a stacked bed catalyst wherein the alkane first passes through the bed of the liganded heavy metal component and then through the bed of the mixed metal oxide catalyst together with the oxygen source. 37. A process according to claim 36 in which the oxygen source is fed into the reactor together with the alkane. 38. A process according to claim 36 in which some or all of the oxygen is introduced into the reactor towards or at the end of the bed of die liganded heavy metal component. 39. A process according to claim 33 in which die alkane is propane.