Method for producing methylmethacrylate
US-2016068464-A1 · Mar 10, 2016 · US
US9969672B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9969672-B2 |
| Application number | US-201515521750-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 7, 2015 |
| Priority date | Oct 31, 2014 |
| Publication date | May 15, 2018 |
| Grant date | May 15, 2018 |
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A process for the preparation of MMA via oxidative esterification in the presence of a catalyst comprising palladium, bismuth, and antimony.
Opening claim text (preview).
What is claimed is: 1. A process for the preparation of methyl methacrylate (MMA) via oxidative esterification, the process comprising contacting methacrolein, methanol, and an oxygen-containing gas in a reaction zone in the presence of a catalyst comprising palladium, bismuth, and antimony under reaction conditions sufficient to produce MMA. 2. The process of claim 1 wherein the catalyst is a heterogeneous catalyst comprising a catalytic metal on a porous carrier or support, where the catalytic metal comprises palladium, bismuth, and antimony. 3. The process of any of claim 1 wherein the weight ratio of palladium to bismuth in the catalyst is from 20:1 to 1:10. 4. The process of claim 1 wherein the weight ratio of Sb to bismuth is from 100:1 to 1:10. 5. The process of claim 1 wherein the catalyst is a supported catalyst and the support comprises at least one of activated carbon, magnesium oxide, zinc oxide, titanium oxide, calcium carbonate, silica-alumina, alumina-silica, silica or alumina. 6. The process of claim 1 wherein the catalyst is a supported catalyst and the amount of the catalytic metal on the support is from 0.1 to 20% by weight, based on the weight of the support. 7. The process of claim 1 wherein the catalyst is a supported catalyst and the surface area of the catalyst is at least 50 m 2 /g. 8. The process of claim 1 wherein the catalyst is a supported catalyst and the median particle size of the supported catalyst is from 1 to 200 microns. 9. The process of claim 1 wherein the catalyst is a supported catalyst and the support comprises at least one of alumina and silica. 10. The process of claim 1 wherein the catalyst is a supported catalyst and the support comprises silica modified with magnesia. 11. The process of claim 1 wherein the catalyst is a supported catalyst and the support comprises primarily silica. 12. The process of claim 1 wherein the catalyst is a supported catalyst and the support is modified with alumina, magnesia, or a combination thereof. 13. The process of claim 1 wherein the weight ratio of palladium to bismuth in the catalyst is from 5:1 to 1:1, and the weight ratio of Sb to bismuth is from 1:1 to 1:4. 14. The process of claim 1 wherein the weight ratio of the catalyst in the reaction zone to methacrolein fed to the reaction zone is from 1:1000 to 20:1. 15. The process of claim 1 wherein the temperature in the reaction zone is from 0° C. to 120° C., and the pressure in the reaction zone is from 50 to 2000 kPa (7.3 to 290 psia).
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