US2008073221A1PendingUtilityA1
Selective Splitting of Substituted Bisbenzylamides and Bisbenzylamines
Est. expiryFeb 15, 2025(expired)· nominal 20-yr term from priority
C07C 209/62C07C 233/05C07C 211/03C25B 3/23C25B 3/09C25B 3/07
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Claims
Abstract
A process for the regioselective cleavage of secondary amines or amides is described.
Claims
exact text as granted — not AI-modified1 . A process for the regioselective cleavage of secondary amines or amides, which comprises the following process steps:
(a′) provision of at least one secondary bisbenzylamine or bisbenzylamide having at least one benzylic hydrogen atom in a solvent; (b′) electrochemical oxidation of the secondary amine or amide in the presence of an electrolyte salt and reaction of the electrolysis intermediate with a nucleophile, giving an electrolysis product mixture; (c′) work-up of the electrolysis product mixture; (d′) hydrolysis of the workup electrolysis product mixture.
2 . (canceled)
3 . The process according to claim 1 , wherein at least one benzyl ring of the bisbenzylamines or bisbenzylamides is substituted by an electron-pushing substituent which exerts a +I effect and/or a +M effect on the benzyl ring.
4 . The process according to claim 1 , wherein a nucleophilic solvent selected from the group consisting of methanol, ethanol, n-propanol, i-propanol and butanol is used in process step (a).
5 . The process according to claim 1 , wherein the electrochemical oxidation is carried out under at least one of the following conditions:
a temperature of from −20 to 60° C.; a current density of from 1 to 1000 mA/cm 2 ; a concentration of the electrolyte salt of from 0.0001 to 5 mol/l.
6 . The process according to any of claim 1 , wherein the electrolysis solution is worked up as follows in (c′):
(c′1) removal of the solvent and addition of water, an organic solvent selected from the group consisting of dichloromethane, chloroform, ethers, esters and hydrocarbons, and an acid; (c′2) extraction of the mixture resulting from process step (c′1) with an organic solvent selected from the group consisting of dichloromethane, chloroform, ethers, esters and hydrocarbons; (c′3) drying of the resulting organic phases; and (c′4) removal of the organic solvent.
7 . The process according to claim 1 , wherein the hydrolysis in (d′) is effected by means of a mixture of sodium hydroxide solution or potassium hydroxide solution and triethanolamine.
8 . The process according to claim 1 , wherein diastereomeric secondary amines or amides are used and the stereochemical purity of the resulting products is not significantly changed by the oxidation.
9 . A method of regioselective oxidation comprising oxidating secondary bisbenzylamines or bisbenzylamides having at least one benzylic hydrogen atom.
10 . A process for the regioselective cleavage of secondary amines or amides, which comprises the following process steps:
(a″) provision of at least one secondary bisbenzylamine or bisbenzylamide having at least one benzylic hydrogen atom in a solvent, with the solvent optionally comprising a nucleophile; (b″) oxidation of the secondary amine or amide by means of 2,3-dichloro-5,6-dicyano-1,4-benzoquinone (DDQ), giving an oxidation product mixture; (c″) reaction of the oxidation product mixture with a nucleophile.
11 . The process according to claim 10 , wherein at least one benzyl ring of the bisbenzylamines or bisbenzylamides is substituted by an electron-pushing substituent which exerts a +I effect and/or a +M effect on the benzyl ring.
12 . The process according to claim 11 , wherein a nucleophilic solvent selected from the group consisting of methanol, ethanol, n-propanol, i-propanol and butanol is used in process step (a).
13 . The process according to claim 11 , wherein the electrochemical oxidation is carried out under at least one of the following conditions:
a temperature of from −20 to 60° C.; a current density of from 1 to 1000 mA/cm 2 ; a concentration of the electrolyte salt of from 0.0001 to 5 mol/l.
14 . The process according to claim 12 , wherein the electrochemical oxidation is carried out under at least one of the following conditions:
a temperature of from −20 to 60° C.; a current density of from 1 to 1000 mA/cm 2 ; a concentration of the electrolyte salt of from 0.0001 to 5 mol/l.
15 . The process according to claim 11 , wherein the electrolysis solution is worked up as follows in process step (c′):
(c′1) removal of the solvent and addition of water, an organic solvent selected from the group consisting of dichloromethane, chloroform, ethers, esters and hydrocarbons, and an acid; (c′2) extraction of the mixture resulting from process step (c′1) with an organic solvent selected from the group consisting of dichloromethane, chloroform, ethers, esters and hydrocarbons; (c′3) drying of the resulting organic phases; (c′4) removal of the organic solvent.
16 . The process according to claim 12 , wherein the electrolysis solution is worked up as follows in process step (c′):
(c′1) removal of the solvent and addition of water, an organic solvent selected from the group consisting of dichloromethane, chloroform, ethers, esters and hydrocarbons, and an acid; (c′2) extraction of the mixture resulting from process step (c′1) with an organic solvent selected from the group consisting of dichloromethane, chloroform, ethers, esters and hydrocarbons; (c′3) drying of the resulting organic phases; (c′4) removal of the organic solvent.
17 . The process according to claim 13 , wherein the electrolysis solution is worked up as follows in process step (c′):
(c′1) removal of the solvent and addition of water, an organic solvent selected from the group consisting of dichloromethane, chloroform, ethers, esters and hydrocarbons, and an acid; (c′2) extraction of the mixture resulting from process step (c′1) with an organic solvent selected from the group consisting of dichloromethane, chloroform, ethers, esters and hydrocarbons; (c′3) drying of the resulting organic phases; (c′4) removal of the organic solvent.
18 . The process according to claim 1 1 , wherein the hydrolysis in process step (d′) is effected by means of a mixture of sodium hydroxide solution or potassium hydroxide solution and triethanolamine.
19 . The process according to claim 12 , wherein the hydrolysis in process step (d′) is effected by means of a mixture of sodium hydroxide solution or potassium hydroxide solution and triethanolamine.
20 . The process according to claim 13 , wherein the hydrolysis in process step (d′) is effected by means of a mixture of sodium hydroxide solution or potassium hydroxide solution and triethanolamine.Join the waitlist — get patent alerts
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