Process for the preparation of polyhydric alcohols
    1.
    发明授权
    Process for the preparation of polyhydric alcohols 失效
    制备多元醇的方法

    公开(公告)号:US3975450A

    公开(公告)日:1976-08-17

    申请号:US502331

    申请日:1974-09-03

    IPC分类号: C07C29/00

    CPC分类号: C07C29/00

    摘要: Polyhydric alcohols are prepared by the aldol condensation of an aldehyde having 1 to 3 hydrogens on the alpha-carbon atom with formaldehyde in the presence of sodium carbonate and the subsequent crossed Cannizzaro reaction wherein the aldol condensation product is reacted with additional formaldehyde and sodium carbonate to form a polyhydric alcohol.

    摘要翻译: 多元醇是通过在碳酸钠的存在下,在α碳原子上具有1至3个氢的醛与醛的醛醇缩合制备的,随后进行交叉的Cannizzaro反应,其中醛醇缩合产物与另外的甲醛和碳酸钠反应 形成多元醇。

    Production of 2,2-disubstituted propiolactones
    2.
    发明授权
    Production of 2,2-disubstituted propiolactones 失效
    2,2-二取代丙内酯的制备

    公开(公告)号:US3994929A

    公开(公告)日:1976-11-30

    申请号:US583338

    申请日:1975-06-02

    IPC分类号: B01J23/20 C07D305/12

    CPC分类号: C07D305/12 B01J23/20

    摘要: The present invention relates to a process for the manufacture of 2,2-disubstituted propiolactones via the pyrolysis of methylene diisoalkylate in the vapor phase over a fixed bed catalyst system. The reaction of the invention is as follows: ##SPC1##Wherein R is alkyl of from 1 to 4 carbon atoms and R.sup.1 is alkyl of from 1 to 4 carbon atoms or phenyl. The catalyst comprises an oxide of a metal selected from the group Ag, U, Zn, Ti, Zr, Th, Ta, Nb, Mo, W, and Sn on a suitable support. A preferred catalyst is the metal oxide-silica gel complex which results from heating the calcined residue of a salt of a metal selected from the group consisting of Ta, Ti, Nb and Zr supported upon a silica gel in the presence of nitrogen and steam at a temperature of from about 650.degree. C. to about 1000.degree. C. The process is operable at temperatures from about 240.degree. C. to about 360.degree. C. with contact times ranging from about 0.1 second to about 30.0 seconds. The gaseous ester feed may, if desired, be diluted with an inert gas such as nitrogen and the reactor may be run at atmospheric, or superatmospheric pressure.

    摘要翻译: 本发明涉及通过气相中的亚甲基二异烷基化物在固定床催化剂体系上的热解制备2,2-二取代的丙内酯的方法。 本发明的反应如下:+ q,10,其中R为1至4个碳原子的烷基,R 1为1至4个碳原子的烷基或苯基。 该催化剂包括在合适的载体上选自Ag,U,Zn,Ti,Zr,Th,Ta,Nb,Mo,W和Sn中的金属的氧化物。 优选的催化剂是金属氧化物 - 硅胶复合物,其通过在氮气和蒸汽的存在下,将负载在硅胶上的选自Ta,Ti,Nb和Zr的金属的煅烧残渣加热, 温度为约650℃至约1000℃。该方法可在约240℃至约360℃的温度下操作,接触时间为约0.1秒至约30.0秒。 如果需要,气态酯进料可以用惰性气体如氮气稀释,并且反应器可以在大气压或超大气压下进行。

    Preparation of nitriles
    3.
    发明授权
    Preparation of nitriles 失效
    腈的制备

    公开(公告)号:US3979432A

    公开(公告)日:1976-09-07

    申请号:US620099

    申请日:1975-10-06

    IPC分类号: C07C120/08

    CPC分类号: C07C253/22

    摘要: An improved process for the production of aliphatic nitriles having two to six carbon atoms by the reaction of an aliphatic carboxylic acid with ammonia in the presence of a catalyst followed by effluent distillation. The improvement lies in the addition of a portion of the aliphatic carboxylic acid after the reactor but before distillation whereby ammonium carboxylate formed in the reaction and dissociated by distillation is reformed to the carboxylate thus preventing the escape of dissociated ammonia and whereby the aliphatic carboxylic acid portion is recycled to the reaction.

    摘要翻译: 通过在催化剂存在下通过脂族羧酸与氨的反应,然后进行流出物蒸馏,制备具有2-6个碳原子的脂族腈的改进方法。 改进之处在于在反应器之后但在蒸馏之前加入一部分脂族羧酸,由此在反应中形成的羧酸铵和通过蒸馏解离的羧酸盐重整成羧酸盐,从而防止解离的氨逸出,由此脂族羧酸部分 被回收到反应。

    Noncatalyzed aldol reaction
    5.
    发明授权
    Noncatalyzed aldol reaction 失效
    非催化醛醇反应

    公开(公告)号:US4017537A

    公开(公告)日:1977-04-12

    申请号:US607160

    申请日:1975-08-25

    IPC分类号: C07C67/08 C07C67/44

    CPC分类号: C07C67/00

    摘要: The process of carrying out aldol condensations either batch-wise or continuously without catalyst with formaldehyde and another aldehyde in the presence of esterifying acid at a temperature of from about 150.degree. C to about 280.degree. C., with from about 170.degree. C. to about 190.degree. C. being preferred.

    摘要翻译: 在约150℃至约280℃的温度下,在约150℃至约280℃的温度下,分别或连续地进行醛醇缩合的过程,不用催化剂与甲醛和另一种醛在酯化酸存在下进行,其中约170℃至约 约190℃是优选的。