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    • 51. 发明授权
    • Dispersed metal sulfide catalysts for hydroprocessing (LAW105)
    • 用于加氢处理的分散金属硫化物催化剂(LAW105)
    • US5648577A
    • 1997-07-15
    • US460410
    • 1995-06-02
    • Teh Chung HoStuart Leon SoledSabato MiseoGary Brice McVickerMichel DaageViktor Buchholz
    • Teh Chung HoStuart Leon SoledSabato MiseoGary Brice McVickerMichel DaageViktor Buchholz
    • B01J31/22B01J23/887B01J23/889B01J27/051B01J37/08B01J37/20C07B35/02C10G45/46C10G45/50C07C5/10
    • B01J37/086B01J23/887B01J23/8878B01J23/8892B01J27/051B01J37/20C10G45/46C10G45/50
    • The present invention is directed toward a catalyst composition prepared by a process comprising: (a) impregnating an oxide precursor selected from the group consisting of rare earth oxide precursors, yttria precursors and mixtures thereof, onto an inorganic refractory oxide support; (b) drying said support at a temperature of about 100.degree. to about 120.degree. C. followed by calcining said support at a temperature of about 400.degree. to about 600.degree. C.; and (c) compositing or depositing on said support of step (b), a catalyst precursor salt represented by (ML)(Mo.sub.y W.sub.1-y O.sub.4).sub.a wherein M comprises Cr and/or one or more divalent promoter metals selected from the group consisting of Mn, Fe, Co, Ni, Cu, Zn and mixtures thereof, wherein y is any value ranging from 0 to 1, and wherein L is one or more neutral, nitrogen-containing ligands at least one of which is a chelating polydentate ligand; a=1 when chromium is not one of the promoter metals and 0.5.ltoreq.a.ltoreq.3 when Cr is one of the promoter metals. (d) sulfiding said deposited or composited support of step (c) with an excess amount of sulfur in the form of one or more sulfur bearing compounds and at a temperature of at least about 250.degree. C. to form catalysts. In a preferred embodiment, the the composited or deposited supports of step (c) may be decomposed in a nonoxidizing atmosphere at a temperature of at least about 250.degree. C. prior to said sulfiding step (d). In a second aspect of the invention there is provided an improved aromatics hydrogenation process.
    • 本发明涉及通过包括以下步骤的方法制备的催化剂组合物:(a)将选自稀土氧化物前体,氧化钇前体及其混合物的氧化物前体浸渍到无机难熔氧化物载体上; (b)在约100至约120℃的温度下干燥所述载体,然后在约400至约600℃的温度下煅烧所述载体; 和(c)在步骤(b)的所述载体上合成或沉积由(ML)(MoyW1-yO4)a表示的催化剂前体盐,其中M包含Cr和/或一种或多种选自以下的二价助催化剂金属: Mn,Fe,Co,Ni,Cu,Zn及其混合物,其中y是0至1的任何值,并且其中L是一种或多种中性含氮配体,其中至少一种是螯合多齿配体; 当Cr不是助催化剂金属之一时,a = 1,当Cr是助催化剂金属之一时,a = 1。 (d)将步骤(c)的沉积或复合载体用一种或多种含硫化合物形式的过量的硫硫化并在至少约250℃的温度下硫化以形成催化剂。 在优选的实施方案中,在所述硫化步骤(d)之前,步骤(c)的复合或沉积的载体可以在非氧化气氛中在至少约250℃的温度下分解。 在本发明的第二方面,提供了一种改进的芳族化合物氢化方法。
    • 54. 发明授权
    • Process of presulfurizing and controlling the activity of catalyst for
treating hydrocarbons
    • 预硫化和控制催化剂用于处理烃的活性的方法
    • US4977117A
    • 1990-12-11
    • US330255
    • 1989-03-29
    • Georges BerrebiPierre Dufresne
    • Georges BerrebiPierre Dufresne
    • B01J23/88B01J23/92B01J27/04B01J37/20B01J38/50C07B61/00C07C1/00C07C5/10C07C5/13C07C5/29C07C13/10C07C13/18C07C67/00C10G11/02C10G45/46C10G45/50C10G47/06
    • B01J37/20
    • The invention involves a process comprising regenerating a catalyst comprising (a) a support containing at least one oxide of a metal or metalloid and (b) at least one active metal, said process comprising in a first stage treating said catalyst in the absence of hydrogen with at least one sulfurizing agent comprising a polysulfide of the formulaR--S.sub.(n) --R'wherein n is 2 to 20, R is an organic radical of 1-150 carbon atoms per molecule and R' is independently a radical as defined for R or a hydrogen atom, whereby said agent is incorporated at least in part in said catalyst, in a first portion of a second stage, treating the catalyst in the absence of hydrogen and in the presence of steam, moist air or moist inert gas, at a temperature up to 275.degree. C., and, in a second portion of the second stage, treating the catalyst in the presence of hydrogen at a temperature of at least 275.degree. C., wherein in the first stage a nitrogen compound is added.
    • 本发明涉及一种包括再生催化剂的方法,该催化剂包含(a)包含至少一种金属或准金属氧化物的载体和(b)至少一种活性金属,所述方法包括在不存在氢气的情况下在第一阶段处理所述催化剂 其中至少一种硫化剂包含式RS(n)-R'的多硫化物,其中n为2至20,R为每分子1-150个碳原子的有机基团,R'独立地为R定义的基团 或氢原子,其中所述试剂至少部分地引入所述催化剂中,在第二阶段的第一部分中,在不存在氢气的情况下和在蒸气,潮湿空气或潮湿惰性气体的存在下处理催化剂, 温度高达275℃,在第二阶段的第二部分,在至少275℃的温度下在氢气存在下处理催化剂,其中在第一阶段加入氮化合物。