REMOVAL OF HALOGENIZED SUBSTANCE FROM NITRIDE MIXTURE CONTAINING THE SAME

    公开(公告)号:JPH10265445A

    公开(公告)日:1998-10-06

    申请号:JP4030898

    申请日:1998-02-23

    Applicant: BASF AG

    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.

    PRODUCTION OF ALKYLAMINE
    2.
    发明专利

    公开(公告)号:JPH11100374A

    公开(公告)日:1999-04-13

    申请号:JP20740698

    申请日:1998-07-23

    Applicant: BASF AG

    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.

    PRODUCTION OF N-SUBSTITUTED CYCLIC AMINE

    公开(公告)号:JPH1072454A

    公开(公告)日:1998-03-17

    申请号:JP15828297

    申请日:1997-06-16

    Applicant: BASF AG

    Abstract: PROBLEM TO BE SOLVED: To enable to industrially simply and profitably obtain the subject compound from a primary amine and a diol by using a specific copper- containing hydrogenation/dehydrogenation catalyst. SOLUTION: This method for producing an N-substituted cyclic amine of formula I comprises reacting (C) a compound of the formula: R -NH2 [R is an (alkoxy)alkyl, an aryl, etc.,] with (D) a compound of the formula: HO-A-OH A is an alkylene (substituted by a group of the formula: R (R is R ), a group of the formula: (CH2 )n -[O-(CH )m ]r , [(m), (n) are each 2-8; (r) is 1-3]} in the presence of a coppercontaining catalyst. The copper-containing catalyst is obtained by impregnating an inactive carrier (e.g. silicon dioxide, a silicate or zeolite) with (A) hydrogen and (B) the aqueous ammine complex solution of an easily pyrolytic copper compound (e.g. copper carbonate, copper oxalate or copper formate)(preferably an ammoniacal copper carbonate solution), drying the impregnated carrier, and subsequently calcining the dried product, and contains the copper in an amount of 5-50wt.% converted into CuO on the basis of the whole amount of the calcined catalyst.

    Production of beta-alkoxynitrile or gamma-alkoxyamine
    5.
    发明专利
    Production of beta-alkoxynitrile or gamma-alkoxyamine 审中-公开
    β-烷氧基硅烷或γ-羟基烷基胺的生产

    公开(公告)号:JPH11279135A

    公开(公告)日:1999-10-12

    申请号:JP1752499

    申请日:1999-01-26

    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 translation: 要解决的问题:通过使用特定的二氮杂双环链烯烃作为碱性催化剂,通过α,β-不饱和腈和醇之间的反应获得目标化合物,而不需要任何预先分离或中和加成反应的催化剂。 溶液:该化合物通过α-β-不饱和腈(如丙烯腈)与一元二元或三元醇(如甲醇,乙醇,2-乙基己醇,2-甲氧基乙醇,苄醇)在-20〜200 (H可以被1-20C烷基,6-20C芳基或7-20C芳基烷基取代;(n)和(m)各自为1-6)作为碱性催化剂,例如 1,5-二氮杂双环[4.3.0]壬烯-5(DBN),1,8-二氮杂双环[5.4.0]十一碳烯-7(DBU)}; 其中所用的催化剂的量是优选的。 基于醇为0.05-5重量%。

    VAPOR-PHASE DEHYDROGENATION OF 1,4-BUTANEDIOL INTO GAMMA-BUTYROLACTONE

    公开(公告)号:JPH10152485A

    公开(公告)日:1998-06-09

    申请号:JP23922397

    申请日:1997-09-04

    Applicant: BASF AG

    Abstract: PROBLEM TO BE SOLVED: To provide a method which effects the subject reaction in the vapor phase advantageously from industrial, economical and environmental aspects in the presence of a catalyst composed of copper and Na2 O supported by a carrier composed of SiO2 and CaO. SOLUTION: This method effects the subject reaction in the presence of free hydrogen by passing 1,4-butanediol over an immobilized phase of catalyst composed of 4 to 40wt.%, preferably 4 to 32wt.%, of copper and 0 to 5wt.%, preferably 0 to 2wt.%, of Na2 O, each percentage being based on the total quantity of the catalyst, supported by a carrier composed of 80 to 100wt.%, preferably 90 to 100wt.%, of SiO2 and 0 to 20wt.%, preferably 0 to 10wt.%, of CaO, where the copper grains having an average diameter of 10 to 100nm are dispersed at a rate of 20 to 50% so as to have a surface area of 10 to 50m /g over the carrier, under the conditions of temperature: 150 to 300 deg.C, preferably 190 to 230 deg.C, absolute pressure: 1 to 40 bar, preferably about 1 bar, and hourly space velocity of 1,4-butanediol: 0.2 to 20kg, preferably 0.5 to 7.5kg, per kg copper, with the carrier gas containing free hydrogen being reused as the recycle gas.

    REACTION OF ORGANIC COMPOUND, AND CATALYST

    公开(公告)号:JPH1053539A

    公开(公告)日:1998-02-24

    申请号:JP12283197

    申请日:1997-04-28

    Applicant: BASF AG

    Abstract: PROBLEM TO BE SOLVED: To provide a method for reacting an organic compound by which the reaction of the organic compound is performed in extremely high yield or nearly complete conversion by using a specific catalyst. SOLUTION: All organic compound of a monomer and a polymer, especially an organic compound having a treatable group by hydrogen such as C-C double bond and C-C triple bond are reacted in the presence of a uniform ruthenium compound or a mixture of two or more kinds thereof deposited on a carrier in situ in the method for reacting an organic compound. The reaction is preferably hydrogenation, dehydrogenation, hydrogenolysis, amination hydrogenation or dehalogenation. The catalyst is the supported catalyst obtained by subjecting a solution of the ruthenium compound or two or more kinds thereof to pass through in the carrier or on the carrier to form the uniform ruthenium compound or mixture of two or more compound thereof deposited on the carrier. The smallest amount of a byproduct or a degrading product is formed during the hydrogenation and the reaction is performed without separation, after- treatment and recycle of the catalyst in the method.

    9.
    发明专利
    未知

    公开(公告)号:DE59805686D1

    公开(公告)日:2002-10-31

    申请号:DE59805686

    申请日:1998-11-26

    Applicant: BASF AG

    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).

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