Method for producing an improved supported catalyst
    3.
    发明申请
    Method for producing an improved supported catalyst 失效
    制备改进的负载型催化剂的方法

    公开(公告)号:US20030130115A1

    公开(公告)日:2003-07-10

    申请号:US10336394

    申请日:2003-01-04

    CPC classification number: B01J27/051 B01J23/755 B01J27/047

    Abstract: Highly active supported catalyst compositions and methods for producing more active supported catalyst compositions are disclosed. Said methods comprise steps for applying an adhesive coating of a catalytically active exfoliated transition metal dichalcogenide and promoters to the surface of a support medium prior to filling the pores of the support medium with catalytically active metals and/or promoters. A new method for applying a surface coating to a support is also disclosed.

    Abstract translation: 公开了高活性负载型催化剂组合物和制备更有活性的负载型催化剂组合物的方法。 所述方法包括在催化活性金属和/或促进剂填充载体介质的孔之前将催化活性的剥离的过渡金属二硫属元素和促进剂的粘合剂涂层施用到载体介质的表面的步骤。 还公开了将表面涂层施加到载体上的新方法。

    Process for sulfiding an additive-containing catalyst
    4.
    发明申请
    Process for sulfiding an additive-containing catalyst 有权
    用于硫化含添加剂的催化剂的方法

    公开(公告)号:US20020013223A1

    公开(公告)日:2002-01-31

    申请号:US09829638

    申请日:2001-04-10

    Abstract: The present invention pertains to a process for sulfiding a catalyst composition comprising at least one hydrogenation metal component of Group VI and/or Group VIII of the Periodic Table, and an organic additive wherein the catalyst composition is first contacted with an organic liquid, followed by the catalyst being contacted with hydrogen and a sulfur-containing compound in the gaseous phase, wherein less than about 40%, preferably less than about 35%, more preferably less than about 25%, most preferably less than about 15%, of the sulfur present in the sulfided catalyst is added with the organic liquid. The process of the present invention makes it possible to use additive-containing catalysts without loss of activity in units which cannot effect gas phase start-up or are required to carry out a pressure test. The organic liquid may be a hydrocarbon with a boiling range of about 150-500null C., preferably gasoline, white spirit, diesel, gas oil, mineral lube oil, or white oil. The step of contacting the catalyst with hydrogen and a sulfur-containing compound may take place in one step at a temperature of about 150-450null C. It may also take place in two steps, with the first step being performed at a temperature which is lower than that of the second step, with the first step being carried out at a temperature of about 100-250null C. and the second step at a temperature of about 150-450null C.

    Abstract translation: 本发明涉及一种硫化催化剂组合物的方法,该催化剂组合物包含至少一种元素周期表第VI族和/或第Ⅷ族氢化金属组分和一种有机添加剂,其中催化剂组合物首先与有机液体接触, 催化剂在气相中与氢气和含硫化合物接触,其中少于约40%,优选小于约35%,更优选小于约25%,最优选小于约15%的硫 存在于硫化催化剂中的有机液体中加入。 本发明的方法使得可以在不能实现气相启动或需要进行压力试验的单位中使用不含活性的添加剂的催化剂。 有机液体可以是沸点为约150-500℃的烃,优选汽油,白酒,柴油,瓦斯油,矿物润滑油或白油。 使催化剂与氢气和含硫化合物接触的步骤可以在约150-450℃的温度下在一个步骤中进行。它也可以在两个步骤中进行,第一步是在 低于第二步骤,第一步骤在约100-250℃的温度下进行,第二步在约150-450℃的温度下进行。

    Process for sulfiding a catalyst containing an S-containing additive
    5.
    发明申请
    Process for sulfiding a catalyst containing an S-containing additive 有权
    硫化含有S添加剂的催化剂的方法

    公开(公告)号:US20020000394A1

    公开(公告)日:2002-01-03

    申请号:US09829624

    申请日:2001-04-10

    Inventor: Sonja Eijsbouts

    Abstract: The present invention pertains to a process for sulfiding a catalyst composition comprising at least one hydrogenation metal component of Group VI and/or Group VIII of the Periodic Table, and an S-containing organic additive wherein the catalyst composition is first contacted with an organic liquid, followed by the catalyst being contacted with hydrogen and a sulfur-containing compound in the gaseous phase. The invention also pertains to the sulfided catalyst composition and its use in hydrotreating. Catalysts sulfided by the process according to the invention show a higher activity than the same catalysts which have not been sulfided. It is preferred to carry out the process according to the invention ex situ, where it solves the problem of difficult start-up and the formation of undesirable side products in the hydrotreating unit. The organic liquid may be a hydrocarbon with a boiling range of about 150-500null C., preferably white oil, gasoline, diesel, gas oil, or mineral lube oil. The S-containing organic additive preferably is a mercapto-compound, more preferably a mercaptocarboxylic acid represented by the general formula HSnullR1nullCOOR, wherein R1 stands for a divalent hydrocarbon group with 1- about 10 carbon atoms and R stands for a hydrogen atom, an alkali metal, an alkaline earth metal, ammonium, or a linear or branched alkyl group having 1 to about 10 carbon atoms.

    Abstract translation: 本发明涉及一种用于硫化催化剂组合物的方法,所述催化剂组合物包含至少一种元素周期表第VI族和/或第Ⅷ族的氢化金属组分和含S的有机添加剂,其中催化剂组合物首先与有机液体 然后催化剂与气相中的氢和含硫化合物接触。 本发明还涉及硫化催化剂组合物及其在加氢处理中的用途。 通过根据本发明的方法硫化的催化剂显示出比未硫化的相同催化剂更高的活性。 优选非原位地进行根据本发明的方法,其中解决了加氢处理单元中难以启动和形成不期望的副产物的问题。 有机液体可以是沸程为约150-500℃的烃,优选白油,汽油,柴油,瓦斯油或矿物润滑油。 含S的有机添加剂优选为巯基化合物,更优选由通式HS-R1-COOR表示的巯基羧酸,其中R1表示具有1〜10个碳原子的二价烃基,R表示氢 原子,碱金属,碱土金属,铵或具有1至约10个碳原子的直链或支链烷基。

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