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71.发明授权
公开(公告)号：EP3110916B1
公开(公告)日：2018-08-15
申请号：EP14816330.6
申请日：2014-12-23
CPC分类号： C10G69/06 , C10G9/36 , C10G11/18 , C10G29/205 , C10G65/10 , C10G65/12 , C10G69/02 , C10G2300/107
摘要： A process for converting high boiling hydrocarbon feedstock into lighter boiling hydrocarbon products in which the lighter boiling hydrocarbon products are suitable feedstock for petrochemical processes.
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72.发明授权PROCESS FOR CONVERTING MIXED WASTE PLASTIC (MWP) INTO VALUABLE PETROCHEMICALS 有权将混合废弃塑料（MWP）转化为可重用石化产品的工艺
公开(公告)号：EP3110912B1
公开(公告)日：2018-03-14
申请号：EP14816324.9
申请日：2014-12-23
IPC分类号： C10G45/00 , C07C45/35 , C07C5/327 , C10G45/02 , C10G47/36 , C10G1/10 , C10G9/36 , C10G65/12 , C10G69/06 , C10G47/00 , C10G69/02 , C10G70/00
CPC分类号： C10G1/10 , C10G9/36 , C10G45/00 , C10G45/02 , C10G47/00 , C10G47/36 , C10G65/12 , C10G69/02 , C10G69/06 , C10G70/00 , C10G2300/1003 , C10G2300/1074 , C10G2300/202 , C10G2300/205
摘要： A process for converting mixed waste plastic (MWP) into valuable petrochemicals including feeding MWP to a pyrolysis reactor, converting the MWP into a gaseous stream and a liquid stream, and further processing the gaseous stream into valuable petrochemicals.
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公开(公告)号：EP3017024B1
公开(公告)日：2017-12-27
申请号：EP14735909.5
申请日：2014-06-30
CPC分类号： C10G69/02 , C10G65/00 , C10G65/10 , C10G65/18 , C10G67/0445 , C10G69/06 , C10G69/14 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2300/107 , C10G2300/1077 , C10G2400/20 , C10G2400/30
摘要： The present invention relates to a process for upgrading refinery heavy residues to petrochemicals, comprising the following steps of: (a) separating a hydrocarbon feedstock in a distillation unit into a to overhead stream and a bottom stream (b) feeding said bottom stream to a hydrocracking reaction area (c) separating reaction products, which are generated from said reaction area of step (b) into a stream rich in mono-aromatics and in a stream rich in poly-aromatics (d) feeding said stream rich in mono-aromatics to a gasoline hydrocracker (GHC) unit, (e) feeding said stream rich in poly-aromatics to a ring opening reaction area.
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公开(公告)号：EP2588572A4
公开(公告)日：2017-11-01
申请号：EP11804104
申请日：2011-06-28
发明人： PRENTICE KRISTA M , DAAGE MICHEL A , DANDEKAR AJIT B , OLIVERI CHRISTOPHER G , VIJAY ROHIT , MCCARTHY STEPHEN J , LAI FRANK WENYIH , FINGLAND BRADLEY R
IPC分类号： C10G45/00
CPC分类号： C10G65/043 , C10G45/06 , C10G45/08 , C10G45/44 , C10G45/52 , C10G45/58 , C10G45/62 , C10G45/64 , C10G47/16 , C10G47/18 , C10G65/046 , C10G65/12 , C10G69/02 , C10G2300/202 , C10G2300/302 , C10G2300/4018 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/10
摘要： An integrated process for producing naphtha fuel, diesel fuel and/or lubricant base oils from feedstocks under sour conditions is provided. The ability to process feedstocks under higher sulfur and/or nitrogen conditions allows for reduced cost processing and increases the flexibility in selecting a suitable feedstock. The sour feed can be delivered to a catalytic dewaxing step without any separation of sulfur and nitrogen contaminants, or with only a high pressure separation so that the dewaxing still occurs under sour conditions. Various combinations of hydrotreating, catalytic dewaxing, hydrocracking, and hydrofinishing can be used to produce fuel products and lubricant base oil products.
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公开(公告)号：EP3221432A1
公开(公告)日：2017-09-27
申请号：EP15816906.0
申请日：2015-11-10
发明人： XU, Xiaochun , LUKASKI, Adrienne, C. , WILSON, Keith , SCHORFHEID, James, John , KAUFMAN, Jeffrey, Lawrence
CPC分类号： C10G45/50 , B01J23/882 , B01J23/883 , B01J23/888 , B01J23/8885 , B01J37/20 , C10G35/06 , C10G45/08 , C10G47/06 , C10G65/02 , C10G65/04 , C10G65/08 , C10G65/12 , C10G67/04 , C10G69/02 , C10G69/08 , C10G2300/1048 , C10G2300/202 , C10G2300/301 , C10G2400/00 , C10M101/02
摘要： Methods are provided for hydroprocessing a feed (such as hydrotreating, hydrocracking, or hydrofining a feed) to generate a product with a reduced or minimized aromatics content relative to the severity of the hydroprocessing conditions. In some types of hydroprocessing applications, it can be desirable to select the severity of hydroprocessing conditions to achieve a desired level of removal for sulfur, a desired level for removal of nitrogen, and/or a desired level for increasing the viscosity index of a feed. The severity for heteroatom removal and/or viscosity index uplift can also correspond to an amount of conversion of a feed to lower boiling point products, so the lowest severity conditions suitable for achieving a product quality can be desirable. By improving the aromatics saturation during hydroprocessing, the severity of subsequent aromatics saturation processes can be reduced.
摘要翻译： 提供了加氢处理进料（例如加氢处理，加氢裂化或加氢精制进料）以产生相对于加氢处理条件的严重程度而言具有降低的或最小化的芳族化合物含量的产物的方法。 在一些类型的加氢处理应用中，可能希望选择加氢处理条件的严重性以达到硫的所需去除水平，去除氮的期望水平和/或提高进料的粘度指数的期望水平 。 杂原子去除和/或粘度指数提升的严重程度也可以对应于进料到较低沸点产物的转化量，因此可以期望适合于实现产品质量的最低严酷条件。 通过改进加氢处理期间的芳烃饱和度，可以降低后续芳烃饱和过程的严重性。
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76.发明公开SYSTEM AND METHODS OF TRIM DEWAXING DISTILLATE FUELS 有权系统VERFAHREN ZUR VERKLEIDUNGSENTPARAFFINIERUNG VON DESTILLBRENNSTOFFEN
公开(公告)号：EP3137579A1
公开(公告)日：2017-03-08
申请号：EP15719956.3
申请日：2015-04-21
IPC分类号： C10G31/06 , C10G51/02 , C10G53/04 , C10G55/02 , C10G55/04 , C10G55/06 , C10G67/02 , C10G69/02
CPC分类号： C10G69/02 , B01J8/0453 , B01J8/0492 , B01J19/006 , B01J19/008 , B01J19/245 , B01J2208/00929 , B01J2219/00774 , B01J2219/24 , C10G15/08 , C10G31/06 , C10G51/02 , C10G53/04 , C10G55/02 , C10G55/04 , C10G55/06 , C10G67/02 , C10G69/04 , C10G69/06 , C10G2300/304 , C10G2300/4012
摘要： Systems and methods are provided for dewaxing a distillate fuel oil by subjecting an at least partially hydroprocessed distillate fuel oil to cavitation to reduce the pour point, reduce the cloud point, reduce the cold filter plugging point, or a combination thereof of the distillate fuel oil.
摘要翻译： 提供了系统和方法，用于使馏出物燃料油脱蜡，使至少部分加氢处理的馏出物燃料油气化以降低倾点，降低浊点，减少冷滤器堵塞点或其蒸馏燃料油的组合 。
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公开(公告)号：EP2880131B1
公开(公告)日：2016-11-02
申请号：EP13750418.9
申请日：2013-07-26
CPC分类号： C10G51/04 , C10G11/05 , C10G45/08 , C10G69/02 , C10G69/04 , C10G69/06 , C10G2300/1074 , C10G2300/307 , C10G2400/02 , C10G2400/04
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公开(公告)号：EP3063254A1
公开(公告)日：2016-09-07
申请号：EP14793080.4
申请日：2014-10-30
摘要： The invention relates to a process for the conversion of a paraffinic feedstock that comprises at least 50 wt % of compounds boiling above 370° C. and which has a paraffin content of at least 60 wt %, an aromatics content of below 1 wt %, a naphthenic content below 2 wt %, a nitrogen content of below 0.1 wt %, and a sulphur content of below 0.1 wt %, the process comprising: a) subjecting the paraffinic feedstock to a hydroprocessing step to obtain an at least partially isomerised feedstock; b) separating the at least partially isomerised feedstock into one or more middle distillate fractions and a first residual fraction, wherein step a) is carried out by contacting the paraffinic feedstock with a first catalyst having hydrocracking and hydroisomerising activity and then with a second catalyst having hydrocracking and hydroisomerising activity, wherein the second catalyst is more active in hydroisomerisation and less active in hydrocracking than the first catalyst.
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79.发明公开PROCESS AND INSTALLATION FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICALS HAVING AN IMPROVED CARBON-EFFICIENCY 审中-公开方法及系统的石油化学品纸品加工原油具有改进的碳效率
公开(公告)号：EP3017019A1
公开(公告)日：2016-05-11
申请号：EP14735552.3
申请日：2014-06-30
发明人： WARD, Andrew Mark , NARAYANASWAMY, Ravichander , OPRINS, Arno Johannes Maria , RAJAGOPALAN, Vijayanand , SCHAERLAECKENS, Egidius Jacoba Maria , VELASCO PELAEZ, Raul
CPC分类号： C10G69/02 , C10G47/02 , C10G47/14 , C10G47/16 , C10G47/20 , C10G65/00 , C10G65/10 , C10G65/18 , C10G2300/104 , C10G2300/1044 , C10G2300/1051 , C10G2300/1055 , C10G2300/1059 , C10G2400/20 , C10G2400/30 , Y02P20/125
摘要： The present invention relates to an integrated process to convert crude oil into petrochemical products comprising crude oil distillation, hydrocracking and olefins synthesis, which process comprises subjecting a hydrocracker feed to hydrocracking to produce LPG and BTX and subjecting the LPG produced in the process to olefins synthesis. Furthermore, the present invention relates to a process installation to convert crude oil into petrochemical products comprising: a crude distillation unit comprising an inlet for crude oil and at least one outlet for one or more of naphtha, kerosene and gasoil; a hydrocracker comprising an inlet for a hydrocracker feed, an outlet for LPG and an outlet for BTX; and a unit for olefins synthesis comprising an inlet for LPG produced by the integrated petrochemical process installation and an outlet for olefins. The hydrocracker feed used in the process and the process installation of the present invention comprises one or more of naphtha, kerosene and gasoil produced by crude oil distillation in the process; and refinery unit-derived light-distillate and/or refinery unit-derived middle-distillate produced in the process. The process and process installation of the present invention have an increased production of petrochemicals at the expense of the production of fuels and an improved carbon efficiency in terms of the conversion of crude oils into petrochemicals.
摘要翻译： 本发明涉及到集成方法原油转化为石油化工产品，包括原油蒸馏，加氢裂化和烯烃合成，该方法包括使加氢裂化进料的加氢裂化，以产生LPG和BTX和经受在此过程中，以烯烃合成产生的LPG ， 进一步地，本发明涉及一种过程装置，以原油转化为石油化工产品，包括：在包括入口，用于原油和用于一种或多种石脑油，煤油和瓦斯油中的至少一个出口的原油蒸馏装置; 水力裂化包括入口，用于在出口的加氢裂化进料为LPG和在出口对BTX的; 和烯烃合成一个单元，用于通过所述集成石油化工工艺和安装出口用于烯烃的制备LPG入口包括。 在该方法中使用的加氢裂化进料和本发明的过程中安装包括一个或多个石脑油，煤油和由原油蒸馏的过程中产生的瓦斯油的; 和精炼单元衍生的光馏出物和/或精炼单元衍生的过程中中间馏分制备。 本发明的方法和过程的安装必须增加生产石化在生产燃料的费用和改善碳效率在原油转化为石油化学产品的条件。
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公开(公告)号：EP2880131A1
公开(公告)日：2015-06-10
申请号：EP13750418.9
申请日：2013-07-26
CPC分类号： C10G51/04 , C10G11/05 , C10G45/08 , C10G69/02 , C10G69/04 , C10G69/06 , C10G2300/1074 , C10G2300/307 , C10G2400/02 , C10G2400/04
摘要： An integrated thermal and catalytic process for improving the yield of middle distillate from heavy petroleum oil feeds comprises cracking the heavy portion (345 °C+) of the feed in a thermal conversion zone, followed by hydrotreating the thermally cracked product and the lighter portion of the feed and then separating the hydrotreated product into a bottoms fraction which is passed to a catalytic cracking step.
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