Heteropoly salts or acid salts deposited in the interior of porous
supports
    1.
    发明授权
    Heteropoly salts or acid salts deposited in the interior of porous supports 失效
    沉积在多孔载体内部的杂多盐或酸盐

    公开(公告)号:US5919725A

    公开(公告)日:1999-07-06

    申请号:US100596

    申请日:1998-06-19

    IPC分类号: B01J27/188 B01J27/18

    CPC分类号: B01J27/188

    摘要: The present invention relates to a catalyst composition, its methods of preparation and its use in aromatic alkylation processes. The composition comprises a heteropoly compound selected from the group consisting of heteropoly salts and heteropolyacid salts deposited in the interior of a porous support selected from the group consisting of silica, titania, and zirconia, wherein said salt of said heteropoly salt and said heteropolyacid salt is selected from the group consisting of ammonium, cesium, potassium, and rubidium salts and mixtures thereof, and wherein said heteropoly salt and said heteropolyacid salt are formed with a heteropolyacid selected from the group consisting of 12-tungstophosphoric, 12-tungstosilicic, 12-molybdophosphoric, and 12-molybdosilicic acid.

    摘要翻译: 本发明涉及一种催化剂组合物及其制备方法及其在芳族烷基化方法中的应用。 组合物包含选自沉积在选自二氧化硅,二氧化钛和氧化锆的多孔载体内部的杂多盐和杂多酸盐的杂多化合物,其中所述杂多盐和所述杂多酸盐的所述盐是 选自由铵,铯,钾和铷盐及其混合物组成的组,并且其中所述杂多盐和所述杂多酸盐由选自12-钨磷酸,12-钨硅酸,12-钼磷酸的杂多酸形成 ,和12-钼硅酸。

    Transalkylation of benzene with heavy catalytic naphtha
    3.
    发明授权
    Transalkylation of benzene with heavy catalytic naphtha 失效
    苯与重催化石脑油的烷基转移

    公开(公告)号:US5406016A

    公开(公告)日:1995-04-11

    申请号:US73026

    申请日:1993-06-07

    IPC分类号: C07C6/12 C10G35/095 C07C5/52

    CPC分类号: C10G35/095 C07C6/126

    摘要: A process for simultaneously converting benzene to predominantly methylbenzenes and reducing the concentration of C.sub.10 + alkyl aromatics in a naphtha boiling range refinery process stream containing both benzene and C.sub.10 + alkyl aromatics by contacting the stream at effective temperatures and pressures with a 12-ring zeolitic material.

    摘要翻译: 一种同时将苯转化为主要甲基苯的方法,并通过在有效温度和压力下与12环沸石材料接触流,在含有苯和C 10 +烷基芳族化合物的石脑油沸程炼油厂工艺流中降低C10 +烷基芳族化合物的浓度。

    Method for the preparation of supported hydrogenation and hydrotreating
catalysts
    5.
    发明授权
    Method for the preparation of supported hydrogenation and hydrotreating catalysts 失效
    负载型氢化和加氢处理催化剂的制备方法

    公开(公告)号:US5336654A

    公开(公告)日:1994-08-09

    申请号:US30751

    申请日:1993-03-11

    摘要: A method for the preparation of catalysts for heteroatom removal, particularly sulfur, from petroleum and synthetic fuel feedstocks. The catalyst is comprised of at least one Group VIII metal, and at least one Group VI metal, on a refractory support. The present method for preparing said catalysts comprises impregnating the Group VIII metal onto the refractory support by use of a Group VIII metal salt of an acid, and impregnating the Group VI metal onto the support by way of a Group VI heteropolyacid, wherein the acid comprising the salt of the Group VIII metal is less acidic than the heteropolyacid. The catalysts are then subjected to a heat treatment which includes a first phase wherein the catalyst is dried of free water and a second phase wherein the catalyst is heated to a temperature up to about 300.degree. C. at a heating rate from about 0.15.degree. C./min to about 15.degree. C./min.

    摘要翻译: 一种从石油和合成燃料原料制备用于杂原子去除的催化剂,特别是硫的方法。 催化剂由至少一种第Ⅷ族金属和至少一种第Ⅵ族金属组成,在耐火载体上。 本发明的制备所述催化剂的方法包括使用第VIII族金属盐将VIII族金属浸渍到耐火载体上,并通过VI族杂多酸将VI族金属浸渍到载体上,其中酸包括 Ⅷ族金属的盐比杂多酸的酸性低。 然后对催化剂进行热处理,其包括其中催化剂被游离水干燥的第一相和第二相,其中将催化剂以约0.15℃的加热速率加热至高达约300℃的温度 /分钟至约15℃/分钟。

    High porosity, high surface area isomerization catalyst
    6.
    发明授权
    High porosity, high surface area isomerization catalyst 失效
    高孔隙度,高表面积异构化催化剂

    公开(公告)号:US5182248A

    公开(公告)日:1993-01-26

    申请号:US699101

    申请日:1991-05-10

    摘要: A novel, high porosity, high surface area catalyst is disclosed which is useful in wax isomerization processes, especially for the production of high viscosity index, low pour point lubricating oil base stocks or blending stocks. The catalyst contains a catalytically active metal component selected from the group consisting of Group VIB and Group VIII metals, and mixtures thereof, preferably Group VIII metals, and mixtures thereof, more preferably noble Group VIII metals and mixtures thereof, most preferably platinum which catalytically active metal component is present in the range of about 0.01 to 5.0 wt. %, and a fluorine content in the range of about 0.01 to about 10.0. The catalyst employs a refractory metal oxide support material, one preferably predominantly (i.e., at least 50 wt. %) alumina, most preferably completely alumina, e.g., gamma or eta alumina. The finished catalyst has a porosity, expressed in terms of pore volume, of at least about 0.50 cc/gram and a surface area such that when the porosity is multiplied by the surface area the product obtained is at least about 107, preferably at least about 110, more preferably at least about 115, most preferably at least about 120.

    摘要翻译: 公开了一种新颖的,高孔隙率的高表面积催化剂,其可用于蜡异构化方法,特别是用于生产高粘度指数,低倾点润滑油基础油或混合料。 催化剂含有选自VIB族和VIII族金属的催化活性金属组分及其混合物,优选VIII族金属及其混合物,更优选贵金属VIII族金属及其混合物,最优选催化活性的铂 金属组分的存在量为约0.01至5.0wt。 %,氟含量在约0.01至约10.0的范围内。 催化剂采用难熔金属氧化物载体材料,优选主要是(即,至少50重量%)的氧化铝,最优选完全氧化铝,例如γ或eta氧化铝。 成品催化剂具有至少约0.50cc /克的孔隙率,以孔体积表示的孔隙率和表面积,使得当孔隙率乘以表面积时,所得产物为至少约107,优选至少约 110,更优选至少约115,最优选至少约120。