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1. 发明公开

EP2895446A1 METHODS OF PRODUCING PARA-XYLENE AND TEREPHTHALIC ACID 审中-公开
标题翻译：工艺用于生产和PARAXYLEN-对苯二甲酸
公开(公告)号：EP2895446A1
公开(公告)日：2015-07-22
申请号：EP13766444.7
申请日：2013-09-13
申请人： Micromidas, Inc.
发明人： MASUNO, Makoto N. , SMITH, Ryan L. , BISSELL, John , FOSTER, Marc , SMITH, Patrick B. , HUCUL, Dennis A. , STARK, Edmund J. , HENTON, Daniel R. , DUMITRASCU, Adina , BRUNE, Katherine
IPC分类号： C07C2/86 , C07C15/08 , C07C51/265 , C07C63/26 , C07C2/46 , C07C2/62 , C07C49/14
CPC分类号： C07C2/865 , C07C2/46 , C07C2/62 , C07C2/86 , C07C2/867 , C07C15/08 , C07C49/14 , C07C51/265 , C07C63/26 , C07C2521/04 , C07C2521/08 , C07C2523/10 , C07C2523/28 , C07C2523/72 , C07C2527/054 , C07C2527/11 , C07C2527/122 , C07C2527/125 , C07C2527/126 , C07C2527/173 , C07C2527/19 , C07C2529/08 , C07C2529/70 , C07C2531/025 , C07C2531/04 , C07C2531/12
摘要： The present disclosure provides methods to produce
para-xylene , toluene, and other compounds from renewable sources (e.g., cellulose, hemicellulose, starch, sugar) and ethylene in the presence of a catalyst. For example, cellulose and/or hemicellulose may be converted into 2,5-dimethylfuran (DMF), which may be converted into
para-xylene by cycloaddition of ethylene to DMF.
Para-xylene can then be oxidized to form terephthalic acid.

2. 发明公开

EP2736630A4 FLUID BED REACTOR WITH STAGED BAFFLES 有权转让
标题翻译： WIRBELBETTREAKTOR MIT ABGESTUFTEN ABLENKBLECHEN
公开(公告)号：EP2736630A4
公开(公告)日：2015-04-22
申请号：EP12817575
申请日：2012-07-25
申请人： EXXONMOBIL CHEM PATENTS INC
发明人： HAN LU , DAVULURI RATHNA P , SMALLEY CHRISTOPHER G , HAGEMEISTER MARK P , SUGITA MASAAKI , FAMOLARO JOSEPH S , TINGER ROBERT G
IPC分类号： B01J8/24 , B01J8/20 , C07C2/64 , C07C15/08
CPC分类号： B01J8/34 , B01J8/1818 , B01J8/1827 , B01J8/1872 , C07C2/864 , C07C2/865 , Y02P20/52 , C07C15/08
摘要： The invention relates to a process of alkylating aromatic hydrocarbons, and more particularly a process of making paraxylene by alkylation of benzene and/or toluene with methanol and/or dimethyl ether, and to an apparatus for carrying out said process, the improvement comprising staged injection of one of the reactants, with the stages separated by structured packing so as to minimize at least one of gas phase back-mixing, by-pass phenomena, and gas bubble size.
摘要翻译：本发明涉及芳族烃的烷基化方法，更具体地说是一种通过用甲醇和/或二甲醚烷基化苯和/或甲苯来制备对二甲苯的方法，以及用于进行所述方法的设备，其改进包括分段注射其中一种反应物，其中阶段由规整填料分离，以使气相回混，旁路现象和气泡尺寸中的至少一个最小化。

3. 发明公开

EP2803407A1 CATALYST FOR PREPARING PARAXYLENE BY MUTUAL CONVERSION OF METHYL ALCOHOL AND/OR DIMETHYL ETHER AND C4 LIQUEFIED GAS, AND PREPARATION METHOD AND APPLICATION THEREFOR 有权
标题翻译：用于生产对二甲苯BY甲醇和/或二甲醚与LPG C4的同时转换使用双金属和硅氧烷改性的催化剂
公开(公告)号：EP2803407A1
公开(公告)日：2014-11-19
申请号：EP12860423.8
申请日：2012-04-26
申请人： Dalian Institute Of Chemical Physics, Chinese Academy of Sciences
发明人： XU, Lei , LIU, Zhongmin , YU, Zhengxi
IPC分类号： B01J29/00 , B01J29/04 , B01J29/40 , B01J37/02 , C07C15/08 , C07C1/20
CPC分类号： B01J31/26 , B01J29/40 , B01J29/405 , B01J31/0204 , B01J31/0274 , B01J31/0275 , B01J2229/186 , B01J2229/32 , B01J2231/005 , C07C2/862 , C07C2/864 , C07C2/865 , C07C2521/04 , C07C2521/08 , C07C2521/16 , C07C2523/06 , C07C2523/08 , C07C2529/40 , Y02P20/52 , Y02P30/20 , C07C15/08
摘要： This application provides a catalyst for producing paraxylene by co-conversion of methanol and/or dimethyl ether and C 4 liquefied gas, and preparation and application thereof. The catalyst is an aromatization molecular sieve catalyst with a shape-selective function co-modified by bimetal and siloxane compound. Methanol and/or dimethyl ether and C 4 liquefied gas are fed in reactor together, wherein aromatization reaction occurring on a modified shape-selective molecular sieve catalyst. The yield of aromatics is effectively improved, in which paraxylene is the main product. In products obtained by co-conversion of methanol and/or dimethyl ether and C 4 liquefied gas, the yield of aromatics is greater than 70wt%, and the content of paraxylene in aromatics is greater than 80wt%, and the selectivity of paraxylene in xylene is greater than 99wt%.
摘要翻译：本申请提供了一种通过甲醇和/或二甲醚和C 4液化气，以及制备和应用它们的相互转化生产对二甲苯的催化剂。该催化剂是芳构化分子筛催化剂与形状选择性功能由双金属和硅氧烷化合物共改性。甲醇和/或二甲醚和C 4液化气送入反应器一起，worin芳构化反应发生的上经修饰的形状选择性分子筛催化剂。芳烃的产量得到了有效提高，其中对二甲苯的主要产品。气体进入由甲醇和/或二甲醚和C 4液化的CO转化获得的产品，芳族化合物的产率大于70重量％，以及在芳族化合物的对二甲苯的含量大于80重量％，和对二甲苯的二甲苯的选择性超过99％重量更大。

4. 发明公开

EP2736630A2 FLUID BED REACTOR WITH STAGED BAFFLES 有权转让
标题翻译：流化床反应器毕业挡板
公开(公告)号：EP2736630A2
公开(公告)日：2014-06-04
申请号：EP12817575.9
申请日：2012-07-25
申请人： ExxonMobil Chemical Patents Inc.
发明人： HAN, Lu , DAVULURI, Rathna, P. , SMALLEY, Christopher, G. , HAGEMEISTER, Mark, P. , SUGITA, Masaaki , FAMOLARO, Joseph, S. , TINGER, Robert, G.
IPC分类号： B01J8/24 , B01J8/20 , C07C15/08 , C07C2/64
CPC分类号： B01J8/34 , B01J8/1818 , B01J8/1827 , B01J8/1872 , C07C2/864 , C07C2/865 , Y02P20/52 , C07C15/08
摘要： The invention relates to a process of alkylating aromatic hydrocarbons, and more particularly a process of making paraxylene by alkylation of benzene and/or toluene with methanol and/or dimethyl ether, and to an apparatus for carrying out said process, the improvement comprising staged injection of one of the reactants, with the stages separated by structured packing so as to minimize at least one of gas phase back-mixing, by-pass phenomena, and gas bubble size.

5. 发明公开

EP2621630A2 REGENERATION OF METAL-CONTAINING CATALYSTS 审中-公开
标题翻译：再生金属加速器KATALYSATOREN
公开(公告)号：EP2621630A2
公开(公告)日：2013-08-07
申请号：EP11831126.5
申请日：2011-08-26
申请人： ExxonMobil Chemical Patents Inc.
发明人： CLEM, Kenneth, R. , IACCINO, Larry, L. , AFEWORKI, Mobae , HENAO, Juan, D. , SANGAR, Neeraj , ZHENG, Xiaobo , DECAUL, Lorenzo, C.
IPC分类号： B01J38/04 , B01J38/10 , B01J27/28 , B01J29/90 , C07C2/86
CPC分类号： C07C2/76 , B01J29/48 , B01J29/90 , B01J38/02 , B01J38/10 , C07C1/12 , C07C2/66 , C07C2/864 , C07C2/865 , C07C5/10 , C07C5/11 , C07C2521/06 , C07C2523/02 , C07C2523/06 , C07C2523/08 , C07C2523/10 , C07C2523/12 , C07C2523/14 , C07C2523/16 , C07C2523/18 , C07C2523/20 , C07C2523/26 , C07C2523/28 , C07C2523/30 , C07C2523/34 , C07C2523/36 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07C2523/50 , C07C2523/52 , C07C2523/72 , C07C2523/745 , C07C2523/75 , C07C2523/755 , C07C2527/22 , C07C2529/08 , C07C2529/18 , C07C2529/40 , C07C2529/60 , C07C2529/65 , C07C2529/70 , C07C2601/14 , C07C2601/16 , C07C2602/26 , C07C2602/28 , C10G50/00 , C10G2300/708 , C10G2400/30 , Y02P20/52 , Y02P20/584 , Y02P20/588 , C07C15/04 , C07C15/24 , C07C11/04 , C07C9/04 , C07C9/06 , C07C15/073 , C07C15/08 , C07C13/18 , C07C13/50 , C07C13/20 , C07C13/48
摘要： In a process for the regeneration of a coked metal-containing catalyst, the coked catalyst is contacted in a regeneration zone with an atmosphere which contains carbon dioxide and carbon monoxide at a temperature of at least 400 °C.
摘要翻译：在一种用于再生含焦炭金属的催化剂的方法中，焦化催化剂在再生区与包含二氧化碳和一氧化碳的气氛在至少400℃的温度下接触。

6. 发明公开

EP2060551A1 Process for producing triptane 审中-公开
标题翻译：生产triptane的过程
公开(公告)号：EP2060551A1
公开(公告)日：2009-05-20
申请号：EP07254491.9
申请日：2007-11-16
申请人： BP p.l.c.
发明人： The designation of the inventor has not yet been filed
IPC分类号： C07C2/86 , C07C9/16 , C07C11/02 , B01J29/06
CPC分类号： C07C2/865 , B01J29/06 , B01J29/082 , B01J29/084 , B01J29/123 , B01J29/126 , B01J29/143 , B01J29/146 , B01J29/40 , B01J29/44 , B01J29/46 , B01J29/70 , B01J29/7007 , B01J29/74 , B01J29/7415 , B01J29/76 , B01J29/7615 , C07C2/864 , C07C2529/08 , C07C2529/12 , C07C2529/14 , C07C2529/40 , C07C2529/44 , C07C2529/46 , C07C2529/70 , C07C2529/74 , C07C2529/76 , C07C9/16 , C07C11/02
摘要： A process for the production of triptane and/or triptene from methanol and/or one or more derivatives thereof and one or more olefins in the presence of a catalyst at a temperature in the range of from 150 to 400°C, in which the catalyst is a zeolite having Brønsted acidity and has a structure selected from:
i. Zeolites having frameworks comprising silicon and aluminium atoms and having a channel structure comprising a ring size of 12 or more non-oxygen framework atoms in 2 or 3 dimensions;
ii. Zeolites having frameworks comprising silicon and aluminium atoms and which have a framework ring comprising 12 or more non-oxygen atoms accessible on the external surface of the zeolite, and a channel structure in which all of the channels have a ring-size of less than 12 non-oxygen framework atoms,

and wherein zeolites of type (ii) comprise alkali metal where methanol is not a reactant.
摘要翻译：在催化剂存在下，在150-400℃范围内的温度下由甲醇和/或其一种或多种衍生物和一种或多种烯烃生产三癸烷和/或三萜的方法，其中催化剂是具有布朗斯台德酸性并具有选自以下的结构的沸石：i。具有包含硅和铝原子并且具有包含12或更多个2维或3维的非氧骨架原子的环尺寸的通道结构的骨架的沸石; II。具有包含硅和铝原子的骨架并且具有包含可在沸石的外表面上获得的12个或更多个非氧原子的骨架环的沸石以及其中所有通道的环尺寸均小于12的通道结构非氧骨架原子，并且其中类型（ii）的沸石包含碱金属，其中甲醇不是反应物。

7. 发明授权

EP0909216B1 ZEOLITE CATALYST AND ITS USE IN HYDROCARBON CONVERSION 失效
标题翻译：沸石催化剂的结构和用法碳氢化合物实施
公开(公告)号：EP0909216B1
公开(公告)日：2004-07-07
申请号：EP97928812.3
申请日：1997-05-29
申请人： ExxonMobil Chemical Patents Inc.
发明人： VERDUIJN, Johannes, P. , MOHR, Gary, D.
IPC分类号： B01J29/80 , C07C5/27 , C07C2/66 , C07C6/12 , C10G11/05
CPC分类号： C10G11/05 , B01J29/005 , B01J29/06 , B01J29/061 , B01J29/084 , B01J29/40 , B01J29/50 , B01J29/60 , B01J29/70 , B01J29/80 , B01J29/83 , B01J29/84 , B01J29/85 , B01J29/87 , B01J2229/42 , B01J2229/62 , C07C1/20 , C07C2/861 , C07C2/864 , C07C2/865 , C07C2/868 , C07C4/06 , C07C5/2708 , C07C5/2737 , C07C5/41 , C07C6/123 , C07C6/126 , C07C2529/035 , C07C2529/08 , C07C2529/18 , C07C2529/40 , C07C2529/50 , C07C2529/65 , C07C2529/70 , C07C2529/80 , C10G29/205 , C10G35/065 , C10G35/095 , C10G45/64 , Y02P20/52 , C07C15/00 , C07C15/08

8. 发明授权

EP0914310B1 AROMATIC CONVERSION PROCESSES AND ZEOLITE CATALYST USEFUL THEREIN 失效
标题翻译：程序履行芳香烃和那里的情况下使用SANTANDER沸石催化剂
公开(公告)号：EP0914310B1
公开(公告)日：2003-10-01
申请号：EP97927943.7
申请日：1997-05-29
申请人： ExxonMobil Chemical Patents Inc.
发明人： HENDRIKSEN, Dan, E. , MOHR, Gary, D. , SMITH, Robert, S. , VERDUIJN, Johannes, P.
IPC分类号： C07C2/66 , C07C6/12 , C07C5/27 , B01J29/80
CPC分类号： C07C6/126 , B01J29/18 , B01J29/40 , B01J29/7007 , B01J29/80 , B01J29/87 , B01J2229/26 , B01J2229/42 , C07C2/66 , C07C2/861 , C07C2/864 , C07C2/865 , C07C2/868 , C07C5/2708 , C07C2529/035 , C07C2529/18 , C07C2529/40 , C07C2529/50 , C07C2529/65 , C07C2529/70 , C07C2529/80 , C07C2529/87 , Y02P20/52 , C07C15/00 , C07C15/08

9. 发明公开

EP0890562A1 Process for producing diarylmethanes or their derivatives 失效
标题翻译： Verfahren zur Herstellung von Diarylmethanen oder von ihren Derivaten
公开(公告)号：EP0890562A1
公开(公告)日：1999-01-13
申请号：EP98112768.1
申请日：1998-07-09
申请人： Nippon Petrochemicals Company, Limited
发明人： Kawamata, Tandanori , Dohi, Hideyuki , Inoue, Satoru , Hayashi, Shozo
IPC分类号： C07C2/86 , C07C37/16
CPC分类号： C07C37/16 , C07C2/865 , C07C37/115 , Y02P20/127 , Y02P20/582 , C07C15/16 , C07C39/16
摘要： A method to produce diarylmethane or its derivatives by condensation reaction can be carried out without difficulty and without the deterioration of catalyst, and the intended product can be produced inexpensively by recovering and recycling used alcohol. In the method, dimethoxymethane and an aromatic compound are reacted at a temperature of 80 to 400°C with an acid catalyst. Further, the method comprises the steps of (1) reacting alcohol with formaldehyde using an acid catalyst to obtain acetal; (2) reacting the acetal and an aromatic compound using an acid catalyst to obtain a reaction mixture containing diarylmethane or its derivatives and alcohol; (3) separating and recovering diarylmethane or its derivatives and alcohol from the reaction mixture, and (4) recycling at least a portion of the recovered alcohol to the step (1).
摘要翻译：通过缩合反应生产二芳基甲烷或其衍生物的方法可以毫无困难地进行，并且不会导致催化剂的劣化，并且可以通过回收和循环使用的醇廉价地生产目的产物。在该方法中，二甲氧基甲烷和芳族化合物在80〜400℃的温度下与酸催化剂反应。此外，该方法包括以下步骤：（1）使用酸催化剂使醇与甲醛反应以获得缩醛; （2）使用酸催化剂使缩醛和芳族化合物反应，得到含有二芳基甲烷或其衍生物和醇的反应混合物; （3）从反应混合物中分离和回收二芳基甲烷或其衍生物和醇，和（4）将至少一部分回收的醇再循环到步骤（1）。

10. 发明授权

EP0104607B1 PROCESS FOR THE PRODUCTION OF PSEUDOCUMENE OR DURENE 失效
标题翻译：生产PSEUDOCUMENE或DURENE的方法
公开(公告)号：EP0104607B1
公开(公告)日：1986-12-30
申请号：EP83109417
申请日：1983-09-22
申请人： IDEMITSU KOSAN COMPANY LIMITED
发明人： SATO, HARUHITO
IPC分类号： B01J21/00 , B01J21/02 , B01J21/06 , B01J29/86 , C07B61/00 , C07C1/00 , C07C2/86 , C07C15/02 , C07C15/08 , C07C67/00
CPC分类号： C07C2/864 , C07C2/865 , C07C2521/02 , C07C2521/08 , C07C2529/86 , C07C15/02

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