专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

31. 发明申请

US20100163458A1 METHOD OF CONVERTING EFFLUENTS OF RENEWABLE ORIGIN INTO FUEL OF EXCELLENT QUALITY BY USING A MOLYBDENUM-BASED CATALYST 有权
标题翻译：通过使用基于钼的催化剂将可再生原料转化为优质燃料的燃料的方法
公开(公告)号：US20100163458A1
公开(公告)日：2010-07-01
申请号：US12644710
申请日：2009-12-22
申请人： Antoine DAUDIN , Laurent Bournay , Thierry Chapus
发明人： Antoine DAUDIN , Laurent Bournay , Thierry Chapus
IPC分类号： C10G45/08 , B01J27/051 , B01J27/19 , B01J21/02 , B01J21/16
CPC分类号： B01J23/28 , B01J27/051 , B01J27/0515 , B01J27/19 , B01J29/74 , C10G3/44 , C10G3/48 , C10G3/50 , C10G3/54 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/4018 , C10G2400/04 , C10G2400/08 , Y02P30/20
摘要： The invention is concerned with a supported or unsupported catalyst comprising an active phase constituted by a sulfur-containing group VIB element, the group VIB element being molybdenum, and a hydrodeoxygenation process with a yield of hydrodeoxygenation product which is greater than or equal to 90% of charges from renewable sources using a catalyst according to the invention.
摘要翻译：本发明涉及负载或未负载的催化剂，其包含由含硫基团VIB元素，VIB族元素为钼构成的活性相和加氢脱氧方法，其加氢脱氧产物的产率大于或等于90％使用根据本发明的催化剂的可再生能源的电荷。

32. 发明授权

US09045701B2 Method of hydrotreating feeds from renewable sources with indirect heating 有权
标题翻译：从间接加热的可再生能源加氢处理饲料的方法
公开(公告)号：US09045701B2
公开(公告)日：2015-06-02
申请号：US12912214
申请日：2010-10-26
申请人： Wilfried Weiss , Laurent Bournay , Thierry Chapus
发明人： Wilfried Weiss , Laurent Bournay , Thierry Chapus
IPC分类号： C10G65/02 , C10G3/00 , C10G65/04
CPC分类号： C10G3/48 , C10G3/46 , C10G3/50 , C10G65/04 , C10G2300/1014 , C10G2300/1018 , C10G2300/4006 , C10G2300/4018 , C10G2300/4081 , C10G2400/04 , C10G2400/08 , Y02P30/20
摘要： The invention describes a method of treating feeds from renewable sources comprising: a hydrotreatment stage a) comprising at least two catalytic zones in which the entry stream comprising said feed mixed with at least a part of a hydrotreated liquid effluent from stage b) is introduced into the first catalytic zone at a temperature comprised between 150 and 260° C., and the effluent from the first catalytic zone is then introduced, mixed with at least a part of a hydrotreated liquid effluent from stage b) and preheated, into the following catalytic zone or zones at a temperature comprised between 260 and 320° C., a stage b) of separation of the effluent from the hydrotreatment stage a) permitting the separation of a gaseous effluent and of a hydrotreated liquid effluent of which at least a part is recycled upstream from each catalytic zone of stage a).
摘要翻译：本发明描述了一种处理来自可再生来源的饲料的方法，包括：加氢处理阶段a）包括至少两个催化区，其中将包含所述进料的进料与至少一部分来自阶段b）的加氢处理的液体流出物混合引入第一催化剂区域在150-260℃的温度下，然后引入来自第一催化区域的流出物，与来自步骤b）的加氢处理的液体流出物的至少一部分混合并预热到下面的催化剂区域或区域，温度为260至320℃，阶段b）将流出物与加氢处理阶段分离a）允许将气态流出物和至少部分为至少一部分的加氢处理液体流出物分离在阶段a）的每个催化区上游再循环。

33. 发明授权

US08962905B2 Process for the continuous hydrogenation of triglyceride containing raw materials using a nickel and molybdenum-based catalyst 有权
标题翻译：使用镍和钼基催化剂连续氢化含甘油三酯的原料的方法
公开(公告)号：US08962905B2
公开(公告)日：2015-02-24
申请号：US13226524
申请日：2011-09-07
申请人： Thierry Chapus , Nathalie Dupassieux , Antoine Daudin
发明人： Thierry Chapus , Nathalie Dupassieux , Antoine Daudin
IPC分类号： C10G3/00 , C10L1/08
CPC分类号： C10G3/60 , C10G3/46 , C10G3/50 , C10G3/54 , C10G2300/1014 , C10G2300/4018 , C10G2300/802 , C10G2400/04 , C10G2400/08 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要： Process for the continuous hydrogenation of triglyceride containing raw materials in a fixed bed reactor system having several catalyst beds arranged in series and comprising at least one hydrogenation catalyst comprising an active phase constituted by a nickel and molybdenum element. The raw material feed, hydrogen containing gas and diluting agent are passed together through the catalyst beds at hydrogenation conditions. The raw material feed stream as well as the stream of hydrogen containing gas are divided into an equal number of different partial streams. These are each passed to one catalyst bed in such a manner that the weight ratio of diluting agent to raw material feed is essentially the same at the entrance of all catalyst beds and does not exceed 4:1. The claimed process is preferably conducted at low temperatures and allows the utilization of existing units due to the low recycle ratio.
摘要翻译：在具有串联排列的几个催化剂床的固定床反应器系统中连续氢化含甘油三酯的原料的方法，并包含至少一种包含由镍和钼元素构成的活性相的氢化催化剂。原料进料，含氢气体和稀释剂在氢化条件下通过催化剂床一起通入。将原料进料流以及含氢气流分成相等数量的不同部分流。将它们分别传送到一个催化剂床，使得稀释剂与原料进料的重量比在所有催化剂床的入口处基本相同，不超过4:1。要求保护的方法优选在低温下进行，并且由于低回收比而允许使用现有的单元。

34. 发明授权

US08552235B2 Process for hydrodeoxygenation of feeds derived from renewable sources with limited decarboxylation conversion using a catalyst based on nickel and molybdenum 有权
标题翻译：使用基于镍和钼的催化剂进行有限脱羧转化的来自可再生能源的进料的加氢脱氧方法
公开(公告)号：US08552235B2
公开(公告)日：2013-10-08
申请号：US12715836
申请日：2010-03-02
申请人： Antoine Daudin , Laurent Bournay , Thierry Chapus
发明人： Antoine Daudin , Laurent Bournay , Thierry Chapus
IPC分类号： C07C1/00
CPC分类号： C11C3/123 , B01J21/04 , B01J23/883 , B01J29/74 , B01J37/28 , B01J2229/20 , B01J2229/42 , C10G3/46 , C10G3/50 , C10G3/54 , C10G3/56 , C10G45/62 , C10G45/64 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C11C3/00 , Y02E50/13 , Y02P30/10 , Y02P30/20
摘要： A process for hydrodeoxygenation of feeds derived from renewable sources with conversion by decarboxylation/decarbonylation limited to at most 10%, using a bulk or supported catalyst comprising an active phase constituted by at least one element from group VIB and at least one element from group VIII, said elements being in the sulphide form, and the atomic ratio of the metal (or metals) from group VIII to the metal (or metals) from group VIB being strictly more than 0 and less than 0.095, said process being carried out at a temperature in the range 120° C. to 450° C., at a pressure in the range 1 MPa to 10 MPa, at an hourly space velocity in the range 0.1 h−1 to 10 h−1, and in the presence of a total quantity of hydrogen mixed with the feed such that the hydrogen/feed ratio is in the range 50 to 3000 Nm3 of hydrogen/m3 of feed.
摘要翻译：通过脱羧/脱羰转化限制为至多10％的来自可再生来源的进料的加氢脱氧的方法，使用包含由至少一种来自VIB族元素和VIII族元素构成的活性相的本体或负载型催化剂所述元素为硫化物形式，并且来自VIB族的金属（或金属）与金属（或金属）的原子比严格大于0且小于0.095，所述方法在温度在120℃至450℃的范围内，在1MPa至10MPa的压力下，以0.1h-1至10h-1的小时空间速度，并且在与进料混合的氢气总量使得氢/进料比在50-3000Nm 3的氢/ m3进料的范围内。

35. 发明授权

US08546626B2 Method of converting effluents of renewable origin into fuel of excellent quality by using a molybdenum-based catalyst 有权
标题翻译：通过使用钼基催化剂将可再生原料的废水转化为优质燃料的方法
公开(公告)号：US08546626B2
公开(公告)日：2013-10-01
申请号：US12644710
申请日：2009-12-22
申请人： Antoine Daudin , Laurent Bournay , Thierry Chapus
发明人： Antoine Daudin , Laurent Bournay , Thierry Chapus
IPC分类号： C07C1/00
CPC分类号： B01J23/28 , B01J27/051 , B01J27/0515 , B01J27/19 , B01J29/74 , C10G3/44 , C10G3/48 , C10G3/50 , C10G3/54 , C10G2300/1014 , C10G2300/1018 , C10G2300/202 , C10G2300/4018 , C10G2400/04 , C10G2400/08 , Y02P30/20
摘要： The invention is concerned with a supported or unsupported catalyst comprising an active phase constituted by a sulfur-containing group VIB element, the group VIB element being molybdenum, and a hydrodeoxygenation process with a yield of hydrodeoxygenation product which is greater than or equal to 90% of charges from renewable sources using a catalyst according to the invention.
摘要翻译：本发明涉及负载或未负载的催化剂，其包含由含硫基团VIB元素，VIB族元素为钼构成的活性相和加氢脱氧方法，其加氢脱氧产物的产率大于或等于90％使用根据本发明的催化剂的可再生能源的电荷。

36. 发明授权

US08324439B2 Method of converting feedstocks from renewable sources to good-quality diesel fuel bases using a zeolite type catalyst 有权
标题翻译：使用沸石型催化剂将来自可再生资源的原料转化为优质柴油燃料基料的方法
公开(公告)号：US08324439B2
公开(公告)日：2012-12-04
申请号：US12489885
申请日：2009-06-23
申请人： Emmanuelle Guillon , Christophe Bouchy , Nathalie Dupassieux , Antoine Daudin , Thierry Chapus
发明人： Emmanuelle Guillon , Christophe Bouchy , Nathalie Dupassieux , Antoine Daudin , Thierry Chapus
IPC分类号： C07C1/00
CPC分类号： C10G3/50 , B01J23/883 , B01J29/74 , B01J29/78 , B01J37/20 , B01J37/28 , C10G3/46 , C10G3/54 , C10G45/02 , C10G45/08 , C10G45/64 , C10G65/043 , C10G2300/1014 , C10G2300/1018 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , Y02P30/20
摘要： A method of treating feedstocks from renewable sources in order to produce diesel fuel bases of excellent quality. The feedstocks used can be, for example, raw vegetable oils or such oils that have been previously subjected to a prerefining stage, animal fats, or mixtures of such feedstocks. The method includes fixed bed catalytic hydrotreatment, followed by fixed bed hydroisomerization with a catalyst based on monodimensional 10 MR zeolite and at least one metal from group VIII and/or VIB.
摘要翻译：一种从可再生能源处理原料以生产出优质柴油燃料基料的方法。所使用的原料可以是例如以前经受预精制阶段，动物脂肪或这些原料的混合物的生植物油或这种油。该方法包括固定床催化加氢处理，然后用基于单维10 MR沸石和至少一种VIII族和/或VIB金属的催化剂进行固定床加氢异构化。

37. 发明申请

US20100325943A1 PROCESS FOR EBULLATED BED HYDROCONVERSION OF FEEDS OF BIO-RENEWABLE ORIGIN FOR THE PRODUCTION OF FUEL BASES 有权
标题翻译：用于生产燃料基础的生物可再生原料进料的EBULLED BED HYDROCONVERSION
公开(公告)号：US20100325943A1
公开(公告)日：2010-12-30
申请号：US12282910
申请日：2008-07-18
申请人： Thierry Chapus , Alain Quignard , Nathalie Dupassieux , Antoine Daudin
发明人： Thierry Chapus , Alain Quignard , Nathalie Dupassieux , Antoine Daudin
IPC分类号： C10L1/19
CPC分类号： C10G49/04 , C10G3/46 , C10G3/48 , C10G3/50 , C10G3/56 , C10G49/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/301 , C10G2300/4018 , C10G2400/06 , C10G2400/08 , Y02P30/20
摘要： The invention concerns a process for hydrotreatment and/or hydroconversion of a feed of bio-renewable origin containing triglyceride and/or fatty acid structures and wherein the fatty chains contain in the range 8 to 25 carbon atoms, said process comprising the following steps: a) hydrotreatment and/or hydroconversion of said bio-renewable feed in an ebullated bed reactor in the presence of a granular catalyst comprising, on an amorphous support, at least one metal or compound of a metal having a hydrodehydrogenating function, to produce a first effluent; b) sending the effluent produced in step a) to a distillation zone from which a gaseous fraction and at least one distillate cut the end point of which is less than 400° C.
摘要翻译：本发明涉及含有甘油三酯和/或脂肪酸结构的生物可再生来源的进料的加氢处理和/或加氢转化的方法，其中所述脂肪链含有8至25个碳原子，所述方法包括以下步骤：）在颗粒催化剂存在下在沸腾床反应器中加氢处理和/或加氢转化所述生物可再生进料，所述颗粒催化剂在无定形载体上包含至少一种具有脱氢功能的金属的金属或化合物，以产生第一流出物 ; b）将步骤a）中产生的流出物送到蒸馏区，蒸馏区中气态馏分和至少一个馏分切断其终点小于400℃。

38. 发明申请

US20100292517A1 PRODUCTION OF VAPOUR-CRACKING LOADS WITH A HIGH YIELD OF THE RESULTING ETHYLENE, PROPYLENE AND POLYMERS BY HYDROPROCESSING OF VEGETABLE OILS 有权
标题翻译：通过植物油的水解生产具有高分子量乙烯，丙烯和聚合物的蒸气破碎负荷
公开(公告)号：US20100292517A1
公开(公告)日：2010-11-18
申请号：US12664132
申请日：2008-06-03
申请人： Quentin Debuisschert , Jean Cosyns , Thierry Chapus , Damien Hudebine
发明人： Quentin Debuisschert , Jean Cosyns , Thierry Chapus , Damien Hudebine
IPC分类号： C07C4/04
CPC分类号： C10G9/36 , C10G3/46 , C10G3/50 , C10G3/54 , C10G45/08 , C10G47/04 , C10G47/06 , C10G69/06 , C10G2300/1003 , C10G2300/1014 , C10G2300/1018 , C10G2300/1044 , C10G2300/1055 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/20 , C11C3/123 , C11C3/126 , Y02P30/20 , Y02P30/42
摘要： The invention describes a process for treatment of a feedstock that is obtained from a renewable source that comprises a hydrotreatment stage in the presence of at least one fixed-bed catalyst, whereby said catalyst comprises a hydro-dehydrogenating function and an amorphous substrate, at a temperature of between 50 and 450° C., at a pressure of between 1 MPa and 10 MPa, at an hourly volumetric flow rate of between 0.1 h−1 and 10 h−1, and in the presence of a total quantity of hydrogen that is mixed with the feedstock such that the hydrogen/feedstock ratio is between 50 and 1000 Nm3 of hydrogen/m3 of feedstock, followed by a separation from the hydrotreated effluent that is obtained from stage a) of hydrogen, gases, and at least one liquid hydrocarbon effluent that consists of at least 50% linear n-paraffins, and a steam-cracking of at least one portion of the liquid hydrocarbon effluent that is obtained from stage b).
摘要翻译：本发明描述了一种处理从可再生来源获得的原料的方法，该方法包括在至少一种固定床催化剂存在下的加氢处理阶段，由此所述催化剂包含加氢脱氢功能和非晶基质，温度为50-450℃，压力为1MPa至10MPa，小时体积流速为0.1h-1至10h-1，在总氢存在下，与原料混合使得氢/原料比为50至1000Nm 3的氢/ m3原料，然后与从氢气，气体和至少一种液体的a）段获得的加氢处理流出物分离由至少50％线性正链烷烃组成的碳氢化合物流出物，以及从阶段b）获得的液体烃流出物的至少一部分的蒸汽裂解。

39. 发明申请

US20100242349A1 PROCESS FOR THE CONTINUOUS HYDROGENATION OF TRIGLYCERIDE CONTAINING RAW MATERIALS 有权
标题翻译：用于连续加氢含有原料的TRIGLYCERIDE的方法
公开(公告)号：US20100242349A1
公开(公告)日：2010-09-30
申请号：US12717403
申请日：2010-03-04
申请人： Detlef Abe , Frank Eschenroder , David Laban , Hartmut Schutter , Laurent Bournay , Thierry Chapus , Nathalie Dupassieux
发明人： Detlef Abe , Frank Eschenroder , David Laban , Hartmut Schutter , Laurent Bournay , Thierry Chapus , Nathalie Dupassieux
IPC分类号： C10L1/19
CPC分类号： C10G3/54 , C10G3/46 , C10G3/50 , C10G3/60 , C10G45/58 , C10G45/72 , C10G2300/1011 , C10G2300/4018 , C10G2300/802 , Y02P30/20
摘要： Process for the continuous hydrogenation of triglyceride containing raw materials in a fixed bed reactor system having several catalyst beds arranged in series and comprising hydrogenation catalyst. The raw material feed, hydrogen containing gas and diluting agent are passed together through the catalyst beds at hydrogenation conditions. The raw material feed stream as well as the stream of hydrogen containing gas are divided into an equal number of different partial streams. These are each passed to one catalyst bed in such a manner that the weight ratio of diluting agent to raw material feed is essentially the same at the entrance of all catalyst beds and does not exceed 4:1. The claimed process is preferably conducted at low temperatures and allows the utilization of existing units due to the low recycle ratio. Further, a sufficient excess of hydrogen is used so that no valuable product is lost through decarb-reactions.
摘要翻译：在具有串联排列并包含氢化催化剂的几个催化剂床的固定床反应器系统中连续氢化含甘油三酯的原料的方法。原料进料，含氢气体和稀释剂在氢化条件下通过催化剂床一起通入。原料进料流以及含氢气流被分成等量的不同的部分流。将它们分别传送到一个催化剂床，使得稀释剂与原料进料的重量比在所有催化剂床的入口处基本相同，不超过4:1。要求保护的方法优选在低温下进行，并且由于低回收比而允许使用现有的单元。此外，使用足够过量的氢气，使得通过脱碳反应不会损失有价值的产物。

40. 发明授权

US06709639B1 Apparatus for purification of raw gasoline from catalytic cracking 有权
标题翻译：用于从催化裂化中净化原料汽油的装置
公开(公告)号：US06709639B1
公开(公告)日：2004-03-23
申请号：US09522179
申请日：2000-03-09
申请人： Thierry Chapus , Blaise Didillon , Christian Marcilly , Charles Cameron
发明人： Thierry Chapus , Blaise Didillon , Christian Marcilly , Charles Cameron
IPC分类号： B01J804
CPC分类号： C10G67/12 , C10G2400/02
摘要： An apparatus for the purification of catalytic cracking gasolines containing dienic and/or acetylenic impurities, and mercaptans, said apparatus comprising at least one selective hydrogenation reactor 3 containing at least one fixed catalyst bed, and having at least one line 1 for introducing a feed, at least one effluent outlet line, and a line supplying hydrogen to the reactor, said reactor being followed by at least one stabilization drum 4 connected to said effluent outlet line, the drum having at least one gas outlet line 5 and at least one stabilized effluent outlet line, and said effluent passing into at least one sweetening reactor 8 comprising at least one effluent inlet line 6 and at least one effluent outlet line, said reactor having close thereto at least one oxidizing agent supply line, said apparatus also comprising at least one drum 9 for degassing the effluent from the sweetening reactor 8, said drum 9 having at least one gas outlet line and at least one outlet line 11 for dedienized, stabilized and sweetened gasoline.
摘要翻译：一种用于纯化含有二烯和/或炔属杂质的催化裂解汽油的装置和硫醇，所述装置包括至少一个含有至少一个固定催化剂床的选择性氢化反应器3，并具有至少一条用于引入进料的管线1，至少一个流出物出口管线和向反应器供应氢气的管线，所述反应器后面连接有至少一个与所述流出物出口管线连接的稳定鼓筒，所述转鼓具有至少一个气体出口管线5和至少一个稳定的流出物出口管线，并且所述流出物进入至少一个甜味反应器8，其包含至少一个流出物入口管线6和至少一个流出物出口管线，所述反应器具有至少一个氧化剂供应管线，所述设备还包括至少一个鼓9用于对来自甜味反应器8的流出物进行脱气，所述滚筒9具有至少一个气体出口管线和至少一个出口管线11 用于发明，稳定和增甜的汽油。

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