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21. 发明申请

US20080289999A1 Process for Pre-Refining Crude Oil with Moderate Multi-Step Hydroconversion of Virgin Asphalt in the Presence of Diluent 审中-公开
标题翻译：在稀释剂存在下对原油沥青进行中等程度的多级加氢转化预炼原油的工艺
公开(公告)号：US20080289999A1
公开(公告)日：2008-11-27
申请号：US11912774
申请日：2006-03-24
申请人： Eric Lenglet
发明人： Eric Lenglet
IPC分类号： C10C3/00
CPC分类号： C10G65/18 , C10G67/049
摘要： For pre-refining a crude oil P, which P is fractionated into several fractions, typically hydrotreating, hydrocracking or hydroconverting some thereof, then re-composing said fractions and in general producing at least two pre-refined oils Pa, Pc, Pa being a high quality non-asphaltenic oil and Pc being a residual oil. The process typically comprises at least one initial distillation step and one deasphalting step SDA with a solvent with a molecular weight of at least 50 to separate a deasphalted oil DAO from a virgin asphalt stream AS. AS is hydroconverted in at least 2 ebullated bed reactors in series, with a moderate conversion of less than 56%, mixed with a virgin diluent comprising light fractions. The DAO is typically hydrocracked with a limited conversion of less than 80%.
摘要翻译：为了预精炼将P馏分成几个馏分的原油P，通常加氢处理，加氢裂化或其中一些加氢转化，然后重新组成所述级分，并且通常生产至少两种预精制油Pa，Pc，Pa为高品质非沥青油，Pc为残油。该方法通常包括至少一个初始蒸馏步骤和一个脱沥青步骤SDA与分子量至少为50的溶剂以分离脱沥青油DAO与原始沥青流AS。 AS在至少2个沸腾床反应器中串联加氢转化，中等转化率小于56％，与包含轻馏分的原始稀释剂混合。 DAO通常加氢裂化，转化率小于80％。

22. 发明授权

US07144559B2 Device and process optimizing the circulation of a suspension in an installation comprising a Fischer-Tropsch reactor 有权
标题翻译：装置和方法优化在包括费 - 托反应器的装置中悬浮液的循环
公开(公告)号：US07144559B2
公开(公告)日：2006-12-05
申请号：US10178906
申请日：2002-06-25
申请人： Jean-Marc Schweitzer , Eric Lenglet , Franck Gaviot-Blanc
发明人： Jean-Marc Schweitzer , Eric Lenglet , Franck Gaviot-Blanc
IPC分类号： B01J8/00 , C07C27/00
CPC分类号： C10G2/342 , B01J8/228 , B01J2208/00256 , B01J2208/003 , B01J2208/00539 , B01J2208/00548 , B01J2219/00247
摘要： Installation for chemical conversion of a feedstock by Fischer-Tropsch reaction comprising a reactor that contains a slurry constituted by at least one suspension of at least one solid in a liquid, a gas feed, a circuit, external to the reactor, of continuous circulation of a stream of slurry, whereby said slurry is drawn off at least one point (A) and reintroduced at least in part at least one other point (B), a section for separation of at least one slurry fluid that passes through said external circuit, whereby said installation also comprises: means allowing to shut down the circulation of said slurry in said circuit, means for introducing under pressure at least one fluid for purging the slurry that is contained in the circuit, and means allowing the circulation of the slurry in said external circuit under conditions such that the Reynolds number is greater than 2,500.
摘要翻译：通过费 - 托反应对原料进行化学转化的装置，包括反应器，该反应器含有由至少一种固体在液体中的至少一种悬浮液，气体进料，反应器外部的回路，连续循环浆料流，其中所述浆料从至少一个点（A）排出并且至少部分地再引入至少一个其他点（B），用于分离通过所述外部回路的至少一种浆液的部分，由此所述安装还包括：允许关闭所述回路中的所述浆料的循环的装置，用于在压力下引入至少一种用于清洗所述回路中包含的浆料的流体的装置，以及允许所述浆料在所述回路中循环的装置在雷诺数大于2500的条件下进行外部电路。

23. 发明授权

US5972206A Flexible steam cracking process and corresponding steam cracking facility 失效
标题翻译：柔性蒸汽裂解工艺及相应的蒸汽裂解设备
公开(公告)号：US5972206A
公开(公告)日：1999-10-26
申请号：US860249
申请日：1997-06-25
申请人： Eric Lenglet , Paul Broutin , Jean-Pierre Burzynski , Herve Cazor , Roland Huin
发明人： Eric Lenglet , Paul Broutin , Jean-Pierre Burzynski , Herve Cazor , Roland Huin
IPC分类号： C10G9/16 , C10G9/36 , C10G9/28 , F28D7/00 , F28D21/00
CPC分类号： C10G9/16 , Y10S585/95
摘要： A flexible steam cracking process for hydrocarbon feeds comprises injection of particles with an average size of between 0.02 mm and 4 mm, at a circulation rate in indirect transfer line exchangers (4) of 20 to 180 m/s, and in a sufficient quantity to limit the increase in temperature at the outlet to the exchangers (4) to a value of less than 100.degree. C. per month, into at least one point upstream of an indirect transfer line exchanger (4), cracking zone (2) remaining in communication with downstream means (6) for the treatment of cooled effluents. At least 70% by weight of the quantity of injected particles is introduced between the outlet to the cracking zone (2) and the tubes of the indirect transfer line exchanger (4). Chemical decoking is carried out in the tubes of the cracking zone at time intervals of less than 4 months by establishing accelerated coke gasification conditions, for example by injecting compounds which catalyse gasification by steam, or by decoking in air and/or steam.
摘要翻译： PCT No.PCT / FR95 / 01717 Sec。 371日期：1997年6月25日 102（e）日期1997年6月25日PCT提交1995年12月22日PCT公布。 WO96 / 20255 PCT出版物日期1996年7月4日用于烃进料的柔性蒸汽裂解方法包括以20至180m / s的间接输送管线交换器（4）中的循环速率注入平均尺寸在0.02mm和4mm之间的颗粒，以及以足够的量将限制出口到交换器（4）的温度升高到小于每月100℃的值到间接输送管线交换器（4）上游的至少一个点，裂化区（2）与下游装置（6）保持通信，用于处理冷却的废水。至少70重量％的注入颗粒的量被引入到裂化区（2）的出口和间接输送管线换热器（4）的管之间。通过建立加速的焦化气化条件，例如通过注入通过蒸汽催化气化的化合物，或通过在空气和/或蒸汽中脱焦来在小于4个月的时间间隔内在裂化区的管中进行化学除焦。

24. 发明授权

US5177292A Method for steam cracking hydrocarbons 失效
标题翻译：蒸汽破碎油料的方法
公开(公告)号：US5177292A
公开(公告)日：1993-01-05
申请号：US623881
申请日：1990-12-12
申请人： Eric Lenglet
发明人： Eric Lenglet
IPC分类号： C10G9/00 , C10G9/16 , C10G9/18 , C10G9/32 , C10G9/36 , F28G1/12
CPC分类号： C10G9/002 , C10G9/16 , C10G9/32 , F28G1/12
摘要： A method of steam cracking hydrocarbons in a steam cracking furnace (10) having tubes (12) connected to indirect quench menas (16) for the gaseous effluent leaving the furnace, the method consisting in allowing a layer of hard coke to form on the inside walls of the furnace tubes (12) and then in injecting a small quantity of solid erosive particles into the steam and hydrocarbon feedstock to be cracked, with the particles being separated from the gaseous effluent in a cyclone (28) provided at the outlet from the indirect quench means. The invention serves in particular to enable a steam cracking installation to operate continuously.
摘要翻译： PCT No.PCT / FR90 / 00273 Sec。 371 1990年12月12日第 102（e）1990年12月12日日期PCT提交1990年4月13日PCT公布。 WO90 / 12852 PCT公开号日本1990年11月1日。一种在蒸汽裂解炉（10）中蒸汽裂解烃的方法，其具有连接到离开炉的气态流出物的间接骤冷气体（16）的管（12），该方法包括：在炉管（12）的内壁上形成硬质焦炭，然后将少量的固体侵蚀性颗粒注入待裂化的蒸汽和烃原料中，将颗粒与旋风分离器中的气态流出物（28 ）设置在间接淬火装置的出口处。本发明特别用于使蒸汽裂解装置能够连续工作。

25. 发明授权

US5139650A Method and installation for steam cracking hydrocarbons 失效
标题翻译：蒸汽破碎油的方法与安装
公开(公告)号：US5139650A
公开(公告)日：1992-08-18
申请号：US646637
申请日：1991-02-04
申请人： Eric Lenglet
发明人： Eric Lenglet
IPC分类号： C07C4/04 , C07C11/02 , C10G9/00 , C10G35/00 , C10G51/02 , F28C3/02 , F28D7/00 , F28F27/00 , F28G1/12
CPC分类号： C10G51/023 , C10G9/002 , F28C3/02 , F28D7/0066 , F28D7/0083 , F28F27/00 , F28G1/12 , F28D2021/0075 , F28F2009/029
摘要： A method and apparatus for steam cracking hydrocarbons in a furnace (10) having rectilinear single-pass tubes (12) which are interconnected at their outlet ends by a manifold (18) within which the steam cracking effluents are subjected to limited pre-quenching by injection of a cooler gaseous medium, with the effluents then being conveyed to quenching means (22). The invention serves in particular to increase the yield of hydrocarbon steam cracking installations.
摘要翻译： PCT No.PCT / FR90 / 00390 Sec。 371日期1991年2月4日 102（e）日期1991年2月4日PCT Filed 1990年6月5日PCT公布。出版物WO90 / 15118 日本1990年12月13日。一种用于在具有直线单通管（12）的炉（10）中蒸汽裂解烃的方法和装置，其在其出口端通过歧管（18）互连，在该歧管内蒸汽裂解废水为通过注入较冷的气体介质进行有限的预淬火，然后将废液输送到淬火装置（22）。本发明特别用于提高烃蒸汽裂解装置的产率。

26. 发明授权

US08425760B2 Process for converting gas into liquids with simplified logistics 有权
标题翻译：使用简化物流将天然气转化为液体的过程
公开(公告)号：US08425760B2
公开(公告)日：2013-04-23
申请号：US12516505
申请日：2007-11-12
申请人： Eric Lenglet , Patrick Chaumette
发明人： Eric Lenglet , Patrick Chaumette
IPC分类号： H01B3/22
CPC分类号： C10G45/58 , C10G2/00 , C10G2300/1022 , C10G2300/1025 , C10G2300/301 , C10G2300/304
摘要： The invention concerns a process for converting a stream of natural or associated gas into liquid fractions, comprising: a) a step for converting said stream of gas into a synthesis gas SG; b) a step FT for Fischer-Tropsch synthesis to convert the SG into liquid fractions; c) a step for fractionating the effluents from the Fischer-Tropsch synthesis into at least one relatively heavy fraction comprising waxes with a boiling point of 565° C. or more and at least one relatively light fraction; d) a step HCKI for isomerization hydrocracking of the relatively heavy fraction, in which at least 75% by weight of the fraction of the feed with a boiling point of more than 565° C. is converted into compounds boiling below 565° C.; e) at least one step for mixing at least the effluents from step HCKI (step d)), the light fraction from step c) and a crude oil P, to thereby produce an oil P*.
摘要翻译：本发明涉及一种将天然或伴生气体流转化为液体馏分的方法，包括：a）将所述气体流转化为合成气SG的步骤; b）费 - 托合成步骤FT将SG转化成液体馏分; c）将来自费 - 托合成的流出物分馏成至少一种相对较重的馏分的步骤，所述馏分包含沸点为565℃以上的蜡和至少一个相对较轻的馏分; d）相对重馏分的异构化加氢裂化的步骤HCKI，其中沸点超过565℃的进料的至少75重量％的馏分转化成沸点低于565℃的化合物; e）至少一个步骤，用于混合至少来自步骤HCKI（步骤d）的流出物，来自步骤c）的轻馏分和原油P，从而产生油P *。

27. 发明授权

US06464949B1 Steam cracking installation with means for protection against erosion 失效
标题翻译：蒸汽裂解装置具有防止侵蚀的手段
公开(公告)号：US06464949B1
公开(公告)日：2002-10-15
申请号：US09202786
申请日：1999-03-08
申请人： Eric Lenglet , Jean-Pierre Burzynski , Gérard Courteheuse , Roland Huin , Yves Gougne
发明人： Eric Lenglet , Jean-Pierre Burzynski , Gérard Courteheuse , Roland Huin , Yves Gougne
IPC分类号： C10G918
CPC分类号： F28F9/02 , C10G9/002 , C10G9/16 , F28D2021/0075 , F28F19/00
摘要： A steam-cracking unit comprises at least one multitube quenching exchanger, equipped with a non-obstructive impact separator for preventing the erosion of the tubular input plate. The impact separator is at least 50% opaque when viewed from transfer pipe. It is arranged inside of an input cone in such a way that there is free passage of at least 40 mm between the periphery of the impact separator and the cone.
摘要翻译：蒸汽裂解装置包括至少一个配有用于防止管状输入板侵蚀的非阻塞性冲击分离器的多管淬火换热器。当从输送管观察时，冲击分离器至少不透明50％。其以输入锥体的内部布置，使得在冲击分离器的周边与锥体之间存在至少40mm的自由通道。

28. 发明授权

US6160192A Steam cracking installation and method with single controlled injection of solid particles in a quenching exchanger 失效
标题翻译：在淬火换热器中单独控制注入固体颗粒的蒸汽裂解装置和方法
公开(公告)号：US6160192A
公开(公告)日：2000-12-12
申请号：US202787
申请日：1999-03-08
申请人： Eric Lenglet , Jean-Pierre Burzynski , Gerard Courteheuse , Roland Huin , Yves Gougne
发明人： Eric Lenglet , Jean-Pierre Burzynski , Gerard Courteheuse , Roland Huin , Yves Gougne
IPC分类号： C10G9/00 , C10G9/16 , C10G9/20 , F28G1/12 , C07C4/04 , F28D7/00
CPC分类号： C10G9/002 , C10G9/16 , F28G1/12 , Y10S585/95
摘要： A steam-cracking unit and a steam-cracking process with controlled injection of solid particles in a quenching exchanger (3) is described. The particles are injected through a single axial injection pipe that is arranged on the axis of input cone (2) of the quenching exchanger, just upstream from an impact separator-diffuser (6) that comprises solid surfaces that are arranged opposite the transfer pipe of the cracked gases toward the exchanger; this impact separator-distributor is located in input cone (2) of the exchanger and is gas-permeable along a number of passages and at least 70% opaque when viewed from the transfer pipe.
摘要翻译： PCT No.PCT / FR97 / 01118 Sec。 371日期1999年3月8日 102（e）1999年3月8日PCT 1997年6月24日PCT公布。公开号WO97 / 49784 日期1997年12月31日描述了一种在淬火换热器（3）中控制注入固体颗粒的蒸汽裂解装置和蒸汽裂解方法。颗粒通过设置在淬火换热器的输入锥体（2）的轴线上的单个轴向喷射管喷射，恰好在冲击分离器 - 扩散器（6）的上游，冲击分离器 - 扩散器（6）包括固体表面，该固体表面与传输管裂化气体朝向交换器; 该冲击分离器分配器位于交换器的输入锥体（2）中，并且沿着多个通道是气体可渗透的，并且当从传送管观察时具有至少70％的不透明度。

29. 发明授权

US5817226A Process and device for steam-cracking a light and a heavy hydrocarbon feedstock 失效
标题翻译：用于蒸汽裂解轻质和重质烃原料的方法和装置
公开(公告)号：US5817226A
公开(公告)日：1998-10-06
申请号：US615319
申请日：1996-07-10
申请人： Eric Lenglet
发明人： Eric Lenglet
IPC分类号： C10G11/20 , C10G9/14 , C10G51/00 , C10G51/02 , C10G9/36 , F28D21/00
CPC分类号： C10G9/14 , C10G2400/20
摘要： There is provided a process and a device with a convection zone (A) and a radiation zone (B) in a furnace (10), whereby the process includes: a first stage of precracking a feedstock of light hydrocarbons (1) and a second stage of final co-cracking of the mixture that is composed of this precracked light feedstock (7) and a feedstock of heavy hydrocarbons (2). The process further includes: separate heating of the two feedstock streams (1 and 2) in the convection zone (A), in which the preheating temperature of each feedstock stream remains below the initial cracking temperature in each case; precracking (5) of the preheated light hydrocarbons; mixing of precracked light hydrocarbon stream (8) while a mixed stream (9) is formed; intense heating of mixed stream (9) to a temperature that is higher than the initial cracking temperature by virtue of the fact that the mixture is introduced into the radiation zone (B) of the furnace (10); and cooling (15) of cracked gases outside the furnace (10).
摘要翻译： PCT No.PCT / EP94 / 02970 371日期：1996年7月10日 102（e）日期1996年7月10日PCT 1994年9月6日PCT PCT。公开号WO95 / 07959 日期1995年3月23日提供了一种在炉（10）中具有对流区（A）和辐射区（B）的工艺和装置，其中该工艺包括：将轻烃原料预裂化的第一阶段 1）和由该预先加工的光原料（7）和重质烃（2）的原料组成的混合物的最终共裂化的第二阶段。该方法还包括：对流区（A）中的两个原料流（1和2）的单独加热，其中每个原料流的预热温度在每种情况下保持低于初始裂解温度; 预热轻烃的预裂化（5）; 在形成混合流（9）的同时混合预先加工的轻质烃流（8）; 由于混合物被引入炉（10）的辐射区（B）的事实，混合物流（9）的强烈加热至高于初始裂解温度的温度; 以及在所述炉（10）外冷却（15）裂化气体。

30. 发明授权

US5183642A Installation for steam cracking hydrocarbons, with solid erosive particles being recycled 失效
标题翻译：蒸汽破碎石油安装，固体颗粒物回收
公开(公告)号：US5183642A
公开(公告)日：1993-02-02
申请号：US700196
申请日：1991-05-30
申请人： Eric Lenglet
发明人： Eric Lenglet
IPC分类号： C10G9/18 , C10G9/16 , C10G9/26 , F28G1/12
CPC分类号： C10G9/16 , F28G1/12
摘要： An installation for steam cracking hydrocarbons comprises at least one hydrocarbon cracking furnace, an indirect quench heat exchanger for the effluents leaving the furnace, direct quench means for said effluent, and means (36, 38) for injecting erosive solid particles into the installation for decoking purposes. The installation also includes a cyclone (10) placed at the outlet from the indirect quench heat exchanger to separate the solid particles from the gaseous effluent, with the solid particle outlet (14) from said cyclone being connected to storage tanks (20, 30) connected in series with isolating valves (16, 28, 34), a source (38) of gas under pressure being provided to raise the pressure in one of the tanks and to inject the solid particles into the installation.
摘要翻译： PCT No.PCT / FR90 / 00711 Sec。 371日期1991年5月30日 102（e）日期1991年5月30日PCT提交1990年10月5日PCT公布。公开号WO91 / 05031 日本1991年4月18日。用于蒸汽裂解烃的装置包括至少一个烃裂解炉，用于离开炉的流出物的间接骤冷换热器，用于所述流出物的直接淬火装置，以及用于注入腐蚀性的装置（36,38）固体颗粒进入安装除焦目的。安装还包括设置在来自间接骤冷换热器的出口处的旋风分离器（10），用于将固体颗粒与气态流出物分离，来自所述旋风分离器的固体颗粒出口（14）连接到储罐（20,30）与隔离阀（16,28,34）串联连接，提供压力气体源（38）以提高其中一个罐中的压力并将固体颗粒注入到设备中。

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