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    • 1. 发明授权
    • Method of refining dihydroxyaryl compound
    • 二羟基芳基化合物的精制方法
    • US06554967B1
    • 2003-04-29
    • US09575886
    • 2000-05-22
    • Shuji TanakaGenji KogaHiroshi KofujiTetsuro Kawashita
    • Shuji TanakaGenji KogaHiroshi KofujiTetsuro Kawashita
    • B01D334
    • C07C37/74C07C39/08
    • A refined dihydroxyaryl compound, for example, catechol, having a high degree of purity and a very low metal content is produced by evaporating a starting dihydroxyaryl compound in a distillation column, condensing the vapor fraction in a condenser connected to a top outlet of the distillation column, and collecting the condensed fraction from the condenser into a storage tank through a conduit, wherein the condenser and optionally the conduit and/or the storage tank have inside surfaces thereof formed from a metal material containing at least 25% by weight of nickel, and the condensed dihydroxyaryl compound fraction is brought into contact with the specific nickel (25% or more)-containing metal inside surface.
    • 通过在蒸馏塔中蒸发起始的二羟基芳基化合物,将蒸馏馏分冷凝在与蒸馏塔顶部相连的冷凝器中,从而制得具有高纯度和非常低的金属含量的精制二羟基芳基化合物,例如邻苯二酚 并且通过管道将冷凝的馏分从冷凝器收集到储罐中,其中冷凝器和任选地导管和/或储罐的内表面由含有至少25重量%镍的金属材料形成, 使缩合的二羟基芳基化合物部分与特定的含镍(25%以上)的金属内表面接触。
    • 4. 发明授权
    • Process and apparatus for producing dihydric phenolic compound
    • 二羟基酚类化合物的制备方法和装置
    • US06262315B1
    • 2001-07-17
    • US09320094
    • 1999-05-26
    • Yukio InabaKazunori FujitaHiroshi Kofuji
    • Yukio InabaKazunori FujitaHiroshi Kofuji
    • C07C3700
    • B01J19/245B01J2219/00103B01J2219/0011C07C37/60Y02P20/52C07C39/08
    • A dihydric phenolic compound is produced, with a high selectivity thereof, by a plurality of oxidation reactors connected to each other in series, by (1) feeding a monohydric phenolic compound with a temperature of 30 to 100° C., a peroxide compound, a catalyst and optionally a ketone compound into a first reactor to oxidize the monohydric phenolic compound, and delivering a resultant reaction mixture containing the produced dihydric phenolic compound and non-reacted monohydric phenolic compound from the first reactor; (2) passing the reaction mixture through one or more reactors succeeding to the first reactor, to further oxidize the monohydric phenolic compound, while, in the steps (1) and (2), a portion of the peroxide compound is fed into the first reactor and the remaining portion of the peroxide compound is fed into at least one succeeding reactor; and (3) delivering a first reaction mixture produced in a rearend reactor and comprising the produced dihydric phenolic compound, the non-reacted monohydric phenolic compound and peroxide compound and the catalyst from the rearend reactor.
    • 通过(1)将温度为30〜100℃的一元酚类化合物,过氧化物化合物,过氧化物化合物, 催化剂和任选的酮化合物转化成第一反应器以氧化一元酚类化合物,并从第一反应器中输送所得的含有所产生的二羟基酚化合物和未反应的一元酚化合物的反应混合物; (2)使反应混合物通过在第一反应器之后的一个或多个反应器,以进一步氧化一元酚类化合物,而在步骤(1)和(2)中,一部分过氧化物被加入第一 将剩余部分的过氧化物进料至至少一个后续反应器; 和(3)在再循环反应器中产生的第一反应混合物,并且包含所产生的二羟基酚化合物,未反应的一元酚类化合物和过氧化物化合物以及来自再循环反应器的催化剂。