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:
The present invention relates to a method for removing halogenide ions from liquid ammonia, characterized in that the liquid ammonia is brought into contact with a strongly basic ion exchanger, wherein the structure of the strongly basic ion exchanger is a covalently bonded polymer matrix. The present invention further relates to the use of an ammonia obtained according to the invention as an educt in the manufacture of amines.
Abstract:
A process for the preparation of a zeolitic material having a structure comprising YO2 and X2O3 is provided, wherein said process comprises the steps of ( 1 ) providing a mixture comprising one or more ammonium compounds of which the ammonium cation has the formula (I): [R1R2NR3R4+(I) and further comprising one or more sources for Y02 and one or more sources for X2O3; (2) crystallizing the mixture provided in step ( 1 ); wherein Y is a tetravalent element, and X is a trivalent element, and wherein the ammonium compounds are preferably derivatized or underivatized N,N-dimethylpyrrolidinium compounds, Nu,Nu-dimethylpiperidinium compounds, Nu,Nu-dimethylhexahydroazepinium compounds, and mixtures thereof, and wherein the molar ratio of ammonium cation having the formula (I) to Y in the mixture provided in step (1) and crystallized in step (2) is equal to or greater than 0.25.
Abstract:
The invention relates to a process for continuously preparing di-C1-3-alkyl succinates by reacting succinic acid with an C1-3-alkanol in the presence of a fixed-bed heterogeneous acidic esterification catalyst in a tubular reactor at a temperature in the range of from 60 to 100°C, wherein a mixture, comprising succinic acid, C1-3-alkanol, mono-C1-3-alkyl succinate, di-C1-3-alkyl succinate and water, is formed in a mixing stage and fed to the entrance of the tubular reactor, and wherein 5 to 75% of the outlet flow rate of the tubular reactor are recycled directly to the mixing stage as a recycle stream, and the molar ratio of C1-3-alkanol to succinic acid added to the mixing zone, and not including the C1-3-alkanol and succinic acid at the recycle stream, being in the range of from 2.0 to 9.5. The invention furthermore relates to a process for separating the reactor effluent of an esterification of succinic acid with an C1-3-alkanol to give di-C1-3-alkyl succinates by distillation, wherein the separation is performed in a divided wall column in which C1-3-alkanol and water are removed in a top draw of the column, di-C1-3-alkyl succinate is removed in a side draw of the column, and wherein mono-C1-3-alkyl succinate and succinic acid are removed in a bottom draw of the column.
Abstract:
Procedimiento para la preparación de un material zeolítico que tiene una estructura de armazón de tipo MFI, que comprende las etapas de: (1) proporcionar una mezcla que comprende una o más fuentes para YO2 y uno o más compuestos que contienen un catión de alqueniltrialquilamonio R1R2R3R4N+ como agente de control de estructura; y (2) cristalizar la mezcla obtenida en la etapa (1) para obtener un material zeolítico; en el que Y es un elemento tetravalente, y en el que R1, R2 y R3 independientemente entre sí representan n-propilo; y R4 representa 2-propen-1-ilo o 1-propen-1-ilo.
Abstract:
Un procedimiento de preparación en contínuo de succinatos de di-alquilo C1-3 por reacción del ácido succínico con un alcanol C1-3 en presencia de un catalizador de esterificación ácida heterogéneo de lecho fijo en un reactor tubular a una temperatura en el intervalo desde 60 a 100ºC, en el que se forma una mezcla, que comprende ácido succínico, alcanol C1-3, succinato de mono-alquilo C1-3, succinato de di-alquilo C1-3 y agua, en una etapa de mezclado y se alimenta a la entrada del reactor tubular, y en el que 5 a 75% del caudal de salida del reactor tubular se recicla directamente a la etapa de mezclado como corriente de reciclaje y estando la proporción molar de alcanol C1-3 respecto al ácido succínico adicionado a la zona de mezcla, y sin incluir el alcanol C1-3 y el ácido succínico de la corriente de reciclaje, en el intervalo desde 2,0 a 9,5.
Abstract:
A method for depleting halide ions from liquid ammonia, which comprises bringing the liquid ammonia into contact with a strongly basic ion exchanger, where the basic structure of the strongly basic ion exchanger is a covalently crosslinked polymer matrix and the content of ammonia in the liquid ammonia is more than 98% by weight.