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    Reverse emulsion aliphatic alkylation process with catalyst-olefin premixing
    3.
    发明授权
    Reverse emulsion aliphatic alkylation process with catalyst-olefin premixing 失效
    反相乳液脂肪族烷基化方法与催化烯烃预混合

    公开(公告)号：US5969206A

    公开(公告)日：1999-10-19

    申请号：US785041

    申请日：1997-01-17

    申请人： Jacques Alagy ,  Jean-Francois Joly ,  Eric Benazzi ,  Jean-Charles Viltard ,  Luis Borges ,  Alain Forestiere

    发明人： Jacques Alagy ,  Jean-Francois Joly ,  Eric Benazzi ,  Jean-Charles Viltard ,  Luis Borges ,  Alain Forestiere

    IPC分类号： C07C2/76 ,  C07B61/00 ,  C07C2/62 ,  C07C9/16 ,  C07C9/21 ,  C10G35/06 ,  C10G35/10 ,  C07C2/58

    CPC分类号： C07C2/62 ,  C07C2527/054 ,  C07C2527/1206

    摘要： The invention concerns a process for the alkylation of at least one isoaffin selected from the group formed by isobutane and isopentane by at least one olefin containing 2 to 6 carbon atoms per molecule in the presence of a liquid acid catalyst, the process comprising mixing a feed comprising the olefin to be converted with an effluent comprising a major portion of isoparaffin in a first mixing zone, and forming an emulsion of said catalyst in a hydrocarbon effluent comprising a major portion of isoparaffin in an emulsifying zone, said effluent constituting the continuous phase of the emulsion thus formed, then mixing a major portion of the emulsion of acid in hydrocarbon effluent with a major portion of the diluted feed comprising the olefin in a second mixing zone, followed by carrying out the majority of the reaction in a reaction zone which is supplied by the major portion of said mixture.

    摘要翻译： 本发明涉及在液体酸催化剂存在下，通过至少一种含有2-6个碳原子的烯烃在异丁烷和异戊烷中形成的至少一种异构烷烃的烷基化方法，该方法包括混合进料 包括在第一混合区域中用包含大部分异链烷烃的流出物转化的烯烃，并且在包含乳化区中的主要部分异链烷烃的烃流出液中形成所述催化剂的乳液，所述流出物构成连续相 由此形成的乳液，然后将大部分酸性乳液在烃流出物中与主要部分的稀释进料在第二混合区中混合，然后在反应区中进行大部分反应，反应区是 由所述混合物的主要部分供应。

    Paraffin isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones
    4.
    发明授权
    Paraffin isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones 有权
    链烷烃异构化方法包括具有至少两个与至少两个异构化区相关联的排出水平的分馏

    公开(公告)号：US5994607A

    公开(公告)日：1999-11-30

    申请号：US129127

    申请日：1998-08-04

    申请人： Jean-Francois Joly ,  Pierre Boucot ,  Michel Thery ,  Olivler Clause ,  Jean-Charles Viltard

    发明人： Jean-Francois Joly ,  Pierre Boucot ,  Michel Thery ,  Olivler Clause ,  Jean-Charles Viltard

    IPC分类号： C10G59/06 ,  C10G65/16 ,  C07C5/13 ,  C07C1/00

    CPC分类号： C10G65/16 ,  C10G59/06

    摘要： The invention concerns a process for isomerising a feed containing essentially hydrocarbons, preferably paraffins containing principally 4 to 8, preferably princiapply to 6 and more principally 5 and/or 6 carbon atoms per molecule, comprising a fractionation zone and at least two isomersation reaction zones, said process comprising carrying out the following steps:(1) sending the feed to a fractionation zone;(2) drawing off at least a portion of the liquid circulating in said zone, via at least two draw-off levels; and(3) sending the major portion of the liquid drawn off in step (2) to at least two isomerisation zones, each isomerisation zone being associated with a draw-off level.

    摘要翻译： 本发明涉及一种异构化基本上烃的方法，所述进料基本上包含烃，优选主要含有4至8，优选原则上至6，更主要为每个分子5和/或6个碳原子的链烷烃，其包含分馏区和至少两个异构化反应区， 所述方法包括进行以下步骤：（1）将进料送至分馏区; （2）经由至少两个抽出水平抽出在所述区域中循环的液体的至少一部分; 和（3）将在步骤（2）中抽出的液体的主要部分送至至少两个异构化区，每个异构化区与排出水平相关联。

    Process for converting hydrocarbons by treatment in a distillation zone comprising extracting a hydrocarbon cut as a side stream, associated with a reaction zone, and its use for hydrogenating benzene
    5.
    发明授权
    Process for converting hydrocarbons by treatment in a distillation zone comprising extracting a hydrocarbon cut as a side stream, associated with a reaction zone, and its use for hydrogenating benzene 有权
    通过在蒸馏区中处理来转化烃的方法，包括萃取与反应区相关的侧流的烃馏分及其用于苯化氢的用途

    公开(公告)号：US06365791B1

    公开(公告)日：2002-04-02

    申请号：US09376054

    申请日：1999-08-17

    申请人： Jean-Louis Ambrosino ,  Jean-Charles Viltard ,  Blaise Didillon

    发明人： Jean-Louis Ambrosino ,  Jean-Charles Viltard ,  Blaise Didillon

    IPC分类号： C07C500

    CPC分类号： C10G45/44

    摘要： The invention provides a process for converting hydrocarbons in which said feed is treated in a distillation zone associated with a reaction zone, the feed for the reaction zone being drawn off at the height of at least one draw-off level, the effluent from the reaction zone being re-introduced into the distillation zone at the height of a re-introduction level, said process being characterized in that a liquid effluent is also withdrawn from the distillation zone at the height of a withdrawal level, said liquid effluent being treated in a gas-liquid side separation zone (splitter), the gaseous effluent being re-introduced into the distillation zone and the liquid effluent being recovered as an intermediate cut. This process can be used to reduce the benzene content of a hydrocarbon cut and to recover a naphtha cut.

    摘要翻译： 本发明提供了一种转化烃的方法，其中所述进料在与反应区相关的蒸馏区中处理，反应区的进料在至少一个排出水平的高度被排出，反应的流出物 区域在再引入水平的高度被重新引入蒸馏区，所述方法的特征在于，在排出水平的高度处还从蒸馏区抽出液体流出物，所述液体流出物在 气 - 液侧分离区（分流器），气态流出物被重新引入蒸馏区，液体流出物作为中间馏分被回收。 该方法可用于降低烃馏分的苯含量并回收石脑油馏分。

    Process for the production of high purity isobutene combining reactive distillation with hydroisomerization, distillation and skeletal isomerization
    7.
    发明授权
    Process for the production of high purity isobutene combining reactive distillation with hydroisomerization, distillation and skeletal isomerization 失效
    生产高纯度异丁烯的方法，其结合反应蒸馏与加氢异构化，蒸馏和骨架异构化

    公开(公告)号：US5969203A

    公开(公告)日：1999-10-19

    申请号：US996122

    申请日：1997-12-22

    申请人： Michel Dorbon ,  Jean-Alain Chodorge ,  Jean Cosyns ,  Jean-Charles Viltard ,  Blaise Didillon

    发明人： Michel Dorbon ,  Jean-Alain Chodorge ,  Jean Cosyns ,  Jean-Charles Viltard ,  Blaise Didillon

    IPC分类号： B01J23/40 ,  B01J23/755 ,  C07B61/00 ,  C07C5/27 ,  C07C7/04 ,  C07C11/09 ,  C07C1/00 ,  C07C5/22

    CPC分类号： C07C11/09 ,  C07C5/2791 ,  C07C2523/42 ,  C07C2523/44 ,  C07C2523/46 ,  C07C2523/755 ,  Y02P20/127 ,  Y10S203/06

    摘要： The invention relates to a process for producing high purity isobutene from a hydrocarbon cut essentially comprising olefinic hydrocarbons containing 4 carbon atoms per molecule including isobutene, also butene-1 and butene-2 compounds in a ratio which substantially corresponds to the thermodynamic equilibrium. The process comprises passing the cut into a distillation zone (3) associated with a hydroisomerization reaction zone, the bottom product of the distillation zone comprising butene-2 compoundw being passed into a second distillation zone (4), preferably an extractive distillation zone, to obtain a first effluent comprising butene-2 compounds as its major portion and a second effluent comprising normal-butane as its major portion, the major portion of the first effluent being passed into a skeletal isomerization zone (2) where the linear butenes are at least partially isomerized to isobutene, at least part of the principal effluent from the skeletal isomerization zone being recycled upstream of the reactive distillation zone (1).

    摘要翻译： 本发明涉及从基本上包含每分子含有4个碳原子的烯烃的烃馏分生产高纯度异丁烯的方法，包括异丁烯，以及基本上对应于热力学平衡的比例的丁烯-1和丁烯-2化合物。 该方法包括将切片通入与加氢异构化反应区相关联的蒸馏区（3），蒸馏区的底部产物包含丁烯-2化合物，其进入第二蒸馏区（4），优选萃取蒸馏区，至 获得包含丁烯-2化合物作为其主要部分的第一流出物和包含正丁烷作为其主要部分的第二流出物，第一流出物的主要部分进入骨架异构化区（2），其中线性丁烯至少为 部分异构化为异丁烯，来自骨架异构化区的至少部分主要流出物被循环在反应蒸馏区（1）的上游。

    Isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones
    8.
    发明授权
    Isomerization process comprising fractionation having at least two draw-off levels associated with at least two isomerization zones 失效
    异构化方法包括具有至少两个与至少两个异构化区相关联的排出水平的分馏

    公开(公告)号：US5831140A

    公开(公告)日：1998-11-03

    申请号：US795703

    申请日：1997-02-04

    申请人： Jean-Fran.cedilla.ois Joly ,  Pierre Boucot ,  Michel Thery ,  Olivier Clause ,  Jean-Charles Viltard

    发明人： Jean-Fran.cedilla.ois Joly ,  Pierre Boucot ,  Michel Thery ,  Olivier Clause ,  Jean-Charles Viltard

    IPC分类号： C10G45/58 ,  C10G49/00 ,  C10G59/06 ,  C07C5/13 ,  C07C1/00

    CPC分类号： C10G59/06 ,  C10G49/002 ,  C10G2400/02

    摘要： The invention concerns a process for isomerizing a feed containing essentially hydrocarbons, preferably paraffins containing principally 4 to 8, preferably principally 4 to 6 and more preferably principally 5 and/or 6 carbon atoms per molecule, comprising a fractionation zone and at least two isomerization reaction zones, said process comprising carrying out the following steps: (1) sending the feed to a fractionation zone; (2) drawing off at least a portion of the liquid circulating in said zone, via at least two draw-off levels; (3) sending the major portion of the liquid drawn off in step (2) to at least two isomerization zones, each isomerization zone being associated with a draw-off level; (4) sending the major portion of the effluents from step (3) to the fractionation zone, substantially adjacent to the draw-off levels; (5) recovering an effluent from the fractionation zone.

    摘要翻译： 本发明涉及使基本上含有烃的原料异构化的方法，优选主要含有分子量为4至8，优选主要为4至6，更优选主要为5和/或6个碳原子的链烷烃，其包含分馏区和至少两个异构化反应 所述方法包括进行以下步骤：（1）将进料送至分馏区; （2）经由至少两个抽出水平抽出在所述区域中循环的液体的至少一部分; （3）将在步骤（2）中抽出的液体的主要部分送至至少两个异构化区，每个异构化区域与排出水平相关联; （4）将大部分流出物从步骤（3）送至分馏区，基本上与排出水平相邻; （5）从分馏区回收流出物。

    Process and device for the simultaneous transfer of material and heat
    9.
    发明授权
    Process and device for the simultaneous transfer of material and heat 失效
    用于同时传送材料和热量的工艺和装置

    公开(公告)号：US5316628A

    公开(公告)日：1994-05-31

    申请号：US656169

    申请日：1991-04-24

    申请人： Jean-Claude Collin ,  Joseph Larue ,  Alexandre Rojey ,  Jean-Charles Viltard

    发明人： Jean-Claude Collin ,  Joseph Larue ,  Alexandre Rojey ,  Jean-Charles Viltard

    IPC分类号： F28F3/06 ,  B01J19/32 ,  C07C9/04 ,  C07C29/86 ,  C07C31/04 ,  F28D9/00 ,  F28D21/00 ,  B01D3/28

    CPC分类号： F28D21/0015 ,  B01J19/32 ,  B01J2219/32206 ,  B01J2219/3221 ,  B01J2219/32213 ,  B01J2219/32227 ,  B01J2219/32237 ,  B01J2219/32255 ,  B01J2219/32408 ,  Y10S159/901

    摘要： A process for simultaneously exchanging material and for exchanging heat, material change being effected between a gas phase and at least one liquid phase by contact and passage in opposite directions of the gas phase and of the at least one liquid phase and heat exchange being effected between a compartment (I) and another compartment (II). In compartment (I) a plurality of spacer plates defining material exchange passages are arranged and the material exchange is effected by causing the at least one liquid phase to flow over a substantially vertical or inclined wall of a corrugated spacer plate having perforations and by causing at least a fraction of the gas phase to traverse simultaneously said perforations in a substantially ascending direction to contact said at least one liquid phase. The heat exchange is effected by circulating a heat exchange fluid in the compartment (II) which has a common wall with the compartment (I).

    摘要翻译： PCT No.PCT / FR90 / 00490 Sec。 371日期1991年4月24日 102（e）日期1991年4月24日PCT Filed 1990年6月29日PCT公布。 出版物WO91 / 00141 日本1991年1月10日。一种用于同时交换材料并交换热的方法，通过气相和至少一种液体的相反方向的接触和通过在气相和至少一个液相之间进行材料变化 在隔室（I）和另一隔间（II）之间进行相位和热交换。 在隔室（I）中，布置了限定材料交换通道的多个间隔板，并且通过使至少一个液相流过具有穿孔的波纹隔板的基本垂直或倾斜的壁并且通过使 至少一部分气相以大体上升的方向同时穿过所述穿孔以接触所述至少一个液相。 热交换是通过在隔室（II）中循环热交换流体来实现的，该隔室（II）与隔室（I）具有共同的壁。