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公开(公告)号：US20240191149A1
公开(公告)日：2024-06-13
申请号：US18444846
申请日：2024-02-19
发明人： Bruce D. Murray , Scott G. Morrison , Kenneth Fountain , Steven R. Horlacher , Vincent D. Mcgahee , Reza Khankal , David Dockter
CPC分类号： C10G69/14 , C10G1/002 , C10G1/10 , C10G67/16 , C10G69/08 , C10G69/126 , C10G2300/1003 , C10G2400/20 , C10G2400/30
摘要： A system for processing plastic waste may include a feed line, a feed fractionator, a hydrotreater, a catalytic reforming unit, a heavy oil cracker, and a steam cracker. A pyrolyzed plastics feed is separated into light, medium, and heavy hydrocarbon streams. The hydrotreater removes sulfur, and the catalytic reforming unit produces a circular aromatic-rich stream. The heavy oil cracker generates cracked streams. The steam cracker produces a circular olefin stream from a cracked stream. A system for processing plastic waste may include the feed line, the feed fractionator, the hydrotreater, a medium hydrocarbon fractionator, the catalytic reforming unit, a full-range reforming unit, the heavy oil cracker, and the steam cracker. The medium hydrocarbon fractionator produces two hydrocarbon streams. The full-range naphtha reforming unit produces a second circular aromatic-rich stream.
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公开(公告)号：US20190016978A1
公开(公告)日：2019-01-17
申请号：US16135132
申请日：2018-09-19
申请人： Ergon, Inc.
IPC分类号： C10G69/08 , C10M101/02 , C10M177/00 , C10G65/12
CPC分类号： C10G69/08 , C10G65/12 , C10G2300/202 , C10G2300/203 , C10G2300/205 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10M101/02 , C10M177/00 , C10M2203/1065 , C10N2220/022 , C10N2220/031 , C10N2230/43
摘要： A process for producing naphthenic base oils from low quality naphthenic crude feedstocks. The naphthenic base oils produced by the process have improved low temperature properties at high yields based on feedstock.
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公开(公告)号：US20180355264A1
公开(公告)日：2018-12-13
申请号：US15988051
申请日：2018-05-24
CPC分类号： C10G67/0418 , C10G7/003 , C10G35/095 , C10G45/08 , C10G45/12 , C10G45/64 , C10G65/043 , C10G65/08 , C10G65/12 , C10G67/0436 , C10G69/08 , C10G2300/1025 , C10G2300/206 , C10G2400/02 , C10G2400/04 , C10G2400/10
摘要： A process of producing Group III base oils, along with a naphtha product and diesel product, from whole waxy crude oil is provided. The inventive process omits the typical vacuum distillation stage and separations to form the typical cuts off of the vacuum tower. By selecting a waxy crude oil suitable for processing without separations, the crude oil may be hydroprocessed, dearomatized, dewaxed, and hydrofinished to produce a Group III base oil. Additionally, the dewaxing catalyst will isomerize the naphtha range molecules to increase the octane value to a suitable level for blending into gasoline and the diesel range molecules to reduce the diesel cloud point.
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公开(公告)号：US10081774B2
公开(公告)日：2018-09-25
申请号：US15279895
申请日：2016-09-29
IPC分类号： C10L1/182 , C10L10/02 , C10G3/00 , C10L1/16 , C10G35/04 , C10G63/00 , C10G65/04 , C10G65/08 , C10G69/04 , C10G69/08 , C10G11/18 , C10G45/02 , C10G45/44 , C10G45/58 , C10L1/02
CPC分类号： C10L1/1824 , C10G3/00 , C10G11/18 , C10G35/04 , C10G45/02 , C10G45/44 , C10G45/58 , C10G63/00 , C10G65/043 , C10G65/08 , C10G69/04 , C10G69/08 , C10G2300/305 , C10G2300/4043 , C10G2300/80 , C10G2400/02 , C10G2400/04 , C10L1/023 , C10L1/1616 , C10L10/02 , C10L2200/0415 , C10L2200/0423 , C10L2230/22 , C10L2270/023 , C10L2290/24 , Y02P30/20
摘要： Systems and processes for the production of fuel and fuel blends involve the production of fuels for blending with one or more alcohols such as ethanol and/or butanol. A method for producing a fuel blend includes blending a light distillate product from an oil refinery with butanol. The fuel blending can be at the oil refinery.
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公开(公告)号：US09796937B2
公开(公告)日：2017-10-24
申请号：US14679075
申请日：2015-04-06
摘要： The present invention concerns a process for the production of light olefins and BTX using a catalytic cracking unit, NCC, processing a naphtha type feed, and an aromatics complex. It can be used to exploit the synergies between these two units. The thermal balance of the NCC, which is intrinsically deficient in coke, is resolved by the optimal use of heat from the reforming furnaces in order to preheat the feed for the NCC, and by introducing at least a portion of the raffinate obtained from the aromatics complex as a mixture with the naphtha.
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公开(公告)号：US20170158974A1
公开(公告)日：2017-06-08
申请号：US15436025
申请日：2017-02-17
IPC分类号： C10G69/08
CPC分类号： C10G69/08 , C01B3/34 , C07C5/367 , C07C5/415 , C07C5/417 , C07C7/005 , C07C7/08 , C07C2529/068 , C07C2529/076 , C10G2400/30 , C07C15/04
摘要： The present invention relates to a method and system for recovering aromatics from a naphtha feedstock obtained from a crude petroleum, natural gas condensate, or petrochemical feedstock. The method and system comprise the steps of recovering an aromatics fraction from the feedstock prior to reforming.
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公开(公告)号：US20170015919A1
公开(公告)日：2017-01-19
申请号：US15279895
申请日：2016-09-29
CPC分类号： C10L1/1824 , C10G3/00 , C10G11/18 , C10G35/04 , C10G45/02 , C10G45/44 , C10G45/58 , C10G63/00 , C10G65/043 , C10G65/08 , C10G69/04 , C10G69/08 , C10G2300/305 , C10G2300/4043 , C10G2300/80 , C10G2400/02 , C10G2400/04 , C10L1/023 , C10L1/1616 , C10L10/02 , C10L2200/0415 , C10L2200/0423 , C10L2230/22 , C10L2270/023 , C10L2290/24 , Y02P30/20
摘要： Systems and processes for the production of fuel and fuel blends involve the production of fuels for blending with one or more alcohols such as ethanol and/or butanol. A method for producing a fuel blend includes blending a light distillate product from an oil refinery with butanol. The fuel blending can be at the oil refinery.
摘要翻译： 用于生产燃料和燃料混合物的系统和方法涉及生产用于与一种或多种醇如乙醇和/或丁醇共混的燃料。 一种生产燃料混合物的方法包括将来自炼油厂的轻馏分产物与丁醇混合。 燃油混合可以在炼油厂。
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公开(公告)号：US09481842B2
公开(公告)日：2016-11-01
申请号：US13624669
申请日：2012-09-21
IPC分类号： C10L1/182 , C10L1/16 , C10G3/00 , C10G35/04 , C10G63/00 , C10G65/04 , C10G65/08 , C10G69/04 , C10G69/08 , C10G11/18 , C10G45/02 , C10G45/44 , C10G45/58 , C10L1/02
CPC分类号： C10L1/1824 , C10G3/00 , C10G11/18 , C10G35/04 , C10G45/02 , C10G45/44 , C10G45/58 , C10G63/00 , C10G65/043 , C10G65/08 , C10G69/04 , C10G69/08 , C10G2300/305 , C10G2300/4043 , C10G2300/80 , C10G2400/02 , C10G2400/04 , C10L1/023 , C10L1/1616 , C10L10/02 , C10L2200/0415 , C10L2200/0423 , C10L2230/22 , C10L2270/023 , C10L2290/24 , Y02P30/20
摘要： Systems and processes for the production of fuel and fuel blends involve the production of fuels for blending with one or more alcohols such as ethanol and/or butanol. A method for producing a fuel blend includes blending a light distillate product from an oil refinery with butanol. The fuel blending can be at the oil refinery.
摘要翻译： 用于生产燃料和燃料混合物的系统和方法涉及生产用于与一种或多种醇如乙醇和/或丁醇共混的燃料。 一种生产燃料混合物的方法包括将来自炼油厂的轻馏分产物与丁醇混合。 燃油混合可以在炼油厂。
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9.发明申请METHODS AND APPARATUSES FOR PRODUCING LINEAR ALKYLBENZENE FROM RENEWABLE OILS 审中-公开从可再生油生产线性烷烃的方法和装置公开(公告)号：US20150376081A1
公开(公告)日：2015-12-31
申请号：US14320088
申请日：2014-06-30
申请人： UOP LLC
CPC分类号： C07C2/66 , C07C4/16 , C07C5/333 , C10G3/00 , C10G29/205 , C10G35/04 , C10G45/58 , C10G59/06 , C10G61/02 , C10G61/04 , C10G69/08 , C10G2300/1014 , C10G2300/1018 , C10G2400/30 , Y02P20/132 , Y02P30/20 , C07C15/107 , C07C11/02 , C07C15/04
摘要： Apparatuses and methods for producing linear alkylbenzene products from renewable oils are provided. An exemplary method includes deoxygenating the renewable oil in a deoxygenation zone to form paraffins. The method fractionates the paraffins to form first and second fractions. The method processes the first fraction of paraffins in a reforming zone to form a reformate stream and recovers a first hydrogen stream from the reforming zone. The method includes forming a LAB stream in a LAB production zone from the second fraction of paraffins and a portion of the reformate stream. Further, the method includes recovering a second hydrogen stream in the LAB production zone and recycling the first hydrogen stream from the reforming zone and the second hydrogen stream from the LAB production zone, wherein substantially all hydrogen recovered from the reforming zone and the LAB production zone is recycled.
摘要翻译： 提供了从可再生油生产线性烷基苯产品的设备和方法。 示例性的方法包括在脱氧区中对可再生油进行脱氧以形成链烷烃。 该方法分馏石蜡以形成第一和第二馏分。 该方法在重整区中处理第一级链烷烃以形成重整产物流并从重整区回收第一氢气流。 该方法包括在第二部分石蜡和重整产物流的一部分的LAB生产区中形成LAB流。 此外，该方法包括回收LAB生产区中的第二氢气流并将来自重整区的第一氢气流和来自LAB生产区的第二氢气流再循环，其中基本上从重整区和LAB生产区回收的所有氢 被回收。
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10.发明申请METHOD FOR PRODUCING OLEFIN AND MONOCYCLIC AROMATIC HYDROCARBON AND APPARATUS FOR PRODUCING ETHYLENE 有权用于生产烯烃和单环芳烃的方法和用于生产乙烯的装置公开(公告)号：US20150275103A1
公开(公告)日：2015-10-01
申请号：US14437298
申请日：2013-10-25
CPC分类号： C10G11/05 , B01J8/02 , B01J2208/027 , C10G35/04 , C10G35/095 , C10G63/04 , C10G69/04 , C10G69/06 , C10G69/08 , C10G2300/1051 , C10G2300/1055 , C10G2400/20 , C10G2400/22 , C10G2400/30 , Y02P20/132
摘要： A method for producing an olefin and a monocyclic aromatic hydrocarbon of the present invention includes a dicyclopentadiene removal treatment step of removing dicyclopentadienes having a dicyclopentadiene skeleton from a feedstock oil which is a thermally-cracked heavy oil obtained from an apparatus for producing ethylene and which has a 90 volume % distillate temperature, as a distillation characteristic, of 390° C. or lower; and a cracking and reforming reaction step of obtaining a product containing an olefin and a monocyclic aromatic hydrocarbon by bringing the feedstock oil having a content of dicyclopentadienes adjusted to 10% by weight or less by treating a part or all of the feedstock oil through the dicyclopentadiene removal step into contact with a catalyst and reacting the feedstock oil.
摘要翻译： 本发明的烯烃和单环芳香族烃的制造方法包括：二乙烯二烯除去处理步骤，从由乙烯生产装置获得的热裂化重油的原料油中除去具有二环戊二烯骨架的二环戊二烯， 作为蒸馏特性的90体积％馏出物温度为390℃以下; 以及通过将二环戊二烯含量调节至10重量％以下的原料油通过二环戊二烯处理一部分或全部原料油而获得含有烯烃和单环芳烃的产物的裂化和重整反应步骤 去除步骤与催化剂接触并使原料油反应。
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