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    • 5. 发明申请
    • Process for producing carbonic ester
    • 生产碳酸酯的方法
    • US20050240045A1
    • 2005-10-27
    • US10522754
    • 2003-08-06
    • Nobuhisa MiyakeTomonari Watanabe
    • Nobuhisa MiyakeTomonari Watanabe
    • C07C68/04C07C69/96
    • C07C68/04C07C69/96
    • A method for producing a carbonic ester, comprising: (1) performing a reaction between an organometal compound mixture and carbon dioxide, the organometal compound mixture comprising a reactive organometal compound and an unregenerable unreactive compound derived from the reactive organometal compound, to thereby obtain a reaction mixture containing a carbonic ester, the unregenerable unreactive compound, and a regenerable metamorphic organometal compound derived from the reactive organometal compound, (2) separating the reaction mixture into a first portion containing the carbonic ester and the unregenerable unreactive compound, and a second portion containing the regenerable metamorphic organometal compound, and (3) reacting the second portion of the reaction mixture with an alcohol to form an organometal compound mixture and water and removing the water from the organometal compound mixture, the organometal compound mixture comprising a reactive organometal compound and an unregenerable unreactive compound derived from the reactive organometal compound.
    • 一种制备碳酸酯的方法,包括:(1)在有机金属化合物混合物和二氧化碳之间进行反应,所述有机金属化合物混合物包含反应性有机金属化合物和衍生自反应性有机金属化合物的不可再生非反应性化合物,从而获得 含有碳酸酯的反应混合物,不可再生的非反应性化合物和衍生自反应性有机金属化合物的可再生的变质有机金属化合物,(2)将反应混合物分离成含有碳酸酯和不可再生非反应性化合物的第一部分, 含有可再生的变质有机金属化合物,和(3)使反应混合物的第二部分与醇反应以形成有机金属化合物混合物和水,并从有机金属化合物混合物中除去水,所述有机金属化合物混合物包含反应性有机金属化合物和 一个未注册者 衍生自反应性有机金属化合物的非反应性化合物。
    • 6. 发明授权
    • Reactor and continuous process to be carried out therewith for the
preparation of ethylene glycol carbonate and propylene glycol carbonate
    • 用于制备乙二醇碳酸酯和丙二醇碳酸酯的反应器和连续方法
    • US5508442A
    • 1996-04-16
    • US251229
    • 1994-05-31
    • Paul WagnerChristine Mendoza-FrohnHans-Josef Buysch
    • Paul WagnerChristine Mendoza-FrohnHans-Josef Buysch
    • C07C68/04C07C69/96C07D317/36C07D317/38C07D321/00C07D323/00
    • C07D317/36C07D317/38Y02P20/142
    • A bubble column reactor is described which is characterized by a slenderness ratio at a ratio of height to diameter of 2 to 50, a feed, at the bottom end of the bubble column, for the ethylene glycol carbonate (EGG) or propylene glycol carbonate (PGC) already present serving as reaction medium, one or more metering sites for the starting materials CO.sub.2 and ethylene oxide (EOX) or propylene oxide (POX) above the feed for the reaction medium, an outlet for the reaction mixture at the top end of the bubble column, a dividing apparatus connected thereto for the reaction mixture flowing off for dividing it into reaction mixture to be taken off and worked up on the one hand and reaction mixture to be recycled on the other hand and additionally a return line to the feed for the reaction mixture to be recycled. This bubble column reactor can be advantageously used in a process for the continuous preparation of EGG or PGC which is carried out in the temperature range from 100.degree. to 200.degree. C., in the pressure range from 5 to 200 bar and at a molar ratio of 1.01 to 1.5 mol of CO.sub.2 per mol of alkylene oxide in EGG or PGC already present as reaction medium in an amount which is 7 to 350 times that of the newly formed EGG or PGC.
    • 描述了泡罩塔反应器,其特征在于高度与直径的比率为2-50的细长比,在气泡塔的底端,乙二醇碳酸酯(EGG)或丙二醇碳酸酯( PGC)作为反应介质,用于反应介质的进料上方的原料CO 2和环氧乙烷(EOX)或环氧丙烷(POX)的一个或多个测量位点,反应混合物的顶部出口 气泡塔,连接到其上的分离装置,用于将反应混合物流出以将其分离成反应混合物,一方面将其除去和处理,另一方面将反应混合物再循环,另外还有一个到进料的回流管 使反应混合物回收。 该气泡塔式反应器可有利地用于连续制备EGG或PGC的方法中,该方法在100至200℃的温度范围内,压力范围为5至200巴,摩尔比 以EGG或PGC中的环氧烷的摩尔量为1.01〜1.5摩尔,作为反应介质,其量为新形成的EGG或PGC的7〜350倍。