| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 1 | 含蒽类化合物、其制备方法及其应用、有机发光器件 | CN201310666464.1 | 2013-12-10 | CN103787822A | 2014-05-14 | 李彦松; 马晓宇; 王辉; 李娜 |
| 本发明提供了一种用于荧光主体材料，空穴注入材料或者空穴传输材料蒽类化合物及其应用,和包含有该有机发光化合物的有机发光器件。所述蒽类化合物的分子结构通式为：其中，R基团选自碳原子数为6～19个原子构成的芳香基、稠环芳基、芳族杂环基或取代的芳族杂环基系列基团。该有机化合物具有良好的热稳定性，是一种高效率长寿命的材料。 | ||||||
| 2 | 含蒽类化合物、其制备方法及其应用、有机发光器件 | CN201610090045.1 | 2013-12-10 | CN105601557A | 2016-05-25 | 李彦松; 马晓宇; 王辉; 李娜 |
| 本发明提供了一种用于荧光主体材料，空穴注入材料或者空穴传输材料蒽类化合物及其应用,和包含有该有机发光化合物的有机发光器件。所述蒽类化合物的分子结构通式为：其中，R基团选自芳族杂环基，所述芳族杂环基由5个碳原子构成。该有机化合物具有良好的热稳定性，是一种高效率长寿命的材料。 | ||||||
| 3 | 含蒽类化合物、其制备方法及其应用、有机发光器件 | CN201310666464.1 | 2013-12-10 | CN103787822B | 2016-04-06 | 李彦松; 马晓宇; 王辉; 李娜 |
| 本发明提供了一种用于荧光主体材料，空穴注入材料或者空穴传输材料蒽类化合物及其应用,和包含有该有机发光化合物的有机发光器件。所述蒽类化合物的分子结构通式为：其中，R基团选自碳原子数为6～19个原子构成的芳香基、稠环芳基、芳族杂环基或取代的芳族杂环基系列基团。该有机化合物具有良好的热稳定性，是一种高效率长寿命的材料。 | ||||||
| 4 | 用烷烃使芳族化合物烷基化的方法和催化剂 | CN201280026407.0 | 2012-06-28 | CN103732564B | 2016-01-20 | Y·特拉; D·盖斯 |
| 公开的是用烷烃使芳族化合物直接烷基化的方法。为此提供明智的催化剂组合。组合物包括钯作为有催化活性的金属，以及锌作为促进剂，或者具有可比较的促进作用的金属如锡。金属包含在沸石载体或者类似的金属有机骨架型或磷酸硅铝型载体中。 | ||||||
| 5 | 用烷烃使芳族化合物烷基化的方法和催化剂 | CN201280026407.0 | 2012-06-28 | CN103732564A | 2014-04-16 | Y·特拉; D·盖斯 |
| 本发明公开的是用烷烃使芳族化合物直接烷基化的方法。为此提供明智的催化剂组合。组合物包括钯作为有催化活性的金属，以及锌作为促进剂，或者具有可比较的促进作用的金属如锡。金属包含在沸石载体或者类似的金属有机骨架型或磷酸硅铝型载体中。 | ||||||
| 6 | JPS52945B1 - | JP11060870 | 1970-12-14 | JPS52945B1 | 1977-01-11 | |
| 7 | Separation of cyclic hydrocarbons with molecular sieve adsorbent | US26337272 | 1972-06-06 | US3840610A | 1974-10-08 | HEDGE J |
| 1. A PROCESS FOR SEPARATING TWO STRUCTURALLY SIMILAR CYCLIC AROMATIC HYDROCARBONS CONTAINING IN THE RANGE OF 1-4 AROMATIC RINGS, AND IN THE RANGE OF 8-36 CARBON ATOMS AND WHEREIN SAID AROMATIC HYDROCARBONS CONTAIN AT LEAST ONE CONDENSED RING, SAID PROCESS COMPRISING: (A) CONTACTING A FLUID FEED MIXTURE COMPRISING SAID CYCLIC AROMATIC HYDROCARBONS WITH A SOLID ABSORBENT COMPRISING A PARTIALLY DEHYDRATED, SUBSTANTIALLY CRYSTALLINE ALUMINO-SILICATE ZEOLITE HAVING A CRITICAL PORE DIAMETER GREATER THAN ABOUT 6A, THE RATIO AL/SI OF THE ALUMINO- SILICATE FRAMEWORK OF THE ZEOLITE BEING IN THE RANGE OF 0.65-0.2, THE ZEOLITE HAVING BEEN PARTIALLY DEHYDRATED BY EXPOSURE TO A TEMPERATURE IN THE RANGE OF 80-300* C., WHEREBY THERE IS OBTAINED A RICH ADSORBENT CONTAINING AN ADSORBATE WHICH IS RICHER IN ONE SAID CYCLIC AROMATIC HYDROCARBON THAN WAS SAID FLUID FEED MIXTURE, AND A RAFFINATE PRODUCT WHICH CONTAINS LESS OF THE ONE SAID CYCLIC AROMATIC HYDROCARBON THAN DID SAID FLUID FEED MIXTURE; (B) SEPARATING SAID RAFFINATE PRODUCT FROM SAID RICH ADSORBENT AND, (C) REMOVING THE ONE SAID CUCLIC AROMATIC HYDROCARBON FROM SAID RICH ADSORBENT.
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| 8 | Separation of 2,7-dimethylnaphthalene from 2,6-dimethylnaphthalene with molecular sieves | US3668267D | 1970-01-30 | US3668267A | 1972-06-06 | HEDGE JOHN A |
| Two structurally similar polycyclic compounds can be separated by contacting a fluid feed mixture containing said compounds with a partially dehydrated molecular sieve zeolite, the ratio Al/Si of the zeolite being in the range of 0.65-0.2. The polycyclic compounds can be heterocyclic or carbocyclic. For example, selective adsorption of 2,7-dimethylnaphthalene from a dimethylnaphthalene concentrate is obtained with sodium Type Y molecular sieves. 2,6-Dimethylnaphthalene can then be crystallized from the unadsorbed raffinate fraction. Separation factors of 6 to 8 are obtained, indicating the unexpected high selectivity of these particular molecular sieves for this adsorption (especially compared to Type X zeolite). A continuous method is disclosed for adsorption and desorption of 2,7-dimethylnaphthalene utilizing Type Y zeolite. Type L zeolite can be used for adsorption and desorption of 2,6-DMN.
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| 9 | Separation of anthracene-phenanthrene mixtures | US3458538D | 1964-01-23 | US3458538A | 1969-07-29 | MAHONEY LEE ROBERT |
| 10 | Separation of isomeric halogenated aromatic compounds | US80096159 | 1959-03-23 | US2958708A | 1960-11-01 | FLECK RAYMOND N; WIGHT CARLYLE G; WISEMAN EDWARD L |
| 11 | Crude anthracene separation | US57568645 | 1945-02-01 | US2438148A | 1948-03-23 | BENNETT CORSON BEN; SHERMAN DETRICK ROBERT |
| 12 | Uniformly, highly dispersed metal catalyst and process for producing the same | US13940053 | 2013-07-11 | USRE46145E1 | 2016-09-13 | Yoshimi Okada; Toshiji Makabe; Masashi Saito; Hiroaki Nishijima |
| Provided are: a uniformly, highly dispersed metal catalyst including a catalyst carrier and a catalyst metal being loaded thereon dispersed throughout the carrier, the uniformly, highly dispersed metal catalyst having excellent performances with respect to catalytic activity, selectivity, life, etc.; and a method of producing the same. The uniformly, highly dispersed metal catalyst includes a catalyst carrier made of a metal oxide and a catalyst metal having catalytic activity, the catalyst metal being loaded on the catalyst carrier, in which the catalyst carrier is a sulfur-containing catalyst carrier having sulfur or a sulfur compound almost evenly distributed throughout the carrier and the catalyst metal is loaded on the sulfur-containing catalyst carrier in a substantially evenly dispersed manner over the entire carrier substantially according to the distribution of the sulfur or the sulfur compound. | ||||||
| 13 | ANTHRACENE COMPOUND, METHOD FOR PREPARING THE SAME, USE THEREOF AND ORGANIC LIGHT EMITTING DEVICE | US14416794 | 2014-05-29 | US20150376085A1 | 2015-12-31 | Yansong LI; Xiaoyu MA; Hui WANG; Na LI |
| Provided are anthracene compound, method for preparing the same and use thereof, as well as organic electroluminescent device containing the same. The anthracene compound represented by a formula: wherein R is selected from C6-C19 aryl, fused ring aryl, or substituted or unsubstituted heterocyclic aryl. | ||||||
| 14 | Process for separation of phenanthrene | US3793387D | 1973-04-06 | US3793387A | 1974-02-19 | SUN Y |
| SEPARATION OF PHENANTHRENE FROM A SOLUTION OF A MIXTURE OF ANTHRACENE AND PHENANTHRENE IN LOWER ALCOHOL OR KETONE, UP TO 30% AQUEOUS MIXTURE THEREOF, OR MIXTURES THEREOF, BY SELECTIVELY PRECIPITATING THE PHENANTHRENE BY THE ADDITION OF WATER.
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| 15 | Extraction of quinonoid hydrocarbons from benzenoid hydrocarbons by means of anhydrous hydrogen fluoride | US68112246 | 1946-07-02 | US2426624A | 1947-09-02 | LIEN ARTHUR P |
| 16 | 均一型高分散金属触媒及びその製造方法 | JP2007522272 | 2006-06-19 | JPWO2006137358A1 | 2009-01-15 | 佳己 岡田; 利治 真壁; 政志 斉藤; 西島 裕明; 裕明 西島 |
| 触媒担体にその担体全体に亘って触媒金属が略均一に分散した状態で担持され、触媒活性や選択性、寿命等において優れた性能を有する均一型高分散金属触媒及びその製造方法を提供する。金属酸化物からなる触媒担体に触媒活性を有する触媒金属を担持させた金属触媒において、上記触媒担体がその担体全体に亘って略均一に分布する硫黄又は硫黄化合物を含有する硫黄含有触媒担体であり、この硫黄含有触媒担体には、上記硫黄又は硫黄化合物の分布に略々応じて、触媒金属が担体全体に亘って略均一に分散して担持されている均一型高分散金属触媒である。 | ||||||
| 17 | Uniform-type high-dispersed metal catalyst and a method of manufacturing the same | JP2007522272 | 2006-06-19 | JP4142733B2 | 2008-09-03 | 佳己 岡田; 政志 斉藤; 利治 真壁; 裕明 西島 |
| 18 | METHOD AND CATALYST FOR THE ALKYLATION OF AROMATIC COMPOUNDS WITH ALKANES | US14118214 | 2012-06-28 | US20140249343A1 | 2014-09-04 | Yvonne Traa; Daniel Geiss |
| Disclosed is a process for the direct alkylation of aromatic compounds with alkanes. To this end a judicious catalyst combination is provided. The composition comprises palladium as a catalytically active metal, and zinc as a promoter, or a metal such as tin having a comparable promoting action. The metals are contained in a zeolite support, or a similar support of a metal organic framework type or a silico alumino phosphate type. | ||||||
| 19 | Uniformly, highly dispersed metal catalyst and process for producing the same | US11922462 | 2006-06-19 | US07985706B2 | 2011-07-26 | Yoshimi Okada; Toshiji Makabe; Masashi Saito; Takako Nishijima |
| Provided are: a uniformly, highly dispersed metal catalyst including a catalyst carrier and a catalyst metal being loaded thereon dispersed throughout the carrier, the uniformly, highly dispersed metal catalyst having excellent performances with respect to catalytic activity, selectivity, life, etc.; and a method of producing the same. The uniformly, highly dispersed metal catalyst includes a catalyst carrier made of a metal oxide and a catalyst metal having catalytic activity, the catalyst metal being loaded on the catalyst carrier, in which the catalyst carrier is a sulfur-containing catalyst carrier having sulfur or a sulfur compound almost evenly distributed throughout the carrier and the catalyst metal is loaded on the sulfur-containing catalyst carrier in a substantially evenly dispersed manner over the entire carrier substantially according to the distribution of the sulfur or the sulfur compound. | ||||||
| 20 | Uniformly, Highly Dispersed Metal Catalyst and Process for Producing the Same | US11922462 | 2006-06-19 | US20090105511A1 | 2009-04-23 | Yoshimi Okada; Toshiji Makabe; Masashi Saito; Takako Nishijima |
| Provided are: a uniformly, highly dispersed metal catalyst including a catalyst carrier and a catalyst metal being loaded thereon dispersed throughout the carrier, the uniformly, highly dispersed metal catalyst having excellent performances with respect to catalytic activity, selectivity, life, etc.; and a method of producing the same. The uniformly, highly dispersed metal catalyst includes a catalyst carrier made of a metal oxide and a catalyst metal having catalytic activity, the catalyst metal being loaded on the catalyst carrier, in which the catalyst carrier is a sulfur-containing catalyst carrier having sulfur or a sulfur compound almost evenly distributed throughout the carrier and the catalyst metal is loaded on the sulfur-containing catalyst carrier in a substantially evenly dispersed manner over the entire carrier substantially according to the distribution of the sulfur or the sulfur compound. | ||||||
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