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    • 2. 发明申请
    • PROCESS FOR THE PRODUCTION OF A 1,2-DIOL, A 1,2-DIOL ETHER, OR AN ALKANOLAMINE
    • 生产1,2-二醇,1,2-二醇醚或烷醇胺的方法
    • US20120065433A1
    • 2012-03-15
    • US13300160
    • 2011-11-18
    • William Herman GERDESJohn Robert LOCKEMEYERDonald James REMUSThomas SZYMANSKIRandall Clayton YEATES
    • William Herman GERDESJohn Robert LOCKEMEYERDonald James REMUSThomas SZYMANSKIRandall Clayton YEATES
    • C07C41/02C07C213/00C07C29/00
    • B01J23/66B01J21/04B01J21/12B01J23/50B01J23/688B01J35/10B01J35/1009B01J35/1038B01J35/1042B01J35/1071B01J35/108B01J37/0018C07C29/106C07D301/10Y02P20/52C07C31/202
    • 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.
    • 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。
    • 4. 发明申请
    • METHOD FOR IMPROVING THE SELECTIVITY OF A CATALYST AND A PROCESS FOR THE EPOXIDATION OF AN OLEFIN
    • 改进催化剂选择性的方法和烯烃环氧化方法
    • US20100160655A1
    • 2010-06-24
    • US12337923
    • 2008-12-18
    • John Robert LOCKEMEYERRandall Clayton YeatesDonald Reinalda
    • John Robert LOCKEMEYERRandall Clayton YeatesDonald Reinalda
    • C07D301/10C07C41/02C07C31/18C07C209/00
    • C07D301/10
    • A method for improving the selectivity of a supported highly selective epoxidation catalyst comprising silver in a quantity of at most 0.17 g per m2 surface area of the support, which method comprises contacting the catalyst, or a precursor of the catalyst comprising the silver in cationic form, with a feed comprising oxygen at a catalyst temperature above 250° C. for a duration of up to 150 hours, and subsequently decreasing the catalyst temperature to a value of at most 250° C.; and a process for the epoxidation of an olefin, which process comprises contacting a supported highly selective epoxidation catalyst comprising silver in a quantity of at most 0.17 g per m2 surface area of the support, or a precursor of the catalyst comprising the silver in cationic form, with a feed comprising oxygen at a catalyst temperature above 250° C. for a duration of up to 150 hours, and subsequently decreasing the catalyst temperature to a value of at most 250° C. and contacting the catalyst with the feed comprising the olefin and oxygen.
    • 一种用于提高载体的高选择性环氧化催化剂的选择性的方法,该催化剂包含银量至多为0.17g / m 2表面积的载体,该方法包括使催化剂或包含阳离子型银的催化剂的前体 ,在催化剂温度高于250℃的情况下使用包含氧的进料持续长达150小时,随后将催化剂温度降至至多250℃的值。 和烯烃的环氧化方法,该方法包括使包含银的负载型高选择性环氧化催化剂以至少0.17g / m 2表面积的载体或包含阳离子形式的银的催化剂前体 使用在催化剂温度高于250℃的氧气的进料,持续长达150小时,随后将催化剂温度降至至多250℃,并将催化剂与包含烯烃的进料接触 和氧气。