A process for the preparation of substituted pyridine compounds and intermediates thereof
US-2024018106-A1 · Jan 18, 2024 · US
US9428446B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9428446-B2 |
| Application number | US-201214377222-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 10, 2012 |
| Priority date | Feb 10, 2012 |
| Publication date | Aug 30, 2016 |
| Grant date | Aug 30, 2016 |
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A new process for the production of APMMEA (aminopropylmethylethanolamine) is proposed. This process comprises at least 2 steps in which MEAPN (monomethylethanolaminopropionitrile) is first produced from MMEA (monomethylethanol amine) and ACN (acrylonitrile) and then said MEAPN is hydrogenated to obtain the corresponding amine, the APMMEA compound. APMMEA may be then eventually purified by several known process, notably by distillation.
Opening claim text (preview).
What is claimed is: 1. A process for the production of APMMEA comprising at least 2 steps: (a) Production of MEAPN from reaction of MMEA and ACN; (b) Hydrogenation of said MEAPN in the presence of a reaction medium comprising a catalyst, inorganic base, and water to produce APMMEA; and (c) Isolation of said APMMEA. 2. The process according to claim 1 , wherein in said step (a) the molar/molar proportion of said MMEA/ACN is comprised between 0.98 and 1.2. 3. The process according to claim 1 , wherein the catalyst is a Raney metal. 4. The process according to claim 1 , wherein said inorganic base is selected from the group consisting of LiOH, NaOH, KOH, RbOH, CsOH and their mixtures. 5. The process according to claim 1 , wherein the amount of said inorganic base added is determined in order to have at least 0.2 mol of base per kilogram of said catalyst. 6. The process according to claim 1 , wherein in said step (b) the hydrogenation reaction is carried out in the presence of said APMMEA as solvent. 7. The process according to claim 6 , wherein the concentration of said APMMEA in the reaction medium is advantageously between 50% and 99% by weight, of the liquid phase of the hydrogenation reaction medium. 8. The process according to claim 1 , wherein in said step (b) the hydrogenation reaction is carried out in the presence of water as other component of the reaction medium. 9. The process according to claim 8 , wherein the water is present in an amount of less than or equal to 50% by weight, in the liquid phase of the total reaction medium. 10. The process according to claim 8 , wherein the water is present in an amount comprised between 0.1 and 15% by weight, in the liquid phase of the total reaction medium. 11. The process according to claim 1 , wherein said APMMEA is purified by continuous or batch distillation in a step (c) at atmospheric or reduced pressure.
by reactions involving the formation of amino groups from compounds containing hydroxy groups or etherified or esterified hydroxy groups · CPC title
by reactions not involving the formation of cyano groups · CPC title
containing cyano groups and singly-bound nitrogen atoms, not being further bound to other hetero atoms, bound to the same saturated acyclic carbon skeleton · CPC title
the nitrogen atom of the amino group being further bound to hydrocarbon groups substituted by amino groups · CPC title
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