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1.发明授权
公开(公告)号：US6103099A
公开(公告)日：2000-08-15
申请号：US148282
申请日：1998-09-04
IPC分类号： C10G2/00 , C10G45/58 , C10G45/60 , C10M105/04 , C10N20/00 , C10N30/02 , C10N40/00 , C10N40/04 , C10N40/08 , C10N40/12 , C10N40/25 , C10N70/00 , C10G25/00
CPC分类号： B01J35/023 , C10G2300/1022 , C10G2300/202 , C10G2300/301 , C10G2300/80 , C10G2400/10 , Y10S208/95
摘要： A lubricating base stock useful for forming lubricants such as a multigrade automotive oils, automatic transmission oils, greases and the like is prepared by hydroisomerizing a waxy hydrocarbon feed fraction having an initial boiling point in the 650-750.degree. F. range and an end point of at least 1050.degree. F., synthesized by a slurry Fischer-Tropsch hydrocarbon synthesis process. The hydroisomerization forms a hydroisomerate containing the desired base stock which is recovered, without dewaxing the hydroisomerate. The hydroisomerization is conducted at conditions effective to convert at least 67 wt. % of the 650-750.degree. F.+ waxy feed hydrocarbons to lower boiling hydrocarbons. When combined with a standard lubricant additive package, these base stocks have been formed into multigrade automotive crankcase oils, transmission oils and hydraulic oils meeting the specifications for these oils.
摘要翻译： 通过将初始沸点在650-750°F范围内的蜡质烃进料馏分加氢异构化，并且终点为止，制备用于形成诸如多级汽车油，自动变速器油，润滑脂等润滑剂的润滑基础油料 至少1050°F，通过浆料费 - 托烃合成方法合成。 加氢异构化形成含有所需原料的加氢异构体，其被回收，而不脱蜡加氢异构体。 加氢异构化在有效转化至少67wt。 ％的650-750°F +蜡质原料烃转化为低沸点烃。 当与标准润滑剂添加剂组合使用时，这些基础油已经形成符合这些油的规格的多级汽车曲轴箱油，变速箱油和液压油。
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公开(公告)号：US06322692B1
公开(公告)日：2001-11-27
申请号：US09532377
申请日：2000-03-21
申请人： Ian A. Cody , Douglas R. Boate , Sandra J. Linek , William J. Murphy , John E. Gallagher , Alberto Ravella , Richard A. Demmin
发明人： Ian A. Cody , Douglas R. Boate , Sandra J. Linek , William J. Murphy , John E. Gallagher , Alberto Ravella , Richard A. Demmin
IPC分类号： E10G704
CPC分类号： C10G65/04 , C10G65/12 , C10G67/0418 , C10G67/0445 , C10G2300/302 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2300/44 , C10G2300/80 , C10G2300/805 , C10G2400/10
摘要： A process for producing a lubricating oil basestock having at least 90 wt. % saturates and a VI of at least 105 by selectively hydroconverting a raffinate from a solvent extraction zone in a two step hydroconversion zone followed by a hydrofinishing zone, and a lubricating oil basestock produced by said process.
摘要翻译： 一种制备具有至少90wt。％的润滑油基础油的方法。 通过在两步加氢转化区域中的溶剂萃取区中选择性地加氢转化萃余液，然后加氢精制区和通过所述方法生产的润滑油基础油。
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公开(公告)号：US06325918B1
公开(公告)日：2001-12-04
申请号：US09531733
申请日：2000-03-21
申请人： Ian A. Cody , Douglas R. Boate , Sandra J. Linek , William J. Murphy , John E. Gallagher , Gary L. Harting
发明人： Ian A. Cody , Douglas R. Boate , Sandra J. Linek , William J. Murphy , John E. Gallagher , Gary L. Harting
IPC分类号： G10G1104
摘要： A process for producing a high VI/low volatility lubricating oil basestock and a lubricating oil basestock prepared by said process. The process comprises subjecting the raffinate from a solvent extraction step to a two step, single stage hydroconversion process wherein the first step involves severe hydroconversion of the raffinate followed by a cold hydrofinishing step.
摘要翻译： 一种生产高VI /低挥发性润滑油基础油的方法和通过所述方法制备的润滑油基础油。 该方法包括使萃余液从溶剂萃取步骤进行到两步，单阶段加氢转化方法，其中第一步骤涉及萃余液的严格加氢转化，然后进行冷加氢精制步骤。
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公开(公告)号：US5935416A
公开(公告)日：1999-08-10
申请号：US23438
申请日：1998-02-13
IPC分类号： C10G73/06 , C10G1/04 , C10G3/00 , C10G17/00 , C10G21/00 , C10G45/60 , C10G47/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G67/04 , C10G71/00 , C10G73/32 , C10G11/02 , C10G25/00
CPC分类号： C10G65/043 , C10G65/04 , C10G65/08 , C10G67/0418 , C10G2400/10 , Y02P30/20
摘要： A process for producing a high VI/low volatility lubricating oil basestock. The process comprises subjecting the raffinate from a solvent extraction step to a two-step, single-stage hydroconversion process wherein the first step involves severe hydroconversion of the raffinate followed by a cold hydrofinishing step. The effluent from the cold hydrofinishing step is then catalytically dewaxed or in the alternative, solvent dewaxed followed by catalytic dewaxing.
摘要翻译： 一种生产高VI /低挥发性润滑油基础油的方法。 该方法包括将来自溶剂萃取步骤的萃余液进行两步，单阶段加氢转化方法，其中第一步骤涉及萃余液的严格加氢转化，随后进行冷加氢精制步骤。 然后将来自冷加氢精制步骤的流出物进行催化脱蜡，或者在溶剂脱蜡之后进行催化脱蜡。
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公开(公告)号：US5911874A
公开(公告)日：1999-06-15
申请号：US768251
申请日：1996-12-17
申请人： Ian A. Cody , Douglas R. Boate
发明人： Ian A. Cody , Douglas R. Boate
IPC分类号： C10G73/06 , C10G7/00 , C10G45/58 , C10G45/60 , C10G65/04 , C10G65/08 , C10G65/12 , C10G67/02 , C10G67/04 , C10G73/00 , C10G73/32 , C10G1/04
CPC分类号： C10G65/04 , C10G65/043 , C10G65/08 , C10G67/0418 , C10G2400/10
摘要： A process for upgrading a wax-containing feedstock to produce a wax and a high VI/low volatility lubricating oil basestock. The process comprises subjecting the raffinate from a solvent extraction step to a two step, single stage hydroconversion process wherein the first step involves severe hydroconversion of the raffinate followed by a cold hydrofinishing step.
摘要翻译： 一种用于升级含蜡原料以生产蜡和高VI /低挥发性润滑油基础油的方法。 该方法包括使萃余液从溶剂萃取步骤进行到两步，单阶段加氢转化方法，其中第一步骤涉及萃余液的严格加氢转化，然后进行冷加氢精制步骤。
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公开(公告)号：US5220106A
公开(公告)日：1993-06-15
申请号：US858455
申请日：1992-03-27
摘要： Organic non-quaternary clathrate salts are useful for separating hydrocarbon feed streams into aromatics rich fraction and aromatics lean fraction. The organic non-quaternary clathrate salts are characterized by having cations containing less than 16 carbon atoms. Preferred salts are collidinium triflate and triethylammonium dihydroxybenzoate.
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公开(公告)号：US6096189A
公开(公告)日：2000-08-01
申请号：US768252
申请日：1996-12-17
申请人： Ian A. Cody , Douglas R. Boate , Sandra J. Alward , William J. Murphy , John E. Gallagher , Alberto Ravella , Richard A. Demmin
发明人： Ian A. Cody , Douglas R. Boate , Sandra J. Alward , William J. Murphy , John E. Gallagher , Alberto Ravella , Richard A. Demmin
IPC分类号： C10G45/58 , C10G65/04 , C10G65/12 , C10G67/04 , C10G73/06 , C10M177/00 , C10G1/04 , C10G71/00
CPC分类号： C10G67/0418 , C10G65/04 , C10G65/043 , C10G2300/1062 , C10G2300/301 , C10G2300/302 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/10
摘要： A process for producing a lubricating oil basestock having at least 90 wt. % saturates and a VI of at least 105 by selectively hydroconverting a raffinate from a solvent extraction zone in a two step hydroconversion zone followed by a hydrofinishing zone.
摘要翻译： 一种制备具有至少90wt。％的润滑油基础油的方法。 通过在两步加氢转化区中随后加氢精制区选择性地将来自溶剂萃取区的萃余液加氢转化至少为105的饱和物。
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公开(公告)号：US5976353A
公开(公告)日：1999-11-02
申请号：US678382
申请日：1996-06-28
申请人： Ian A. Cody , Douglas R. Boate , Sandra J. Alward , William J. Murphy , John E. Gallagher , Gary L. Harting
发明人： Ian A. Cody , Douglas R. Boate , Sandra J. Alward , William J. Murphy , John E. Gallagher , Gary L. Harting
IPC分类号： C10G73/06 , C10G45/60 , C10G65/04 , C10G65/08 , C10G65/12 , C10G67/04 , C10G73/32 , C10G1/04 , C10G11/02 , C10G25/00
CPC分类号： C10G67/0418 , C10G65/04 , C10G65/043 , C10G65/08 , C10G2400/10
摘要： A process for producing a high VI/low volatility lubricating oil basestock. The process comprises subjecting the raffinate from a solvent extraction step to a two step, single stage hydroconversion process wherein the first step involves severe hydroconversion of the raffinate followed by a cold hydrofinishing step.
摘要翻译： 一种生产高VI /低挥发性润滑油基础油的方法。 该方法包括使萃余液从溶剂萃取步骤进行到两步，单阶段加氢转化方法，其中第一步骤涉及萃余液的严格加氢转化，然后进行冷加氢精制步骤。
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公开(公告)号：US5935417A
公开(公告)日：1999-08-10
申请号：US23573
申请日：1998-02-13
IPC分类号： C10G45/58 , C10G1/04 , C10G3/00 , C10G17/00 , C10G21/00 , C10G47/02 , C10G65/04 , C10G65/12 , C10G67/04 , C10G71/00 , C10G73/06 , C10M177/00 , C10G11/04
CPC分类号： C10G65/04 , C10G65/043 , C10G67/0418 , C10G2400/10 , Y02P30/20
摘要： A process for producing a lubricating oil basestock having at least 90 wt. % saturates and a VI of at least 105 by selectively hydroconverting a raffinate from a solvent extraction zone in a two step hydroconversion zone followed by a hydrofinishing zone and a dewaxing zone.
摘要翻译： 一种制备具有至少90wt。％的润滑油基础油的方法。 通过在两步加氢转化区中随后加氢精制区和脱蜡区选择性地将来自溶剂萃取区的残液选择性地加氢转化至少为105的饱和物。
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