Process for producing dimethylamine in preference to mono- and trimethylamines by gas phase catalytic reaction of ammonia with methanol

• US 4,582,936 A
• Filed: 06/06/1984
• Issued: 04/15/1986
• Est. Priority Date: 06/08/1983
• Status: Expired due to Term

• Current Assignee: Mitsubishi Rayon Company Limited (Mitsubishi Chemical Holdings Corporation)
• Original Assignee: Nitto Kagaku Kogyo Kabushiki Kaisha
• Inventors: Fukatsu, Michio, Fujita, Takeyuki, Yagi, Junsuke, Ashina, Yoshiro
• Primary Examiner(s): Shaver, Paul F.
• Application Number:
  US06/617,636
• Time in Patent Office: 678 Days
• Field of Search: 564/479, 564/480, 564/469, 564/463, 585/481, 585/475, 502/77, 502/67, 502/64, 502/78, 502/85
• US Class Current: 564/479
• CPC Class Codes: B01J 2229/36 Steaming
• CPC Class Codes: B01J 29/18 of the mordenite type
• CPC Class Codes: B01J 29/50 of the erionite or offretite type, e.g. zeolite T, as exemplified by patent document US2950952

Abstract

A process for the selective production of dimethylamine in preference to mono- and trimethylamines by a catalytic vapor phase reaction of ammonia and methanol over a zeolite selected from mordenite, clinoptilolite and erionite is disclosed, wherein the improvement is characterized by the fact that the zeolite used has been contacted with steam at a temperature of 250° to 700° C.

Claims

1. In a process for production of dimethylamine by a gas phase reaction of ammonia and methanol over a catalyst of a zeolite selected from the group consisting of mordenite, clinoptilolite, and erionite, wherein a mixture of methylamines is produced, the improvement wherein said catalyst is previously and separately from said reaction of ammonia and methanol contacted with an atmosphere comprising steam at a temperature of from 250°

to 700°

C., thereby to increase the content of dimethylamine in the methylamine mixture produced above the content of dimethylamine resulting from said reaction over the catalyst in the absence of such contact of the catalyst with steam.

2. The process according to claim 1, wherein the catalyst is mordenite, clinoptilolite or erionite which has not yet been used for the reaction of ammonia and methanol.

3. The process according to claim 1, wherein the catalyst is mordenite, clinoptilolite or erionite which has already been used for the reaction of ammonia and methanol.

4. The process according to claim 1, wherein the catalyst is contacted with the atmosphere comprising steam under a steam pressure of 1 to 70 atm. for 1 to 400 hours at a temperature of 350°

to 500°

C.

5. The process according to claim 1, wherein the catalyst is contacted with the atmosphere comprising steam under a pressure of 5 to 30 atm. for 10 to 30 hours at a temperature of 350°

to 500°

C.

6. The process according to claim 1, wherein the catalyst has an alkali metal content adjusted to from 1 to 7% by weight as calculated on the basis of the oxide thereof.

7. The process according to claim 1, wherein the reaction of ammonia and methanol is a continuous reaction conducted under the conditions of a temperature of 250°

to 500°

C., a pressure of 1 to 50 atm., N/C of 0.2 to 6 and a space velocity of 360 to 18,000 hr^-1 as calculated based on the data under 1 atm. and 0°

C.

8. The process according to claim 1, wherein the zeolite is mordenite.