Method for the production of phenol and acetone
View Patent ↗A method for the production of phenol and acetone from a cumene hydroperoxide mixture comprises a first stage and a second stage and at least two serially connected reactors, wherein the first stage comprises decomposition of a cumene hydroperoxide mixture in the presence of a catalyst mixture to form a dicumyl peroxide mixture, and the second stage comprises formation of a phenol and acetone mixture from decomposition of the dicumyl peroxide mixture formed in the first stage, wherein, the first stage further comprises: a) forming a catalyst mixture by combining sulfuric acid and phenol in a weight ratio of from 2:1 to 1:1000 in a catalyst formation reactor, b) holding the catalyst mixture in the catalyst formation reactor at a temperature of about 20 to 80° C. for about 1 to 600 minutes; and, c) adding the catalyst mixture to the cumene hydroperoxide mixture to form the phenol and acetone mixture. The proposed method permits a significant reduction in the yield of hydroxyacetone that causes deterioration in the quality of commercial phenol.
1. A method for the production of phenol and acetone from a cumene hydroperoxide mixture comprising: a first stage and a second stage and at least two serially connected reactors, wherein the first stage comprises decomposition of a cumene hydroperoxide mixture in the presence of a catalyst mixture to form a dicumyl peroxide mixture, and the second stage comprises formation of a phenol and acetone mixture from decomposition of the dicumyl peroxide mixture formed in the first stage, wherein the first stage further comprises:
a) forming a catalyst mixture by combining sulfuric acid and phenol in a weight ratio of from 2:1 to 1:1000 in a catalyst formation reactor;
b) holding the catalyst mixture in the catalyst formation reactor at a temperature of about 20 to 80° C. for about 1 to 600 minutes; and,
c) adding the catalyst mixture to the cumene hydroperoxide mixture to form the phenol and acetone mixture.
2. The method of claim 1 , wherein the sulfuric acid is an aqueous sulfuric acid solution comprising at least 75 wt. % sulfuric acid.
3. The method of claim 1 , wherein the sulfuric acid is fuming sulfuric acid (oleum).
4. The method of claim 1 , wherein water is added in the second stage in an amount of up to 1% of the reaction mass.
5. The method of claim 1 , wherein the reaction temperature of the first stage is between 40 and 75° C., and wherein the reaction temperature of the second stage is between 90 and 140° C.
6. The method of claim 1 , wherein the sulfuric acid to phenol ratio is from 1:1 to 1:5.
7. The method of claim 1 , wherein the catalyst mixture in step b) is held at a temperature of from about 35 to 45° C.
8. The method of claim 1 , wherein the reaction time in step b) is from about 60 to about 300 minutes.
9. The method of claim 1 , wherein the first stage cleavage temperature is from about 40 to 70° C. and the second stage cleavage temperature is from about 110 to 135° C.
10. The method of claim 1 , wherein the sulfuric acid has a concentration of at least 90% sulfuric acid.
11. The method of claim 1 , wherein the phenol and acetone mixture formed has a reduced level of hydroxyacetone as compared to a phenol and acetone mixture formed using a catalyst that is only sulfuric acid.
12. A method for the production of phenol and acetone from a cumene hydroperoxide mixture comprising: a first stage and a second stage and at least two serially connected reactors, wherein the first stage comprises decomposition of a cumene hydroperoxide mixture in the presence of a catalyst mixture to form a dicumyl peroxide mixture, and the second stage comprises formation of a phenol and acetone mixture from decomposition of the dicumyl peroxide mixture formed in the first stage, wherein the first stage further comprises:
a) forming a catalyst mixture by combining sulfuric acid and phenol in a weight ratio of from 2:1 to 1:1000 in a catalyst formation reactor, wherein the sulfuric acid is an aqueous sulfuric acid solution comprising at least 75 wt. % sulfuric acid;
b) holding the catalyst mixture in the catalyst formation reactor at a temperature of about 20 to 80° C. for about 1 to 600 minutes; and
c) adding the catalyst mixture to the cumene hydroperoxide mixture to form the phenol and acetone mixture.
13. The method of claim 12 , wherein the sulfuric acid is fuming sulfuric acid (oleum).
14. The method of claim 12 , wherein the catalyst mixture in step b) is held at a temperature of from about 35 to 45° C.
15. The method of claim 12 , wherein the reaction time in step b) is from about 60 to about 300 minutes.
16. The method of claim 12 , wherein the phenol and acetone mixture formed has a reduced level of hydroxyacetone as compared to a phenol and acetone mixture formed using a catalyst that is only sulfuric acid.
17. A method for the production of phenol and acetone from a cumene hydroperoxide mixture comprising: a first stage and a second stage and at least two serially connected reactors, wherein the first stage comprises decomposition of a cumene hydroperoxide mixture in the presence of a catalyst mixture to form a dicumyl peroxide mixture, and the second stage comprises formation of a phenol and acetone mixture from decomposition of the dicumyl peroxide mixture formed in the first stage, wherein the first stage further comprises:
a) forming the catalyst mixture in a catalyst formation reactor by combining sulfuric acid and phenol in a weight ratio of from 2:1 to 1:1000, wherein the sulfuric acid is an aqueous sulfuric acid solution comprising at least 75 wt. % sulfuric acid;
b) holding the catalyst mixture in the catalyst formation reactor at a temperature of about 35 to 45° C. for about 60 to 300 minutes; and
c) adding the catalyst mixture to the cumene hydroperoxide mixture to form the phenol and acetone mixture,
wherein the phenol and acetone mixture formed has a reduced level of hydroxyacetone as compared to a phenol and acetone mixture formed using a catalyst that is only sulfuric acid.
18. The method of claim 17 , wherein the sulfuric acid is fuming sulfuric acid (oleum).
19. The method of claim 17 , wherein the first stage cleavage temperature is from about 40 to 70° C. and the second stage cleavage temperature is from about 110 to 135° C.