Method of producing epsilon-caprolactam

Patent metadata

Field	Value
Publication number	US-10364218-B2
Application number	US-201615758664-A
Country	US
Kind code	B2
Filing date	Sep 8, 2016
Priority date	Sep 11, 2015
Publication date	Jul 30, 2019
Grant date	Jul 30, 2019

Abstract

A method of producing ε-caprolactam from 3-oxoadipic acid includes: step 1 of mixing at least one selected from the group consisting of 3-oxoadipic acid and salts thereof with a catalyst and a solvent in the presence of hydrogen to produce 3-hydroxyadipic acid; and step 2 of reacting the 3-hydroxyadipic acid which is a product of step 1, a salt or carboxylic acid derivative thereof, or a mixture of these with hydrogen and ammonia.

First claim

The invention claimed is:

1. A method of producing ε-caprolactam, comprising: step 1 of mixing at least one selected from the group consisting of 3-oxoadipic acid and salts thereof with a catalyst and a solvent in the presence of hydrogen to produce 3-hydroxyadipic acid; and step 2 of reacting the 3-hydroxyadipic acid which is a product of step 1, a salt or carboxylic acid derivative thereof, or a mixture thereof with hydrogen and ammonia.

2. The method according to claim 1 , wherein the solvent is an aqueous solvent or an organic solvent having a polarity value of 0 to 0.3.

3. The method according to claim 1 , wherein the solvent is an organic solvent containing more than 50 vol % of at least one selected from the group consisting of ether solvents and ester solvents.

4. The method according to claim 1 , wherein the solvent is an organic solvent containing more than 50 vol % of at least one selected from tetrahydrofuran, dioxane, 1,2-dimethoxyethane, diglyme, and ethyl acetate.

5. The method according to claim 1 , wherein step 1 is carried out under conditions of (i) or (ii):
(i) in an aqueous solvent at a reaction temperature of 0° C. to 50° C.;
(ii) in an organic solvent having a polarity value of 0 to 0.3 at a reaction temperature of not lower than 0° C. and lower than 75° C.

6. The method according to claim 1 , wherein step 2 is carried out in the presence of a catalyst.

7. The method according to claim 6 , wherein the catalyst used in step 2 comprises one or more metals selected from the group consisting of palladium, platinum, ruthenium, rhodium, rhenium, nickel, iridium, osmium, copper and chromium.

8. The method according to claim 1 , wherein the catalyst used in step 1 comprises one or more metals selected from the group consisting of palladium, platinum, ruthenium, rhodium, rhenium, nickel, iridium, osmium, copper, and chromium.

9. The method according to claim 8 , wherein the metal is supported on at least one support selected from the group consisting of alumina, carbon, silica, titania, zirconia, tantalum oxide, niobium oxide, and zeolite.

10. The method according to claim 1 , wherein the partial pressure of hydrogen in step 1 and step 2 is 0.1 MPa to 10 MPa at ordinary temperature in terms of gauge pressure.

11. The method according to claim 1 , wherein the reaction temperature in step 2 is 150° C. to 280° C.

12. The method according to claim 2 , wherein the solvent is an organic solvent containing more than 50 vol % of at least one selected from the group consisting of ether solvents and ester solvents.

13. The method according to claim 2 , wherein the solvent is an organic solvent containing more than 50 vol % of at least one selected from tetrahydrofuran, dioxane, 1,2-dimethoxyethane, diglyme, and ethyl acetate.

14. The method according to claim 2 , wherein step 1 is carried out under conditions of (i) or (ii):
(i) in an aqueous solvent at a reaction temperature of 0° C. to 50° C.;
(ii) in an organic solvent having a polarity value of 0 to 0.3 at a reaction temperature of not lower than 0° C. and lower than 75° C.

15. The method according to claim 2 , wherein step 2 is carried out in the presence of a catalyst.

16. The method according to claim 3 , wherein the solvent is an organic solvent containing more than 50 vol % of at least one selected from tetrahydrofuran, dioxane, 1,2-dimethoxyethane, diglyme, and ethyl acetate.

17. The method according to claim 3 , wherein step 1 is carried out under conditions of (i) or (ii):
(i) in an aqueous solvent at a reaction temperature of 0° C. to 50° C.;
(ii) in an organic solvent having a polarity value of 0 to 0.3 at a reaction temperature of not lower than 0° C. and lower than 75° C.

18. The method according to claim 3 , wherein step 2 is carried out in the presence of a catalyst.

19. The method according to claim 4 , wherein step 1 is carried out under conditions of (i) or (ii):
(i) in an aqueous solvent at a reaction temperature of 0° C. to 50° C.;
(ii) in an organic solvent having a polarity value of 0 to 0.3 at a reaction temperature of not lower than 0° C. and lower than 75° C.

20. The method according to claim 4 , wherein step 2 is carried out in the presence of a catalyst.

21. A method of producing 3-hydroxyadipic acid comprising mixing at least one selected from the group consisting of 3-oxoadipic acid and salts thereof with a catalyst in the presence of hydrogen under the conditions of (i) or (ii):
(i) in an aqueous solvent at a reaction temperature of 0° C. to 50° C.;
(ii) in an organic solvent having a polarity value of 0 to 0.3 at a reaction temperature of not lower than 0° C. and lower than 75° C.

Assignees

• Toray Industries

Inventors

• Tsukamoto Daijiro
• Ito Masateru
• Yamada Katsushige
• Yamashita Kohei
• Akahira Masato
• Yamauchi Koji

Classifications

• B01J23/464

  Rhodium · CPC title

• C07B61/00

  Other general methods · CPC title

• B01J23/468

  Iridium · CPC title

• B01J23/26

  Chromium · CPC title

• B01J23/42

  Platinum · CPC title