Method for preparing diamino-dicyclohexyl methane

Patent metadata

Field	Value
Publication number	US-9580380-B2
Application number	US-201314761890-A
Country	US
Kind code	B2
Filing date	Nov 22, 2013
Priority date	May 22, 2013
Publication date	Feb 28, 2017
Grant date	Feb 28, 2017

Abstract

Disclosed is a method for preparing diamino-dicyclohexyl methane (H 12 MDA) by hydrogenation of diamino-diphenyl methane (MDA). In the process, 4,4′-MDA used as the starting material is firstly hydrogenated to prepare 4,4′-H 12 MDA. When the activity of the catalyst is reduced, the feed is switched from 4,4′-MDA to the mixture of 2,4′-MDA and 4,4′-MDA, and then when the conversion is stabilized, the feed is switched to 4,4′-MDA again. The deactivated catalyst is activated on line by switching the feed to the mixture of 2,4′-MDA and 4,4′-MDA. 4,4′-H 12 MDA having the trans-trans isomer content of 16˜24 wt % is produced, and the mixture of 2,4′-H 12 MDA and 4,4′-H 12 MDA is also produced, wherein the content of 2,4′-H 12 MDA in the mixture is 4˜15 wt %.

First claim

The invention claimed is:

1. A continuous method for preparing diamino-dicyclohexyl methane, wherein said continuous method comprises the following steps:
1) 4,4′-diamino-diphenyl methane feed is hydrogenated in a reactor packed with catalyst to prepare 4,4′-diamino-dicyclohexyl methane at the conversion of 98-99.99%;
2) When the conversion in step 1) is 90-98%, the feed is switched from 4,4′-diamino-diphenyl methane to a mixture of 2,4′-diamino-diphenyl methane and 4,4′-diamino-diphenyl methane, and the hydrogenation reaction is continued to prepare 2,4′-diamino-dicyclohexyl methane and 4,4′-diamino-dicyclohexyl methane;
3) After the conversion of the mixture of 2,4′-diamino-diphenyl methane and 4,4′-diamino-diphenyl methane in step 2) is ≧90% and the reaction is lasted at said conversion for 20-40 h, the feed is switched from the mixture of 2,4′-diamino-diphenyl methane and 4,4′-diamino-diphenyl methane to 4,4′-diamino-diphenyl methane, and the hydrogenation reaction is continued to prepare 4,4′-diamino-dicyclohexyl methane.

2. The continuous method as claimed in claim 1 , wherein the 4,4′-diamino-diphenyl methane feed is composed of 98-100 wt % 4,4′-diamino-diphenyl methane, 0-2 wt % 2,4′-diamino-diphenyl methane, 0-1 wt % N-methyl-4,4′-diamino diphenyl methane, and 0-1 wt % other impurities, based on the total weight of the 4,4′-diamino-diphenyl methane feed.

3. The continuous method as claimed in claim 1 , wherein the mixture of 2,4′-diamino-diphenyl methane and 4,4′-diamino-diphenyl methane is composed of 83-95 wt % 4,4′-diamino-diphenyl methane, 3-16 wt % 2,4′-diamino-diphenyl methane, 0-1 wt % N-methyl-4,4′-diamino-diphenyl methane, and 0-1 wt % other impurities, based on the total weight of the mixture.

4. The continuous method as claimed in claim 1 , wherein said catalyst is a supported metal catalyst, wherein the metal is one or more selected from Group VIIIB metals, the support is one or more selected from rare earth, diatomaceous earth, alumina, activated carbon, lithium aluminate, spinel, titania, silica and silica-alumina oxides, and the weight ratio of the metal and the support is 1-10:100.

5. The continuous method as claimed in claim 1 , wherein said catalyst is a mixture of Rh/Al 2 O 3 and Ru/Al 2 O 3 , wherein the weight ratio of Rh/Ru is 1-50:1.

6. The continuous method as claimed in claim 5 , wherein the amount of Rh/Al 2 O 3 is 0.5-5 wt %, based on the total weight of the reaction solution in the reaction tank.

7. The continuous method as claimed in claim 1 , wherein the 4,4′-MDA feed is supplied in the presence of or in the absence of a solvent, and the concentration of 4,4′-MDA in the solution is 40-60 wt %.

8. The continuous method as claimed in claim 1 , wherein the mixture of 2,4′-MDA and 4,4′-MDA is supplied in the presence of or in the absence of a solvent, and the total concentration of 2,4′-MDA and 4,4′-MDA in the solution is 40-60 wt %.

9. The continuous method as claimed in claim 7 , wherein said solvent comprises one or more selected from cyclohexane, dioxane, tetrahydrofuran, cyclohexylamine, dicyclohexylamine, methanol, ethanol, isopropanol, n-butanol, 2-butanol and methyl cyclohexane.

10. The continuous method as claimed in claim 1 , wherein the productivity of the catalyst for 4,4′-diamino-diphenyl methane in the step 1) is 0.4-1 g MDA/g cat/min, and the productivity of the catalyst for the mixture of 2,4′-diamino-diphenyl methane and 4,4′-diamino-diphenyl methane in the step 2) is 0.4-1 g MDA/g cat/min; and the reaction temperature of hydrogenation is 100-190° C., and the absolute reaction pressure is 5-15 MPa.

11. The continuous method as claimed in claim 2 , wherein the 4,4′-diamino-diphenyl methane feed is composed of 99-100wt% 4,4′-diamino-diphenyl methane, 0-1wt% 2,4′-diamino-diphenyl methane, 0-0.5wt% N-methyl-4,4′-diamino-diphenyl methane, and 0-0.5wt% other impurities, based on the total weight of the 4,4′-diamino-diphenyl methane feed.

12. The continuous method as claimed in claim 3 , wherein the 4,4′-diamino-diphenyl methane feed is composed of 85-95wt% 4,4′-diamino-diphenyl methane, 5-15wt% 2,4′-diamino-diphenyl methane, 0-0.5wt% N-methyl-4,4′-diamino-diphenyl methane, and 0-0.5wt% other impurities, based on the total weight of the mixture.

13. The continuous method as claimed in claim 4 , wherein the metal is one or more selected from Pt, Rh, Ru, Ir and Pd.

14. The continuous method as claimed in claim 5 , wherein the weight ratio of Rh/Ru is 30-40:1, wherein the content of Rh is 3-7wt%; and the contend of Ru is 3-7wt%.

15. The continuous method as claimed in claim 14 , wherein the content of Rh is 4-6wt%, and the contend of Ru is 4-6wt%.

16. The continuous method as claimed in claim 6 , wherein the amount of Rh/Al 2 O 3 is 1-3wt%.

17. The continuous method as claimed in claim 7 , wherein the 4,4′-MDA feed is supplied in the presence a solvent, and the concentration of 4,4′-MDA in the solution is about 50wt%.

18. The continuous method as claimed in claim 8 , wherein the mixture of 2,4′-MDA and 4,4′-MDA is supplied in the presence of a solvent, and the total concentration of 2,4′-MDA and 4,4′-MDA in the solution is about 50wt%.

19. The continuous method as claimed in claim 9 , wherein said solvent is tetrahydrofuran.

Assignees

• Wanhua Chemical Group Co Ltd
• Wanhua Chemical (Ningbo) Co Ltd

Inventors

• Li Xin
• Chen Hao
• Zhang Congying
• Gao Shan
• Liu Zhenguo
• Wang Weijia
• Tang Lei
• Liu Zhipeng
• Li Yuan
• Jiang Qingmei
• Song Jinhong
• Hua Weiqi
• Ding Hao

Classifications

• Y02P20/584

  Recycling of catalysts · CPC title

• B01J38/08

  using ammonia or derivatives thereof · CPC title

• B01J23/96

  of catalysts comprising metals, oxides or hydroxides of the noble metals · CPC title

• C07C2601/14

  The ring being saturated · CPC title

• C07C209/72 Primary

  by reduction of six-membered aromatic rings · CPC title