专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

21. 发明授权

US06281402B1 Alternated process for olefin metathesis 有权
标题翻译：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。

22. 发明授权

US5853551A Process for the separation of alpha-olefins by distillation of an effluent comprising ethylene and 1-butene 失效
标题翻译：通过蒸馏出包含乙烯和1-丁烯的流出物来分离α-烯烃的方法
公开(公告)号：US5853551A
公开(公告)日：1998-12-29
申请号：US720384
申请日：1996-07-23
申请人： Pierre Boucot , Jean-Alain Chodorge , Alain Forestiere , Yves Glaize , Fran.cedilla.ois Hughes
发明人： Pierre Boucot , Jean-Alain Chodorge , Alain Forestiere , Yves Glaize , Fran.cedilla.ois Hughes
IPC分类号： C07C7/05 , B01D3/34 , B01D3/14
CPC分类号： C07C7/05
摘要： The invention concerns a process for the separation of a mixture comprising ethylene, 1-butene, alpha-olefins containing at least 6 carbon atoms per molecule and possibly heavier hydrocarbon products, the ethylene content of the mixture being in the range 30% to 70% by weight, in which separation is effected in a distillation zone to obtain an overhead fraction comprising the major portion of the ethylene present in the mixture and between 0% and 100% by weight of the 1-butene present in the mixture, the process being characterized in that the zone is also supplied with supplemental 1-butene in an amount in the range 1 to 40 times the quantity (by weight) of 1-butene present in the mixture. In a preferred implementation of the process of the invention, the mixture originates form a homogenous liquid phase ethylene oligomerisation zone.
摘要翻译：本发明涉及一种分离包含乙烯，1-丁烯，每分子含有至少6个碳原子的α-烯烃和可能较重烃产物的混合物的混合物的方法，该混合物的乙烯含量在30％至70％的范围内，，其中在蒸馏区中进行分离以获得包含混合物中存在的乙烯的主要部分和0重量％至100重量％的混合物中存在的1-丁烯的塔顶馏分，该方法为其特征在于，该区域还提供了在混合物中存在的1-丁烯的量（重量）的1至40倍的量的补充的1-丁烯。在本发明方法的优选实施方案中，混合物起始形成均相液相乙烯齐聚区。

23. 发明授权

US5755841A Process and device for manufacturing synthesis gas and application 失效
标题翻译：制造合成气和应用的工艺和装置
公开(公告)号：US5755841A
公开(公告)日：1998-05-26
申请号：US631909
申请日：1996-04-12
申请人： Pierre Boucot , Paul Gateau , Jerome Weill
发明人： Pierre Boucot , Paul Gateau , Jerome Weill
IPC分类号： B01J8/04 , C01B3/02 , C01B3/36 , C01B3/38 , C07C1/04 , C07C29/151 , C07C31/04 , C01B3/24
CPC分类号： B01J8/0484 , B01J8/0453 , B01J8/0492 , C01B3/025 , C01B3/36 , C01B3/382 , C07C1/041 , C07C29/1516 , B01J2208/025 , C01B2203/142 , C01B2203/82
摘要： The present invention relates to a process and to a device for manufacturing synthetic gas. The reactor in accordance with the invention comprises within a single housing: a non catalytic combustion chamber (1) comprising at least one fuel injection element (2) and at least one oxidizer injection element (3) so as to achieve a partial combustion in said chamber referred to as "sufficient residence time chamber", and at least one catalytic bed (4) into which the gases coming from combustion chamber (1) run, and further comprising at least one additional oxidizer injection element (6) and at least one fuel injection element (7). The reactor and the process in accordance with the invention may be applied to any chemical manufacturing utilizing synthetic gas.
摘要翻译：本发明涉及一种制造合成气体的方法和装置。根据本发明的反应器包括在单个壳体内：非催化燃烧室（1），其包括至少一个燃料喷射元件（2）和至少一个氧化剂注入元件（3），以便在所述称为“足够的停留时间室”的室，以及至少一个催化床（4），来自燃烧室（1）的气体流入其中，并且还包括至少一个附加的氧化剂注入元件（6）和至少一个燃料喷射元件（7）。根据本发明的反应器和方法可以应用于利用合成气体的任何化学制造。

24. 发明授权

US5705138A Process for manufacturing synthetic gas and associated utilization 失效
标题翻译：制造合成气及相关利用的工艺
公开(公告)号：US5705138A
公开(公告)日：1998-01-06
申请号：US679725
申请日：1996-07-12
申请人： Jean-Herve Le Gal , Michel Maute , Pierre Boucot
发明人： Jean-Herve Le Gal , Michel Maute , Pierre Boucot
IPC分类号： B01J8/08 , C01B3/36 , C01B3/38 , C01B3/40 , C10K1/00
CPC分类号： B01J8/085 , C01B3/36 , C01B3/363 , C01B3/382 , C01B3/40 , C01B2203/1041 , C01B2203/1052 , C01B2203/1064 , C01B2203/1082 , C01B2203/1094
摘要： The invention relates to the manufacturing of synthetic gas according to which the following stages are performed within a single housing: partial combustion in a non catalytic combustion chamber, contacting of the combustion gases with a catalytic element, complementary injection of oxidizer in the catalytic bed. According to the invention, maximum direct contact is provided between the combustion gases and a surface of the catalytic bed so as to reduce the formation of soots.
摘要翻译：本发明涉及合成气体的制造，其中在单个壳体内执行以下阶段：在非催化燃烧室中部分燃烧，使燃烧气体与催化元件接触，在催化床中互补注入氧化剂。根据本发明，在燃烧气体和催化床的表面之间提供最大的直接接触，以便减少烟灰的形成。

25. 发明授权

US08206489B2 Method of deacidizing a gas with a fractional regeneration absorbent solution with control of the water content of the solution 有权
$Method of deacidizing a gas with a fractional regeneration absorbent solution with control of the water content of the solution$
标题翻译：使用分级再生吸收剂溶液使气体脱酸的方法，控制溶液的含水量
公开(公告)号：US08206489B2
公开(公告)日：2012-06-26
申请号：US12158346
申请日：2006-12-19
申请人： Renaud Cadours , Pierre-Louis Carrette , Pierre Boucot
发明人： Renaud Cadours , Pierre-Louis Carrette , Pierre Boucot
IPC分类号： B01D53/14
CPC分类号： B01D53/1468 , B01D53/1425 , B01D53/1493
摘要： The present invention relates to a method of deacidizing a gaseous effluent, wherein the following stages are carried out: a) contacting the gaseous effluent with an absorbent solution so as to obtain a gaseous effluent depleted in acid compounds and an absorbent solution laden with acid compounds, the absorbent solution being selected for its property to form two separable phases when it absorbs an amount of acid compounds, b) separating the absorbent solution laden with acid compounds into two fractions: a first absorbent solution fraction depleted in acid compounds and a second absorbent solution fraction enriched in acid compounds, c) regenerating the second fraction so as to release part of the acid compounds, d) mixing a predetermined amount of water with the first absorbent solution fraction obtained in stage b) or with the regenerated absorbent solution fraction obtained in stage c), then e) recycling the first absorbent solution fraction and the regenerated absorbent solution as the absorbent solution.
摘要翻译：本发明涉及一种使气态流出物脱酸的方法，其中进行以下阶段：a）使气态流出物与吸收剂溶液接触，以获得贫酸化合物和含有酸化合物的吸收剂溶液当吸收剂溶液吸收一定量的酸化合物时，选择吸收剂溶液以形成两个可分离相，b）将装载有酸化合物的吸收剂溶液分离成两部分：将酸性化合物和第二吸收剂富含酸化合物的溶液馏分，c）再生第二馏分以释放部分酸化合物，d）将预定量的水与步骤b）中获得的第一吸收剂溶液馏分或所得到的再生吸收剂溶液馏分在阶段c）中，e）回收第一吸收剂溶液级分和再生的吸收剂溶液作为吸收剂溶液。

26. 发明申请

US20100011958A1 Method of Deacidizing a Gas with a Fractional Regeneration Absorbent Solution with Control of the Water Content of the Solution 有权
标题翻译：用控制溶液含水量的分数再生吸收剂对气体进行脱酸的方法
公开(公告)号：US20100011958A1
公开(公告)日：2010-01-21
申请号：US12158346
申请日：2006-12-19
申请人： Renaud Cadours , Pierre-Louis Carrette , Pierre Boucot
发明人： Renaud Cadours , Pierre-Louis Carrette , Pierre Boucot
IPC分类号： B01D53/14
CPC分类号： B01D53/1468 , B01D53/1425 , B01D53/1493
摘要： The present invention relates to a method of deacidizing a gaseous effluent, wherein the following stages are carried out: a) contacting the gaseous effluent with an absorbent solution so as to obtain a gaseous effluent depleted in acid compounds and an absorbent solution laden with acid compounds, the absorbent solution being selected for its property to form two separable phases when it absorbs an amount of acid compounds, b) separating the absorbent solution laden with acid compounds into two fractions: a first absorbent solution fraction depleted in acid compounds and a second absorbent solution fraction enriched in acid compounds, c) regenerating the second fraction so as to release part of the acid compounds, d) mixing a predetermined amount of water with the first absorbent solution fraction obtained in stage b) or with the regenerated absorbent solution fraction obtained in stage c), then e) recycling the first absorbent solution fraction and the regenerated absorbent solution as the absorbent solution.
摘要翻译：本发明涉及一种使气态流出物脱酸的方法，其中进行以下阶段：a）使气态流出物与吸收剂溶液接触，以获得贫酸化合物和含有酸化合物的吸收剂溶液当吸收剂溶液吸收一定量的酸化合物时，选择吸收剂溶液以形成两个可分离相，b）将装载有酸化合物的吸收剂溶液分离成两部分：将酸性化合物和第二吸收剂富含酸化合物的溶液馏分，c）再生第二馏分以释放部分酸化合物，d）将预定量的水与步骤b）中获得的第一吸收剂溶液馏分或所得到的再生吸收剂溶液馏分在阶段c）中，e）回收第一吸收剂溶液级分和再生的吸收剂溶液作为吸收剂溶液。

27. 发明申请

US20070286783A1 METHOD OF DEACIDIZING A GASEOUS EFFLUENT WITH EXTRACTION OF THE PRODUCTS TO BE REGENERATED 审中-公开
标题翻译：用于提取待再生产品的气体洗涤液的方法
公开(公告)号：US20070286783A1
公开(公告)日：2007-12-13
申请号：US11745512
申请日：2007-05-08
申请人： Pierre-Louis Carrette , Bruno Delfort , Renaud Cadours , Arnaud Baudot , Elsa Jolimaitre , Lionel Magna , Pierre Boucot
发明人： Pierre-Louis Carrette , Bruno Delfort , Renaud Cadours , Arnaud Baudot , Elsa Jolimaitre , Lionel Magna , Pierre Boucot
IPC分类号： B01D53/48 , B01D53/50 , B01D53/62
CPC分类号： B01D53/1425 , B01D53/1456 , B01D53/1493
摘要： The present invention relates to a method of deacidizing a gaseous effluent comprising at least one of the acid compounds as follows: H2S, mercaptans, CO2, COS, SO2, CS2, wherein the following stages are carried out: a) contacting the acid compounds contained in said effluent with reactive compounds forming a liquid, so as to obtain a gaseous effluent depleted in acid compounds and a first liquid fraction comprising products formed by reaction of the reactive compounds with acid compounds, and reactive compounds that did not react with acid compounds, b) contacting said products contained in the first liquid fraction with extraction compounds forming a second liquid fraction so as to obtain a product-depleted first liquid fraction and a product-enriched second liquid fraction, c) recycling to stage a) the first liquid fraction obtained in stage b), said first liquid fraction obtained making up at least part of said liquid, d) regenerating the second liquid fraction obtained in stage b) so as to release acid compounds in gaseous form and to obtain a mixture of reactive compounds and of extraction compounds.
摘要翻译：本发明涉及一种使包含至少一种酸化合物的气态流出物脱酸的方法如下：H 2 S，硫醇，CO 2，COS，SO，其中进行以下阶段：a）使包含在所述流出物中的酸化合物与形成液体的反应性化合物接触，以获得气态流出物贫酸化合物和包含通过反应性化合物与酸化合物反应形成的产物的第一液体馏分，以及不与酸性化合物反应的反应性化合物，b）使包含在第一液体馏分中的所述产物与形成第二液体的萃取化合物接触液体馏分，以获得产物贫化的第一液体馏分和产物富集的第二液体馏分，c）循环至a）在步骤b）中获得的第一液体馏分，所获得的所述第一液体馏分构成至少部分说液体，d）再生在步骤b）中获得的第二液体馏分，以释放气态的酸化合物，并获得反应性化合物和萃取化合物的混合物。

28. 发明授权

US6121505A Process for synthesizing and purifying olefins comprising dehydrogenating a paraffin 失效
标题翻译：合成和纯化烯烃的方法，包括使石蜡脱氢
公开(公告)号：US6121505A
公开(公告)日：2000-09-19
申请号：US103524
申请日：1998-06-24
申请人： Charles Bronner , Reynald Bonneau , Pierre Boucot , Alain Forestiere
发明人： Charles Bronner , Reynald Bonneau , Pierre Boucot , Alain Forestiere
IPC分类号： C07C5/333 , C07C11/02 , C07C5/327 , C07C1/00 , C07C5/373 , C07C7/00 , C10G9/00
CPC分类号： C07C11/02 , C07C5/333
摘要： The present invention relates to a process for the production of olefins from a hydrocarbon cut, comprising a step for separating at least one paraffin contained in the hydrocarbon cut, a step for dehydrogenating the paraffin and a step for purifying the hydrogen produced during dehydrogenation, at least a part of that hydrogen being recycled to the dehydrogenation step. The invention is of particular application to the preparation of olefins containing 3 to 5 carbon atoms per molecule from a C.sub.3 to C.sub.5 hydrocarbon cut containing at least one paraffin.
摘要翻译：本发明涉及一种从烃切割生产烯烃的方法，包括分离烃馏分中所含的至少一种石蜡的步骤，用于使石蜡脱氢的步骤和用于纯化在脱氢过程中产生的氢气的步骤将该氢的至少一部分再循环至脱氢步骤。本发明特别适用于从含有至少一种链烷烃的C 3 -C 5烃馏分制备每分子含3至5个碳原子的烯烃。

29. 发明授权

US5733514A Process and device for manufacturing synthesis gas and application 失效
标题翻译：制造合成气和应用的工艺和装置
公开(公告)号：US5733514A
公开(公告)日：1998-03-31
申请号：US782496
申请日：1997-01-10
申请人： Pierre Boucot , Paul Gateau , Michel Maute , Philippe Courty , Jerome Weill
发明人： Pierre Boucot , Paul Gateau , Michel Maute , Philippe Courty , Jerome Weill
IPC分类号： B01J8/02 , B01J8/04 , B01J23/00 , B01J23/78 , C01B3/36 , C01B3/38 , C01B3/24
CPC分类号： B01J23/002 , B01J23/005 , B01J23/78 , B01J8/02 , B01J8/0278 , B01J8/0403 , C01B3/36 , C01B3/382 , B01J2208/00495 , B01J2208/0053 , B01J2219/182 , Y02P20/52
摘要： The present invention relates to a process and a device for manufacturing synthesis gas. The reactor according to the invention comprises within a single housing: A non catalytic combustion chamber (1) comprising at least one device (2) for injecting a fuel and at least one device (3) for injecting an oxidizer so as to achieve a partial combustion in said chamber, and at least one catalytic bed (4) which the gases coming from combustion chamber (1) run into, and also comprising at least one device (6) for injecting an additional oxidizer. The reactor and the process according to the invention may be applied to any chemical manufacturing utilizing synthesis gas, such as the manufacturing of ammonia, urea, methanol, higher hydrocarbons, etc.
摘要翻译：本发明涉及一种制造合成气的方法和装置。根据本发明的反应器包括在单个壳体内：非催化燃烧室（1），其包括用于喷射燃料的至少一个装置（2）和用于注入氧化剂的至少一个装置（3），以实现部分所述室中的燃烧和来自燃烧室（1）的气体的至少一个催化床（4）进入，并且还包括用于注入另外的氧化剂的至少一个装置（6）。根据本发明的反应器和方法可以应用于利用合成气的任何化学制造，例如氨，尿素，甲醇，高级烃等的制造。

30. 发明授权

US5632787A Process and device for manufacturing synthesis gas and application 失效
标题翻译：制造合成气和应用的工艺和装置
公开(公告)号：US5632787A
公开(公告)日：1997-05-27
申请号：US382587
申请日：1995-02-02
申请人： Pierre Boucot , Paul Gateau , Michel Maute , Philippe Courty , Jerome Weill
发明人： Pierre Boucot , Paul Gateau , Michel Maute , Philippe Courty , Jerome Weill
IPC分类号： B01J8/02 , B01J8/04 , B01J23/00 , B01J23/78 , C01B3/36 , C01B3/38 , C01B3/24
CPC分类号： B01J23/002 , B01J23/005 , B01J23/78 , B01J8/02 , B01J8/0278 , B01J8/0403 , C01B3/36 , C01B3/382 , B01J2208/00495 , B01J2208/0053 , B01J2219/182 , Y02P20/52
摘要： A reactor for manufacturing synthesis gas as a single housing, equipped with a non-catalytic combustion chamber having at least one device for injecting a fuel and at least one device for injecting an oxidizer so as to achieve partial combustion in said chamber, and at least one catalytic bed from which the gases coming from the combustion chamber discharge into, said catalytic bed being equipped with at least one device for injecting an additional oxidizer. A process for operating the reactor may be applied to any chemical manufacturing utilizing synthesis gas, such as the manufacturing of ammonia, urea, methanol, higher hydrocarbons, etc.
摘要翻译：一种用于制造合成气作为单个壳体的反应器，其装备有具有至少一个用于喷射燃料的装置的非催化燃烧室和至少一个用于注入氧化剂的装置，以便在所述室中实现部分燃烧，并且至少一个催化床，来自燃烧室的气体从该催化床排出，所述催化床配备有至少一个用于注入另外的氧化剂的装置。用于操作反应器的方法可以应用于使用合成气的任何化学制造，例如氨，尿素，甲醇，高级烃等的制造。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式