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    • 1. 发明授权
    • Process for halogenation of aldehydes and production of oximes therefrom
    • 醛的卤化和肟的生产方法
    • US4155933A
    • 1979-05-22
    • US894870
    • 1978-04-10
    • John H. BonfieldAndiappan K. MurthyDonald Pickens
    • John H. BonfieldAndiappan K. MurthyDonald Pickens
    • C07C45/00C07C45/63C07C47/14C07C67/00C07C313/00C07C319/20C07C323/47C07C131/00
    • C07C45/63
    • In the halogenation under reflux conditions of an unhalogenated aldehyde of the formula ##STR1## with Cl.sub.2, Br.sub.2 or I.sub.2, the aldehyde and halogen are continuously fed into a reactor at a molar ratio of halogen to unhalogenated aldehyde between about 0.8:1 and about 1.1:1 and water is continuously fed into the unhalogenated reactor at a rate of between about 1% and about 20% by weight of aldehyde. The product .alpha.-haloaldehyde is thiohydrocarbylated and then oximated to form a 2-hydrocarbylthioaldoxime of the formula ##STR2## with improved yield and quality because of the improved yield and quality of unhalogenated .alpha.-haloaldehyde. An exemplary process includes the chlorination of isobutyraldehyde (IBA) to form .alpha.-chloroisobutyraldehyde (CIBA), the thiomethylation of CIBA to form 2-methyl-2 methylthio-propionaldehyde (MTIBA) and the oximation of MTIBA to form 2-methylthio-propionaldehyde oxime (aldicarb oxime or ADO).
    • 在式Cl 1,Br 2或I 2的未卤化醛的回流条件下,将醛和卤素以约0.8:1至约1.1的卤素与非卤化醛的摩尔比连续进料到反应器中 :1和水以醛的约1重量%至约20重量%的速率连续进料到未卤化反应器中。 产物α-卤代烃被硫代烃基化,然后氧化形成式“IMAGE”的2-烃基硫代醛肟,其产率和质量得到改善,因为改善了产生和质量的非卤代α-卤代醛。 一个示例性的方法包括异丁醛(IBA)氯化以形成α-氯异丁醛(CIBA),CIBA的甲硫基化形成2-甲基-2-甲硫基 - 丙醛(MTIBA)和肟化MTIBA以形成2-甲硫基 - 丙醛肟 (涕灭威肟或ADO)。
    • 3. 发明授权
    • Cyclohexanone distillation process
    • 环己酮蒸馏工艺
    • US4306944A
    • 1981-12-22
    • US165905
    • 1980-07-03
    • Andiappan K. MurthyDavid Y. Hsieh
    • Andiappan K. MurthyDavid Y. Hsieh
    • B01D3/14C07C29/80C07C45/82
    • C07C29/80B01D3/146C07C45/82C12C11/02C07C2101/14Y10S203/20
    • An improved process of distilling a cyclohexanone-rich overhead stream in a first still from a feed mixture comprising cyclohexanone, phenol and cyclohexanol of the type wherein a cyclohexanone-rich stream is withdrawn as a part of an overheads condensate from the first still and a phenol-rich stream is withdrawn as a part of a reboiled bottom stream from the first still. The improvement includes withdrawing a side stream substantially free of phenol from above the point where the feed mixture is fed to the first column and separating the side stream in a second still into a second cyclohexanone-rich overhead stream and a bottom stream containing cyclohexanone and cyclohexanol. The second cyclohexanone-rich stream may be returned to the first still.
    • 一种改进的蒸馏富含环己酮的塔顶馏出物的方法,仍然是包含环己酮,苯酚和环己醇的进料混合物,其中富含环己酮的物流作为来自第一馏分的塔顶馏出物冷凝物的一部分,苯酚 作为来自第一静止物的再沸腾的底部流的一部分被抽出。 该改进包括从进料混合物进料到第一塔的点以上将基本上不含苯酚的侧流排出,并将侧流在第二塔中分离成第二富含环己酮的塔顶馏出物流和含有环己酮和环己醇的塔底料流 。 第二富含环己酮的流可以返回到第一静止物。