专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明公开

EP3580310A1 PROCESS FOR THE PRODUCTION OF ISOPARAFFINIC FLUIDS WITH LOW AROMATICS CONTENT 审中-公开
公开(公告)号：EP3580310A1
公开(公告)日：2019-12-18
申请号：EP18703608.2
申请日：2018-02-13
申请人： Total Marketing Services
发明人： DUPUY, Carole , LE LANNIC DROMARD, Katell
IPC分类号： C10G45/32 , C10G50/00 , C07C2/02 , C07C5/13 , C10G45/44 , C10G45/02

2. 发明公开

EP2597077A2 Alternative paths to alcohols and hydrocarbons from biomass 审中-公开
标题翻译：替代Wege zur Herstellung von Alkoholen und Kohlenwasserstoffen aus Biomasse
公开(公告)号：EP2597077A2
公开(公告)日：2013-05-29
申请号：EP13150072.0
申请日：2009-12-02
申请人： The Texas A&M University System
发明人： The designation of the inventor has not yet been filed
IPC分类号： C07C1/24 , C07C1/32 , C07C2/02 , C07C29/149 , C07C31/08 , C07C67/04 , C07C69/14 , C12P7/40 , C10G3/00 , C10G50/00
CPC分类号： C12P7/40 , C07C1/24 , C07C2/02 , C07C29/149 , C07C67/04 , C10G3/00 , C10G50/00 , C10G2300/1011 , C10G2300/4081 , C10G2300/42 , C10G2400/20 , C10G2400/22 , Y02P30/20 , C07C31/08 , C07C69/14
摘要： A method of producing hydrocarbons from biomass by converting at least a portion of the biomass into a carboxylic acid, a ketone, or an ammonium carboxylate salt, reacting at least one of a portion of the carboxylic acid, a portion of the ketone, or a portion of the ammonium carboxylate salt in an oligomerization reactor as at least part of a process that produces an oligomerization product and separating hydrocarbons from the oligomerization product.
摘要翻译：将生物质的至少一部分转化为羧酸，酮或羧酸铵盐，从生物质生产烃的方法，使羧酸的一部分，酮的一部分或部分羧酸铵盐在低聚反应器中作为产生低聚产物并从低聚产物中分离烃的方法的至少一部分。

3. 发明公开

EP2447237A3 Alternative paths to alcohols and hydrocarbons from biomass 审中-公开
标题翻译：用于生产生物质醇类和烃类的替代路线
公开(公告)号：EP2447237A3
公开(公告)日：2012-06-27
申请号：EP12000124.3
申请日：2009-12-02
申请人： The Texas A&M University System
发明人： The designation of the inventor has not yet been filed
IPC分类号： C07C1/24 , C07C2/02 , C07C29/149 , C07C31/08 , C07C67/04 , C07C69/14 , C12P7/40
CPC分类号： C12P7/40 , C07C1/24 , C07C2/02 , C07C29/149 , C07C67/04 , C10G3/00 , C10G50/00 , C10G2300/1011 , C10G2300/4081 , C10G2300/42 , C10G2400/20 , C10G2400/22 , Y02P30/20 , C07C31/08 , C07C69/14
摘要： A method of producing alcohols, hydrocarbons, or both from biomass by converting biomass into a carboxylic acid, reacting the carboxylic acid with an olefin to produce an ester and hydrogenolyzing the ester to produce alcohol. A method of producing hydrocarbons from biomass by converting at least a portion of the biomass into a carboxylic acid, a ketone, or an ammonium carboxylate salt, reacting at least one of a portion of the carboxylic acid, a portion of the ketone, or a portion of the ammonium carboxylate salt in an oligomerization reactor as at least part of a process that produces an oligomerization product and separating hydrocarbons from the oligomerization product.

4. 发明授权

EP1513791B1 PROCESS AND APPARATUS FOR CATALYTIC DISTILLATIONS 有权
标题翻译：方法和装置催化蒸馏
公开(公告)号：EP1513791B1
公开(公告)日：2011-06-15
申请号：EP03733858.9
申请日：2003-04-16
申请人： Catalytic Distillation Technologies
发明人： GROTEN, Willibrord, A. , MARASCHINO, Mario, J.
IPC分类号： C07C41/00 , C07C2/02 , C07C2/56 , B01D3/34 , B01D3/00
CPC分类号： B01D3/141 , B01D3/009 , C07C2/06 , C07C2/66 , C07C5/03 , C07C5/10 , C07C5/23 , C07C5/2506 , C07C5/27 , C07C41/06 , C07C41/42 , C07C319/18 , Y02P20/127 , C07C43/046
摘要： A process for reacting a first component with itself or a second component to produce a third component in which a first material comprising a first component or said first component and a second component is fed to divided wall column having a catalytic distillation structure in at least one of the separate vertical sections of the divided wall column where concurrently: (1) a first component alone or with a second component is contacted with a catalytic distillation structure in a distillation reaction zone thereby catalytically reacting at least a portion of the first component with itself or with the second component to form a product and (2) a first mixture comprising the first component and the product or the first component, the second component and the product; and withdrawing the product from the distillation column reactor; while within the column concurrently with the catalytic reaction and fractionation a second mixture is fractionated, which contains the first component and the product or first and second components (if a second component is present) and the product in a parallel and separate distillation non reaction zone to fractionate the product and withdrawing the product from said distillation non reaction zone. For example, tertiary amyl methyl ether may be prepared by reacting methanol with isoamylene in a C5 stream utilizing a distillation column reactor wherein the distillation column reactor comprises one side of a divided wall column. On one side the product, tertiary amyl methyl ether, is separated from the unreacted methanol and C5's and on the other side the remaining isoamylenes are reacted with methanol and a separation of the tertiary amyl methyl ether and C5's from the methanol/C5 azeotrope is effected.

5. 发明公开

EP2265563A2 PROCESS FOR SYNTHETIC LUBRICANT PRODUCTION 有权转让
标题翻译：一种用于生产合成润滑脂
公开(公告)号：EP2265563A2
公开(公告)日：2010-12-29
申请号：EP09723220.1
申请日：2009-03-18
申请人： ExxonMobil Research and Engineering Company
发明人： PATIL, Abhimanyu, O. , YANG, Norman , WU, Margaret, M.
IPC分类号： C07C2/02
CPC分类号： C07C2/22 , C07C2/34 , C07C2527/126 , C07C2531/14 , C07C2531/22 , C08F210/14 , C10G50/02 , C10G2400/10 , C08F2500/17
摘要： A process for the preparation of oligomeric poly alpha-olefins includes oligomerizing low molecular weight PAO oligomer in the presence of a Lewis acid catalyst such as promoted aluminum trichloride or boron trifluoride under oligomerization conditions. The low molecular weight PAO oligomers used as a feed or feed component of the present process are the light olefinic by-product fractions including the dimers and light fractions from the metallocene-catalyzed PAO oligomerization process which are characterized by a molecular weight of 150 to 600 and a terminal olefin (vinylidene) content of at least 25%.

6. 发明公开

EP1915403A1 VERFAHREN ZUR POLYMERISATION ETHYLENISCH UNGESÄTTIGTER POLYISOBUTEN 审中-公开
标题翻译：烯属不饱和聚异丁烯的方法聚合
公开(公告)号：EP1915403A1
公开(公告)日：2008-04-30
申请号：EP06792800.2
申请日：2006-08-11
申请人： BASF SE
发明人： RATH, Hans Peter , WALTER, Hans-Michael , NUYKEN, Oskar , KUEHN, Fritz Elmar , ZHANG, Yanmei , YEONG, Hui Yee
IPC分类号： C08F10/10 , C07F1/08 , C07C2/02 , C07C2/08 , C08F4/10
CPC分类号： C07F5/027 , C08F10/10 , C08F210/10 , C08F4/10 , C08F212/08
摘要： The invention relates to a method for polymerising ethylenically unsaturated monomers, wherein ethylenically unsaturated monomers are polymerised in the presence of a solvent-stable transition metal complex having slightly co-ordinating anions as polymer catalysts. The invention also relates to specific solvent-stable transition metal complexes having slightly co-ordinating anions. The invention also relates to highly reactive copolymers which are made of monomers comprising isobutene and at least one vinylaromatic compound which can be obtained according to said inventive method.

7. 发明公开

EP1745006A4 METHODS OF 1,3-ENYNE PREPARATION USING COPPER (I) CATALYSTS 审中-公开
标题翻译： VERFAHREN ZUR HERSTELLUNG冯1,3-ENYNEN MITTELS KUPFER-（I）-KATALYSATOREN
公开(公告)号：EP1745006A4
公开(公告)日：2008-04-23
申请号：EP05780040
申请日：2005-04-27
申请人： UNIV MASSACHUSETTS
发明人： VENKATARAMAN DHANDAPANI , BATES CRAIG G , SEAJUENG PRANORM
IPC分类号： C07C69/73 , C07B37/04 , C07C2/02 , C07C2/86 , C07C67/04 , C07C67/10 , C07C67/343 , C07C205/56 , C07C319/20 , C07C323/62 , C07D213/55 , C07D333/16 , C07D333/24 , C12N9/00
CPC分类号： C07C205/56 , B01J31/1805 , B01J31/1815 , B01J31/183 , B01J31/2217 , B01J2231/4266 , B01J2531/16 , C07B37/04 , C07C2/861 , C07C67/343 , C07C201/12 , C07C253/30 , C07C319/20 , C07C2527/167 , C07C2531/24 , C07C2602/10 , C07D213/55 , C07D333/16 , C07D333/24 , C12N9/00 , C07C11/28 , C07C69/65 , C07C69/606 , C07C69/738 , C07C69/76 , C07C69/618 , C07C69/734 , C07C323/62 , C07C255/57
摘要： A copper(I) bi-dentate ligand complex-catalyzed procedure for synthesis of 1,3-enynes. The methods and/or systems of this invention afford a variety of enynes, tolerate a variety of sensitive functional groups, and can be employed without resort to expensive palladium reagents.
摘要翻译：铜（I）双齿配体配合物催化的1,3-烯炔合成方法。本发明的方法和/或系统提供各种烯炔，可耐受各种灵敏的官能团，并且可以在不使用昂贵的钯试剂的情况下使用。

8. 发明授权

EP1313560B1 CATALYST FOR AROMATIC C-O, C-N, and C-C BOND FORMATION 有权
标题翻译：催化剂的芳族C-O，C-N和C-C键形成
公开(公告)号：EP1313560B1
公开(公告)日：2007-12-19
申请号：EP01965857.4
申请日：2001-08-06
申请人： Yale University
发明人： HARTWIG, John, F. , SHELBY, Quinetta , KATAOKA, Noriyasu
IPC分类号： B01J31/00 , C07F17/02 , C07C2/02 , C07C43/02 , C07C43/20 , C07C209/00 , C07C211/00 , C07D307/02 , C07D307/87 , C07D311/00 , B01J31/22 , B01J31/24
CPC分类号： B01J31/2404 , B01J31/2295 , B01J2231/4205 , B01J2231/4277 , B01J2531/80 , B01J2531/824 , B01J2531/828 , B01J2531/842 , B01J2531/847 , C07C1/321 , C07C41/16 , C07C45/68 , C07C45/70 , C07C201/12 , C07C209/10 , C07C213/02 , C07C221/00 , C07C227/08 , C07C253/30 , C07C269/06 , C07D295/023 , C07D295/073 , C07D295/096 , C07D295/155 , C07F17/00 , C07C47/575 , C07C49/784 , C07C47/55 , C07C47/546 , C07C49/84 , C07C211/47 , C07C211/48 , C07C211/52 , C07C211/54 , C07C211/55 , C07C211/57 , C07C217/84 , C07C217/92 , C07C229/60 , C07C255/41 , C07C255/58 , C07C271/28 , C07C205/06 , C07C205/35 , C07C205/37 , C07C43/205 , C07C43/2055 , C07C43/225
摘要： The present invention is directed to a transition metal catalyst, comprising a Group 8 metal and a ligand having the structure (I), wherein R', R' and R'' are organic groups having 1-15 carbon atoms, n = 1-5, and m = 0-4. The present invention is also directed to a method of forming a compound having an aromatic or vinylic carbon-oxygen, carbon-nitrogen, or carbon-carbon bond using the above catalyst. The catalyst and the method of using the catalyst are advantageous in preparation of compounds under mild conditions of approximately room temperature and pressure.

9. 发明公开

EP1628937A4 METHOD TO TRANSPORT ENERGY 审中-公开
标题翻译：方法交通能源
公开(公告)号：EP1628937A4
公开(公告)日：2007-04-11
申请号：EP04705277
申请日：2004-01-26
申请人： DALTON ROBERT C
发明人： DALTON ROBERT C
IPC分类号： C07C1/00 , C07C2/00 , C07C2/02 , C07C2/76 , C07C11/02 , C07C27/26 , C10J1/00 , C10L3/00 , C10L3/02 , C10L3/10 , F17C20060101 , F28D15/00
CPC分类号： C10L3/10 , C10L3/00 , Y02P20/128
摘要： A method is used to increase the energy content of a pipeline and other vessels that are designed to carry natural gas under ambient conditions, in a compressed state or in a liquefied state. Methane and other gas are used as the feedstock. Methane from natural gas fields, coal beds or derived from hydrogen reacting with coal are primary energy sources for this method. Also, this method could provide an abundant source for hydrogen production. Energy from hydrogen is used for fuel cell applications that generate electricity and power motor vehicles. This method is capable to increase the energy capacity of current natural gas pipelines and other storage and transport vessels.

10. 发明公开

EP1739069A1 Procédé de préparation d'une coupe diesel par oligomérisation 有权转让
标题翻译： Verfahren zur Herstellung einer Dieselfraktion durch寡聚化
公开(公告)号：EP1739069A1
公开(公告)日：2007-01-03
申请号：EP06290881.9
申请日：2006-05-23
申请人： Institut Français du Pétrole
发明人： Louret, Sylvain , Coupard, Vincent , Simon, Laurent
IPC分类号： C07C2/02 , C10G50/00
CPC分类号： C10G50/00
摘要： La présente invention porte sur un procédé de préparation d'une coupe gazole qui comprend les étapes successives suivantes :
1) une oligomérisation d'une coupe d'hydrocarbures oléfiniques en C2-C12, de préférence en C3-C7 et plus préférentiellement encore en C3-C5,
2) une séparation du mélange de produits obtenu lors de l'étape 1), en trois coupes : une coupe légère contenant les hydrocarbures oléfiniques en C4 et/ou en C5 n'ayant pas réagi, une coupe intermédiaire présentant une T95 comprise entre 200-220°C, et une coupe lourde comprenant le complément,
la T95 étant la température à laquelle 95% en poids de produit est évaporé, telle que déterminée selon la méthode normalisée ASTM D2887;
3) une oligomérisation de la coupe intermédiaire obtenue à l'étape de séparation, ladite coupe intermédiaire étant mélangée avec au moins une partie de la coupe légère en C4-C5 issue de ladite étape de séparation dans des proportions telles que le rapport massique entre la coupe intermédiaire et la coupe oléfinique en C4-C5 soit compris entre 60/40 et 80/20.
摘要翻译：柴油（21）馏分的制备包括使2-12C，优选3-5C烯烃部分低聚，其中C是碳原子; 将获得的混合物分离成三个级分，其包含含有4C和/或5C的具有小于100℃，优选小于50℃的蒸馏点（T95）的4C和/或5C烯烃的未反应轻馏分，（I）具有180-240℃，优选200-220℃的T95，和具有大于240℃，优选大于220℃的T95的重馏分; 并用重量比为60:40-80:20的轻馏分低聚（I）。

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