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1.发明授权Crystalline silica zeolite-containing catalyst and hydrocarbon hydroprocesses utilizing the same 失效含有结晶二氧化硅沸石的催化剂和使用其的烃加氢处理
公开(公告)号：US4443329A
公开(公告)日：1984-04-17
申请号：US440868
申请日：1982-11-12
IPC分类号： B01J29/035 , C10G49/08 , C10G47/12
CPC分类号： B01J29/035 , C10G49/08
摘要： A catalyst is provided which comprises a crystalline silica zeolite, a hydrogenation component and a support. The catalyst may be a physical mixture of the zeolite and the supported hydrogenation component or a composite catalyst. Hydrocarbon hydroprocessing processes such as hydroconversion and hydrodesulfurization utilizing the catalyst are also provided. The catalyst is particularly suited for the simultaneous pour point reduction and hydrodesulfurization of hydrocarbonaceous oils.
摘要翻译： 提供了包含结晶二氧化硅沸石，氢化组分和载体的催化剂。 催化剂可以是沸石和负载的氢化组分的物理混合物或复合催化剂。 还提供烃加氢处理如加氢转化和使用催化剂的加氢脱硫。 催化剂特别适用于同时进行降烃和烃油的加氢脱硫。
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公开(公告)号：US4464252A
公开(公告)日：1984-08-07
申请号：US410250
申请日：1982-08-23
CPC分类号： C10G25/003
摘要： A process wherein a regenerated, spent sulfided vanadium-containing Group VIII metal, Group VI-B metal, or Group VI-B/Group VIII metals containing catalyst is contacted with a stream of an oxygen-containing gas and the coke burned therefrom to regenerate the catalyst. The regenerated catalyst as such, or after reduction of the catalytic metals by contact with hydrogen, can be used as an adsorbent to remove essentially all of the sulfur from a naphtha feed which contains as much as 50 weight ppm sulfur, and greater.
摘要翻译： 一种方法，其中将再生的废硫化钒的VIII族金属，VI-B族金属或含有VI-B / VIII族金属的催化剂与含氧气体流和从其燃烧的焦炭接触以再生 催化剂。 再生的催化剂本身，或者通过与氢接触还原催化金属，可以用作吸附剂，以从含有多达50重量ppm硫的石脑油进料中基本上除去所有硫。
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公开(公告)号：US4513090A
公开(公告)日：1985-04-23
申请号：US281860
申请日：1981-07-09
CPC分类号： B01J29/035 , B01J29/04 , C10G45/64 , C10G49/08
摘要： A catalyst is provided which comprises a crystalline silica zeolite, a hydrogenation component and a support. The catalyst may be a physical mixture of the zeolite and the supported hydrogenation component or a composite catalyst. Hydrocarbon hydroprocessing processes such as hydroconversion and hydrodesulfurization utilizing the catalyst are also provided. The catalyst is particularly suited for the simultaneous pour point reduction and hydrodesulfurization of hydrocarbonaceous oils.
摘要翻译： 提供了包含结晶二氧化硅沸石，氢化组分和载体的催化剂。 催化剂可以是沸石和负载的氢化组分的物理混合物或复合催化剂。 还提供烃加氢处理如加氢转化和使用催化剂的加氢脱硫。 催化剂特别适用于同时进行降烃和烃油的加氢脱硫。
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4.发明授权公开(公告)号：US06913688B2
公开(公告)日：2005-07-05
申请号：US10274021
申请日：2002-10-18
申请人： John C. Coker , Garland B. Brignac , Thomas R. Halbert , John G. Matragrano , Brij Gupta , Robert C. Welch , William E. Winter, Jr.
发明人： John C. Coker , Garland B. Brignac , Thomas R. Halbert , John G. Matragrano , Brij Gupta , Robert C. Welch , William E. Winter, Jr.
CPC分类号： C10G65/04 , C10G45/08 , C10G2300/202 , C10G2300/207 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2400/02 , C10L1/06
摘要： A process for the selective hydrodesulfurization of olefinic naphtha streams containing a substantial amount of organically bound sulfur and olefins. The olefinic naphtha stream is selectively hydrodesulfurized in a first sulfur removal stage and resulting product stream, which contains hydrogen sulfide and organosulfur is fractionated at a temperature to produce a light fraction containing less than about 100 wppm organically bound sulfur and a heavy fraction containing greater than about 100 wppm organically bound sulfur. The light fraction is stripped of at least a portion ofits hydrogen sulfide and can be collected or passed to gasoline blending. The heavy fraction is passed to a second sulfur removal stage wherein at least a portion of any remaining organically bound sulfur is removed.
摘要翻译： 一种含有大量有机结合的硫和烯烃的烯烃石脑油流选择性加氢脱硫的方法。 烯烃石脑油流在第一个硫去除阶段中选择性加氢脱硫，并在含有硫化氢和有机硫的所得产物流在一定温度下分馏，生成含有少于约100wppm有机结合硫的轻馏分，含有大于 约100wppm有机结合硫。 将轻馏分汽提至少一部分硫化氢，并可收集或通过汽油混合。 将重馏分送至第二硫去除阶段，其中除去至少一部分剩余的有机结合的硫。
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公开(公告)号：US5336395A
公开(公告)日：1994-08-09
申请号：US41135
申请日：1993-03-29
申请人： Joanne K. Pabst , William E. Winter, Jr. , Stephen N. Vaughn , Claude C. Culross , Steve D. Reynolds
发明人： Joanne K. Pabst , William E. Winter, Jr. , Stephen N. Vaughn , Claude C. Culross , Steve D. Reynolds
摘要： This invention is directed to a staged process for producing liquids from coal or similar carbonaceous feeds combining a pretreatment stage and a liquefaction stage. In the process, the feed is reacted with carbon monoxide and water at an elevated temperature and pressure. The so pretreated coal is sent to a liquefaction reactor, wherein the coal is reacted at a somewhat higher temperature in the presence of hydrogen and catalyst to produce valuable liquid fuels or feedstocks.
摘要翻译： 本发明涉及一种从预处理阶段和液化阶段结合的煤或类似碳质饲料生产液体的分段方法。 在此过程中，进料在升高的温度和压力下与一氧化碳和水反应。 这样预处理的煤被送到液化反应器，其中煤在氢和催化剂的存在下在稍高的温度下反应，以产生有价值的液体燃料或原料。
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公开(公告)号：US5070053A
公开(公告)日：1991-12-03
申请号：US631561
申请日：1990-12-21
CPC分类号： C10G11/05 , B01J21/12 , B01J37/0018 , B01J37/02 , C10G11/04
摘要： Disclosed is a FCC catalyst composite, and a method of making said composite comprised of an alumina-on-silica additive, an inorganic refractory oxide, and optionally a zeolite material.
摘要翻译： 公开了一种FCC催化剂复合材料，以及由氧化铝 - 二氧化硅添加剂，无机难熔氧化物和任选的沸石材料制成所述复合材料的方法。
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公开(公告)号：US4062762A
公开(公告)日：1977-12-13
申请号：US723152
申请日：1976-09-14
CPC分类号： C10G67/16 , C10G2400/02
摘要： A sulfur-containing naphtha is separated into at least three fractions. Each fraction is desulfurized separately by a different desulfurization method. Subsequently, the desulfurized fractions are recombined. The intermediate boiling point naphtha fraction is desulfurized by an alkali metal desulfurization process, preferably in the presence of added hydrogen.
摘要翻译： 含硫石脑油被分成至少三个馏分。 每个馏分通过不同的脱硫方法分开脱硫。 随后，将脱硫馏分重组。 中间沸点石脑油馏分通过碱金属脱硫方法脱硫，优选在加入氢气的情况下进行脱硫。
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8.发明授权公开(公告)号：US06231753B1
公开(公告)日：2001-05-15
申请号：US09448961
申请日：1999-11-24
申请人： Craig A. McKnight , Thomas R. Halbert , John P. Greeley , Garland B. Brignac , Richard A. Demmin , William E. Winter, Jr. , Bruce R. Cook
发明人： Craig A. McKnight , Thomas R. Halbert , John P. Greeley , Garland B. Brignac , Richard A. Demmin , William E. Winter, Jr. , Bruce R. Cook
IPC分类号： C10G45104
CPC分类号： C10G45/08 , B01J23/85 , B01J23/882 , B01J35/0006 , C10G65/04 , C10G2300/1044 , C10G2300/202 , C10G2300/207 , C10G2300/4018 , C10G2400/02
摘要： Selective and deep desulfurization of a high sulfur content mogas naphtha, with reduced product mercaptans and olefin loss, is achieved by a two stage, vapor phase hydrodesulfurization process with interstage separation of at least 80 vol. % of the H2S formed in the first stage from the first stage, partially desulfurized naphtha vapor effluent fed into the second stage. At least 70 wt. % of the sulfur is removed in the first stage and at least 80 wt. % of the remaining sulfur is removed in the second stage, to achieve a total at least 95 wt. % feed desulfurization, with no more than a 60 vol. % feed olefin loss. The second stage temperature and space velocity are preferably greater than in the first. The hydrodesulfurization catalyst preferably contains a low metal loading of Co and Mo metal catalytic components on an alumina support.
摘要翻译： 通过两级气相加氢脱硫工艺实现了具有降低产物硫醇和烯烃损失的高硫含量的沼气石脑油的选择性和深度脱硫，其中级间分离至少为80体积％。 在第一阶段的第一阶段形成的H2S的％，部分脱硫的石脑油蒸汽流出物进料到第二阶段。 至少70wt。 在第一阶段中除去硫的百分比，并且至少80wt。 在第二阶段除去剩余硫的％，以达到总计至少95wt。 ％进料脱硫，不超过60体积。 ％进料烯烃损失。 第二级温度和空间速度优选大于第一级。 加氢脱硫催化剂优选在氧化铝载体上含有Co和Mo金属催化组分的低金属负载量。
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公开(公告)号：US5300212A
公开(公告)日：1994-04-05
申请号：US965107
申请日：1992-10-22
CPC分类号： C10G45/16
摘要： Disclosed is a process wherein a two-stage hydroconversion process for converting a heavy hydrocarbonaceous feedstock to lower boiling products which process comprises: (a) reacting the feedstock in a first reaction stage at hydroconversion conditions which include temperature from about 650.degree. F. to 900.degree. F., and hydrogen partial pressure ranging from about 50 to 5000 psig in the presence of a metal compound which is convertible to a solid, non-colloidal, metal-containing catalyst, said metal selected from the group consisting of metals from Groups IVB, VB, VIB, VIIB, and VIII, of the Periodic Table of the Elements, wherein said metal compound is: (i) soluble in the hydrocarbonaceous feed; or (ii) soluble in an organic medium that can be dispersed in the hydrocarbonaceous oil, or (iii) soluble in water resulting in an aqueous solution which can then be dispersed in the hydrocarbonaceous feedstock; (b) passing the resulting product stream to a second reaction stage where it is reacted under slurry hydrotreating conditions which include: (i) temperature in the range of 650.degree. F. to 750.degree. F., with the promise that this slurry hydrotreating stage be operated at a temperature at least 25.degree. F. less than the first stage, and (ii) hydrogen partial pressures in the range of 800 to 4000 psig, and in the presence of hydrogen and a hydrotreating catalyst comprised of at least one Group VI metal and at least one Group VIII catalyst, on an inorganic oxide support.
摘要翻译： 公开了一种方法，其中用于将重质烃原料转化为较低沸点产物的两阶段加氢转化方法包括：（a）在加氢转化条件下在第一反应阶段使原料反应，所述加氢转化条件包括约650°F至900 在可转换成固体非胶体金属的催化剂的金属化合物的存在下，约50-5000psig的氢分压，所述金属选自IVB族的金属 ，VB，VIB，VIIB和VIII，其中所述金属化合物是：（i）可溶于烃类进料; 或（ii）可溶于可分散在含烃油中的有机介质，或（iii）可溶于水，得到水溶液，然后将其分散在含烃原料中; （b）将所得产物流送至第二反应阶段，在第二反应阶段，其在浆料加氢处理条件下反应，其包括：（i）在650华氏度至750华氏度的温度范围内，预期该浆料加氢处理阶段 在比第一阶段低至少25°F的温度下操作，和（ii）在800至4000psig范围内的氢分压，以及在氢气和由至少一种VI组成的加氢处理催化剂存在下 金属和至少一种VIII族催化剂，在无机氧化物载体上。
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公开(公告)号：US5152885A
公开(公告)日：1992-10-06
申请号：US631301
申请日：1990-12-18
CPC分类号： B01J23/8993 , B01J37/086 , C10G45/10
摘要： A process for removing heteroatoms from a hydrocarbonaceous feedstock using a catalyst composition comprised of: about 0.005 to 5.0 wt. % noble metal, about 0.5 to 5 wt. % of at least one Group VIII metal, and about 3 to 18 wt. % of a Group VI metal, and a refractory support, wherein the noble metal is incorporated into the refractory support by use of a precursor represented by ML.sub.2 when the noble metal is Pt or Pd, and ML.sub.3, when the noble metal is Rh or Ir, where M is the noble metal and L is a ligand selected from the dithiocarbamates, dithiophosphates, dithiophosphinates, xanthates, thioxanthates, and further wherein L has organo groups having a sufficient number of carbon atoms to render the noble metal complex soluble in oil.
摘要翻译： 一种使用催化剂组合物从烃原料中除去杂原子的方法，所述催化剂组合物包含：约0.005-5.0wt。 ％贵金属，约0.5〜5wt。 ％的至少一种第Ⅷ族金属，和约3至18wt。 ％的VI族金属和耐火载体，其中当贵金属为Pt或Pd时，使用由ML2表示的前体和ML3将贵金属掺入耐火载体中，当贵金属为Rh或Ir 其中M是贵金属，L是选自二硫代氨基甲酸盐，二硫代磷酸盐，二硫代磷酸盐，黄原酸盐，硫代黄酸盐的配体，并且其中L具有足够数目的碳原子的有机基团，以使贵金属络合物溶于油。
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