Process for reductive amination of aliphatic cyanoaldehydes to aliphatic diamines
A process for reductive amination of aliphatic cyanoaldehydes to aliphatic diamines comprising (1) providing a mixture of 1,3-cyanocyclohexane carboxaldehyde and/or 1,4-cyanocyclohexane carboxaldehyde; (2) contacting said mixture with a metal carbonate based solid bed or a weak base anion exchange resin bed at a temperature from 15 to 40 ° C. for a period of at least 1 minute; (3) thereby treating said mixture, wherein said treated mixture has a pH in the range of 6 to 9; (4) feeding said treated mixture, hydrogen, and ammonia into a continuous reductive amination reactor system; (6) contacting said treated mixture, hydrogen, and ammonia with each other in the presence of one or more heterogeneous metal based catalyst systems at a temperature from 80 ° C. to 160 ° C. and a pressure from 700 to 3500 psig; (7) thereby producing one or more cycloaliphatic diamines is provided.
1. A process for reductive amination of aliphatic cyanoaldehydes to aliphatic diamines comprising: providing a mixture of one or more cycloaliphatic cyanoaldehydes, optionally water and optionally one or more solvents, wherein said one or more cycloaliphatic cyanoaldehydes are selected from the group consisting of 1,3-cyanocyclohexane carboxaldehyde, 1,4-cyanocyclohexane carboxaldehyde, mixtures thereof, and combinations thereof; contacting said mixture with a metal carbonate based solid bed or a weak base anion exchange resin bed at a temperature in the range of 15 to 40° C. for a period of at least 1 minute or more; thereby treating said mixture; neutralizing said treated mixture, wherein said neutralized treated mixture has a pH in the range of 6 to 9; feeding said neutralized treated mixture, hydrogen, and ammonia into a continuous reductive amination reactor system; contacting said neutralized treated mixture, hydrogen, and ammonia with each other in the presence of one or more heterogeneous metal based catalyst systems at a temperature in the range of from 80° C. to 160° C. and a pressure in the range of from 700 to 3500 psig; thereby producing one or more cycloaliphatic diamines, wherein said one or more cycloaliphatic diamines are diamines selected from the group consisting of 1,3-bis(aminomethyl)cyclohexane, 1,4-bis(aminomethyl)cyclohexane, combinations thereof, and mixtures thereof
wherein said process has a space velocity in the range of 0.1 to 10.0 per hour, and wherein the weight ratio of the cycloaliphatic diamines to one or more heterogeneous metal based catalyst systems is greater than 500.
2. A process for reductive amination of aliphatic cyanoaldehydes to aliphatic diamines comprising: providing a mixture of one or more cycloaliphatic cyanoaldehydes, optionally water, and optionally one or more solvents, wherein said one or more cycloaliphatic cyanoaldehydes are selected from the group consisting of 1,3-cyanocyclohexane carboxaldehyde, 1,4-cyanocyclohexane carboxaldehyde, mixtures thereof, and combinations thereof; contacting said mixture with a metal carbonate based solid bed or a weak base anion exchange resin bed at a temperature in the range of 15 to 40 ° C. for a period of at least 1 minute or more; thereby treating said mixture, wherein said treated mixture has a pH in the range of 6 to 9; feeding said treated mixture, hydrogen, and ammonia into a continuous reductive amination reactor system; contacting said treated mixture, hydrogen, and ammonia with each other in the presence of one or more heterogeneous metal based catalyst systems at a temperature in the range of from 80 ° C. to 160 ° C. and a pressure in the range of from 700 to 3500 psig; thereby producing one or more cycloaliphatic diamines, wherein said one or more cycloaliphatic diamines are diamines selected from the group consisting of 1,3-bis(aminomethyl)cyclohexane, 1,4-bis(aminomethyl)cyclohexane, combinations thereof, and mixtures thereof
wherein said process has a space velocity in the range of 0.1 to 10.0 per hour, and wherein the weight ratio of the cycloaliphatic diamines to one or more heterogeneous metal based catalyst systems is greater than 500.