Production of Alpha, Omega-Diols
US-2016023975-A1 · Jan 28, 2016 · US
US10919837B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10919837-B2 |
| Application number | US-201716083594-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 10, 2017 |
| Priority date | Mar 11, 2016 |
| Publication date | Feb 16, 2021 |
| Grant date | Feb 16, 2021 |
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The present invention concerns a process for forming a primary or a secondary amine via amination reaction comprising: reacting an alcohol with an amine in the presence of a zeolite comprising a transition metal chosen in the group consisting of Group 8 to 12 elements of the Periodic Table and any combination thereof.
Opening claim text (preview).
The invention claimed is: 1. A process for forming a primary or a secondary amine, comprising reacting: A first reactant having 5-30 carbon atoms and one or two primary hydroxyl functionalities, with A second reactant being NH 3 or a reactant having primary amine functionality, in the presence of at least one zeolite comprising a transition metal selected from the group consisting of Ru, Rh, Pd, and any combination thereof, and wherein the reaction is conducted on a gas-liquid-solid tri-phase reactor connected with a condense column and a collection tank, and wherein the gas pressure is from 0 barg to 10 barg. 2. The process according to claim 1 , wherein the first reactant is a compound of formula (I): R 1 (—OH) x (I) Wherein: x is 1 or 2 R 1 is a straight, branched or cyclic C 5 -C 30 hydrocarbon group. 3. The process according to claim 2 , wherein R 1 is selected from the group consisting of: C 5 -C 12 straight aliphatic hydrocarbon group, benzyl, furfuryl and tetrahydrofurfuryl. 4. The process according to claim 3 , wherein the first reactant is selected from the group consisting of: 1-pentanol, 1-hexanol, 1-heptanol, 1-octanol, 1-nonanol, 1-decanol, furfuryl alcohol, 2,5 furandimethanol, 2,5-tetrahydrofuranedimethanol, benzyl alcohol, 1,6-hexandiol and 1,7-heptandiol. 5. The process according to claim 1 , wherein the second reactant is a compound of formula (II): R 2 —NH 2 (II) Wherein: R 2 is H or a straight, branched or cyclic hydrocarbon group. 6. The process according to claim 5 , wherein R 2 is H or C 1 -C 5 alkyl. 7. The process according to claim 1 , wherein the primary or secondary amine produced is a compound of formula (III): R′(—NHR 2 ) x (III) Wherein: x is 1 or 2 le is a straight, branched or cyclic C 5 -C 30 hydrocarbon group R 2 is H or a straight, branched or cyclic hydrocarbon group. 8. The process according to claim 1 , wherein a secondary amine is produced and is a compound of formula (IV): R 1 2 NH (IV) Wherein: R 1 is a straight, branched or cyclic C 5 -C 30 hydrocarbon group. 9. The process according to claim 1 , wherein the primary amine or secondary amine produced is selected from the group consisting of: 1-pentylamine, 1-hexylamine, 1-heptylamine, 1-octylamine, 1-nonylamine and 1-decylamine, benzylamine, furan-2-ylmethanamine, (tetrahydrofuran-2,5-diyl) dimethanamine, (furan-2,5-diyl) dimethanamine, 1,6-hexamethylenediamine, and 1,7-heptamethylenediamine. 10. The process according to claim 1 , wherein the process comprises a third reactant being hydrogen. 11. The process according to claim 1 , wherein the molecular ratio of silica/alumina in zeolite is comprised between 5 and 300. 12. The process according to claim 1 , wherein the zeolite is selected from the group consisting of: ZSM-5, Beta, zeolite Y and mordenite. 13. The process according to claim 1 , wherein the loading amount of transition metal on zeolite is between 5% and 10% by weight. 14. The process according to claim 1 , wherein the weight ratio of zeolite comprising a transition metal selected from the group consisting of Ru, Rh, Pd, and any combination thereof to first reactant is between 5% and 20% by weight. 15. The process according to claim 1 , wherein the reaction temperature is between 120 and 280° C.
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