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    • 5. 发明公开
    • Method for production of esterified product
    • Verfahren zur Herstellung von veresterten Verbindungen
    • EP0989108A2
    • 2000-03-29
    • EP99118597.6
    • 1999-09-21
    • Nippon Shokubai Co., Ltd.
    • Hirata, TsuyoshiYuasa, Tsutomu
    • C07C67/08
    • C07C67/08Y10S526/932C07C69/54
    • A method for the production of an esterified product is provided which affords an esterified product with high quality by repressing, during the esterification reaction of an alcohol with (meth)acrylic acid, the occurrence of impurities, particularly gel, to be formed owing to the polymerization of the alcohol and the (meth)acrylic acid as raw materials, the esterified product consequently formed, or the mixture thereof. Specifically, a method for the production of an esterified product of this invention comprises esterifying an alcohol represented by the following formula (1):

              R 1 O(R 2 O) n H     (1)

      wherein R 1 represents a hydrocarbon group of 1 to 30 carbon atoms, R 2 O represents an oxyalkylene group of 2 to 18 carbon atoms, providing that the repeating units, R 2 O, may be the same or different and that when the R 2 O's are in the form of a mixture of two or more species, the repeating units, R 2 O, may be added either in a block form or in a random form, and n represents an average addition mol number of oxyalkylene groups and is in the range of 0 to 300, with (meth)acrylic acid in a dehydrating solvent in the presence of an acid catalyst and a polymerization inhibitor, wherein a reaction temperature during the esterification reaction is not higher than 130 °C and a circulation speed of the solvent during the esterification reaction is not less than 0.5 cycle/hour.
    • 提供了一种生产酯化产物的方法,其通过在醇与(甲基)丙烯酸的酯化反应期间通过压制提供高质量的酯化产物,由于 醇和(甲基)丙烯酸作为原料的聚合,因此形成的酯化产物或其混合物。 具体地说,本发明的酯化产物的制造方法包括将下式(1)表示的醇酯化:R 1 O(R 2 O)n H其中R 1表示烃基, 1至30个碳原子,R 2 O表示2至18个碳原子的氧化烯基团,条件是重复单元R 2 O可以相同或不同,并且当R 2 O是 以两种或更多种的混合物的形式,重复单元R 2 O可以以嵌段形式或无规形式加成,n表示氧化烯基的平均加成摩尔数,并且在 在酸催化剂和聚合抑制剂的存在下,在脱水溶剂中,使用(甲基)丙烯酸,与(甲基)丙烯酸反应,其中酯化反应中的反应温度不高于130℃,循环速度为 酯化反应中的溶剂不小于0.5循环/小时。