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    • 2. 发明授权
    • Isomerization process using novel catalyst
    • 使用新型催化剂的异构化方法
    • US07022889B2
    • 2006-04-04
    • US10804358
    • 2004-03-19
    • Ralph D. GillespieMichelle J. CohnLynn H. Rice
    • Ralph D. GillespieMichelle J. CohnLynn H. Rice
    • C07C5/13
    • B01J27/053B01J21/066B01J23/63B01J23/894B01J37/0205C10G2400/02
    • A process for the isomerization of a feedstream comprising C5–C6 hydrocarbons where the process involves charging hydrogen and a feedstream comprising at least normal C5–C6 hydrocarbons into an isomerization zone and contacting said hydrogen and feedstream with an isomerization catalyst at isomerization conditions to increase the branching of the feedstream hydrocarbons and produce an isomerization effluent stream comprising at least normal pentane, normal hexane, methylbutane, dimethylbutane, and methylpentane has been discovered. The catalyst used is a solid acid catalyst comprising a support comprising a sulfated oxide or hydroxide of at least an element of Group IVB (IUPAC 4) of the Periodic Table, a first component selected from the group consisting of at least one lanthanide-series element, mixtures thereof, and yttrium, and a second component selected from the group of platinum-group metals and mixtures thereof.
    • 含有C 5 -C 6烃的进料流的异构化方法,其中该方法包括加入氢气和至少含有正常C 5 -C 15烃的进料流 将-C 6 -C 6烃转化成异构化区,并使异构化催化剂在异构化条件下使所述氢和原料流与异构化催化剂接触以增加原料流烃的分支,并产生异构化流出物流,其至少包含正常戊烷,正常 已经发现己烷,甲基丁烷,二甲基丁烷和甲基戊烷。 所使用的催化剂是一种固体酸催化剂,其包括含有至少元素周期表第IVB族(IUPAC 4)元素的硫酸化氧化物或氢氧化物的载体,选自至少一种镧系元素元素 ,其混合物和钇,以及选自铂族金属及其混合物的第二组分。
    • 3. 发明授权
    • Combination reforming and isomerization process
    • 组合重整和异构化过程
    • US07875757B2
    • 2011-01-25
    • US12129253
    • 2008-05-29
    • Douglas A. NafisGregory F. MaherLynn H. RiceWilliam D. SchlueterRalph D. GillespieMichelle J. Cohn
    • Douglas A. NafisGregory F. MaherLynn H. RiceWilliam D. SchlueterRalph D. GillespieMichelle J. Cohn
    • C07C5/27
    • C10G45/62C10G35/085C10G35/095
    • A reforming and isomerization process has been developed. A reforming feedstream is charged to a reforming zone containing a reforming catalyst and operating at reforming conditions to generate a reforming zone effluent. Hydrogen and an isomerization feedstream is charged into an isomerization zone to contact an isomerization catalyst at isomerization conditions to increase the branching of the hydrocarbons. The isomerization catalyst is a solid acid catalyst comprising a support comprising a sulfated oxide or hydroxide of at least an element of Group IVB, a first component being at least one lanthanide series element, mixtures thereof, or yttrium, and a second component being a platinum group metal or mixtures thereof. The reforming zone effluent and the isomerization zone effluent are each separated to form a light ends stream and a product stream. The light ends streams are combined for processing in a net gas re-contacting zone.
    • 已经开发了改性和异构化方法。 将重整进料流装入含有重整催化剂的重整区,并在重整条件下操作以产生重整区流出物。 将氢气和异构化原料流装入异构化区以在异构化条件下与异构化催化剂接触以增加烃的支化。 异构化催化剂是包含载体的固体酸催化剂,其包含至少一种IVB族元素的硫酸化氧化物或氢氧化物,第一组分为至少一种镧系元素,其混合物或钇,第二组分为铂 组金属或其混合物。 重整区流出物和异构化区流出物各自分离以形成轻馏分流和产物流。 轻馏分流合并用于在净气体再接触区域中进行处理。