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公开(公告)号：US4456699A
公开(公告)日：1984-06-26
申请号：US485308
申请日：1983-04-15
CPC分类号： B01J37/10 , B01J21/02 , B01J21/12 , B01J27/16 , B01J35/10 , B01J35/1019 , B01J35/1047 , B01J35/1061 , C10G2300/107
摘要： A catalyst support is prepared from a composite comprising alumina and one or more oxides of phosphorus by forming the composite into a shaped support material having at least 0.8 cc/gm of its pore volume in pores having diameters of 0 nm (0 .ANG.) to 120 nm (1,200 .ANG.) and at least 0.1 cc/gm of its pore volume in pores having diameters of 120 nm (1,200 .ANG.) to 5,000 nm (50,000 .ANG.) and heating said shaped support material in the presence of steam at sufficient elevated temperature, steam pressure, and time period to increase the average pore diameter of said shaped support in the absence of any appreciable reduction in pore volume.A catalyst is prepared by impregnating the steam-treated support with at least one hydrogenating metal.The catalyst can be used suitably in hydrocarbon conversion processes, such as a process for the hydrodemetallization of a hydrocarbon stream containing asphaltenes and a substantial amount of metals.
摘要翻译： 催化剂载体由包含氧化铝和一种或多种磷的氧化物的复合材料制成，通过将复合材料形成为直径为0nm（0安格姆）至120的孔中至少具有0.8cc / gm孔体积的成形载体材料 nm（1200 ANGSTROM），并且在直径为120nm（1,200）至5,000nm（50,000）的孔中，其孔体积至少为0.1cc / gm，并且在足够高的温度下在蒸汽存在下加热所述成形载体材料， 蒸汽压力和时间段，以在没有任何明显的孔体积减小的情况下增加所述成形支撑件的平均孔径。 通过用至少一种氢化金属浸渍蒸汽处理的载体来制备催化剂。 催化剂可以适用于烃转化方法，例如含有沥青质的烃物流和大量金属的加氢脱金属的方法。
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公开(公告)号：US4191635A
公开(公告)日：1980-03-04
申请号：US967416
申请日：1978-12-07
CPC分类号： B01J23/8878 , B01J23/28 , B01J35/10 , C10G69/04 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J35/1085 , C10G2300/107
摘要： A heavy hydrocarbon stream containing metals, asphaltenes, nitrogen compounds, and sulfur compounds is (a) contacted with hydrogen and a hydrotreating catalyst containing molybdenum and chromium, either as metals, as oxides, as sulfides, or mixtures thereof, deposed on a large-pore, catalytically active alumina to reduce the metals content in said stream, to convert the asphaltenes, nitrogen compounds, and sulphur compounds in said stream, the catalyst has a pore volume within the range of about 0.4 cc/gm to about 0.8 cc/gm, a surface area within the range of about 150 m.sup.2 /gm to about 300 m.sup.2 /gm, and an average pore diameter within the range of about 100 A (10 nm) to about 200 A (20 nm); and (b) at least a portion of the hydrotreated stream is cracked with a cracking catalyst to produce gasoline and distillates in improved yields. The catalyst in step (a) may also contain cobalt.
摘要翻译： 含有金属，沥青质，氮化合物和硫化合物的重质烃流是（a）与氢气和含有钼和铬的加氢处理催化剂接触，所述催化剂含有钼和铬，作为氧化物，作为硫化物或其混合物， 孔，催化活性氧化铝以降低所述料流中的金属含量，以转化所述料流中的沥青质，氮化合物和硫化合物，催化剂的孔体积在约0.4cc / g至约0.8cc / g的范围内 ，约150m 2 / gm至约300m 2 / gm范围内的表面积和在约100A（10nm）至约200A（20nm）范围内的平均孔径; 和（b）加氢处理物流的至少一部分用裂解催化剂裂化，以提高产率生产汽油和馏出物。 步骤（a）中的催化剂也可以含有钴。
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公开(公告)号：US4306965A
公开(公告)日：1981-12-22
申请号：US181433
申请日：1980-08-04
CPC分类号： B01J23/8878 , B01J35/10 , C10G45/08 , B01J21/12 , B01J35/1019 , B01J35/1042 , B01J35/1061
摘要： A process for hydrotreating a hydrocarbon stream such as petroleum distillate and similar hydrocarbon materials by contacting said stream with hydrogen and a catalyst comprising a porous refractory inorganic oxide support and deposited thereon hydrogenation components comprising chromium, molybdenum and at least one Group VIII metal. This process enables improved removal of nitrogen and sulfur, particularly from gas oils.
摘要翻译： 通过使所述物流与氢和包含多孔耐火无机氧化物载体的催化剂接触并在其上沉积有包含铬，钼和至少一种VIII族金属的氢化组分的催化剂来加氢处理烃流如石油馏出物和类似烃物质的方法。 该方法能够改善氮和硫的去除，特别是瓦斯油的去除。
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公开(公告)号：US4549957A
公开(公告)日：1985-10-29
申请号：US506293
申请日：1983-06-21
IPC分类号： B01J23/28 , B01J23/88 , B01J27/16 , B01J35/10 , B01J37/10 , C10G45/04 , C10G49/04 , C10G45/08 , C10G45/20
CPC分类号： B01J35/108 , B01J23/28 , B01J23/88 , B01J27/16 , B01J35/10 , B01J37/10 , C10G49/04 , B01J21/12 , C10G2300/107
摘要： Hydrotreating catalysts comprise a hydrogenating component and a support comprising at least one porous refractory inorganic oxide, said catalyst having BET surface area of 150 to about 190 m.sup.2 /g, nitrogen desorption pore volume of 0.8 to about 1.2 cc/g in micropores with radii up to 600 .ANG., with at least 0.7 cc/g of such micropore volume in pores having radii ranging from 50 to 600 .ANG., mercury penetration pore volume of 0.1 to about 0.5 cc/g in macropores with radii of 600 to 25,000 .ANG. and bulk density of about 0.3 to about 0.5 g/cc. Hydrotreating process comprises contacting a hydrocarbon feed susceptible to upgrading with hydrogen in the presence of the aforesaid catalysts under hydrotreating conditions. The catalyt and process are particularly useful in hydrotreating feeds comprising high metals or high metals and sulfur content materials.
摘要翻译： 加氢处理催化剂包括氢化组分和包含至少一种多孔耐火无机氧化物的载体，所述催化剂具有150至约190m 2 / g的BET表面积，具有半径的微孔中的氮解吸孔体积为0.8至约1.2cc / g 至600，在孔中具有至少0.7cc / g这样的微孔体积，半径范围为50至600，大孔中的汞渗透孔体积为0.1至约0.5cc / g，半径为600至25,000，体积密度 为约0.3至约0.5g / cc。 加氢处理方法包括在加氢处理条件下在上述催化剂存在下使容易升级的烃进料接触。 催化剂和方法在加氢处理包含高金属或高金属和硫含量材料的进料中特别有用。
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公开(公告)号：US4297242A
公开(公告)日：1981-10-27
申请号：US168297
申请日：1980-07-14
IPC分类号： B01J21/04 , B01J23/24 , B01J23/28 , B01J35/10 , C10G45/04 , C10G45/08 , C10G65/04 , B01J27/02 , B01J23/16
CPC分类号： B01J35/10 , B01J23/24 , B01J23/28 , B01J21/04 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J35/108 , C10G2300/107
摘要： Disclosed is a two-stage catalytic process for hydrodemetallation and hydrodesulfurization of heavy hydrocarbon streams containing asphaltenes and a substantial amount of metals. The first stage of this process comprises contacting the feedstock in a first reaction zone with hydrogen and a demetallation catalyst comprising hydrogenation metal selected from Group VIB and/or Group VIII deposed on a large-pore, high surface area inorganic oxide support; the second stage of the process comprises contacting the effluent from the first reaction zone with a catalyst consisting essentially of hydrogenation metal selected from Group VIB deposed on a smaller-pore, catalytically active support comprising alumina, said second-stage catalyst having a surface area within the range of about 150 m.sup.2 /gm to about 300 m.sup.2 /gm, having a majority of its pore volume in pore diameters within the range of about 80 A to about 130 A, and the catalyst has a pore volume within the range of about 0.4 cc/gm to about 0.9 cc/gm.
摘要翻译： 公开了用于含有沥青质和大量金属的重质烃流的加氢脱金属和加氢脱硫的两阶段催化方法。 该方法的第一阶段包括使第一反应区中的原料与氢气和脱金属催化剂接触，所述脱金属催化剂包含选自分布在大孔，高表面积无机氧化物载体上的VIB族和/或VIII族的氢化金属; 该方法的第二阶段包括将来自第一反应区的流出物与基本上由选自组分VIB的氢化金属组成的催化剂接触，所述组VIB位于包含氧化铝的较小孔催化活性载体上，所述第二级催化剂的表面积在 约150m 2 / gm至约300m 2 / gm的范围，其孔径的大部分孔径在约80至约130的范围内，并且催化剂的孔体积在约0.4的范围内 cc / gm至约0.9cc / gm。
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公开(公告)号：US4225421A
公开(公告)日：1980-09-30
申请号：US20072
申请日：1979-03-13
CPC分类号： B01J35/10 , B01J23/28 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J35/1066 , B01J35/109 , C10G2300/107
摘要： A process for hydrodemetallation and hydrodesulfurization of hydrocarbon feedstock containing asphaltenes and metals by contacting said feedstock with hydrogen and a bimodal catalyst consisting essentially of at least one active original hydrogenation metal selected from Group VIB deposited on a support comprising alumina wherein said catalyst has a surface area within the range of about 140 to about 300 m.sup.2 /gm, a total pore volume based upon measurement by mercury penetration within the range of about 0.4 cc/gm to about 1.0 cc/gm, and comprising about 60% to about 95% of its micropore volume in micropores having diameters within the range of about 50 A to about 200 A, 0% to about 15% of its micropore volume in pores having diameters within the range of about 200 A to about 600 A and about 3% to about 30% of said total pore volume based upon measurements by mercury penetration in macropores having diameters of 600 A or greater.
摘要翻译： 通过使所述原料与氢和双键催化剂接触，该催化剂主要由选自沉积在包含氧化铝的载体上的至少一种活性原始氢化金属组成的双峰催化剂进行加氢脱金属和加氢脱硫的方法，其中所述催化剂具有表面积 在约140至约300m 2 / gm的范围内，基于通过汞渗透测量在约0.4cc / gm至约1.0cc / gm范围内的总孔体积，并且包含其约60％至约95％ 直径在约50A至约200A范围内的微孔中的微孔体积，其孔径中的微孔体积的0％至约15％，其直径在约200至约600的范围内，并且约3％至约30 基于直径为600A或更大的大孔中汞渗透测量的所述总孔体积的百分比。
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公开(公告)号：US4224144A
公开(公告)日：1980-09-23
申请号：US21575
申请日：1979-03-19
CPC分类号： B01J35/10 , C10G45/08 , B01J21/12 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1061
摘要： A process for hydrotreating a hydrocarbon stream such as petroleum distillate and similar hydrocarbon materials by contacting said stream with hydrogen and a catalyst comprising a porous refractory inorganic oxide support and deposited thereon hydrogenation components comprising chromium, molybdenum and at least one Group VIII metal. This process enables improved removal of nitrogen and sulfur, particularly from gas oils.
摘要翻译： 通过使所述物流与氢和包含多孔耐火无机氧化物载体的催化剂接触并在其上沉积有包含铬，钼和至少一种VIII族金属的氢化组分的催化剂来加氢处理烃流如石油馏出物和类似烃物质的方法。 该方法能够改善氮和硫的去除，特别是瓦斯油的去除。
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8.发明授权Catalyst and support, their methods of preparation, and processes employing same 失效催化剂和载体，它们的制备方法和使用它们的方法
公开(公告)号：US4495062A
公开(公告)日：1985-01-22
申请号：US485185
申请日：1983-04-15
IPC分类号： B01J21/02 , B01J21/12 , B01J23/28 , B01J27/16 , B01J35/10 , B01J37/10 , C10G45/04 , C10G47/12 , C10G45/08
CPC分类号： B01J37/10 , B01J21/02 , B01J21/12 , B01J23/28 , B01J27/16 , B01J35/10 , B01J35/1019 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J35/108 , C10G2300/107
摘要： A catalyst support is prepared from a composite comprising two or more inorganic oxides by forming the composite into a shaped support material having at least 0.8 cc/gm of its pore volume in pore diameters of 0 nm (0 .ANG.) to 120 nm (1,200 .ANG.) and at least 0.1 cc/gm of its pore volume in pore diameters of 120 nm (1,200 .ANG.) to 5,000 nm (50,000 .ANG.) and heating said shaped support material in the presence of steam at sufficient elevated temperature, steam pressure, and time period to increase the average pore diameter of said shaped support in the absence of any appreciable reduction in pore volume. The inorganic oxide composite is selected from the group consisting of a mixture of alumina and silica; a mixture of alumina, silica, and oxides of phosphorus; a mixture of alumina and oxides of phosphorus; a mixture of alumina and boria; a mixture of alumina, boria and oxides of phosphorus; and a mixture of alumina, magnesia, and oxides of phosphorus, the oxides of phosphorus being calculated as P.sub.2 O.sub.5 and the quantities being based upon the weight of the composite.A catalyst is prepared by impregnating the steam-treated support with at least one hydrogenating metal.The catalyst can be used suitably in hydrocarbon conversion processes, such as a process for the hydrodemetallization of a hydrocarbon stream containing asphaltenes and a substantial amount of metals.
摘要翻译： 催化剂载体由包含两种或更多种无机氧化物的复合材料制备，通过将复合材料形成为孔径为0nm（0安格姆）至120纳米（1,200安格姆）的孔体积至少为0.8cc /克的成形载体材料 ）和至少0.1cc / gm的孔径为120nm（1,200安格姆）至5,000nm（50,000安培）的孔体积，并在蒸汽存在下在足够高的温度，蒸汽压力和时间下加热所述成形的支撑材料 在没有任何明显的孔体积减小的情况下增加所述成形载体的平均孔径。 无机氧化物复合材料选自氧化铝和二氧化硅的混合物; 氧化铝，二氧化硅和磷的氧化物的混合物; 氧化铝和磷的氧化物的混合物; 氧化铝和氧化硼的混合物; 氧化铝，氧化硼和磷的氧化物的混合物; 以及氧化铝，氧化镁和磷的氧化物的混合物，磷的氧化物计算为P 2 O 5，其数量基于复合材料的重量。 通过用至少一种氢化金属浸渍蒸汽处理的载体来制备催化剂。 催化剂可以适用于烃转化方法，例如含有沥青质的烃物流和大量金属的加氢脱金属的方法。
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9.发明授权
公开(公告)号：US4431525A
公开(公告)日：1984-02-14
申请号：US371815
申请日：1982-04-26
CPC分类号： B01J35/10 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J35/1085 , C10G2300/107
摘要： There is disclosed a process for hydrotreating a heavy hydrocarbon stream containing metals, asphaltenes, nitrogen compounds, and sulfur compounds to reduce the contents of these contaminants. The process comprises contacting said stream in the presence of hydrogen and under suitable hydrotreating conditions in sequence with a first catalyst in a first reaction zone, a second catalyst in a second reaction zone, and a third catalyst in a third reaction zone. The first catalyst comprises a Group VIB metal and/or a Group VIII metal on a porous inorganic oxide support; the second catalyst consists essentially of at least one hydrogenation metal selected from Group VIB deposed on a support material comprising alumina; and the third catalyst comprises a hydrogenating component comprising molybdenum, chromium, and cobalt on a large-pore, catalytically-active alumina. Each catalyst has specific physical properties.
摘要翻译： 公开了一种加氢处理含有金属，沥青质，氮化合物和硫化合物的重质烃流的方法，以减少这些污染物的含量。 该方法包括在氢气存在下，在合适的加氢处理条件下，将第一催化剂在第一反应区，第二反应区中的第二催化剂和第三反应区中的第三催化剂依次接触。 第一催化剂在多孔无机氧化物载体上包含VIB族金属和/或Ⅷ族金属; 第二催化剂基本上由至少一种氢化金属组成，所述氢化金属选自ⅤB组，其包含氧化铝的载体材料; 并且第三催化剂包含在大孔催化活性氧化铝上的包含钼，铬和钴的氢化组分。 每种催化剂都具有特定的物理性质。
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10.发明授权Catalyst and support, their methods of preparation, and processes employing same 失效催化剂和载体，它们的制备方法和使用它们的方法
公开(公告)号：US4399057A
公开(公告)日：1983-08-16
申请号：US274499
申请日：1981-06-17
IPC分类号： B01J21/02 , B01J21/04 , B01J21/12 , B01J23/22 , B01J23/28 , B01J27/16 , B01J35/10 , B01J37/10 , C10G45/04 , B01J27/14 , B01J20/00 , B01J21/00
CPC分类号： B01J37/10 , B01J21/02 , B01J21/12 , B01J23/28 , B01J27/16 , B01J35/10 , B01J35/1019 , B01J35/1047 , B01J35/1061 , B01J35/1066 , B01J35/109 , C10G2300/107
摘要： Shaped catalyst which can be prepared by use of steam.
摘要翻译： 可以使用蒸汽制备的成型催化剂。
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