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    PROCESS FOR THE PRODUCTION OF A 1,2-DIOL, A 1,2-DIOL ETHER, OR AN ALKANOLAMINE
    4.
    发明申请
    PROCESS FOR THE PRODUCTION OF A 1,2-DIOL, A 1,2-DIOL ETHER, OR AN ALKANOLAMINE 有权
    生产1,2-二醇，1,2-二醇醚或烷醇胺的方法

    公开(公告)号：US20120065433A1

    公开(公告)日：2012-03-15

    申请号：US13300160

    申请日：2011-11-18

    申请人： William Herman GERDES ,  John Robert LOCKEMEYER ,  Donald James REMUS ,  Thomas SZYMANSKI ,  Randall Clayton YEATES

    发明人： William Herman GERDES ,  John Robert LOCKEMEYER ,  Donald James REMUS ,  Thomas SZYMANSKI ,  Randall Clayton YEATES

    IPC分类号： C07C41/02 ,  C07C213/00 ,  C07C29/00

    CPC分类号： B01J23/66 ,  B01J21/04 ,  B01J21/12 ,  B01J23/50 ,  B01J23/688 ,  B01J35/10 ,  B01J35/1009 ,  B01J35/1038 ,  B01J35/1042 ,  B01J35/1071 ,  B01J35/108 ,  B01J37/0018 ,  C07C29/106 ,  C07D301/10 ,  Y02P20/52 ,  C07C31/202

    摘要： A catalyst which comprises a carrier and silver deposited on the carrier, which carrier has a surface area of at least 1.3 m2/g, a median pore diameter of more than 0.8 μm, and a pore size distribution wherein at least 80% of the total pore volume is contained in pores with diameters in the range of from 0.1 to 10 μm and at least 80% of the pore volume contained in the pores with diameters in the range of from 0.1 to 10 μm is contained in pores with diameters in the range of from 0.3 to 10 μm; process for the preparation of a catalyst which process comprises depositing silver on a carrier, wherein the carrier has been obtained by a method which comprises forming a mixture comprising: a) from 50 to 95 weight percent of a first particulate a-alumina having a median particle size (d50) of from 5 to 100 μm; b) from 5 to 50 weight percent of a second particulate a-alumina having a d50 which is less than the d50 of the first particulate a-alumina and which is in the range of from 1 to 10 μm; and c) an alkaline earth metal silicate bond material; weight percent being based on the total weight of a-alumina in the mixture; and firing the mixture to form the carrier; a process for the epoxidation of an olefin, which process comprises reacting a feed comprising an olefin and oxygen in the presence of a said catalyst; and a process for preparing a 1,2-diol, a 1,2-diol ether or an alkanolamine.

    摘要翻译： 一种催化剂，其包含沉积在载体上的载体和银，该载体的表面积至少为1.3m 2 / g，中值孔径大于0.8μm，孔径分布为总共至少80％ 孔体积包含在直径在0.1至10μm范围内的孔中，并且直径在0.1至10μm范围内的孔中所含的孔体积的至少80％包含在直径范围内的孔中 为0.3〜10μm; 一种制备催化剂的方法，该方法包括在载体上沉积银，其中载体已经通过包括形成混合物的方法获得，所述方法包括：a）50至95重量％的第一颗粒状α-氧化铝，其具有中间 粒度（d50）为5〜100μm; b）5至50重量％的具有小于第一颗粒α-氧化铝的d50并且在1至10μm范围内的d50的第二颗粒状α-氧化铝; 和c）碱土金属硅酸盐粘合材料; 重量百分比基于混合物中α-氧化铝的总重量; 并将混合物烧制成载体; 一种烯烃环氧化方法，该方法包括在所述催化剂存在下使包含烯烃和氧的进料反应; 和1,2-二醇，1,2-二醇醚或链烷醇胺的制备方法。

    PROCESS FOR THE START-UP OF AN EPOXIDATION PROCESS
    5.
    发明申请
    PROCESS FOR THE START-UP OF AN EPOXIDATION PROCESS 审中-公开
    环氧化过程启动的过程

    公开(公告)号：US20130253209A1

    公开(公告)日：2013-09-26

    申请号：US13613896

    申请日：2012-09-13

    申请人： Randall Clayton YEATES

    发明人： Randall Clayton YEATES

    IPC分类号： C07D301/10

    CPC分类号： C07D301/10 ,  Y02P20/142 ,  Y02P20/52

    摘要： The present disclosure provides processes for the start-up of an ethylene epoxidation process comprising: a. contacting a high selectivity epoxidation catalyst with a feed comprising ethylene, oxygen and an organic chloride for a period of time such that vinyl chloride is produced and capable of being detected in a reactor outlet stream or a recycle gas loop; b. increasing the temperature of the high selectivity epoxidation catalyst to at least about 220° C.; c. subsequently reducing the level of organic chloride in the feed over a period of from about 12 to about 36 hours so as to increase the temperature of the catalyst to a temperature of from about 250° C. to about 265° C.; and d. subsequently adjusting the level of organic chloride in the feed to a value sufficient to produce ethylene oxide at a substantially optimum selectivity at a temperature of from about 250° C. to about 265° C.

    摘要翻译： 本公开提供了启动乙烯环氧化方法的方法，包括：a。 使高选择性环氧化催化剂与包含乙烯，氧气和有机氯化物的进料接触一段时间，使得生产氯乙烯并能够在反应器出口流或再循环气体回路中检测; b。 将高选择性环氧化催化剂的温度升高至至少约220℃。 C。 随后在约12至约36小时的时间内降低进料中有机氯化物的水平，从而将催化剂的温度升高至约250℃至约265℃的温度; 和d。 随后在约250℃至约265℃的温度下将进料中的有机氯化物的水平调节至足以产生环氧乙烷的值，其值基本上为最佳选择性。