Preparation of propane oxidation catalysts
US-9517451-B2 · Dec 13, 2016 · US
US9492814B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9492814-B2 |
| Application number | US-201414783218-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 7, 2014 |
| Priority date | Apr 8, 2013 |
| Publication date | Nov 15, 2016 |
| Grant date | Nov 15, 2016 |
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In accordance with the invention, there is provided a novel catalyst composition comprising MoVGaPdNbXY, wherein X comprises La, Te, Ge, Zn, In, or W; and Y comprises Al or Si; wherein Mo, V, Ga, Pd, Nb, La, Te, Ge, Zn, In, W, Al, or Si are optionally present in combination with oxygen; wherein the catalyst does not comprise an additional element that acts as a catalyst in the conversion of a propylene to the product. Also, disclosed is a method for the conversion of a propylene to a carboxylic acid moiety by contacting the propylene with the disclosed catalyst.
Opening claim text (preview).
What is claimed is: 1. A catalyst for the conversion of propylene to a product comprising a carboxylic acid moiety, wherein the catalyst comprises: MoVGaPdNbXY, wherein X is La, Te, Ge, Zn, In, or W; and Y is Al or Si; wherein one or more of Mo, V, Ga, Pd, Nb, La, Te, Ge, Zn, In, W, Al, and/or Si are optionally present in combination with oxygen; wherein the product does not comprise substantially any acrolein. 2. The catalyst of claim 1 , wherein the product does not comprise any acrolein. 3. A catalyst for the conversion of propylene to a product comprising a carboxylic acid moiety, wherein the catalyst consists essentially of: MoVGaPdNbXY, wherein X is La, Te, Ge, Zn, In, or W; and Y is Al or Si; wherein Mo, V, Ga, Pd, Nb, La, Te, Ge, Zn, In, W, Al, and/or Si are optionally present in combination with oxygen; and wherein the product does not comprise substantially any acrolein. 4. The catalyst of claim 3 , wherein the catalyst is present on a support. 5. The catalyst of claim 3 , wherein the catalyst comprises: Mo a V b Ga c Pd d Nb e X f Y g wherein a is 1; b is present in an amount that ranges from 0.01 to 0.90; c is present in an amount that ranges from greater than 0 to 0.20; d is present in an amount that ranges from 0.0000001 to 0.20; e is present in an amount that ranges from greater than 0 to 0.20; f is present in an amount that ranges from greater than 0 to 0.80; and g is present in an amount that ranges from greater than 0.50 to 0.90; wherein the numerical values of a, b, c, d, e, f, and g represent the relative gram-atom ratios of the elements in the catalyst. 6. The catalyst of claim 3 , wherein the product comprises acetic acid, acrylic acid, or propanoic acid, or a combination thereof. 7. The catalyst composition of claim 3 , wherein the catalyst converts the propylene to the product comprising the carboxylic acid moiety in a single stage. 8. A method for the conversion of propylene to a product comprising a carboxylic acid moiety, wherein the method comprises: contacting the propylene with a catalyst, wherein the catalyst comprises: MoVGaPdNbXY, wherein X is La, Te, Ge, Zn, In, or W; and Y is Al or Si; wherein Mo, V, Ga, Pd, Nb, La, Te, Ge, Zn, In, W, Al, and/or Si are optionally present in combination with oxygen; and wherein the product does not comprise substantially any acrolein. 9. The method of claim 8 , wherein the product comprises acetic acid, acrylic acid, or propanoic acid, or a combination thereof. 10. The method of claim 8 , wherein the method does not comprise an additional catalyst. 11. The method of claim 8 , wherein the method comprises a single stage process with a single catalyst. 12. The catalyst of claim 1 , wherein the catalyst is present on a support. 13. The catalyst of claim 1 , wherein the catalyst comprises: Mo a V b Ga c Pd d Nb e X f Y g wherein a is 1; b is present in an amount that ranges from 0.01 to 0.90; c is present in an amount that ranges from greater than 0 to 0.20; d is present in an amount that ranges from 0.0000001 to 0.20; e is present in an amount that ranges from greater than 0 to 0.20; f is present in an amount that ranges from greater than 0 to 0.80; and g is present in an amount that ranges from greater than 0.50 to 0.90; wherein the numerical values of a, b, c, d, e, f, and g represent the relative gram-atom ratios of the elements in the catalyst. 14. The catalyst of claim 1 , wherein the product comprises acetic acid, acrylic acid, or propanoic acid, or a combination thereof. 15. The catalyst of claim 1 , wherein the catalyst converts the propylene to the product comprising the carboxylic acid moiety in a single stage. 16. The catalyst of claim 1 , wherein less than 1% of acrolein is formed in the product using the catalyst. 17. The catalyst of claim 3 , wherein less than 1% of acrolein is formed in the product using the catalyst. 18. The method of claim 8 , wherein less than 1% of acrolein is formed in the product using the catalyst.
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