Cyclohexanone distillation process
    71.
    发明授权
    Cyclohexanone distillation process 失效
    环己酮蒸馏工艺

    公开(公告)号:US4306944A

    公开(公告)日:1981-12-22

    申请号:US165905

    申请日:1980-07-03

    Abstract: 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a feed mixture comprising cyclohexanone, phenol and cyclohexanol of the type wherein a cyclohexanone-rich stream is withdrawn as a part of an overheads condensate from the first still and a phenol-rich stream is withdrawn as a part of a reboiled bottom stream from the first still.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.

    Abstract translation: 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。

    Process for the preparation of 3-phenoxy-benzaldehydes
    72.
    发明授权
    Process for the preparation of 3-phenoxy-benzaldehydes 失效
    3-苯氧基 - 苯甲醛的制备方法

    公开(公告)号:US4275241A

    公开(公告)日:1981-06-23

    申请号:US89010

    申请日:1979-10-29

    CPC classification number: C07C47/575 C07C45/29 C07C45/292 C07C45/82

    Abstract: A process for the preparation of a-phenoxy-benzaldehyde which comprises contacting the 3-phenoxy-benzyl alcohol of the formula ##STR1## wherein R.sup.1 and R.sup.2 are identical or different and represent hydrogen or halogen with an aqueous solution of a dichromate in the presence of aqueous sulphuric acid at a temperature in the range of 50.degree. to 125.degree. C. The 3-phenoxy-benzaldehyde can be in a mixture of other organic compounds such as obtained by hydrolyzing a 3-phenoxy toluene chlorinated in the side chain at a temperature of 140.degree.-210.degree. C. under pressure.

    Abstract translation: 一种制备苯氧基苯甲醛的方法,该方法包括使下式的“3-苯氧基苯甲醇”与其中R1和R2相同或不同并且在存在下与重铬酸盐的水溶液代表氢或卤素 的硫酸水溶液在50至125℃的温度范围内。3-苯氧基 - 苯甲醛可以是其它有机化合物的混合物,例如通过水解在侧链中氯化的3-苯氧基甲苯, 温度为140°-210℃。

    Recovery of acetone produced by carbonylation
    73.
    发明授权
    Recovery of acetone produced by carbonylation 失效
    通过羰基化回收丙酮

    公开(公告)号:US4252748A

    公开(公告)日:1981-02-24

    申请号:US974291

    申请日:1978-12-29

    Abstract: Acetone produced as a by-product in the reaction of methyl acetate with carbon monoxide and hydrogen in the presence of a Group VIII noble metal catalyst and methyl iodide is recovered from the reaction mixture by supplying acetone to provide an acetone to methyl iodide molar ratio of at least 1:10 and distilling the mixture comprising methyl iodide, acetone and methyl acetate to separate substantially all of the methyl iodide and the supplied acetone and some of the methyl acetate from the remaining acetone and methyl acetate and thereafter separating the acetone from the methyl acetate.

    Abstract translation: 在第VIII族贵金属催化剂和甲基碘存在下,乙酸甲酯与一氧化碳和氢气在乙酸甲酯和氢气的反应中作为副产物产生的丙酮通过供应丙酮从反应混合物中回收,得到丙酮至甲基碘的摩尔比 至少1:10,并蒸馏含有甲基碘,丙酮和乙酸甲酯的混合物,从剩余的丙酮和乙酸甲酯中分离基本上所有的甲基碘和所提供的丙酮和一些乙酸甲酯,然后将丙酮从甲基 乙酸盐。

    Process for the manufacture of acetaldehyde
    75.
    发明授权
    Process for the manufacture of acetaldehyde 失效
    乙醛生产工艺

    公开(公告)号:US4237073A

    公开(公告)日:1980-12-02

    申请号:US50313

    申请日:1979-06-20

    CPC classification number: C07C45/82 C07C45/34 C07C45/783 C07C45/83

    Abstract: Process for the manufacture of acetaldehyde by reaction of ethylene and oxygen in the presence of an aqueous solution of palladium and copper chloride, in which continuously part of the latter solution is regenerated by heating it outside of the reactor. The gaseous mixture leaving the reactor is treated (a) by cooling with recycling of the condensate formed to the reactor and completion of the water portion that has not condensed during cooling, by the addition of water to the reactor, (b) by washing of the cooled gas mixture with water whereby an aqueous acetaldehyde solution is obtained, (c) by extractive distillation of this solution using water as extraction agent. Next, pure acetaldehyde is obtained as an overhead product in a further distillation step. The water demand of step (b) and optionally additionally of steps (a) and/or (c) is satisfied with the waste water obtained in the bottoms of the last distillation step and the residual waste water in each case is discharged.

    Abstract translation: 在钯和氯化铜水溶液存在下,通过乙烯和氧气的反应制备乙醛的方法,其中通过将反应器外的其中加热将其后续的一部分溶液再生。 (a)通过将形成的反应器的冷凝物和在冷却期间未冷凝的水部分的再循环冷却,通过向反应器中加入水进行冷却处理(a),(b)通过洗涤 用水冷却的气体混合物,得到乙醛水溶液,(c)通过使用水作为提取剂萃取蒸馏该溶液。 接下来,在进一步的蒸馏步骤中,作为塔顶产物获得纯乙醛。 满足步骤(b)的需水量和任选的步骤(a)和/或(c)的要求,满足最后一个蒸馏步骤底部获得的废水,并排出每种情况下的残留废水。

    Separation of cyclohexylbenzene from a
cyclohexylbenzene-cyclohexanone-phenol admixture
    76.
    发明授权
    Separation of cyclohexylbenzene from a cyclohexylbenzene-cyclohexanone-phenol admixture 失效
    环己基苯与环己基苯 - 环己酮 - 苯酚混合物的分离

    公开(公告)号:US4230638A

    公开(公告)日:1980-10-28

    申请号:US36268

    申请日:1979-05-04

    Abstract: Cyclohexylbenzene is separated from a cyclohexylbenzene-cyclohexanone-phenol admixture by liquid-liquid extraction with a non-polar solvent such as hexadecane and a polar solvent, such as sulfolane, diethylene glycol, or mixtures with water. Cyclohexylbenzene is separated from the non-polar phase by fractional distillation. Phenol and cyclohexanone are separated from the polar solvent by fractional distillation.

    Abstract translation: 将环己基苯与环己基苯 - 环己酮 - 苯酚混合物通过液 - 液萃取与非极性溶剂如十六烷和极性溶剂如环丁砜,二甘醇或与水的混合物分离。 通过分馏从非极性相分离环己基苯。 苯酚和环己酮通过分馏从极性溶剂中分离出来。

    Process for the purification of benzaldehyde
    78.
    发明授权
    Process for the purification of benzaldehyde 失效
    苯甲醛纯化方法

    公开(公告)号:US4197261A

    公开(公告)日:1980-04-08

    申请号:US952609

    申请日:1978-10-18

    Applicant: Jan Elmendorp

    Inventor: Jan Elmendorp

    CPC classification number: C07C45/78 C07C45/36 C07C45/82

    Abstract: Crude benzaldehyde, and especially benzaldehyde prepared by the oxidation of toluene with a gas containing molecular oxygen, will contain certain impurities which will cause unwarranted discoloration and olfactory problems. These impurities can be effectively removed by treating the benzaldehyde with an oxidizing agent and then distillation.

    Abstract translation: 通过用含有分子氧的气体氧化甲苯制备的粗苯甲醛,特别是苯甲醛将含有某些杂质,这将导致无理的变色和嗅觉问题。 这些杂质可以通过用氧化剂处理苯甲醛然后蒸馏而被有效地除去。

    Process for separating 11-cyanoundecanoic acid, cyclohexanone and .epsilon.
-
    80.
    发明授权
    Process for separating 11-cyanoundecanoic acid, cyclohexanone and .epsilon. - 失效
    分离11-氰基十一烷酸,环己酮和{68-己内酰胺的方法

    公开(公告)号:US4165328A

    公开(公告)日:1979-08-21

    申请号:US901089

    申请日:1978-04-28

    CPC classification number: C07C255/00 C07C45/783 C07C45/80 C07C45/82 C07D201/16

    Abstract: Disclosed is a process for separating 11-cyanoundecanoic acid, cyclohexanone and .epsilon.-caprolactam from a pyrolysis product obtained by pyrolyzing 1,1'-peroxydicyclohexylamine in the presence of steam at a temperature of 300.degree. to 1,000.degree. C. The pyrolysis product is first contacted with a mixture comprised of aqueous ammonia and at least one organic solvent selected from benzene, toluene and xylene, and the so prepared liquid is separated into the oily layer and the aqueous layer. On one hand, the oily layer is distilled to separate cyclohexanone therefrom. On the other hand, the aqueous layer is acidified to a pH of below 4.0 by adding thereto a mineral acid and maintained at a temperature of 40.degree. to 100.degree. C. to separate crude 11-cyanoundecanoic acid in molten form from the aqueous layer, and then, the separated crude molten 11-cyanoundecanoic acid is washed with hot water to extract .epsilon.-caprolactam therefrom.

    Abstract translation: 公开了一种通过在300℃至1000℃的温度下在1,1'-二氧化二环己基胺蒸气存在下热解得到的热解产物中分离出11-氰基十一烷酸,环己酮和ε-己内酰胺的方法。热解产物是先 与由氨水和选自苯,甲苯和二甲苯中的至少一种有机溶剂组成的混合物接触,将如此制备的液体分离成油层和水层。 一方面,将油层蒸馏以分离出环己酮。 另一方面,通过向其中加入无机酸将水层酸化至pH值低于4.0,并保持在40℃至100℃的温度下,将熔融形式的粗的11-氰基十一烷酸与水层分离, 然后,将分离的粗熔融的11-氰基十一烷酸用热水洗涤以从其中提取ε-己内酰胺。

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