Method for oxidizing hydrocarbons in liquid phase
View Patent ↗A method of oxidizing hydrocarbons in liquid phase is provided. According to this method, a liquid-phase oxidation reaction of hydrocarbons is carried out by using an organic compound capable of chelating metals as auxiliary agent, represented by formula (II), in the presence of an oxygen-containing gas and a transition metal catalyst. Accordingly, the conversion degree of the hydrocarbon is increased, and the overall yields of products are improved while the selectivity of catalytic oxidation reaction is still high.
1. A method for oxidizing hydrocarbon in liquid phase, comprising using a compound represented by formula (II) as an auxiliary agent to perform a liquid-phase oxidation reaction of the hydrocarbon in presence of an oxygen-containing gas and a cobalt halide as a catalyst:
wherein R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 and R 13 are independently selected from the group consisting of hydrogen, halogen, nitro, cyano, hydroxy, carbonyl, carboxyl, amino, amido, C 1 -6 alkyl, C 1-6 alkoxy, C 3-12 cycloalkyl, C 3-12 cycloalkoxy, C 3-12 cycloalkanoyl, C 6-20 aryl, C 7-20 arylalkyl, and C 7-20 alkylaryl, or R 6 and R 7 , R 7 and R 8 , R 8 and R 9 , R 10 and R 11 , R 11 and R 12 , or R 12 and R 13 are joined mutually to form an aromatic or non-aromatic ring, which is optionally substituted with halogen, nitro, cyano, hydroxy, carbonyl, carboxyl, amino, and/or amido, wherein the C 1-6 alkyl, C 1-6 alkoxy, C 3-12 cycloalkyl, C 3-12 cycloalkoxy, C 3-12 cycloalkanoyl, C 6-20 aryl, C 7-20 arylalkyl, and C 7-20 alkylaryl are optionally substituted with halogen, nitro, cyano, hydroxy, carbonyl, carboxyl, amino, and/or amido, and R 14 represents chemical bond, oxy, ester group, ketone group, pyridonyl, C 1-6 alkyl, C 1-6 alkenyl, C 1-6 alkylamino, C 1-6 alkoxy, C 1-6 alkanoyl, C 3-12 cycloalkyl, C 6-20 aryl, C 7-20 arylalkyl, or C 7-20 alkylaryl, wherein the C 1-6 alkyl and C 1-6 alkenyl are optionally substituted with halogen, nitro, cyano, hydroxy, carbonyl, carboxyl, amino, and/or amido.
2. The method according to claim 1 , wherein the R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 and R 13 are independently selected from the group consisting of hydrogen, halogen, nitro, cyano, and carboxyl, or R 6 and R 7 , R 7 and R 8 , R 8 and R 9 , R 10 and R 11 , R 11 and R 12 , or R 12 and R 13 are joined mutually to form an aromatic or non-aromatic ring, which is optionally substituted with halogen, nitro, cyano, and/or carboxyl, and R 14 represents chemical bond, oxy, ester group, ketone group, pyridonyl, C 1-6 alkyl, or C 1-6 alkenyl, wherein the C 1-6 alkyl and C 1-6 alkenyl are optionally substituted with halogen, nitro, hydroxy, and/or amino.
3. The method according to claim 1 , wherein the hydrocarbon is cycloalkane with 3 to 12 carbon atoms.
4. The method according to claim 3 , wherein the hydrocarbon is cyclohexane.
5. The method according to claim 1 , wherein the catalyst is cobaltous chloride hexahydrate.
6. The method according to claim 1 , wherein the catalyst has a concentration of from 0.1 to 100 ppm by weight based on cobalt metal ions.
7. The method according to claim 6 , wherein the catalyst has a concentration of from 0.5 to 20 ppm by weight based on cobalt metal ions.
8. The method according to claim 1 , wherein the catalyst to the auxiliary agent has a molar ratio of from 1:0.05 to 1:10.
9. The method according to claim 8 , wherein the catalyst to the auxiliary agent has a molar ratio of from 1:0.1 to 1:8.
10. The method according to claim 1 , wherein the oxidation reaction is performed at a pressure of from 4 to 20 kg/cm 2 .
11. The method according to claim 10 , wherein the oxidation reaction is performed at a pressure of from 6 to 14 kg/cm 2 .
12. The method according to claim 1 , wherein the oxidation reaction is performed at a temperature of from 120 to 180° C.
13. The method according to claim 12 , wherein the oxidation reaction is performed at a temperature of from 145 to 170° C.
14. A method for oxidizing hydrocarbon in liquid phase, comprising using a compound represented by formula (III) as an auxiliary agent to perform a liquid-phase oxidation reaction of the hydrocarbon in presence of an oxygen-containing gas and a cobalt halide as a catalyst:
wherein R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 and R 13 are independently selected from the group consisting of hydrogen, halogen, nitro, cyano, hydroxy, carbonyl, carboxyl, amino, amido, C 1 -6 alkyl, C 1-6 alkoxy, C 3-12 cycloalkyl, C 3-12 cycloalkoxy, C 3-12 cycloalkanoyl, C 6-20 aryl, C 7-20 arylalkyl, and C 7-20 alkylaryl, or R 6 and R 7 , R 7 and R 8 , R 8 and R 9 , R 9 and R 10 , R 10 and R 11 , R 11 and R 12 , or R 12 and R 13 are joined mutually to form an aromatic or non -aromatic ring, which is optionally substituted with halogen, nitro, cyano, hydroxy, carbonyl, carboxyl, amino, and/or amido, wherein the C 1-6 alkyl, C 1-6 alkoxy, C 3-12 cycloalkyl, C 3-12 cycloalkoxy, C 3-12 cycloalkanoyl, C 6-20 aryl, C 7-20 arylalkyl, and C 7-20 alkylaryl are optionally substituted with halogen, nitro, cyano, hydroxy, carbonyl, carboxyl, amino, and/or amido.
15. The method according to claim 14 , wherein the R 6 , R 7 , R 8 , R 9 , R 10 , R 11 , R 12 and R 13 are independently selected from the group consisting of hydrogen, halogen, nitro, cyano, and carboxyl, or R 6 and R 7 , R 7 and R 8 , R 8 and R 9 , R 9 and R 10 , R 10 and R 11 , R 11 and R 12 , or R 12 and R 13 are joined mutually to form an aromatic or non-aromatic ring, which is optionally substituted with halogen, nitro, cyano, and/or carboxyl.
16. The method according to claim 14 , wherein the hydrocarbon is cycloalkane with 3 to 12 carbon atoms.
17. The method according to claim 16 , wherein the hydrocarbon is cyclohexane.
18. The method according to claim 14 , wherein the catalyst is cobaltous chloride hexahydrate.
19. The method according to claim 14 , wherein the catalyst has a concentration of from 0.1 to 100 ppm by weight based on cobalt metal ions.
20. The method according to claim 19 , wherein the catalyst has a concentration of from 0.5 to 20 ppm by weight based on cobalt metal ions.
21. The method according to claim 14 , wherein the catalyst to the auxiliary agent has a molar ratio of from 1:0.05 to 1:10.
22. The method according to claim 21 , wherein the catalyst to the auxiliary agent has a molar ratio of from 1:0.1 to 1:8.
23. The method according to claim 14 , wherein the oxidation reaction is performed at a pressure of from 4 to 20 kg/cm 2 .
24. The method according to claim 23 , wherein the oxidation reaction is performed at a pressure of from 6 to 14 kg/cm 2 .
25. The method according to claim 14 , wherein the oxidation reaction is performed at a temperature of from 120 to 180° C.
26. The method according to claim 25 , wherein the oxidation reaction is performed at a temperature of from 145 to 170° C.