Amination process using nickel-rhenium catalysts

• US 4,123,462 A
• Filed: 01/07/1976
• Issued: 10/31/1978
• Est. Priority Date: 01/07/1976
• Status: Expired due to Term

• Current Assignee: Union Carbide Corporation (Dow, Inc.)
• Original Assignee: Union Carbide Corporation (Dow, Inc.)
• Inventors: Best, Donald C.
• Primary Examiner(s): Douglas, Winston A.
• Assistant Examiner(s): Doll, John J.
• Application Number:
  US05/647,065
• Time in Patent Office: 1,028 Days
• Field of Search: 260/585 B, 260/268 SY, 260/585 R, 260/566 R, 260/585 C, 252/455 R, 252/459, 252/466 J, 252/432
• US Class Current: 564/480
• CPC Class Codes: B01J 23/8896 Rhenium
• CPC Class Codes: C07C 209/16 with formation of amino groups bound to acyclic carbon atoms or to carbon atoms of rings other than six-membered aromatic rings
• CPC Class Codes: C07C 209/28 by reduction with other reducing agents
• CPC Class Codes: C07C 211/06 containing only n- or iso-propyl groups
• CPC Class Codes: C07C 211/10 Diaminoethanes
• CPC Class Codes: C07C 211/11 Diaminopropanes

Abstract

The present invention concerns a new nickel-rhenium catalyst and method of preparing said catalyst. The invention also relates to the catalytic amination of lower aliphatic alkane derivatives such as alkanemono-ols, alkanediols and alcoholamines utilizing the new nickel-rhenium catalyst.

Claims

1. In the process for aminating a lower aliphatic alkane derivative with ammonia in the presence of a solid catalyst wherein the products comprise both economically desirable alkylamines and undesirable by-products of lesser economic significance, the improvement in selectivity and increased conversion, evidenced by the production of a substantially greater amount of said valuable alkylamines together with concomitant reduction in the yield of undesirable by-products from a given alkane charge, which comprises reacting under amination conditions said alkane charge with ammonia in the presence of hydrogen and a nickel-rhenium catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths and silica-titanias, wherein said catalyst has a total nickel and rhenium metal content of 3-30% by weight of the support and the atom ratio of the nickel to the rehnium present is in the range from about 2:

1 to about 30;

1.

2. The process of claim 1 wherein said alkane derivative contains from one to six carbon atoms and at least one functional group capable of being replaced by an amino group by the catalytic amination process.

3. The process of claim 1 wherein said alkane derivative contains from one to six carbon atoms and at least one hydroxy functional group.

4. The process of claim 1 wherein the desirable alkylamine product is ethylenediamine and the alkane derivative is selected from the group consisting of ethylene glycol, monoethanolamine, and mixtures thereof.

5. The process of claim 1 wherein said catalyst is comprised of boron in addition to nickel and rhenium.

6. The process of claim 1 wherein said catalyst is comprised of boron and cobalt in addition to nickel and rhenium.

7. The process of claim 1 wherein said support material is an α

-alumina.

8. The process of claim 1 wherein said support material is a silica-alumina.

9. The process of claim 4 wherein the ammonia is present in an amount greater than the stochiometric amount required by the alkane derivative coreactant that is present.

10. The process of claim 9 wherein the ammonia is present in an amount in the range 2-15 times the stochiometric amount required by the alkane derivative coreactant.

11. A process for producing lower aminoalkanes by the catalytic amination of lower aliphatic alkane derivatives selected from lower alkanemono-ols, lower alkanediols, lower alkanolamines, and mixtures thereof, said process comprising the step of reacting said alkane derivatives with ammonia under pressure, at a temperature of from 125°

C to 350°

C, and in the presence of hydrogen and an active nickel-rhenium catalyst, said catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths, and silicatitanias, wherein the nickel and rhenium metal content is from 3-30% by weight of the support material and the atom ratio of the nickel to the rhenium present is in the range from about 2;

1 to about 30;

1, and wherein said catalyst is present in a catalytic amount.

12. The process of claim 11 wherein the catalyst is activated by heating it in the presence of hydrogen in the temperature range 200°

-600°

C.

13. The process of claim 11 wherein the pressure during the reaction is in the range of 500 to 5,000 psig.

14. The process of claim 11 wherein the lower aliphatic alcohol is 1,3-propanediol.

15. The process of claim 11 wherein the lower aliphatic alcohol is selected from ethanol and 2-propanol.

16. A process for producing ethylenediamine by the catalytic amination of a compound selected from the group consisting of ethylene glycol, monoethanolamine, ethyleneoxide, ethyleneimine, and mixtures thereof, said process comprising reacting said compound with ammonia in the presence of hydrogen and a Ni-Re catalyst comprising rhenium and nickel impregnated on a support material selected from the group consisting of aluminas, silicas, silica-aluminas, kieselguhrs or diatomaceous earths, and silica-titanias, said catalyst having a total nickel and rhenium metal content of 3-30% by weight of the support and a nickel to rhenium atom ratio in the range from about 2:

1 to about 30;

1 and wherein said catalyst is activated in the presence of hydrogen at elevated temperature, and wherein the temperature of the amination reaction is in the range 125°

-350°

C, the pressure is 500-5000 psig and the amount of ammonia present is in excess of 2 times the stochiometric amount required by the compound.