Abstract:
PROBLEM TO BE SOLVED: To provide a method for economically, selectively and efficiently reducing the content of amine existing in N-substituted lactams as an impurity. SOLUTION: The method for reducing the amine content of amine-contaminated N-substituted lactams comprises treating the contaminated N-substituted lactams with an acid macroporous cation exchanger. COPYRIGHT: (C)2011,JPO&INPIT
Abstract:
In a process for preparing 3-aminomethyl-3,5,5-trimethylcyclohexylamine (isophoronediamine, IPDA) having a cis/trans isomer ratio of at least 70/30 from 3-cyano-3,5,5-trimethylcyclohexanone (isophoronenitrile, IPN), NH 3 and H 2 , the hydrogenation is carried out at from 50 to 200° C. and a pressure of from 50 to 300 bar in the presence of a hydrogenation catalyst having an alkali metal content of
Abstract:
Production of pyrroles (I) or pyridines (III), comprises dehydrogenating the corresponding pyrrolidines (II) or piperidines (IV) in the presence of a supported noble metal catalyst comprises performing the reaction in the presence of 1-50 wt.% water. Production of pyrroles of formula (I) or pyridines of formula (III), comprises dehydrogenating the corresponding pyrrolidines of formula (II) or piperidines of formula (IV) in the presence of a supported noble metal catalyst comprises performing the reaction in the presence of 1-50 wt.% water. R -R = H or 1-6C aliphatic group.
Abstract:
Process for the continuous preparation of N-methyl-2-pyrrolidone (NMP) by reacting gamma-butyrolactone (GBL) with monomethylamine (MMA) in the liquid phase, wherein GBL and MMA are used in a molar ratio of from 1:1.08 to 1:2 and the reaction is carried out at from 320 to 380° C. and an absolute pressure of from 70 to 120 bar.
Abstract:
Método para la producción de 3-aminometil-3,5,5-trimetilciclohexilamina (isoforondiamina, IPDA) con una relación de isómeros cis/trans de por lo menos 70/30 a partir de 3-ciano-3,5,5-trimetilciclohexanona (isoforonnitrilo, IPN), NH2, y H2, donde es hidrogenado en presencia de un catalizador que contiene 55 a 98% en peso de cobalto, 0,2 a 15% en peso de fósforo y 0,2 a 15% en peso de manganeso así como dado el caso rutenio, calculado en cada caso como óxido y referido al peso total de catalizador, a temperaturas de 50 a 200ºC y una presión de 50 a 300 bar, caracterizado porque el contenido de metal alcalino del catalizador de hidrogenación es
Abstract:
In a process for preparing 3-aminomethyl-3,5,5-trimethylcyclohexylamine (isophoronediamine, IPDA) having a cis/trans isomer ratio of at least 70/30 from 3-cyano-3,5,5-trimethylcyclohexanone (isophoronenitrile, IPN), NH 3 and H 2 , the hydrogenation is carried out at from 50 to 200° C. and a pressure of from 50 to 300 bar in the presence of a hydrogenation catalyst having an alkali metal content of