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    Integral method for desulphurization of a hydrocarbon cracking or stream cracking effluent
    64.
    发明授权
    Integral method for desulphurization of a hydrocarbon cracking or stream cracking effluent 失效
    烃裂化或流裂解流出物脱硫的整体方法

    公开(公告)号：US07344635B2

    公开(公告)日：2008-03-18

    申请号：US10503807

    申请日：2003-01-22

    申请人： Patrick Briot ,  Pierre Boucot ,  Alain Forestiere ,  Nathalie Marchal-George ,  Florent Picard

    发明人： Patrick Briot ,  Pierre Boucot ,  Alain Forestiere ,  Nathalie Marchal-George ,  Florent Picard

    IPC分类号： C10G45/02

    CPC分类号： C10G69/123 ,  C10G29/205

    摘要： Process for desulfurization of an effluent for cracking or steam-cracking hydrocarbons, more particularly a gasoline for example for catalytic cracking that comprises the elimination of thiophenic compounds by alkylation of these compounds, followed by a distillation, a hydrocracking of said alkyl-thiophenic compounds, then a hydrodesulfurization of the effluent that is obtained from the hydrocracking zone. In a preferred embodiment, this process comprises a preliminary stage for separating the cracking or steam-cracking effluent into three fractions, and proposes sending to the alkylation stage only the intermediate fraction that is low in heavy basic nitrogen-containing compounds that are initially present in the effluents that are to be alkylated.

    摘要翻译： 用于裂化或蒸汽裂解烃的流出物的脱硫方法，更具体地，例如用于催化裂解的汽油，其包括通过这些化合物的烷基化除去噻吩化合物，然后蒸馏，所述烷基 - 噻吩化合物的加氢裂化， 然后从加氢裂化区获得的流出物的加氢脱硫。 在优选的实施方案中，该方法包括用于将裂化或蒸汽裂解流出物分离成三个馏分的初步阶段，并且建议仅向最初存在于重质碱性含氮化合物中的低碱性含氮化合物的中间馏分 待烷基化的废水。

    Process for the valorization of a charge of hydrocarbons and for reducing the vapor pressure of said charge
    67.
    发明授权
    Process for the valorization of a charge of hydrocarbons and for reducing the vapor pressure of said charge 有权
    用于使碳氢化合物加压并且用于降低所述电荷的蒸汽压力的方法

    公开(公告)号：US07161052B2

    公开(公告)日：2007-01-09

    申请号：US10653426

    申请日：2003-09-03

    申请人： Patrick Briot ,  Vincent Coupard ,  Alain Forestiere ,  Eric Llido ,  Thierry Poussereau

    发明人： Patrick Briot ,  Vincent Coupard ,  Alain Forestiere ,  Eric Llido ,  Thierry Poussereau

    IPC分类号： C07C2/68 ,  C07C2/04 ,  C07C2/00

    CPC分类号： C10G29/205 ,  C10G50/00

    摘要： A process is described for the valorization of a charge of hydrocarbons and for reducing the vapour pressure of said charge, comprising three steps: a step a) consisting of separating said charge of hydrocarbons into a fraction (O1) comprising essentially compounds containing 5 carbon atoms, including at least 2% by weight of pentenes, a step b) consisting of placing said fraction (O1) in contact with a cut of hydrocarbons (O2) at least partly comprising hydrocarbons having a number of carbon atoms between 6 and 10, including at least 2% by weight of olefins, and a step c) consisting of separating the effluents originating from step b) into a gasoline cut (α) the upper distillation point of which is less than 100° C. and a kerosene cut (β) having a distillation range between 100° C. and 300° C.

    摘要翻译： 描述了一种用于增加烃类和降低所述电荷的蒸气压的方法，包括三个步骤：步骤a）由将所述烃分离成基本上含有5个碳原子的化合物的馏分（O1）组成的步骤 ，包括至少2重量％的戊烯，步骤b）将所述馏分（O1）与至少部分包含6至10个碳原子的烃的馏分（O 2）接触，包括 至少2重量％的烯烃，以及步骤c），其通过将来自步骤b）的流出物分离成上馏分小于100℃的汽油馏分（α）和煤油切割（β ），其蒸馏范围为100℃至300℃。

    Alternated process for olefin metathesis
    69.
    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。

    Process for obtaining butene-1
    70.
    发明授权
    Process for obtaining butene-1 有权
    获得丁烯-1的方法

    公开(公告)号：US06242662B1

    公开(公告)日：2001-06-05

    申请号：US09229958

    申请日：1999-01-14

    申请人： Michel Dorbon ,  François Hugues ,  Jean-Charles Viltard ,  Blaise Didillon ,  Alain Forestiere

    发明人： Michel Dorbon ,  François Hugues ,  Jean-Charles Viltard ,  Blaise Didillon ,  Alain Forestiere

    IPC分类号： C07C525

    CPC分类号： C07C11/08 ,  C07C5/2556 ,  C07C7/04 ,  C07C2523/40 ,  C07C2523/755

    摘要： For obtaining butene-1 from butene-2, a charge containing at least one of the isomers of butene-2 is introduced into a distillation zone linked to a hydro-isomerization zone. Part of the effluent from the bottom of the distillation column is removed from the distillation zone, heated in a heat exchanger and passed into an external hydro-isomerization zone. The hydro-isomerization effluent is removed from the hydro-isomerization zone, cooled in a heat exchanger, and then reintroduced into the distillation zone. Effluent containing butene-1 is withdrawn from the top of the column of the distillation zone.

    摘要翻译： 为了从丁烯-2获得丁烯-1，将含有至少一种丁烯-2异构体的电荷引入连接到加氢异构化区的蒸馏区。 将蒸馏塔底部的一部分流出物从蒸馏区除去，在热交换器中加热并进入外部加氢异构化区。 将加氢异构化流出物从加氢异构化区域除去，在热交换器中冷却，然后再引入蒸馏区。 含有丁烯-1的流出物从蒸馏区的塔顶排出。