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公开(公告)号：US20110155635A1
公开(公告)日：2011-06-30
申请号：US12945765
申请日：2010-11-12
申请人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
发明人： Manuela Serban , Alakananda Bhattacharyya , Beckay J. Mezza , Kurt Vanden Bussche , Christopher P. Nicholas , Warren K. Bennion
CPC分类号： C10G21/06 , C10G21/12 , C10G21/20 , C10G21/24 , C10G21/28 , C10G55/02 , C10G57/00 , C10G2300/107 , C10G2300/1077 , C10G2300/205 , C10G2300/206 , C10G2300/4081 , C10G2300/44 , C10G2300/805
摘要： A process for removing a metal from a resid feed includes contacting the resid feed comprising the metal with a resid-immiscible ionic liquid to produce a resid and resid-immiscible ionic liquid mixture, and separating the mixture to produce a resid effluent having a reduced metal content relative to the resid feed.
摘要翻译： 用于从渣油中除去金属的方法包括将包含金属的残渣进料与残渣不混溶的离子液体接触以产生渣油和残渣不混溶的离子液体混合物，并分离混合物以产生具有还原金属的残渣流出物 相对于残留饲料的内容。
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12.发明申请公开(公告)号：US20130153464A1
公开(公告)日：2013-06-20
申请号：US13555769
申请日：2012-07-23
IPC分类号： C10G67/02
CPC分类号： C10G69/04 , C10G55/06 , C10G67/04 , C10G2300/1074
摘要： A process for removing a refractory nitrogen compound from a hydroprocessed vacuum gas oil feed includes contacting the hydroprocessed vacuum gas oil feed comprising the nitrogen compound with a VGO-immiscible phosphonium ionic liquid to produce a hydroprocessed vacuum gas oil and VGO-immiscible phosphonium ionic liquid mixture, and separating the mixture to produce a hydroprocessed vacuum gas oil effluent having a reduced refractory nitrogen compound content relative to the vacuum gas oil feed.
摘要翻译： 从加氢真空瓦斯油原料中除去难熔氮化合物的方法包括使包含氮化合物的加氢真空瓦斯油进料与VGO不混溶的鏻离子液体接触以产生加氢处理的真空瓦斯油和VGO不混溶的鏻离子液体混合物 并分离混合物以产生相对于减压瓦斯油进料具有降低的耐难氮氮化合物含量的加氢处理的减压瓦斯油流出物。
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13.发明授权Extraction of polycyclic aromatic compounds from petroleum feedstocks using ionic liquids 有权使用离子液体从石油原料萃取多环芳香族化合物公开(公告)号：US08574426B2
公开(公告)日：2013-11-05
申请号：US13447385
申请日：2012-04-16
CPC分类号： C10G21/18 , C10G21/24 , C10G2300/1074 , C10G2300/206
摘要： The present invention involves a process for removing one or more polycyclic aromatic hydrocarbon compounds from a vacuum gas oil comprising contacting the vacuum gas oil with a vacuum gas oil-immiscible phosphonium ionic liquid to produce a mixture comprising the vacuum gas oil and the vacuum gas oil-immiscible phosphonium ionic liquid, and separating the mixture to produce a vacuum gas oil effluent and a vacuum gas oil-immiscible phosphonium ionic liquid effluent, the vacuum gas oil-immiscible phosphonium ionic liquid effluent comprising the polycyclic aromatic hydrocarbon compound.
摘要翻译： 本发明涉及一种从真空瓦斯油中除去一种或多种多环芳族烃化合物的方法，包括使真空瓦斯油与真空瓦斯油不混溶的鏻离子液体接触以产生包含真空瓦斯油和减压瓦斯油 并且分离混合物以产生真空瓦斯油流出物和真空瓦斯油不混溶的鏻离子液体流出物，所述真空瓦斯油不混溶的鏻离子液体流出物包含多环芳族烃化合物。
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14.发明申请EXTRACTION OF POLYCYCLIC AROMATIC COMPOUNDS FROM PETROLEUM FEEDSTOCKS USING IONIC LIQUIDS 有权使用离子液体从石油饲料中萃取多环芳烃化合物公开(公告)号：US20130153470A1
公开(公告)日：2013-06-20
申请号：US13447385
申请日：2012-04-16
CPC分类号： C10G21/18 , C10G21/24 , C10G2300/1074 , C10G2300/206
摘要： The present invention involves a process for removing one or more polycyclic aromatic hydrocarbon compounds from a vacuum gas oil comprising contacting the vacuum gas oil with a vacuum gas oil-immiscible phosphonium ionic liquid to produce a mixture comprising the vacuum gas oil and the vacuum gas oil-immiscible phosphonium ionic liquid; and separating the mixture to produce a vacuum gas oil effluent and a vacuum gas oil-immiscible phosphonium ionic liquid effluent, the vacuum gas oil-immiscible phosphonium ionic liquid effluent comprising the polycyclic aromatic hydrocarbon compound.
摘要翻译： 本发明涉及一种从真空瓦斯油中除去一种或多种多环芳族烃化合物的方法，包括使真空瓦斯油与真空瓦斯油不混溶的鏻离子液体接触以产生包含真空瓦斯油和减压瓦斯油 - 可混溶的鏻离子液体; 并分离混合物以产生真空瓦斯油流出物和真空瓦斯油不混溶的鏻离子液体流出物，所述真空瓦斯油不混溶的鏻离子液体流出物包含多环芳烃化合物。
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15.发明授权公开(公告)号：US08574427B2
公开(公告)日：2013-11-05
申请号：US13555769
申请日：2012-07-23
CPC分类号： C10G69/04 , C10G55/06 , C10G67/04 , C10G2300/1074
摘要： A process for removing a refractory nitrogen compound from a hydroprocessed vacuum gas oil feed includes contacting the hydroprocessed vacuum gas oil feed comprising the nitrogen compound with a VGO-immiscible phosphonium ionic liquid to produce a hydroprocessed vacuum gas oil and VGO-immiscible phosphonium ionic liquid mixture, and separating the mixture to produce a hydroprocessed vacuum gas oil effluent having a reduced refractory nitrogen compound content relative to the vacuum gas oil feed.
摘要翻译： 从加氢真空瓦斯油原料中除去难熔氮化合物的方法包括使包含氮化合物的加氢真空瓦斯油进料与VGO不混溶的鏻离子液体接触以产生加氢处理的真空瓦斯油和VGO不混溶的鏻离子液体混合物 并分离混合物以产生相对于减压瓦斯油进料具有降低的耐难氮氮化合物含量的加氢处理的减压瓦斯油流出物。
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16.发明授权公开(公告)号：US08414851B2
公开(公告)日：2013-04-09
申请号：US12813534
申请日：2010-06-11
CPC分类号： B01J14/005 , B01J8/18 , C10G11/18 , C10G29/205 , C10G35/04 , C10G57/005
摘要： The apparatus converts ethylene in a dilute ethylene stream and dilute benzene in an aromatic containing stream via alkylation to heavier hydrocarbons. The catalyst may be a zeolite such as UZM-8. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, and hydrogen and selectively converts benzene. At least 40 wt-% of the ethylene in the dilute ethylene stream and at least 20 wt-% of the benzene in the dilute benzene stream can be converted to heavier hydrocarbons.
摘要翻译： 该装置将稀乙烯流中的乙烯和通过烷基化的含芳烃的物流中的苯稀释成较重的烃。 催化剂可以是沸石如UZM-8。 该催化剂耐受诸如硫化氢，碳氧化物和氢气的杂质，并选择性地转化苯。 稀乙烯流中至少40重量％的乙烯和稀苯流中至少20重量％的苯可以转化为较重的烃。
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公开(公告)号：US20100249474A1
公开(公告)日：2010-09-30
申请号：US12416029
申请日：2009-03-31
IPC分类号： C07C2/12
CPC分类号： C07C2/12 , B01J21/12 , B01J23/755 , B01J23/888 , B01J29/7046 , B01J37/0072 , B01J38/30 , B01J2229/42 , C07C2/24 , C07C2521/12 , C07C2523/30 , C07C2523/755 , C07C2523/888 , C10G57/02 , Y02P20/584 , Y02P30/48
摘要： The process and apparatus converts ethylene in a dilute ethylene stream that may be derived from an FCC product to heavier hydrocarbons. The catalyst may be an amorphous silica-alumina base with a Group VIII and/or VIB metal. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, hydrogen and ammonia. At least 40 wt-% of the ethylene in the dilute ethylene stream can be converted to heavier hydrocarbons.
摘要翻译： 该方法和装置将可能从FCC产物衍生的稀乙烯流中的乙烯转化成较重的烃。 催化剂可以是具有VIII族和/或VIB族金属的无定形二氧化硅 - 氧化铝基质。 该催化剂耐受进料杂质如硫化氢，碳氧化物，氢气和氨。 稀乙烯流中至少40重量％的乙烯可以转化成较重的烃。
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18.发明申请APPARATUS FOR THE REDUCTION OF GASOLINE BENZENE CONTENT BY ALKYLATION WITH DILUTE ETHYLENE 有权通过与稀释乙烯进行烷基化还原汽油苯含量的装置公开(公告)号：US20110305602A1
公开(公告)日：2011-12-15
申请号：US12813534
申请日：2010-06-11
IPC分类号： B01J8/18
CPC分类号： B01J14/005 , B01J8/18 , C10G11/18 , C10G29/205 , C10G35/04 , C10G57/005
摘要： The apparatus converts ethylene in a dilute ethylene stream and dilute benzene in an aromatic containing stream via alkylation to heavier hydrocarbons. The catalyst may be a zeolite such as UZM-8. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, and hydrogen and selectively converts benzene. At least 40 wt-% of the ethylene in the dilute ethylene stream and at least 20 wt-% of the benzene in the dilute benzene stream can be converted to heavier hydrocarbons.
摘要翻译： 该装置将稀乙烯流中的乙烯和通过烷基化的含芳烃的物流中的苯稀释成较重的烃。 催化剂可以是沸石如UZM-8。 该催化剂耐受诸如硫化氢，碳氧化物和氢气的杂质，并选择性地转化苯。 稀乙烯流中至少40重量％的乙烯和稀苯流中至少20重量％的苯可以转化为较重的烃。
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公开(公告)号：US08021620B2
公开(公告)日：2011-09-20
申请号：US12416032
申请日：2009-03-31
CPC分类号： B01J23/755 , B01J21/12 , B01J23/888 , B01J29/70 , B01J38/30 , C08F110/02 , Y02P20/584 , Y02P30/48 , C08F2/01 , C08F2500/02
摘要： The process and apparatus converts ethylene in a dilute ethylene stream that may be derived from an FCC product to heavier hydrocarbons. The catalyst may be an amorphous silica-alumina base with a Group VIII and/or VIB metal. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, hydrogen and ammonia. At least 40 wt-% of the ethylene in the dilute ethylene stream can be converted to heavier hydrocarbons.
摘要翻译： 该方法和装置将可能从FCC产物衍生的稀乙烯流中的乙烯转化成较重的烃。 催化剂可以是具有VIII族和/或VIB族金属的无定形二氧化硅 - 氧化铝基质。 该催化剂耐受进料杂质如硫化氢，碳氧化物，氢气和氨。 稀乙烯流中至少40重量％的乙烯可以转化成较重的烃。
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公开(公告)号：US08748681B2
公开(公告)日：2014-06-10
申请号：US12416026
申请日：2009-03-31
IPC分类号： C07C2/12
CPC分类号： C07C2/10 , C07C2521/12 , C07C2523/24 , C07C2523/30 , C07C2523/755 , C07C2523/888
摘要： The process and apparatus converts ethylene in a dilute ethylene stream that may be derived from an FCC product to heavier hydrocarbons. The catalyst may be an amorphous silica-alumina base with a Group VIII and/or VIB metal. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, hydrogen and ammonia. At least 40 wt-% of the ethylene in the dilute ethylene stream can be converted to heavier hydrocarbons.
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