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公开(公告)号：US5037529A
公开(公告)日：1991-08-06
申请号：US459403
申请日：1989-12-29
IPC分类号： C10G59/02
CPC分类号： C10G59/02
摘要： High purity benzene and high octane alkylaromatic gasoline can be obtained via a dual stage reforming process utilizing a non-acidic Group VIII metal containing microporous crystalline silicate catalyst in the first stage followed by first stage effluent treatment over acidic zeolite catalyst operating under conditions in the second stage to upgrade the first stage effluent in RON, in aromatic content or both.
摘要翻译： 高纯度苯和高辛烷值的烷基芳烃汽油可以通过双阶段重整方法获得，该方法利用在第一阶段中使用含非极性Ⅷ族金属的微孔结晶硅酸盐催化剂，然后在第二阶段的条件下在酸性沸石催化剂上进行第一阶段流出物处理 在RON，芳香含量或两者都升级第一阶段流出物的阶段。
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2.发明授权Low acidity catalyst for conversion of paraffins to olefins and/or aromatics 失效用于将烷烃转化为烯烃和/或芳族化合物的低酸度催化剂
公开(公告)号：US5108969A
公开(公告)日：1992-04-28
申请号：US571470
申请日：1990-08-22
申请人： Kenneth J. Del Rossi , Ralph M. Dessau , Albin Huss, Jr. , Garry W. Kirker , David O. Marler , Randall D. Partridge
发明人： Kenneth J. Del Rossi , Ralph M. Dessau , Albin Huss, Jr. , Garry W. Kirker , David O. Marler , Randall D. Partridge
CPC分类号： C07C5/41 , B01J29/04 , C07C2/12 , C07C2529/04 , C07C2529/70
摘要： A low acidity Group VIII metal-containing zeolite MCM-22 catalyst, said zeolite exhibiting an Alpha value of not greater than about 150, is provided for conversion of aliphatic C.sub.2 to C.sub.12 hydrocarbon(s) to olefin(s) and/or aromatic(s).
摘要翻译： 提供了低含量的含VIII族金属的沸石MCM-22催化剂，所述沸石表现出不大于约150的α值，用于将脂族C2转化为C12烃到烯烃和/或芳族（ s）。
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3.发明授权Process for the conversion of paraffins to olefins and/or aromatics and non-acidic zeolite catalyst therefor 失效将烷烃转化为烯烃和/或芳族化合物和非酸性沸石催化剂的方法
公开(公告)号：US4962250A
公开(公告)日：1990-10-09
申请号：US469650
申请日：1990-01-24
CPC分类号： C07C5/41 , B01J29/04 , B01J29/7276 , B01J29/7476 , C07C5/333 , C07C2529/04
摘要： Aliphatic C.sub.2 to C.sub.12 hydrocarbon(s) are converted to olefin(s) and/or aromatic(s) in the presence of an essentially non-acidic Group VIII metal species-containing zeolite MCM-22 catalyst.
摘要翻译： 在基本上非酸性的含Ⅷ族金属的沸石MCM-22催化剂的存在下，脂族C 2至C 12烃转化为烯烃和/或芳族烃。
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公开(公告)号：US4935566A
公开(公告)日：1990-06-19
申请号：US295954
申请日：1989-01-11
IPC分类号： B01J29/44 , B01J29/74 , C07C5/41 , C10G35/085 , C10G35/095
CPC分类号： C10G35/095 , B01J29/0354 , B01J29/064 , B01J29/44 , B01J29/74 , B01J29/7415 , C07C5/417
摘要： An improved, low-pressure dehydrocyclization and/or reforming process based on a non-acidic metal containing crystalline microporous tin catalyst, in which the feed is rich in low octane hydrocarbons, such as paraffins, and in which the product has increased aromatic content and increased octane value over that of the feed.
摘要翻译： 基于非酸性金属的结晶微孔锡催化剂的改进的低压脱氢环化和/或重整方法，其中进料富含低辛烷烃，如链烷烃，其中产物具有增加的芳族含量， 辛烷值增加超过饲料。
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5.发明授权
公开(公告)号：US5124497A
公开(公告)日：1992-06-23
申请号：US419928
申请日：1989-10-11
CPC分类号： C07C5/417 , B01J29/44 , B01J2229/26 , B01J2229/42 , B01J29/65 , B01J29/70
摘要： A process for producing monosubstituted monoalkylaromatics from C.sub.8 +n-paraffins-containing feeds, by contacting the feeds with a non-acid catalyst comprising a microporous crystalline material containing tin, indium, thallium or lead, is disclosed.
摘要翻译： 公开了一种通过使进料与含有锡，铟，铊或铅的微孔结晶材料的非酸催化剂接触来从C8 +正链烷烃进料生产单取代单烷基芳烃的方法。
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6.发明授权Process for the conversion of paraffins to olefins and/or aromatics and low acidity zeolite catalyst therefor 失效将链烷烃转化为烯烃和/或芳族化合物和低酸性沸石催化剂的方法
公开(公告)号：US5019664A
公开(公告)日：1991-05-28
申请号：US469648
申请日：1990-01-24
申请人： Kenneth J. Del Rossi , Ralph M. Dessau , Albin Huss, Jr. , Garry W. Kirker , David O. Marler , Randall D. Partridge
发明人： Kenneth J. Del Rossi , Ralph M. Dessau , Albin Huss, Jr. , Garry W. Kirker , David O. Marler , Randall D. Partridge
CPC分类号： B01J29/04 , C07C2/12 , C07C5/41 , C07C2529/04 , C07C2529/70
摘要： Aliphatic C.sub.2 to C.sub.12 hydrocarbon(s) are converted to olefin(s) and/or aromatic(s) in the presence of a low acidity Group VIII metal-containing zeolite MCM-22 catalyst, said zeolite exhibiting an Alpha value of not greater than about 150.
摘要翻译： 在低酸性第Ⅷ族金属沸石MCM-22催化剂存在下，脂族C 2至C 12烃转化为烯烃和/或芳族，所述沸石表现出不大于 约150。
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7.发明授权
公开(公告)号：US4849567A
公开(公告)日：1989-07-18
申请号：US138430
申请日：1987-12-28
IPC分类号： B01J29/44 , C07C5/333 , C07C5/41 , C10G35/095
CPC分类号： C10G35/095 , B01J29/44 , C07C5/417
摘要： A catalytic dehydrogenation to produce the unsaturated analogs of aliphatic compounds with high process selectivity for the unsaturated analog production. The catalytic dehydrogenation comprises contacting the aliphatic compound, under dehydrogenation conditions, with a catalyst composition comprising a dehydrogenation metal and indium containing non-acidic crystalline microporous material.
摘要翻译： 催化脱氢以生产脂肪族化合物的不饱和类似物，具有高不饱和类似物生产的工艺选择性。 催化脱氢包括在脱氢条件下使脂族化合物与包含脱氢金属和含有非铟酸性结晶微孔材料的铟的催化剂组合物接触。
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8.发明授权
公开(公告)号：US4922050A
公开(公告)日：1990-05-01
申请号：US353584
申请日：1989-05-18
IPC分类号： B01J29/44 , C07C5/333 , C07C5/41 , C10G35/095
CPC分类号： C10G35/095 , B01J29/44 , C07C5/417
摘要： A catalytic dehydrogenation to produce the unsaturated analogs of aliphatic compounds with high process selectivity for the unsaturated analog production. The catalytic dehydrogenation comprises contacting the aliphatic compound, under dehydrogenation conditions, with a catalyst composition comprising a dehydrogenation metal and indium containing non-acidic crystalline microporous material.
摘要翻译： 催化脱氢以生产脂肪族化合物的不饱和类似物，具有高不饱和类似物生产的工艺选择性。 催化脱氢包括在脱氢条件下使脂族化合物与包含脱氢金属和含有非铟酸性结晶微孔材料的铟的催化剂组合物接触。
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9.发明授权Integrated hydroprocessing scheme for production of premium quality distillates and lubricants 失效一体化加氢处理方案，用于生产优质馏出物和润滑油
公开(公告)号：US4764266A
公开(公告)日：1988-08-16
申请号：US19983
申请日：1987-02-26
摘要： An integrated refining scheme for hydroprocessing high boiling fractions such as gas oil and catalytically cracked cycle oils to produce premium quality distillates, especially jet fuels and naphthas suitable for reforming into high octane gasoline. In addition, unconverted, high boiling fractions suitable for processing by conventional refining techniques into high quality, low pour point lube base stocks are obtained. The integrated hydroprocessing comprises a first stage hydrocracking step employing an aromatic selective hydrocracking catalyst based on a large pore size acidic component such as amorphous alumina or silica alumina or a large pore size zeolite such as zeolite X or zeolite Y. The hydrocracking may be operated either in a naphtha directing mode under conditions of moderate to high severity or under conditions of low to moderate severity to produce a relatively higher proportion of product boiling in the middle distillate range. The unconverted fraction from the hydrocracking step is passed to a second step in which it is hydroprocessed over a zeolite beta catalyst with additional hydrogenation-dehydrogenation functionality. In this stage, the paraffins remaining in the feed are attacked by the zeolite beta to form isoparaffins and conditions may be controlled to favor hydroisomerization over hydrocracking so as to increase the yield of middle distillate product, especially of high isoparaffinic jet fuels and diesel fuel.
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10.发明授权Hydrotreating/isomerization process to produce low pour point distillate fuels and lubricating oil stocks 失效加氢处理/异构化工艺生产低倾点馏出燃料和润滑油库存
公开(公告)号：US4518485A
公开(公告)日：1985-05-21
申请号：US557696
申请日：1983-12-02
摘要： A process for dewaxing a hydrocarbon feedstock with a relatively high pour point and containing paraffins selected from the group of normal paraffins and slightly branched paraffins and sulfur and nitrogen compounds which comprises subjecting said oil to hydrotreating in a hydrotreating zone operated at hydrotreating conditions sufficient to remove at least a portion of said sulfur and nitrogen compounds and subjecting said hydrotreated oil to catalytic dewaxing by contacting said oil with a catalyst comprising zeolite beta having a silica/alumina ratio of at least 30:1 and a hydrogenation/dehydrogenation component under isomerization conditions.
摘要翻译： 一种使具有较高倾点的烃原料脱蜡并含有选自正构烷烃和轻支化链烷烃和硫和氮化合物的链烷烃的方法，其包括使所述油在加氢处理区中加氢处理，所述加氢处理区在加氢处理条件下操作，所述加氢处理条件足以除去 所述硫和氮化合物的至少一部分，并使所述加氢处理的油通过使所述油与二氧化硅/氧化铝比为至少30:1的沸石β和在异构化条件下的氢化/脱氢组分接触的催化剂进行催化脱蜡。
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