Abstract:
PROBLEM TO BE SOLVED: To remove a halogenized substance from a nitrile mixture for enabling the production of an amine from the nitrile mixture afterwards by heat/treating the nitrile mixture containing the halogenized substance, adding a base to the heat-treated nitrile mixture and removing the base from the neutral mixture. SOLUTION: This method for removing a halogenized material presenting as a form of a phase transition catalyst from a nitrile mixture, is to perform a heat-treatment the nitride mixture containing the halogenized substance at 50-350 deg.C. The heat treatment is performed by setting the pressure and temperature for distilling the nitrile in the mixture at 50 m bar pressure, and 227-230 deg.C bottom temperature and 163 deg.C top temperature. Then, after adding 5-50 wt.% concentration of a base such as NaO into the nitrile mixture while agitating, the halogenized substance is removed from the nitrile mixture. And then, by hydrogenating the obtained nitrile in the presence of a catalyst such as Ni and Co at 60-160 deg.C, especially preferably 90130 deg.C to form an amine.
Abstract:
PROBLEM TO BE SOLVED: To provide an economic method for manufacture of N-ethyl- diisopropylamine in an excellent space-time yield capable of carrying out in a discontinuous method or continuous method. SOLUTION: This method comprises the reaction of acetaldehyde, diisopropylamine and hydrogen at elevated temperature and pressurized condition in the presence of the hydrogenating catalyst, using a catalyst including oxide type supporting material selected from a group selected zirconium dioxide, titanium dioxide, aluminum oxide, silicone dioxide, zinc oxide, magnesium oxide, cerium dioxide, clay and zeolite and their mixtures.
Abstract:
PROBLEM TO BE SOLVED: To produce the subject compound useful for the dehydrohalogenation of organic compounds or synthesis, etc., of polymers in high yield without requiring the use of an acidic catalyst by reacting a specific lactone with a specified diamine while removing water of reaction during the progress of the reaction. SOLUTION: A lactone represented by formula I [R and R are each H or the like; (m) is 2-12] (e.g. γ-butyrolactone) is reacted with a diamine represented by formula II [R and R are each H or the like; (n) is 2-12] (e.g. 1,3-diaminopropane), preferably in at least 1:1.5 initial molar ratio of the lactone to the diamine, preferably continuously over the total reactional time, preferably at 170-220 deg.C for 5-100 hr while eliminating water of reaction and preferably with the aid of an azeotropic agent to produce the objective compound represented by formula III e.g. 1,5-diazabicyclo[4.3.0]non-5-ene}.
Abstract:
PROBLEM TO BE SOLVED: To economically and continuously obtain an alkylamine in a simplified apparatus by preheating only an amine stream or only an aldehyde stream fed by separated stream during feed and reacting the amine with the aldehyde on a fixed bed catalyst in a reactor. SOLUTION: Only an aldehyde stream [e.g. formaldehyde aqueous solution having 50-90 wt.%, preferably 65-75 wt.% water content based on total weight of the solution] or only an amine stream (preferably 30-80 wt.% piperazine aqueous solution) fed by separated stream is preheated during a feed (a molar ratio of piperazine to formaldehyde is 1:1.0 to 1:5, preferably 1:2 to 1:2.7) is and the aldehyde is reacted with the amine in a reactor in which these compounds are mixed in a catalyst bed on a fixed bed catalyst in the presence of an isolated hydrogen to continuously provide the objective alkylamine.
Abstract:
PROBLEM TO BE SOLVED: To enable hydroformylating a polymer in the state of an aqueous dispersion by using a specific catalyst under specific conditions. SOLUTION: This method for hydroformylating an ethylenic unsaturated polymer comprises reacting (C) carbon monoxide and (D) hydrogen with (B) the aqueous dispersion of a polymer having ethylenic unsaturated double bonds in the presence of (A) a hydroformylation catalyst under a condition that the catalyst is at least partially impregnated into the phase of the polymer or at least into the boundary of the polymer/aqueous phase. The component A is preferably the salt or complex of cobalt, rhodium or ruthenium, especially rhodium. The reaction conditions are preferably selected from a temperature range of 50-150 deg.C and a pressure range of 20-300 bars. The polymer dispersion preferably contains a (co)polymer produced from 10-100wt.% of at least one conjugated diene and 0-90wt.% of at least one monoolefinic unsaturated monomer capable of copolymerizable with the diene.
Abstract:
PROBLEM TO BE SOLVED: To obtain the subject compound by reaction between an α,β-unsaturated nitrile and an alcohol using a specific diazabicycloalkene as basic catalyst without the need of any prior separation or neutralization of the catalyst for the addition reaction. SOLUTION: This compound is obtained by reaction between an α,β-unsaturated nitrile (e.g. acrylonitrile) and a monohydric, dihydric or trihydric alcohol (e.g. methanol, ethanol, 2-ethylhexanol, 2-methoxyethanol, benzyl alcohol) at -20 to 200°C using a diazabicycloalkene of the formula (H may be substituted with a 1-20C alkyl, 6-20C aryl or 7-20C arylalkyl; (n) and (m) are each 1-6) as basic catalyst {e.g. 1,5-diazabicyclo[4.3.0]nonene-5(DBN), 1,8- diazabicyclo[5.4.0]undecene-7(DBU)}; wherein the amount of the catalyst to be used is pref. 0.05-5 wt.% based on the alcohol. COPYRIGHT: (C)1999,JPO
Abstract:
Die vorliegende Erfindung betrifft ein Verfahren zur Hydroformylierung von Polymerisaten, die ethylenisch ungesättigte Doppelbindungen enthalten, durch Umsetzung wäßriger Dispersionen der Polymerisate mit Wasserstoff und Kohlenmonoxid in Gegenwart geeigneter Hydroformylierungskatalysatoren. Die Erfindung betrifft weiterhin die nach diesem Verfahren erhältlichen Polymerisatdispersionen sowie die hydroformylierten Polymerisate selbst.
Abstract:
PROCEDIMIENTO PARA LA PREPARACION DE ETERES CICLICOS INSATURADOS DE FORMULA I EN LA CUAL Z ES - (CHR 4 ) Q - O - (CHR 4 ) Q - O -, Q ES 0, 1, 2 O 3, Y R 1 , R SUP,2 , R 3 , R 4 SON HIDROGENO O ALQUILO DE C 1 HASTA C 4 , POR REACCION DE DIOLES DE FORMULA GENERAL II EN LA CUAL Z, R 1 , R 2 Y R 3 TIENEN LOS SIGNIFICADOS ANTES CITADOS, EN FASE LIQUIDA Y A TEMPERATURAS DE 150 HASTA 300 °C EN PRESENCIA DE UN CATALIZADOR DE SOPORTE QUE CONTIENE COBALTO Y QUE NO ESTA ACTIVADO POR REDUCCION ANTES DE SU UTILIZACION, QUE CONTIENE COBALTO Y UN METAL NOBLE POR IMPREGNACION CON UN SOL, DEL GRUPO DEL PLATINO, PALADIO, RODIO, IRIDIO, RUTENIO, OSMIO, RENIO O SUS MEZCLAS, SOBRE UN SOPORTE INERTE, CARACTERIZADO PORQUE EL CATALIZADOR SOPORTE ESTA CARGADO CON AZUFRE, ASI COMO CATALIZADORES DE SOPORTE, QUE CONTIENEN COBALTO Y METALES NOBLES QUE ESTAN CARGADOS CON AZUFRE.
Abstract:
A process for the production of beta -alkoxy-nitriles which is carried out in the presence of a basic diazabicycloalkene catalyst. Production of beta -alkoxy-nitriles which involves reaction of alpha , beta -unsaturated nitriles with mono-, di- or tri- valent alcohols in the presence of a basic diazabicycloalkene of formula (1), at (-) 20-200 degrees C. n, m = 1-6; and where the 1-4 H atoms are optionally substituted by R -R ; R -R = 1-20C alkyl, 6-20C aryl or 7-20C arylalkyl. An Independent claim is also included for a production process of a gamma -alkoxy-amine by hydrogenation of the beta -alkoxy-nitrile in the presence of a hydrogenation catalyst and the catalyst of formula (1).
Abstract:
A process for the hydroformylation of polymers containing ethylenic double bonds (I) by reacting (I) with carbon monoxide (CO) in presence of a hydroformylation catalyst, the reaction being carried out in an aqueous dispersion of (I) under conditions such that the catalyst is at least partly in the polymer phase or at least partly in the polymer/water interface. Also claimed are (i) polymer dispersions obtained by this process and (ii) polymers obtained from these dispersions by removing the aqueous solvent.