초록 ▼

A process for producing an ethylenamine, which comprises reacting ammonia and/or an ethylenamine with an ethanolamine in the presence of hydrogen to obtain an ethylenamine having an increased number of ethylene chains over the ammonia and/or the ethylenamine used as the starting material, wherein a

A process for producing an ethylenamine, which comprises reacting ammonia and/or an ethylenamine with an ethanolamine in the presence of hydrogen to obtain an ethylenamine having an increased number of ethylene chains over the ammonia and/or the ethylenamine used as the starting material, wherein a catalyst comprising Ni, X and M elements wherein X is Re, Ir, Pt or Pd, and when X is Re, Ir or Pb, M is at least one rare earth element selected from the group consisting of scandium, yttrium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium and lutetium, and when X is Pd, M is at least one member selected from the group consisting of rare earth elements is used for the reaction.

대표청구항 ▼

1. A process for producing an ethylenamine, which comprises: reacting ammonia and/or an ethylenamine with an ethanolamine in the presence of hydrogen and a catalyst comprising Ni, X and M elements, wherein X is Re, Ir, Pt or Pd and M is at least one rare earth element selected from the group cons

1. A process for producing an ethylenamine, which comprises: reacting ammonia and/or an ethylenamine with an ethanolamine in the presence of hydrogen and a catalyst comprising Ni, X and M elements, wherein X is Re, Ir, Pt or Pd and M is at least one rare earth element selected from the group consisting of scandium, yttrium, praseodymium, neodymium, samarium, europium, gadolinium, terbium, dysprosium, holmium, erbium, thulium, ytterbium and lutetium, thereby preparing an ethylenamine having an increased number of ethylene chains over the ammonia and/or ethylenamine staring material. 2. The process according to claim 1, wherein Ni in the catalyst is in the form of nickel metal or nickel oxide, X in the catalyst is in the form of metal or an oxide and M in the catalyst is in the form of metal or an oxide. 3. The process according to claim 1, wherein the atomic ratio of Ni/X is from 1 to 100, and the atomic ratio of Ni/M is from 0.5 to 100. 4. The process according to claim 1, wherein the reaction is conducted in a suspended bed system, and the catalyst is used in an amount of from 0.1 to 20% by weight relative to the total weight of the starting materials. 5. The process according to claim 1, wherein the ethanolamine is monoethanolamine, diethanolamine, triethanolamine, N-(2-aminoethyl)ethanolamine or N-(2-hydroxyethyl)piperazine. 6. The process according to claim 1, wherein the ethylenamine used as the starting material is ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine, piperazine, N-(2-aminoethyl)piperazine or triethylenediamine. 7. The process according to claim 1, wherein the reaction of ammonia with an ethanolamine is conducted at a molar ratio of the ammonia/the ethanolamine of from 1 to 50. 8. The process according to claim 1, wherein the reaction of an ethylenamine with an ethanolamine is conducted at a molar ratio of the ethylenamine/the ethanolamine of from 0.1 to 20. 9. The process according to claim 1, wherein the hydrogen is supplied at a molar ratio of the hydrogen/the ethanolamine of from 0.01 to 5. 10. The process according to claim 1, wherein the reaction is conducted at a temperature of from 110° to 290° C. 11. The process according to claim 1, wherein the reaction is conducted in a liquid phase.