Process for the conversion of aliphatic cyclic amines to aliphatic diamines
A process for conversion of aliphatic bicyclic amines to aliphatic diamines including contacting one or more bicyclic amines selected from the group consisting of 3-azabicyclo[3.3.1]nonane and azabicyclo[3.3.1]non-2-ene with ammonia and hydrogen, and alcohols in the presence of heterogeneous metal based catalyst systems, a metal selected from the group consisting of Co, Ni, Ru, Fe, Cu, Re, Pd, and their oxides at a temperature from 140° C. to 200° C. and a pressure from 1540 to 1735 psig for at least one hour reactor systems; forming a product mixture comprising aliphatic diamine(s), bicyclic amine(s), ammonia, hydrogen, and alcohol(s); removing said product mixture from the reactor system; removing at least some of the ammonia, hydrogen, water, alcohols, bicyclic amines from said product mixture; thereby separating the aliphatic diamines from said product mixture.
1. A process for conversion of aliphatic cyclic amines to aliphatic diamines comprising the steps of:
selecting one or more bicyclic amines;
contacting said one or more bicyclic amines selected from the group consisting of 3-azabicyclo[3.3.1]nonane and azabicyclo[3.3.1]non-2-ene with ammonia and hydrogen, optionally water, and optionally one or more alcohols in the presence of one or more heterogeneous metal based catalyst systems comprising a metal selected from the group consisting of Co, Ni, Ru, Fe, Cu, Re, Pd, oxides thereof, mixtures thereof, and combinations thereof at a temperature in the range of from 140° C. to about 250° C. and a pressure in the range of from 1540 to 1735 psig for a period in the range of at least one hour or more in one or more reactor systems, wherein the ammonia is present in in the range of from 79 to 88 mole equivalent;
forming a product mixture comprising one or more aliphatic diamines, a portion of said one or more bicyclic amines, a portion of said ammonia, a portion of said hydrogen, optionally water, and a portion of said one or more solvents;
removing said product mixture from the reactor system;
removing at least a portion of said portion of ammonia, said portion of hydrogen, or mixture thereof from said product mixture via venting;
removing at least a portion of said portion of water via distillation;
removing at least a portion of said portion of one or more alcohols via distillation;
removing at least a portion of said portion of one or more bicyclic amines;
thereby separating said one or more aliphatic diamines from said product mixture; and
thereby converting said one or more bicyclic amines selected from the group consisting of 3-azabicyclo[3.3.1]nonane and azabicyclo[3.3.1]non-2-ene to one or more aliphatic diamines selected from the group consisting of 1,3-bis(aminomethyl)cyclohexane and hexamethylene diamine.
2. The process of claim 1 , wherein said one or more reactor systems comprise one or more continuous reactors, one or more batch reactors, or one or more semi-batch reactors, or combinations thereof in series, in parallel, or combinations thereof.
3. The process of claim 1 , wherein said one or more heterogeneous metal based catalyst systems is a bulk metal catalyst system, sponge-metal catalyst system, supported metal catalyst system, mixtures thereof, or combinations thereof.
4. The process of claim 1 , wherein said one or more heterogeneous metal based catalyst systems comprises a bulk Co based catalyst system.
5. The process of claim 1 , wherein said one or more heterogeneous metal based catalyst systems further comprises one or more promoters or one or more binding agents.
6. The process of claim 5 , wherein said one or more promoters are selected from the group consisting of alkali metals and alkaline earth metals.
7. The process of claim 5 , wherein said one or more binding agents comprise silicon oxide, aluminum oxide, titanium oxide, zirconium oxide, mixtures thereof, or combinations thereof.