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    • 1. 发明授权
    • Process for making a lubricating composition
    • 润滑组合物的制造方法
    • US06288296B1
    • 2001-09-11
    • US09497949
    • 2000-02-04
    • Stephen J. MillerGerald P. HuffmanNaresh Shah
    • Stephen J. MillerGerald P. HuffmanNaresh Shah
    • C07C1502
    • C10G69/126C10G1/002C10G65/043
    • The invention includes a process of making a lubricating oil composition including: a process for making a high VI lubricating oil composition including the steps of (1) contacting a waste plastics feed including mainly polyethylene in a pyrolysis zone at pyrolysis conditions, whereby at least a portion of the waste plastics feed is cracked, thereby forming a pyrolysis zone effluent including 1-olefins and n-paraffins; (2) passing the pyrolysis zone effluent, including a heavy fraction and a middle fraction, the pyrolysis effluent middle fraction including 1-olefins, to a separations zone; where the pyrolysis effluent heavy fraction portion is separated from the pyrolysis effluent middle fraction; (3) passing the pyrolysis effluent middle fraction to a dimerization zone, where at least a portion of the pyrolysis effluent middle fraction is converted to a lube oil range material; and (4) passing at least a portion of the lube oil range material to a catalytic isomerization dewaxing zone, where at least a portion of the lube oil range material is contacted with a isomerization dewaxing catalyst at isomerization dewaxing conditions thereby forming a high VI lubricating oil composition.
    • 本发明包括一种制备润滑油组合物的方法,其包括:一种制备高VI润滑油组合物的方法,包括以下步骤:(1)在热解条件下使热解段中主要包含聚乙烯的废塑料进料接触,由此至少 废塑料进料的一部分被裂化,从而形成包含1-烯烃和正链烷烃的热解区流出物; (2)将含有1-烯烃的热解流出物中间馏分的热解区流出物(包括重馏分和中间馏分)通入分离区; 其中热解流出物重馏分部分与热解流出物中间馏分分离; (3)将热解流出物中间馏分通入二聚区,其中至少一部分热解流出物中间馏分转化为润滑油范围的材料; 和(4)将润滑油范围材料的至少一部分通入催化异构化脱蜡区,其中至少一部分润滑油范围的材料在异构化脱蜡条件下与异构化脱蜡催化剂接触,从而形成高VI润滑 油组成。
    • 2. 发明授权
    • Method for conversion of waste plastics to lube oil
    • 将废塑料转化为润滑油的方法
    • US6150577A
    • 2000-11-21
    • US224554
    • 1998-12-30
    • Stephen J. MillerGerald P. HuffmanNaresh Shah
    • Stephen J. MillerGerald P. HuffmanNaresh Shah
    • C10G1/00C10G1/02C10G1/10C10G65/04C07C5/13C10G35/04C10G55/04
    • C10G1/10C10G1/002C10G1/02C10G65/043
    • The invention includes a process of making a lubricating oil composition including: a process for making a high VI lubricating oil composition including the steps of (1) contacting a waste plastics feed including mainly polyethylene in a pyrolysis zone at pyrolysis conditions, whereby at least a portion of the waste plastics feed is cracked, thereby forming a pyrolysis zone effluent including 1-olefins and n-paraffins; (2) passing the pyrolysis zone effluent, including a heavy fraction and a middle fraction, the pyrolysis effluent middle fraction including 1-olefins, to a separations zone; where the pyrolysis effluent heavy fraction portion is separated from the pyrolysis effluent middle fraction; (3) passing the pyrolysis effluent heavy fraction to a hydrogenation zone; and (4) passing at least a portion of the hydrogenation zone effluent to a catalytic isomerization dewaxing zone, where at least a portion of the hydrogenation zone effluent is contacted with a isomerization dewaxing catalyst at isomerization dewaxing conditions thereby forming a high VI lubricating oil composition.
    • 本发明包括一种制备润滑油组合物的方法,包括:一种制备高VI润滑油组合物的方法,包括以下步骤:(1)在热解条件下使热解段中主要包含聚乙烯的废塑料进料接触,由此至少 废塑料进料的一部分被裂化,从而形成包含1-烯烃和正链烷烃的热解区流出物; (2)将含有1-烯烃的热解流出物中间馏分的热解区流出物(包括重馏分和中间馏分)通入分离区; 其中热解流出物重馏分部分与热解流出物中间馏分分离; (3)将热解流出物重馏分通入氢化区; 和(4)将至少一部分氢化区流出物通入催化异构化脱蜡区,其中至少一部分氢化区流出物与异构化脱蜡催化剂在异构化脱蜡条件下接触,从而形成高VI润滑油组合物 。
    • 4. 发明授权
    • Catalytic conversion of hydrocarbons to hydrogen and high-value carbon
    • 碳氢化合物催化转化为氢和高碳
    • US06875417B1
    • 2005-04-05
    • US10279489
    • 2002-10-24
    • Naresh ShahDevadas PanjalaGerald P. Huffman
    • Naresh ShahDevadas PanjalaGerald P. Huffman
    • B01J23/755B01J23/80B01J23/84B01J23/881B01J23/89B01J37/00B01J37/03B01J37/18C01B3/26
    • B82Y30/00B01J23/755B01J23/80B01J23/84B01J23/881B01J23/8906B01J37/0009B01J37/03B01J37/18C01B3/26C01B2203/0277C01B2203/1041C01B2203/1047C01B2203/1076C01B2203/1241
    • The present invention provides novel catalysts for accomplishing catalytic decomposition of undiluted light hydrocarbons to a hydrogen product, and methods for preparing such catalysts. In one aspect, a method is provided for preparing a catalyst by admixing an aqueous solution of an iron salt, at least one additional catalyst metal salt, and a suitable oxide substrate support, and precipitating metal oxyhydroxides onto the substrate support. An incipient wetness method, comprising addition of aqueous solutions of metal salts to a dry oxide substrate support, extruding the resulting paste to pellet form, and calcining the pellets in air is also discloses. In yet another aspect, a process is provided for producing hydrogen from an undiluted light hydrocarbon reactant, comprising contacting the hydrocarbon reactant with a catalyst as described above in a reactor, and recovering a substantially carbon monoxide-free hydrogen product stream. In still yet another aspect, a process is provided for catalytic decomposition of an undiluted light hydrocarbon reactant to obtain hydrogen and a valuable multi-walled carbon nanotube coproduct.
    • 本发明提供了用于实现未稀释的轻烃催化分解成氢产物的新催化剂,以及制备这种催化剂的方法。 在一个方面,提供了一种通过混合铁盐水溶液,至少一种另外的催化剂金属盐和合适的氧化物底物载体以及将金属羟基氧化物沉淀到基材载体上来制备催化剂的方法。 初始润湿方法,包括将金属盐水溶液加入到干氧化物基质载体中,将所得糊料挤出成颗粒形式,并在空气中煅烧颗粒。 在另一方面,提供了用于从未稀释的轻烃反应物生产氢的方法,包括如上所述在反应器中使烃反应物与催化剂接触,并回收基本上一氧化碳的氢产物流。 在另一方面,提供了一种用于未稀释的轻烃反应物的催化分解以获得氢气和有价值的多壁碳纳米管副产物的方法。