公开(公告)号：US07687050B2

公开(公告)日：2010-03-30

申请号：US11523741

申请日：2006-09-20

Applicant: Alexandre Rojey ,  Stephane Bertholin ,  Fabrice Giroudiere ,  Eric Lenglet

Inventor： Alexandre Rojey ,  Stephane Bertholin ,  Fabrice Giroudiere ,  Eric Lenglet

IPC: C01B3/24 ,  C01B3/00 ,  B01J8/06

CPC classification number: 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

Abstract: For producing synthesis gas, SG, from a hydrocarbon feed and optionally from recycled compounds, F, 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; 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; and the synthesis gas SG is produced by mixing SG1 and SG2.

Abstract translation: 为了从烃进料和任选地来自再循环的化合物F生产合成气，SG，补充有蒸汽的第一进料F1在多管反应器 - 交换器R中经历蒸汽重整，其包括多个反应管（38），其包含蒸汽 重整催化剂和含有所述管的壳，以产生第一合成气SG1; 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是第二进料F2的氧在0.5至12MPa的压力下的分段部分氧化流， 以产生第二合成气SG2; 并且通过混合SG1和SG2产生合成气SG。

公开(公告)号：US07560495B2

公开(公告)日：2009-07-14

申请号：US11483778

申请日：2006-07-11

Applicant: Jean-Marc Schweitzer ,  Eric Lenglet ,  Franck Gaviot-Blanc

Inventor： Jean-Marc Schweitzer ,  Eric Lenglet ,  Franck Gaviot-Blanc

IPC: C07C27/00

CPC classification number: C10G2/342 ,  B01J8/228 ,  B01J2208/00256 ,  B01J2208/003 ,  B01J2208/00539 ,  B01J2208/00548 ,  B01J2219/00247

Abstract: To facilitate operation of a facility for chemical conversion of a feed that comprises a reactor (2) containing a slurry constituted by at least one suspension of at least one solid in a liquid, a gas supply, and a circuit that is external of the reactor, for continuous movement of a slurry stream, wherein the external circuit withdraws slurry from the reactor from at least one point (A) and re-introduces at least a portion of the slurry at at least one other point (B), the facility is further provided with means for stopping circulation of the slurry in the circuit; means for pressurized introduction of at least one fluid for draining the slurry contained in the circuit; and means for circulating the slurry in the external circuit under conditions such that the Reynolds number is more than 2500.

Abstract translation: 为了便于进行化学转化的设备的操作，该设备包括含有由至少一种固体在液体中的至少一种悬浮液构成的浆料的反应器（2），气体供应源和在反应器外部的回路 ，用于浆料流的连续运动，其中所述外部回路从至少一个点（A）从所述反应器中抽出浆料，并且在至少一个其他点（B）再次引入所述浆料的至少一部分，所述设备是 还设置有用于阻止浆料在回路中循环的装置; 用于加压引入至少一种用于排出包含在电路中的浆料的流体的装置; 以及用于在雷诺数超过2500的条件下使浆料循环在外部回路中的装置。

公开(公告)号：US20070014703A1

公开(公告)日：2007-01-18

申请号：US11483778

申请日：2006-07-11

Applicant: Jean-Mare Schweitzer ,  Eric Lenglet ,  Franck Gaviot-Blanc

Inventor： Jean-Mare Schweitzer ,  Eric Lenglet ,  Franck Gaviot-Blanc

IPC: B01J8/18 ,  F27B15/08

CPC classification number: C10G2/342 ,  B01J8/228 ,  B01J2208/00256 ,  B01J2208/003 ,  B01J2208/00539 ,  B01J2208/00548 ,  B01J2219/00247

Abstract: To facilitate operation of a facility for chemical conversion of a feed that comprises a reactor (2) containing a slurry constituted by at least one suspension of at least one solid in a liquid, a gas supply, and a circuit that is external of the reactor, for continuous movement of a slurry stream, wherein the external circuit withdraws slurry from the reactor from at least one point (A) and re-introduces at least a portion of the slurry at at least one other point (B), the facility is further provided with means for stopping circulation of the slurry in the circuit; means for pressurized introduction of at least one fluid for draining the slurry contained in the circuit; and means for circulating the slurry in the external circuit under conditions such that the Reynolds number is more than 2500.

Abstract translation: 为了便于进行化学转化的设备的操作，该设备包括含有由至少一种固体在液体中的至少一种悬浮液构成的浆料的反应器（2），气体供应源和在反应器外部的回路 ，用于浆料流的连续运动，其中所述外部回路从至少一个点（A）从所述反应器中抽出浆料，并且在至少一个其他点（B）再次引入所述浆料的至少一部分，所述设备是 还设置有用于阻止浆料在回路中循环的装置; 用于加压引入至少一种用于排出包含在电路中的浆料的流体的装置; 以及用于在雷诺数超过2500的条件下使浆料循环在外部回路中的装置。

公开(公告)号：US06919048B2

公开(公告)日：2005-07-19

申请号：US10084493

申请日：2002-02-28

Applicant: Frédéric Hoffmann ,  Eric Lenglet ,  Philippe Mege

Inventor： Frédéric Hoffmann ,  Eric Lenglet ,  Philippe Mege

IPC: B01J8/06 ,  B01J8/00 ,  B01J8/04 ,  B01J8/12 ,  C07B61/00 ,  C07C5/333 ,  C07C11/02 ,  B01J8/08

CPC classification number: B01J8/085 ,  B01J8/003 ,  B01J8/004 ,  B01J8/0426 ,  B01J8/0496 ,  B01J8/125 ,  B01J2208/00168 ,  B01J2219/185 ,  B01J2219/1943

Abstract: An elongate reaction vessel and process includes at least two stages in the vertical direction in which an endothermic or exothermic catalytic reaction is carried out and comprises: a catalytic reaction zone (12a, 12b) per stage (6, 7); introducing (2) a reaction fluid to a stage adapted for transverse motion of the fluid across the whole vertical extent of the reaction zone; introducing and extracting the catalyst; a heat exchanger (5a) for reaction fluids located inside the vessel between two successive reaction zones; means (6) for transporting reaction fluids from one stage to another preferably connected to the exchanger of the stage under consideration and to the inlet for reaction fluids of the subsequent stage; and means for recovering reaction fluids downstream of the last stage. The temperature variation in each zone and the temperature level are respectively adjusted by the thickness of each zone and by heat exchange.

Abstract translation: 细长的反应容器和方法包括沿垂直方向的至少两个阶段，其中进行吸热或放热的催化反应，并包括：每个阶段（6,7）的催化反应区（12a，12b）; 将反应流体引入（2）适于在反应区的整个垂直范围内流体横向运动的阶段; 引入和提取催化剂; 位于两个连续反应区之间的反应流体的热交换器（5a）; 用于将反应流体从一个阶段转移到另一个阶段的装置（6），优选地连接到所考虑的阶段的交换器和后续阶段的反应流体的入口; 以及用于在最后阶段下游回收反应流体的装置。 每个区域的温度变化和温度水平分别通过每个区域的厚度和通过热交换来调整。

公开(公告)号：US06488839B1

公开(公告)日：2002-12-03

申请号：US09568050

申请日：2000-05-10

Applicant: Eric Lenglet ,  Christian Busson ,  Luc Nougier

Inventor： Eric Lenglet ,  Christian Busson ,  Luc Nougier

IPC: C10G936

CPC classification number: C07C4/04 ,  C10G2400/20 ,  Y10S585/925

Abstract: A steam-cracking process with a very high degree of severity of a feedstock that comprises at least 20% by weight of hydrocarbons of the group that is formed by ethane and propane in which the feedstock that is diluted with water vapor is circulated in the radiation zone of a furnace, in at least one pipe with a length L≧14 m and a hydraulic diameter that is greater than or equal to 34 mm in the end portion of the pipe at least, is described under the following conditions of dwell time &tgr; and furnace output temperature COT: 120 ms≦&tgr;≦2800 ms and 858° C.≦COT≦1025° C. to obtain a conversion of at least 77% of ethane of the feedstock if the feedstock contains ethane and/or a conversion of at least 96% of the propane of the feedstock if the feedstock contains propane, and to maintain this conversion for a cycle time that is greater than or equal to about 8 days.

Abstract translation: 包含至少20重量％的由乙烷和丙烷形成的基团的烃的至少20重量％的原料严重程度的蒸汽裂解方法，其中用水蒸气稀释的原料在辐射中循环 至少一根长度为L> = 14m的管道，至少在管道端部大于或等于34mm的水力直径的炉的区域在以下停留时间条件下描述 tau和炉输出温度COT：120ms <= tau <= 2800ms和858℃<= COT <= 1025℃，以获得至少77％的原料乙烷的转化率，如果原料含有乙烷和 /或如果原料含有丙烷，则原料的丙烷的至少96％的转化率，并保持该转化率大于或等于约8天的循环时间。

公开(公告)号：US5820747A

公开(公告)日：1998-10-13

申请号：US836147

申请日：1997-06-25

Applicant: Eric Lenglet ,  Paul Broutin ,  Jean-Pierre Burzynski ,  Herve Cazor ,  Roland Huin

Inventor： Eric Lenglet ,  Paul Broutin ,  Jean-Pierre Burzynski ,  Herve Cazor ,  Roland Huin

IPC: C10G9/00 ,  C10G9/16 ,  C10G9/36 ,  B01J8/08 ,  C10G9/18

CPC classification number: C10G9/002 ,  C10G9/16

Abstract: A steam cracking process and facility is described which comprises injection of erosive powder to effect at least partial decoking of transfer line exchangers without interrupting the steam cracking stream. The powder, preferably injected just upstream of the transfer line exchangers (TLE) (4), is separated from the cracked gases in primary gas/solid separators (5), temporarily stored in receiving drums at a controlled temperature and evacuated to a common powder storage and/or treatment module by pneumatic transfer by means of a relatively low flow of uncondensable gas. The process and facility can be used to collect solid fragments generated by injection of chemical compounds which are catalysts for the gasification of coke by steam.

Abstract translation: PCT No.PCT / FR95 / 01718 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。 公开号WO96 / 20256 日期1996年7月4日描述了一种蒸汽裂解过程和设备，其包括喷射侵蚀性粉末以在不中断蒸汽裂解流的情况下至少部分地转移转移线交换器。 优选在输送管线交换器（TLE）（4）的上游注入的粉末与初级气体/固体分离器（5）中的裂化气体分离，在受控的温度下临时储存在接受鼓中并抽真空至普通粉末 储存和/或处理模块通过气流传递通过相对低的不可冷凝气体流动。 该方法和设备可用于收集通过注入化学化合物产生的固体碎片，化合物是通过蒸汽气化焦炭的催化剂。

公开(公告)号：US20100276334A1

公开(公告)日：2010-11-04

申请号：US12516505

申请日：2007-11-12

Applicant: Eric Lenglet ,  Patrick Chaumette

Inventor： Eric Lenglet ,  Patrick Chaumette

IPC: H01B3/22 ,  C10G65/02

CPC classification number: C10G45/58 ,  C10G2/00 ,  C10G2300/1022 ,  C10G2300/1025 ,  C10G2300/301 ,  C10G2300/304

Abstract: 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*.

Abstract translation: 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 *。

公开(公告)号：US20090308788A1

公开(公告)日：2009-12-17

申请号：US11912771

申请日：2006-03-24

Applicant: Eric Lenglet

Inventor： Eric Lenglet

IPC: C10G45/00 ,  C10C3/00 ,  C10G69/04

CPC classification number: C10G67/049 ,  C10G45/14 ,  C10G47/24 ,  C10G65/18

Abstract: A process for pre-refining a crude oil P is described in which P is fractionated into several fractions, some of which are typically hydrotreated, hydrocracked or hydroconverted, then said fractions are re-composed and at least three pre-refined oils Pa, Pb, Pc are produced, Pc being a residual asphaltenic oil and Pa and Pb being two non asphaltenic oils having different ratios R wherein: R=(0.9N+0.5VGO+)/(MD+0.1VGO+), in which: N=naphtha [30° C./170° C.]; MD=middle distillates: [170° C./260° C.] and VGO+=fraction boiling above 360° C.R translates as the relative potential of a non residual oil to be converted into gasoline with respect to middle distillates during its subsequent refining.

Abstract translation: 描述了一种用于预精炼原油P的方法，其中P被分馏成几个级分，其中一些通常被加氢处理，加氢裂化或加氢转化，然后所述级分重新组成，并且至少三种预精制油Pa，Pb ，Pc为残留沥青质油，Pa和Pb为不同比例R的两种非沥青油，其中：R =（0.9N + 0.5VGO +）/（MD + 0.1VGO +），其中：N =石脑油[ 30℃。 MD =中间馏分：[170℃/ 260℃]和VGO + =沸点高于360℃的馏分.R转化为在其后续期间相对于中间馏分转化为汽油的非残余油的相对电位 精制。

公开(公告)号：US20080011643A1

公开(公告)日：2008-01-17

申请号：US10591339

申请日：2005-02-15

Applicant: Eric Lenglet ,  Alexandre Rojey

Inventor： Eric Lenglet ,  Alexandre Rojey

IPC: C10G67/00 ,  C01B3/34 ,  C10G67/04 ,  E21B43/16 ,  C10G49/00

CPC classification number: C10G67/00

Abstract: Use, in a gas production region, of a purified field gas in which:a) said gas is converted into hydrogen;b) a conventional sulphur-containing transportable fluid crude P1 is supplied;c) P1 is treated without discharging carbon, comprisinga desulphurizing treatment step by hydrotreatment, hydroconversion or hydrocracking of a fraction boiling above 343° C., consuming hydrogen;a step for reducing the quantity of vacuum residue by segregation and/or conversion of a portion of said vacuum residue;so as to produce a pre-refined asphaltenes-free oil refinery feedstock PA, and a residual easily transportable liquid oil refinery feedstock;d) evacuating said prerefined oil PA to an oil port.

Abstract translation: 在气体生产区域中使用纯化的场气，其中：a）将所述气体转化为氢气; b）提供常规的含硫可运输流体原油P1; c）P1处理而不排出碳，其包括通过加氢处理，加氢转化或加氢裂化沸点高于343℃的馏分进行脱硫处理步骤，消耗氢气; 通过分离和/或转化所述减压渣油的一部分来减少真空残渣量的步骤; 以便生产预精制无沥青的炼油原料P A A和残留的容易运输的液体炼油原料; d）将所述预精炼油P A A A抽空到油口。

公开(公告)号：US20060216218A1

公开(公告)日：2006-09-28

申请号：US11442328

申请日：2006-05-30

Applicant: Eric Lenglet ,  Nicolas Boudet ,  Frederic Hoffmann

Inventor： Eric Lenglet ,  Nicolas Boudet ,  Frederic Hoffmann

IPC: B01J8/08

CPC classification number: B01J8/0496 ,  B01J8/0438 ,  B01J8/12

Abstract: A chemical conversion reactor contains a substantially vertical catalytic bed between an upper end and a lower end and comprises, in combination: close to its upper end, at least one means for introducing a solid catalyst, means for introducing and evacuating said feed allowing its flow in a substantially horizontal direction through the catalytic bed, means for heating said feed integrated into said reactor, said reactor comprising, close to its lower end, at least one means for extraction of the catalyst, which extraction is differentiated between an upstream portion and a downstream portion of said catalytic bed, with respect to the direction of flow of said feed.

Abstract translation: 化学转化反应器在上端和下端之间包含基本上垂直的催化床，其组合包括：靠近其上端的至少一个用于引入固体催化剂的装置，用于引入和排空所述进料允许其流动的装置 在通过催化床的基本上水平的方向上，用于加热集成到所述反应器中的所述进料的装置，所述反应器包括靠近其下端的至少一个用于萃取催化剂的装置，所述提取在上游部分和 所述催化床的下游部分相对于所述进料的流动方向。