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    • 2. 发明授权
    • KONTINUIERLICHES VERFAHREN ZUR HERSTELLUNG VON PSEUDOJONONEN UND JONONEN
    • 哥本哈根维多利亚ZER HERSTELLUNG VON PSEUDOJONONEN UND JONONEN
    • EP1562885B1
    • 2007-09-05
    • EP03778290.1
    • 2003-10-28
    • BASF Aktiengesellschaft
    • DOBLER, WalterBAHR, NicolausBREUER, KlausKINDLER, Alois
    • C07C45/54C07C49/203C07C403/16
    • C07C403/16C07C45/54C07C2601/14C07C2601/16C07C49/203
    • The invention relates to a continuous process for producing pseudoionones of general formulas (I) and (I′) as well as isomers thereof, whereby: R1 represents CH3 or (a); R2 and R3 represent hydrogen, CH3 or C2H5, and; R4 and R5 represent hydrogen or CH3. These pseudoionones are produced by reacting an aldehyde of formula (II) with an excess of a ketone of general formula (III), whereby R1, R2 and R3 have the aforementioned meanings, in the presence of water and alkali hydroxide at an increased temperature and in a homogeneous solution. The inventive process is characterized in that: a) the intermixing of the homogeneous solution consisting of aldehyde, ketone and aqueous alkali lye occurs at a temperature ranging from 10 to 120 °C; b) the undissolved water and alkali hydroxide contained in the reaction mixture are subsequently separated out; c) while avoiding back mixing, the homogeneous reaction mixture is then guided through a reactor, which permits a residence time ranging from 2 to 300 minutes, at a temperature that is 10 to 120 °C higher than the boiling point of the lowest-boiling component and under a vapor pressure p ranging from 106 to 107 Pa; d) the reaction mixture is cooled by expansion; e) ketone is removed from the reaction mixture using vapor flowing in the opposite direction and; f) the raw product is dried and rid from excessive aldehyde and secondary components via a rectification column.
    • 本发明涉及用于制备通式(I)和(I')的假阳离子及其异构体的连续方法,其中:R 1表示CH 3或( 一个); R 2和R 3代表氢,CH 3或C 2 H 5, ,和; R 4和R 5代表氢或CH 3。 这些假性离子是通过使式(II)的醛与过量的通式(III)的酮反应制得的,由此R 1,R 2和R 2 在水和碱性氢氧化物的存在下,在升高的温度和均匀的溶液中,具有上述含义。 本发明的方法的特征在于:a)由醛,酮和碱性碱液组成的均匀溶液的混合在10至120℃的温度下进行; b)随后将反应混合物中所含的未溶解的水和氢氧化碱分离出来; c)同时避免反混合,然后将均匀的反应混合物引导通过反应器,其允许在比最低浓度的沸点高10至120℃的温度下2至300分钟的停留时间, 沸腾成分,并且在10 -6至10 7 Pa范围内的蒸汽压力p; d)通过膨胀冷却反应混合物; e)使用沿相反方向流动的蒸汽从反应混合物中除去酮; f)将原料干燥并通过精馏塔除去过量的醛和次要组分。