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    Process for dehydrating and fractionating a low-pressure natural gas
    1.
    发明授权
    Process for dehydrating and fractionating a low-pressure natural gas 失效
    低压天然气脱水和分馏的方法

    公开(公告)号：US06767388B2

    公开(公告)日：2004-07-27

    申请号：US10108860

    申请日：2002-03-29

    申请人： Fabrice Lecomte ,  Béatrice Fischer ,  Jean-Charles Viltard

    发明人： Fabrice Lecomte ,  Béatrice Fischer ,  Jean-Charles Viltard

    IPC分类号： B01D5314

    CPC分类号： C10L3/102 ,  B01D53/002 ,  B01D53/263 ,  C10L3/10 ,  F25J3/0209 ,  F25J3/0233 ,  F25J3/0242 ,  F25J2200/80 ,  F25J2205/02 ,  F25J2205/50 ,  F25J2220/66 ,  F25J2270/04

    摘要： Process for dehydrating/fractionating a low-pressure wet natural gas containing “heavy” constituents and “light” constituents includes a stage a) in which at least a fraction of the wet gas at temperature T0 is contacted with an aqueous liquid phase L'1 containing methanol, the gas carrying along substantially all of the methanol contained in phase L'1. In a stage b), the gas from stage (a) is cooled to a temperature T1 lower than temperature T0, producing a gas phase G1 at equilibrium with a hydrocarbon-containing liquid phase L1 containing C3+ and an aqueous liquid phase L'1 containing methanol. In stage c), phase L'1 is sent to stage (a), and in stage d), said phase G1 is fractionated by distillation carried out by continuous thermal exchange with a cooling fluid, so as to extract the “light” constituents (gas phase G2) and the “heavy” constituents (condensed phase L2).

    摘要翻译： 含有“重”成分和“轻”成分的低压湿天然气的脱水/分馏方法包括阶段a），其中在温度T0的至少一部分湿气与水相L 1相接触 含有甲醇的气体，该气体基本上包含在L'1相中所包含的所有甲醇。 在阶段b）中，来自阶段（a）的气体被冷却到比温度T0低的温度T1，产生与含有C3 +的含烃液相L1和含水液相L平衡的气相G1 '1含甲醇。 在阶段c）中，将阶段L'1送入阶段（a），在阶段d）中，通过与冷却液连续热交换进行蒸馏对所述相G1进行分馏，从而提取“轻”成分 （气相G2）和“重”成分（冷凝相L2）。

    Process for the treatment of a hydrocarbon feedstock
    3.
    发明授权
    Process for the treatment of a hydrocarbon feedstock 有权
    用于处理烃原料的方法

    公开(公告)号：US07452458B2

    公开(公告)日：2008-11-18

    申请号：US11194592

    申请日：2005-08-02

    申请人： Eric Sanchez ,  Béatrice Fischer

    发明人： Eric Sanchez ,  Béatrice Fischer

    IPC分类号： C10G5/04 ,  C10G5/00 ,  C10G5/06

    CPC分类号： C10G49/22 ,  C10G35/04

    摘要： Process for treatment of a hydrocarbon feedstock that comprises a hydrocarbon-containing liquid phase and hydrogen, in which the feedstock is separated under a pressure P1 into a liquid L1 and a gas G1, that is compressed and brought into contact with a portion of L1 under a pressure P2>2×P1 to recover a liquid L2 and a hydrogen-rich gas G2; L2 is fractionated to obtain a stabilized liquid L4a that is free of LPG and lighter products, a liquid stream of LPG, and a gas stream G4 that is recycled, and in which one of gas streams: recompressed G1 and G4 is in counter-current contact with an unstabilized liquid AL that is obtained from or extracted from L1 or L2, whereby this unstabilized liquid is supercooled by at least 10° C. below its bubble point at pressure P2.

    摘要翻译： 用于处理包含含烃液相和氢气的烃原料的方法，其中原料在压力P 1下分离成液体L 1和气体G 1，其被压缩并与部分 的L 1在压力P 2> 2×P 1下回收液体L 2和富氢气体G 2; 将L 2分馏以获得不含LPG和较轻产物，液化石油气流和循环的气流G 4的稳定液体L 4 a，其中气流中的一种：再压缩G 1和G 4与从L 1或L 2获得或从L 1或L 2中提取的未稳定液体AL逆流接触，由此将该不稳定液体在压力P 2下低于其起泡点至少10℃。

    Process and device for separation of at least one acid gas that is contained in a gas mixture
    4.
    发明授权
    Process and device for separation of at least one acid gas that is contained in a gas mixture 失效
    用于分离包含在气体混合物中的至少一种酸性气体的方法和装置

    公开(公告)号：US06442969B1

    公开(公告)日：2002-09-03

    申请号：US09846784

    申请日：2001-05-02

    申请人： Alexandre Rojey ,  Béatrice Fischer ,  Ari Minkkinen

    发明人： Alexandre Rojey ,  Béatrice Fischer ,  Ari Minkkinen

    IPC分类号： F25J300

    CPC分类号： F25J3/0266 ,  B01D53/002 ,  C01B32/50 ,  F25J3/0209 ,  F25J3/0219 ,  F25J3/0223 ,  F25J3/0233 ,  F25J2200/80 ,  F25J2210/12 ,  F25J2220/66 ,  F25J2245/02 ,  Y02C10/12 ,  Y02P20/152 ,  Y10S62/929

    摘要： For the separation of acid, carbon dioxide and/or hydrogen sulfide from a gaseous mixture comprising at least one lighter gas, e.g. methane, the gaseous mixture (1) is precooled at least once during a heat exchange operation E2; the resultant precooled gas mixture, flowing upwardly is cooled and rectified simultaneously in an approximately vertical heat exchange zone (ER) forming a downwardly-flowing countercurrent liquid reflux; the resultant rectified gaseous fraction (8) depleted in acid gases and enriched in light gas is collected at the top of the vertical exchange zone; and (d) a liquid fraction (4) enriched in acid gas components is collected at the bottom of the exchange zone. The collected liquid fraction (4) can be expanded and evaporated to provide cooling. The system has particular application for the treatment of natural gas or in petroleum refining or recovery operations.

    摘要翻译： 用于从包含至少一种较轻气体的气体混合物中分离酸，二氧化碳和/或硫化氢， 甲烷，气体混合物（1）在热交换操作E2期间被预冷至少一次; 向上流动的所得预冷气体混合物在大致垂直的热交换区（ER）中同时冷却并整流，形成向下流动的逆流液体回流; 在垂直交换区的顶部收集所产生的贫酸气体和富含轻质气体的精馏气态馏分（8） 和（d）在交换区的底部收集富含酸性气体成分的液体馏分（4）。 收集的液体馏分（4）可以膨胀和蒸发以提供冷却。 该系统特别适用于天然气处理或炼油或回收操作。

    High-pressure gas fractionating process and system
    5.
    发明授权
    High-pressure gas fractionating process and system 失效
    高压气体分馏过程及系统

    公开(公告)号：US06318119B1

    公开(公告)日：2001-11-20

    申请号：US09471084

    申请日：1999-12-23

    申请人： Béatrice Fischer ,  Jean-Charles Viltard

    发明人： Béatrice Fischer ,  Jean-Charles Viltard

    IPC分类号： F25J300

    CPC分类号： C10L3/10 ,  F25J3/0209 ,  F25J3/0233 ,  F25J3/0242 ,  F25J2200/70 ,  F25J2200/80 ,  F25J2205/04 ,  F25J2205/50 ,  F25J2220/66 ,  F25J2220/68 ,  F25J2240/02 ,  F25J2245/02 ,  F25J2270/02 ,  F25J2270/04

    摘要： Process allowing to fractionate a gas, wherein: the gas is cooled from T0 to a temperature T1, at least part of gas phase G1 is sent to an expansion stage (X1) in order to obtain a mixed phase M2 at a temperature T2 and at a pressure P2, mixed phase M2 is sent to a heat exchange stage where it serves as a cooling agent, and after which it is heated, liquid phase L1 is sent to an expansion stage, the heated mixed phase and the expanded liquid phase are sent to a separation stage so as to obtain a gas phase and a liquid phase, and the gas phase is fractionated by distillation performed by means of continuous heat exchange with mixed phase M2, and the light constituents are extracted as gas and the heavy constituents as condensates, the fractionation stage being performed after the stage of expansion of mixed phase M2.

    摘要翻译： 允许分馏气体的方法，其中：将气体从T0冷却至温度T1，将气相G1的至少一部分送至膨胀级（X1），以获得温度为T2的混合相M2 将压力P2，混合相M2送入作为冷却剂的热交换阶段，然后加热，将液相L1送入膨胀阶段，将加热的混合相和膨胀液相送入 进入分离阶段以获得气相和液相，并且通过与混合相M2的连续热交换进行蒸馏分馏气相，并且将轻组分作为气体提取，重组分作为缩合物提取， 分馏阶段在混合相M2的膨胀阶段之后进行。

    Use of a two-phase turbine in a hydrotreatment process
    6.
    发明授权
    Use of a two-phase turbine in a hydrotreatment process 失效
    在加氢处理过程中使用两相涡轮机

    公开(公告)号：US07384541B2

    公开(公告)日：2008-06-10

    申请号：US10909430

    申请日：2004-08-03

    申请人： Yves Charron ,  Béatrice Fischer

    发明人： Yves Charron ,  Béatrice Fischer

    IPC分类号： C10G45/00 ,  F02C6/00

    CPC分类号： F04D31/00 ,  C10G45/00 ,  C10G47/00

    摘要： After passing into reaction section R, the hydrocarbon feedstock C mixed with hydrogen H is expanded in device D. The expansion is brought about by a single-phase turbine until a gas volume ratio of 5% is reached, then expansion is brought about in a two-phase turbine of the rotodynamic type.

    摘要翻译： 在进入反应段R后，与氢H混合的烃原料C在装置D中膨胀。膨胀由单相涡轮机引起，直到达到5％的气体体积比，然后在 旋转动力型的两相涡轮机。

    Process for dehydrating and stripping a wet natural gas
    7.
    发明授权
    Process for dehydrating and stripping a wet natural gas 失效
    湿天然气脱水和汽提的方法

    公开(公告)号：US06793714B2

    公开(公告)日：2004-09-21

    申请号：US10108494

    申请日：2002-03-29

    申请人： Fabrice Lecomte ,  Béatrice Fischer ,  Jean-Charles Viltard

    发明人： Fabrice Lecomte ,  Béatrice Fischer ,  Jean-Charles Viltard

    IPC分类号： B01D5314

    CPC分类号： B01D53/263 ,  B01D53/002 ,  C10L3/10

    摘要： In a process for dehydration/fractionation of a wet natural gas containing heavy constituents and light constituents, In the presence of methanol, aqueous liquid phases are combined and the resultant combined aqueous liquid phase contacted with the first part of the gas to be scrubbed, which carries along the major part of the methanol, which allows to collect practically pure water. Before this step, all or part of one or both of the aqueous liquid phases and/or all or part of the aqueous liquid phase from a washing zone is sent to a distillation stage where practically pure methanol is collected at the top and a methanol-depleted aqueous liquid phase is collected at the bottom prior to being sent back to the first stage or used for the washing stage.

    摘要翻译： 在含有重组分和轻组分的湿天然气的脱水/分馏过程中，在甲醇的存在下，将水相液相合并，并将所得的混合水相液体与待洗涤的气体的第一部分接触， 携带甲醇的主要部分，允许收集几乎纯净的水。 在该步骤之前，将来自洗涤区的水性液相和/或全部或部分水性液相的全部或部分全部或部分送入蒸馏阶段，其中在顶部收集几乎纯的甲醇， 在回送到第一阶段或用于洗涤阶段之前，在底部收集贫化的含水液相。

    Alternated process for olefin metathesis
    8.
    发明授权
    Alternated process for olefin metathesis 有权
    烯烃复分解的交替过程

    公开(公告)号：US06281402B1

    公开(公告)日：2001-08-28

    申请号：US09208585

    申请日：1998-12-10

    申请人： Vincent Coupard ,  François Hugues ,  Dominique Commereuc ,  Béatrice Fischer ,  Pierre Boucot ,  Alain Forestiere

    发明人： Vincent Coupard ,  François Hugues ,  Dominique Commereuc ,  Béatrice Fischer ,  Pierre Boucot ,  Alain Forestiere

    IPC分类号： C07C604

    CPC分类号： C07C6/04 ,  C07C2521/04 ,  C07C2523/36 ,  Y02P20/584

    摘要： The present invention relates to a process for continuous metathesis or disproportionation of olefins, comprising at least 2 phases, a reaction phase a) carried out in a zone comprising at least one reactor containing at least one fixed bed of catalyst and a regeneration phase b) carried out in a zone comprising at least one reactor containing at least one fixed bed of catalyst, characterized in that at least one reactor passes from one phase to the other in alternation. In FIG. 1, the feed containing olefins traverses reactor R1 in riser mode. The feed to be treated containing olefins is introduced into reactor R1 via line 1a. In this reactor, the olefins contained in the feed undergo metathesis or disproportionation, then the effluent leaves the circuit via line 11. Simultaneously, reactor R2 is placed in catalyst regeneration phase, the different regeneration gases are introduced into reactor R2 via line 2b and leave this reactor via line 2c. Passage from the operating phase of a reactor to the catalyst regeneration phase thereof is carried out as follows: the reactor for which the catalyst is to be regenerated is isolated from the remainder of the apparatus, the hydrocarbons contained in the reactor are evacuated, then the reactor is purged. Said reactor is then connected to a regeneration loop and undergoes regeneration of its catalyst, and at the end of the regeneration phase, the reactor and the regeneration loop are purged.

    摘要翻译： 本发明涉及一种烯烃的连续复分解或歧化方法，包括至少两相，在包含至少一个含有至少一个催化剂固定床和再生阶段的反应器的区域中进行的反应相a） 在包含至少一个包含至少一个催化剂固定床的反应器的区域中进行，其特征在于至少一个反应器交替地从一个相转移到另一个相。 在图 如图1所示，含有烯烃的进料以提升管方式穿过反应器R1。 待处理含烯烃的进料通过管线1a引入反应器R1。 在该反应器中，进料中所含的烯烃经过复分解或歧化，然后流出物通过管线11离开回路。同时，将反应器R2置于催化剂再生阶段，不同的再生气体通过管线2b引入反应器R2，并留下 该反应器经由管线2c。 从反应器的操作阶段到催化剂再生阶段的通过如下进行：将待再生催化剂的反应器与装置的其余部分分离，将反应器中包含的烃抽真空，然后 反应器被清除。 然后将所述反应器连接到再生回路并经历其催化剂的再生，并且在再生阶段结束时，将反应器和再生回路清除。