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31. 发明申请

US20080223751A1 Non Asphaltenic Oil 有权
标题翻译：非沥青油
公开(公告)号：US20080223751A1
公开(公告)日：2008-09-18
申请号：US12067522
申请日：2006-09-14
申请人： Eric Lenglet
发明人： Eric Lenglet
IPC分类号： C10G35/00
CPC分类号： C10G67/049 , C10G45/14 , C10G47/24 , C10G65/18
摘要： A reconstituted non-asphaltenic oil Pa comprising at least 28% by weight of naphtha N, having a ratio R of 1.5 or more and a gasoline potential, POTg, in the range 47 to 70, in which: R=(0.9 N+0.5 VGO+)/(MD+0.1 VGO+), POTg=0.9N+0.5 VGO+, with in % by weight: N=naphtha: [30° C./170° C.]; MD=middle distillates: ]170° C./360° C.] and VGO+=fraction boiling above 360° C.R indicates the relative gasoline potential of a non residual oil over middle distillates during its subsequent refining.
摘要翻译：包含至少28重量％的比例R为1.5以上和汽油电位POTg的石脑油N在47至70的范围内的重构非沥青油Pa，其中：R =（0.9N + 0.5 VGO +）/（MD + 0.1 VGO +），POTg = 0.9N + 0.5 VGO +，以重量％计：N =石脑油：[30℃/ 170℃]。 MD =中间馏分：] 170℃/ 360℃]和VGO + =沸点高于360℃的馏分.R表示在其随后的精炼过程中不含中间馏分的非残油的相对汽油电势。

32. 发明授权

US07357855B2 Reactor for chemical conversion of a feed with added heat, and crosswise flow of feed and catalyst 有权
标题翻译：用于加热进料的化学转化反应器，以及进料和催化剂的横向流动
公开(公告)号：US07357855B2
公开(公告)日：2008-04-15
申请号：US11442328
申请日：2006-05-30
申请人： Eric Lenglet , Nicolas Boudet , Frédéric Hoffman
发明人： Eric Lenglet , Nicolas Boudet , Frédéric Hoffman
IPC分类号： C10G35/00 , B01J8/00
CPC分类号： B01J8/0496 , B01J8/0438 , B01J8/12
摘要： Described are a reactor for carrying out a chemical conversion process in a catalytic bed with mechanism for supplying heat integrated into the reactor, and with a very compact reaction zone, combined with efficient use of the catalyst, and a process for converting a feed, such as a hydrocarbon feed, undergoing an endothermic reaction using the disclosed reactor.
摘要翻译：描述了一种用于在催化床中进行化学转化过程的反应器，其具有用于提供集成到反应器中的热的机构，并且具有非常紧凑的反应区，结合有效使用催化剂，以及用于转化进料的方法作为烃进料，使用所公开的反应器进行吸热反应。

33. 发明申请

US20080069766A1 Process for producing synthesis gas by steam reforming and partial oxidation 有权
标题翻译：通过蒸汽重整和部分氧化制备合成气的方法
公开(公告)号：US20080069766A1
公开(公告)日：2008-03-20
申请号：US11523741
申请日：2006-09-20
申请人： Alexandre Rojey , Stephane Bertholin , Fabrice Giroudiere , Eric Lenglet
发明人： Alexandre Rojey , Stephane Bertholin , Fabrice Giroudiere , Eric Lenglet
IPC分类号： C01B3/26
CPC分类号： C01B3/382 , B01J8/0496 , B01J8/067 , B01J2208/00221 , B01J2208/00309 , B01J2208/00539 , C01B3/384 , C01B3/386 , C01B2203/0233 , C01B2203/0255 , C01B2203/0261 , C01B2203/0283 , C01B2203/0415 , C01B2203/043 , C01B2203/0805 , C01B2203/0811 , C01B2203/0844 , C01B2203/1241 , C01B2203/1294 , C01B2203/141 , C01B2203/142 , C01B2203/143 , Y02E60/324
摘要： A process for producing synthesis gas, SG, from a hydrocarbon feed and optionally from recycled compounds, F, is described in which: a first feed F1 supplemented with steam undergoes steam reforming in a multi-tube reactor-exchanger R comprising a plurality of reaction tubes (38) containing a steam reforming catalyst and a shell containing said tubes, to produce a first synthesis gas SG1; said reaction tubes (38) are heated principally by convection by circulating a fluid HF in the shell external to said tubes, in which HF is a staged partial oxidation stream with oxygen of a second feed F2 at a pressure in the range 0.5 to 12 MPa, to produce a second synthesis gas SG2; the synthesis gas SG is produced by mixing SG1 and SG2. FIG. 1 to be published.
摘要翻译：描述了从烃进料和任选地来自再循环化合物F生产合成气SG的方法，其中：补充有蒸汽的第一进料F 1在多管反应器 - 交换器R中进行蒸汽重整，其包含多个含有蒸汽重整催化剂的反应管（38）和含有所述管的壳，以产生第一合成气SG 1; 所述反应管（38）主要通过对流来加热所述管外部的壳体中的流体HF，其中HF是分级部分氧化流，其中第二进料F 2的氧在0.5至12的压力下 MPa，以产生第二合成气SG 2; 通过混合SG 1和SG 2制备合成气SG。图。 1发表。

34. 发明授权

US07264782B2 Reactor device having an enclosure made of refractory material and a containment envelope for bringing about chemical reactions requiring heat exchange 失效
$Reactor device having an enclosure made of refractory material and a containment envelope for bringing about chemical reactions requiring heat exchange$
标题翻译：具有由耐火材料制成的外壳的反应器装置和用于引起需要热交换的化学反应的容纳外壳
公开(公告)号：US07264782B2
公开(公告)日：2007-09-04
申请号：US10087981
申请日：2002-03-05
申请人： Luc Nougier , Eric Lenglet
发明人： Luc Nougier , Eric Lenglet
IPC分类号： B01J19/00
CPC分类号： C01B17/0495 , B01J12/005 , B01J19/249 , B01J2219/00081 , B01J2219/00135 , B01J2219/00155 , B01J2219/00166 , B01J2219/2453 , B01J2219/2458 , B01J2219/2467 , B01J2219/2493 , C07C4/04 , C07C5/32 , C10G9/18
摘要： Reactor device (R) for carrying out chemical reactions requiring heat exchange, the reactor is elongate along an axis (XX′), and has, at a first end, at least one orifice (16) for supplying at least one reactant, at an opposite end, at least one orifice (18) for evacuating the effluents formed, a plurality of heat exchangers (12) separated by at least one internal partition (14) and passages for circulating the reactant or reactants and/or effluents, provided between the heat exchangers and the internal partitions. The reactor (R) has at least one enclosure (10) made of refractory material providing heat insulation and containing a heat exchangers (12) and internal partitions (14). The enclosure is contained in an envelope (20) to contain the reactant or reactants and/or effluents circulating inside the reactor.
摘要翻译：用于进行需要热交换的化学反应的反应器装置（R），所述反应器沿着轴线（XX'）是细长的，并且在第一端具有用于供应至少一种反应物的至少一个孔口（16）至少一个用于排出形成的流出物的孔口（18），由至少一个内部隔板（14）分开的多个热交换器（12）和用于使反应物或反应物和/或流出物循环的通道，热交换器和内部隔板。反应器（R）具有由耐火材料制成的至少一个外壳（10），其提供隔热并且包含热交换器（12）和内部隔板（14）。外壳包含在封套（20）中以容纳在反应器内循环的反应物或反应物和/或流出物。

35. 发明授权

US07070742B2 Reactor for chemical conversion of a feedstock in the presence of a diluent, with heat inputs and feedstock/catalyst cross-circulation 有权
标题翻译：在稀释剂存在下进行化学转化的反应器，具有热量输入和原料/催化剂交叉循环
公开(公告)号：US07070742B2
公开(公告)日：2006-07-04
申请号：US10432774
申请日：2001-11-07
申请人： Eric Lenglet , Nicolas Boudet , Frédéric Hoffmann
发明人： Eric Lenglet , Nicolas Boudet , Frédéric Hoffmann
IPC分类号： B01J8/08 , B01J8/12 , F28D13/00 , F28D21/00
CPC分类号： B01J8/0496 , B01J8/003 , B01J8/0035 , B01J8/0438 , B01J8/087 , B01J8/12 , B01J2208/00115 , B01J2208/00707
摘要： A reactor with integrated heat for carrying out a chemical conversion process in the presence of a gaseous diluent supplied through one or more ports at the upper and/or lower ends of a catalytic bed through which a feed moves substantially horizontally, and a process for converting a feed, such as a hydrocarbon feed in the reactor.
摘要翻译：一种具有集成热量的反应器，用于在存在气态稀释剂的情况下进行化学转化过程，所述气体稀释剂通过一个或多个端口在催化床的上端和/或下端通过基本上水平地移动而进入其中; 进料，如反应器中的烃进料。

36. 发明授权

US06824902B2 Process and device for production of electricity in a fuel cell by oxidation of hydrocarbons followed by a filtration of particles 失效
标题翻译：在燃料电池中通过氧化烃然后过滤颗粒来生产电的方法和装置
公开(公告)号：US06824902B2
公开(公告)日：2004-11-30
申请号：US10067921
申请日：2002-02-08
申请人： Eric Lenglet , Pierre Boucot , Gérard Henri Martin
发明人： Eric Lenglet , Pierre Boucot , Gérard Henri Martin
IPC分类号： H01M806
CPC分类号： C01B3/48 , C01B3/32 , C01B3/36 , C01B3/583 , C01B2203/0227 , C01B2203/0261 , C01B2203/0283 , C01B2203/04 , C01B2203/044 , C01B2203/045 , C01B2203/0465 , C01B2203/047 , C01B2203/0485 , C01B2203/066 , C01B2203/0844 , C01B2203/0883 , C01B2203/1276 , C01B2203/1294 , C01B2203/142 , C01B2203/147 , C01B2203/1604 , C01B2203/1609 , C01B2203/1614 , C01B2203/1628 , C01B2203/1652 , C01B2203/169 , H01M8/0612 , H01M8/0662 , H01M2008/1293 , H01M2300/0074 , H01M2300/0082 , Y02P20/129 , Y02P70/56
摘要： The present invention relates to a process for the production of electricity in a fuel cell from hydrocarbons that includes passing a cooled effluent in a first circuit having at least one filter for depositing soot in the filter. The filter is regenerated when concurrently passing the cooled effluent in a second circuit. The present invention also relates to a device for implementing the process.
摘要翻译：本发明涉及一种用于从碳氢化合物在燃料电池中生产电力的方法，该方法包括将具有至少一个过滤器的第一回路中的冷却流出物通过以将过滤器沉积在过滤器中。当在第二回路中同时使冷却的流出物通过时，过滤器被再生。本发明还涉及一种用于实现该过程的装置。

37. 发明授权

US5965013A Steam cracking method and plant using controlled injection of solid particles into a quenching exchanger 失效
标题翻译：蒸汽裂化方法和工厂使用控制注入固体颗粒进入淬火换热器
公开(公告)号：US5965013A
公开(公告)日：1999-10-12
申请号：US836148
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： C10G9/00 , C10G9/16 , F28G1/12 , C10G9/36 , C10G9/28 , F28D7/00 , F28D21/00
CPC分类号： C10G9/002 , C10G9/16 , F28G1/12 , B01J2208/0084 , Y10S585/95
摘要： A facility and a process for steam cracking include controlled injection of solid particles into a transfer line exchanger (3). The particles are injected via injection lines, numbering between 1 and 8, just upstream of an impact-diffuser (6) comprising solid surfaces disposed on either side of the line for transfer of the cracked gases to the exchanger; this impact-diffuser is located in the inlet cone (2) of the exchanger, is permeable to the gases via a plurality of passages and at least 70% opaque viewed from the transfer line.
摘要翻译： PCT No.PCT / FR95 / 01721 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 / 20259 PCT出版物日期1996年7月4日一种设备和蒸汽裂解方法包括将固体颗粒控制注入传输线换热器（3）。颗粒通过注射管线注入，编号在1和8之间，紧邻冲击扩散器（6）的上游，冲击扩散器（6）包括设置在管线两侧的固体表面，用于将裂化气体转移到交换器; 该冲击扩散器位于交换器的入口锥体（2）中，通过多个通道可透过气体，并且从传输线观察至少70％的不透明度。

38. 发明授权

US5186815A Method of decoking an installation for steam cracking hydrocarbons, and a corresponding steam-cracking installation 失效
标题翻译：破坏蒸汽破碎油的安装方法及相应的蒸汽破碎装置
公开(公告)号：US5186815A
公开(公告)日：1993-02-16
申请号：US623730
申请日：1990-12-12
申请人： Eric Lenglet
发明人： Eric Lenglet
IPC分类号： C10G9/16 , F28G1/12
CPC分类号： C10G9/16 , F28G1/12 , Y10S585/95
摘要： A method of decoking the inside walls of a hydrocarbon steam-cracking installation by means of solid particles of very small size, which particles are injected into the hydrocarbon feedstock flowing through tubes (12) of the steam-cracking furnace (10) and through indirect quench means (16). A cyclone (28) at the outlet from said indirect-quench means serving to separate the solid particles from the gaseous products and enabling the solid particles to be recycled through the installation after being mixed with a liquid or a gas and after their pressure has been raised. The invention also relates to a steam-cracking installation enabling the method to be performed.
摘要翻译： PCT No.PCT / FR90 / 00272 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 / 12851 PCT出版物日期：1990年11月1日。一种利用非常小尺寸的固体颗粒对烃蒸汽裂解装置的内壁进行脱焦的方法，该颗粒被注入流过蒸汽裂化管（12）的烃原料中炉（10）和间接淬火装置（16）。来自所述间接骤冷装置的出口处的旋风分离器（28）用于将固体颗粒与气态产物分离，并使固体颗粒在与液体或气体混合之后并且在它们的压力已经被上调。本发明还涉及能够执行该方法的蒸汽裂解装置。

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