Method for the production of ethyleneamines

Patent metadata

Field	Value
Publication number	US-12221402-B2
Application number	US-202017436293-A
Country	US
Kind code	B2
Filing date	Feb 26, 2020
Priority date	Mar 6, 2019
Publication date	Feb 11, 2025
Grant date	Feb 11, 2025

Abstract

The present invention relates to a process for preparing alkanolamines and ethyleneamines in the liquid phase, by reacting ethylene glycol and/or monoethanolamine with ammonia in the presence of an amination catalyst which is obtained by reducing a catalyst precursor, wherein the preparation of the catalyst precursor comprises a step a) in which a catalyst precursor comprising one or more catalytically active components of Sn, Cu and Ni, and a step b) in which the catalyst precursor prepared in step a) is contacted with a soluble Re compound.

First claim

The invention claimed is:

1. A process for preparing alkanolamines and ethyleneamines in the liquid phase, by reacting ethylene glycol, monoethanolamine, or a combination thereof with ammonia in the presence of an amination catalyst which is obtained by reducing a catalyst precursor, wherein the preparation of the catalyst precursor comprises a step a) in which a catalyst precursor comprising one or more catalytically active components of Sn, Cu and Ni is prepared by coprecipitation or by precipitative application, and a step b) in which the catalyst precursor prepared in step a) is contacted with a soluble Re compound by post-impregnating the catalyst precursor with an impregnating solution comprising the soluble Re compound.

2. The process according to claim 1 , wherein the catalyst precursor prepared in step a) additionally comprises catalytically active components of Co.

3. The process according to claim 1 , wherein the catalyst precursor in step a) is prepared by coprecipitation and comprises in the range from 1% to 95% by weight of catalytically active components selected from the group consisting of Sn, Cu, Ni, and mixtures thereof, calculated as CuO, NiO and SnO respectively and based in each case on the total mass of the catalyst precursor.

4. The process according to claim 1 , wherein the catalyst precursor is prepared by precipitative application in step a) and, comprises in the range from 5% to 95% by weight of support material and in the range from 5% to 90% by weight of catalytically active components selected from the group consisting of Sn, Cu, Ni, and mixtures thereof, calculated as CuO, NiO and SnO respectively and based in each case on the total mass of the catalyst precursor.

5. The process according to claim 2 , wherein the catalyst precursor prepared in step a) comprises,
0.2% to 5% by weight of catalytically active components of tin, calculated as SnO,
1% to 20% by weight of catalytically active components of copper, calculated as CuO,
5% to 35% by weight of catalytically active components of nickel, calculated as NiO, and
5% to 35% by weight of catalytically active components of cobalt, calculated as CoO, and
15% to 80% by weight of catalytically active components of aluminum, calculated as Al 2 O 3 as support material,
based on the total mass of the catalyst precursor.

6. The process according to claim 5 , wherein the catalyst precursor is prepared in the presence of tin nitrate and a complexing agent.

7. The process according to claim 1 , wherein the Re concentration in the impregnating solution is in the range of 0.1 to 50% by weight.

8. The process according to claim 1 , wherein the catalyst precursor in step b) is contacted with a soluble compound of an active metal or an added catalyst element other than Re.

9. The process according to claim 1 , wherein the catalyst precursor in step b) is contacted with a soluble Ru compound and/or a soluble Co compound by post-impregnating the catalyst precursor with an impregnating solution comprising a soluble Ru compound and/or a soluble Co compound and the Ru concentration in the impregnating solution being in the range of 0.1 to 50% by weight or the Co concentration in the impregnating solution being in the range of 0.1 to 20% by weight.

10. The process according to claim 1 , wherein the catalyst precursor is dried after step b) before reducing the catalyst precursor to obtain the amination catalyst.

11. The process according to claim 10 , wherein the catalyst precursor comprises 0.1% to 20% by weight of catalytically active components of Re, calculated as ReO 3 and based on the total mass of the catalyst precursor after the last drying step.

12. The process according to claim 10 , wherein the catalyst precursor comprises 0.1% to 50% by weight of catalytically active components of Co, calculated as CoO and based on the total mass of the catalyst precursor after the last drying step or wherein the catalyst precursor comprised 0.1% to 50% by weight of catalytically active components of Ru, calculated as RuO 2 and based on the total mass of the catalyst precursor after the last drying step.

13. The process according to claim 1 , wherein the catalyst precursors prepared in step a) are further processed by performing one or more of the following processing steps before submitting the catalyst precursor to step b):
aa) liquid separation,
ab) washing,
ac) drying,
ad) calcination,
ae) shaping.

14. The process according to claim 1 , wherein the reaction of ethylene glycol or monoethanolamine with ammonia is effected in the liquid phase at a pressure of 5 to 30 MPa and a temperature in the range from 80 to 350° C.

Assignees

• Basf Se

Inventors

• Becker Barbara
• Heidemann Thomas
• Bebensee Regine Helga
• Koch Eva
• Melder Johann-Peter
• Luyken Hermann
• Oezkozanoglu Claudia
• Kehrer Jens

Classifications

• B01J37/16

  Reducing · CPC title

• B01J37/082

  Decomposition and pyrolysis · CPC title

• B01J37/04

  Mixing {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• B01J37/03

  Precipitation; Co-precipitation · CPC title

• B01J37/024

  Multiple impregnation or coating · CPC title