Method for producing at least one of α, β-unsaturated aldehyde and α, β-unsaturated carboxylic acid
View Patent ↗Disclosed is a method for producing at least one of an α,β-unsaturated aldehyde and an α,β-unsaturated carboxylic acid from an alcohol in a liquid phase through a simple process. Namely, at least one of an α,β-unsaturated aldehyde and an α,β-unsaturated carboxylic acid is produced by dehydrating and oxidizing an alcohol in a liquid phase at 110 to 250° C. in the presence of molecular oxygen and a noble metal-containing catalyst. Alternatively, at least one of an α,β-unsaturated aldehyde and an α,β-unsaturated carboxylic acid is produced by dehydrating and oxidizing an alcohol in a liquid phase in the presence of molecular oxygen, a noble metal-containing catalyst, and an acidic substance.
1. A method, which comprises
dehydrating and oxidizing an alcohol in a liquid phase, in one vessel, in the presence of molecular oxygen and a noble metal-comprising catalyst at a temperature in the range of 110 to 250° C., thereby obtaining at least one of an α,β-unsaturated aldehyde and an α,β-unsaturated carboxylic acid from the alcohol.
2. A method, which comprises
dehydrating and oxidizing an alcohol in a liquid phase, in one vessel, in the presence of molecular oxygen, a noble metal-comprising catalyst, and an acidic substance having a H 0 , a Hammett Acidity Function, of not higher than +4.8, thereby obtaining at least one of an α,β-unsaturated aldehyde and an α,β-unsaturated carboxylic acid from the alcohol.
3. The method according to claim 1 , wherein said dehydrating and oxidizing are carried out simultaneously.
4. The method according to claim 2 , wherein said dehydrating and oxidizing are carried out simultaneously.
5. The method according to claim 1 , wherein said alcohol is at least one member selected from the group consisting of isopropanol, t-butanol, and n-butanol.
6. The method according to claim 2 , wherein said alcohol is at least one member selected from the group consisting of isopropanol, t-butanol, and n-butanol.
7. The method according to claim 1 , wherein said alcohol is t-butanol.
8. The method according to claim 2 , wherein said alcohol is t-butanol.
9. The method according to claim 1 , wherein said noble metal-comprising catalyst comprises at least one noble metal selected from the group consisting of palladium, platinum, rhodium, ruthenium, iridium, gold, silver, and osmium.
10. The method according to claim 2 , wherein said noble metal-comprising catalyst comprises at least one noble metal selected from the group consisting of palladium, platinum, rhodium, ruthenium, iridium, gold, silver, and osmium.
11. The method according to claim 1 , wherein said noble metal-comprising catalyst comprises at least one noble metal selected from the group consisting of palladium, platinum, rhodium, ruthenium, iridium, gold, silver, and osmium, where the at least one noble metal is present in the noble metal-comprising catalyst in an amount of at least 50% by mass.
12. The method according to claim 2 , wherein said noble metal-comprising catalyst comprises at least one noble metal selected from the group consisting of palladium, platinum, rhodium, ruthenium, iridium, gold, silver, and osmium, where the at least one noble metal is present in the noble metal-comprising catalyst in an amount of at least 50% by mass.
13. The method according to claim 2 , wherein said acidic substance is at least one member selected from the group consisting of a sulfuric acid, a phosphoric acid, phosphomolybdic acid, a salt of phosphomolybdic acid, phosphotungstic acid, a salt of phosphotungstic acid, silicomolybdic acid, a salt of silicomolybdic acid, silicotungstic acid, a salt of silicotungstic acid, silica, alumina, silica-alumina, γ-alumina, zirconia, and titania, a HY zeolite and mordenite, and an acidic ion-exchange resin.
14. The method according to claim 1 , wherein said noble metal-comprising catalyst is present on a carrier that has a specific surface area of from 100 to 5,000 m 2 /g.
15. The method according to claim 2 , wherein said noble metal-comprising catalyst is present on a carrier that has a specific surface area of from 100 to 5,000 m 2 /g.
16. The method according to claim 1 , wherein said dehydrating and oxidizing are carried out a pressure of from 0 to 10 MPa.
17. The method according to claim 2 , wherein said dehydrating and oxidizing are carried out a pressure of from 0 to 10 MPa.
18. The method according to claim 1 , wherein said dehydrating and oxidizing are carried out a pressure of from 2 to 7 MPa.
19. The method according to claim 2 , wherein said dehydrating and oxidizing are carried out a pressure of from 2 to 7 MPa.
20. The method according to claim 2 , wherein
said alcohol is t-butanol,
said noble metal-comprising catalyst comprises palladium and is present on a silica support,
said acidic substance comprises silica, and
a product obtained by said dehydrating and oxidizing comprises methacrolein and methacrylic acid.