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    • 8. 发明申请
    • Two-Stage, Gas Phase Process for the Manufacture of Alkylene Glycol
    • 用于制备亚烷基二醇的两相气相工艺
    • US20100036176A1
    • 2010-02-11
    • US12533753
    • 2009-07-31
    • Joseph C. NoronhaElbert J. CampbellBrian T. KeenDick A. NagakiHwaili SooDavid A. SpearsJohn F. Szul
    • Joseph C. NoronhaElbert J. CampbellBrian T. KeenDick A. NagakiHwaili SooDavid A. SpearsJohn F. Szul
    • C07C29/03
    • C07C29/106C07D301/06C07C31/202
    • A two-stage, gas phase process for manufacturing alkylene glycol (e.g., ethylene glycol) from an alkene (e.g., ethylene), oxygen and water, the process comprising the steps of: (A) Contacting under gas phase, oxidation conditions gaseous alkene and oxygen over a heterogeneous oxidation catalyst to produce a gaseous oxidation product comprising alkylene oxide, water and unreacted alkene; (B) Contacting under gas phase, hydrolysis conditions the gaseous oxidation product of (A) with added water over a heterogeneous hydrolysis catalyst to produce a gaseous alkylene glycol and unreacted alkene; and (C) Recycling the unreacted alkene of (B) to (A). The hydrolysis catalyst is selected from the group consisting of hydrotalcites, metal-loaded zeolites, phosphates, and metal-loaded ion-exchanged molecular sieves. The process improves over the conventional two-stage process by the elimination of steps and equipment to recover and refine alkylene oxide, the use of less water in the hydrolysis reaction, and the elimination of the entire evaporation train used in the recovery of alkylene glycol.
    • 用于从烯烃(例如乙烯),氧气和水制造亚烷基二醇(例如乙二醇)的两阶段气相方法,该方法包括以下步骤:(A)在气相,氧化条件下接触气态烯烃 和氧在异相氧化催化剂上产生包含环氧烷,水和未反应的烯烃的气态氧化产物; (B)在气相下接触,水解条件下将(A)的气态氧化产物与加入的水在非均相水解催化剂上反应生成气态的亚烷基二醇和未反应的烯烃; 和(C)将(B)的未反应烯烃回收至(A)。 水解催化剂选自水滑石,负载金属的沸石,磷酸盐和负载金属的离子交换分子筛。 该方法通过消除步骤和设备来回收和改进氧化烯,在水解反应中使用较少的水以及消除用于回收亚烷基二醇的整个蒸发系统,改进了常规的两阶段方法。
    • 9. 发明申请
    • Process for the production of alkylene oxide using a gas-phase promoter system
    • 使用气相促进剂体系生产环氧烷的方法
    • US20070032670A1
    • 2007-02-08
    • US10571508
    • 2004-08-09
    • Liping ZhangHwaili SooJuliana Serafin
    • Liping ZhangHwaili SooJuliana Serafin
    • C07D301/06
    • C07D301/10Y02P20/582
    • An improved process for the manufacture of ethylene oxide through the epoxidation of ethylene using a catalyst comprising silver and at least one efficiency-enhancing salt of a member of a redox-half reaction pair. Added to the epoxidation reaction is a two-component gas-phase promoter system comprising a chlorine-containing component (for example ethyl chloride, methyl chloride, vinyl chloride and ethylene dichloride), and a nitrogen-containing component of nitric oxide and other compounds capable of generating under reaction conditions at least one gaseous efficiency-enhancing member of a redox-half reaction pair comprising NO, NO2, N2O3 or N2O4. The amount of each component of said gaseous promoter is adjusted to maintain the ration of N* to Z* less than or equal to 1 wherein, N* is the nitric oxide equivalent in ppmv, ranging from 1 to 20 ppmv and Z*=ethyl chloride equivalent (ppmv)*100 percent/ethane equivalent (mol percent)*100 ranging from 5 to 40 ppmv.
    • 通过使用包含银和至少一种氧化还原半反应对成员的效率增强盐的催化剂通过乙烯环氧化制备环氧乙烷的改进方法。 添加到环氧化反应中是包含含氯组分(例如氯乙烷,甲基氯,氯乙烯和二氯乙烷)的二组分气相促进剂体系,以及一氧化氮和其它化合物的含氮组分 在反应条件下产生氧化还原半反应对的至少一种气体效率增强成分,其包含NO,NO 2,N 2 O 3, >或N 2 O 4。 调整所述气体促进剂的每种组分的量以保持N *至Z *的比例小于或等于1,其中N *是以ppmv计的一氧化氮当量,范围为1至20ppmv,Z * =乙基 氯化物当量(ppmv)* 100%/乙烷当量(摩尔%)* 100为5〜40ppmv。