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    • 84. 发明授权
    • Staged purification of contaminated propylene oxide
    • 污染环氧丙烷的分阶段净化
    • US5354430A
    • 1994-10-11
    • US140995
    • 1993-10-26
    • William K. Culbreth, IIIYu-Hwa E. SheuDavid G. Pottratz
    • William K. Culbreth, IIIYu-Hwa E. SheuDavid G. Pottratz
    • B01D3/40C07D301/32C07D303/04
    • C07D301/32B01D3/40
    • Contaminants are removed from impure propylene oxide by fractionating in a first column to remove overhead essentially all of the pentenes and pentanes and most of the oxygen-containing impurities to provide a partially purified first propylene oxide bottoms fraction, extractively distilling the first bottoms fraction in a second extractive column using a C.sub.2 to C.sub.6 alkylene glycol extractive distillation agent to form a second overhead fraction comprising propylene oxide, hexenes, hexanes, water, residual quantities of pentenes and pentanes and oxygen-containing impurities, extractively distilling the second overhead fraction in a third column using a C.sub.6 to C.sub.10 alkane hydrocarbon extractive distillation agent to form a third bottoms fraction comprising the extractive distillation agent, propylene oxide, hexenes, hexanes, residual quantities of pentenes and pentanes and water, and extractively distilling said third bottoms fraction in a fourth column using a C.sub.6 to C.sub.10 alkane hydrocarbon extractive distillation agent to form a fourth overhead fraction consisting essentially of propylene oxide.
    • 污染物通过在第一塔中分馏除去不纯的环氧丙烷,基本上除去基本上所有的戊烯和戊烷以及大部分含氧杂质以提供部分纯化的第一环氧丙烷底部馏分,将第一底部馏分在 第二萃取柱,使用C2至C6亚烷基二醇萃取蒸馏剂以形成包含环氧丙烷,己烯,己烷,水,残余量的戊烯和戊烷和含氧杂质的第二塔顶馏分,在第三塔中馏出第二塔顶馏分 使用C6至C10烷烃萃取蒸馏剂形成包含萃取蒸馏剂,环氧丙烷,己烯,己烷,残余量的戊烯和戊烷和水的第三塔底馏分,并将所述第三塔底馏分在第四塔中萃取蒸馏 使用C6至C10烷烃 萃取蒸馏剂以形成基本上由环氧丙烷组成的第四塔顶馏分。
    • 88. 发明授权
    • Method for production of ethylene oxide
    • 环氧乙烷生产方法
    • US5292904A
    • 1994-03-08
    • US942632
    • 1992-09-09
    • Masayuki SawadaYukihiko Kakimoto
    • Masayuki SawadaYukihiko Kakimoto
    • B01J8/06C07D301/10C07D303/04
    • B01J8/067C07D301/10B01J2208/00212B01J2208/00221B01J2208/00256B01J2208/00274B01J2219/00777
    • The production of ethylene oxide by the catalytic vapor phase oxidation of ethylene with a molecular oxygen-containing gas is effected in a reactor provided with a preheating zone, a reaction zone, a cooling zone, a partition plate separating the first two portions from the third portion, and a multiplicity of reaction tubes piercing the two separated sections by a method which comprises supplying hot water to the cooling zone of the reactor, forwarding zone of the hot water discharged from the cooling zone to a gas-liquid separation tank, circulating the remainer of the hot water in conjunction with the cooling hot water to the cooling zone, supplying the hot water separated in the gas-liquid separation tank to the reaction zone to remove the heat of the oxidation reaction, and circulating the hot water extracted in the form of a gas-liquid mixed phase to the gas-liquid separation tank. The method is excellent to prevent isomerization of ethylene oxide to acetaldelyde which is impurity, excels in thermal efficiency and exhibits ideal durability of the partition plate.
    • 通过在含有分子氧气体的乙烯的催化气相氧化中生产环氧乙烷是在具有预热区域,反应区域,冷却区域的反应器,将前两个部分与第三个 部分和多个反应管穿过两个分开的部分,方法包括向冷却区的冷却区供给热水,将从冷却区排出的热水的转运区域送入气液分离槽, 剩余的热水与冷却热水一起连接到冷却区,将分离在气液分离罐中的热水供应到反应区以除去氧化反应的热量,并将在 形式的气液混合相到气液分离罐。 该方法优异地防止环氧乙烷异构化为杂质的乙缩醛,热效率优异,并且表现出理想的隔板耐久性。