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    • 1. 发明公开
    • METHOD FOR SYNTHESIZING SAPO MOLECULAR SIEVE BY SOLVOTHERMAL METHOD AND CATALYST PREPARED THEREBY
    • 法合成SAPO分子七个由SOLVOTHERMISCHES过程,并在这个过程中制得的催化剂
    • EP2660203A4
    • 2017-04-12
    • EP11852524
    • 2011-06-24
    • DALIAN INST CHEMICAL PHYSICS CAS
    • TIAN PENGLIU ZHONGMINZHANG YINGFAN DONGSU XIONG
    • C01B39/54B01J29/85C01B37/08
    • B01J29/85C01B37/08C01B39/54C07C1/20C07C2529/85Y02P30/42
    • A solvothermal synthesis process of the SAPO molecular sieves and catalysts prepared thereby are provided. The synthesis process comprises the following steps: a) an organic amine, an aluminum source, a phosphorus source, a silicon source, and water are mixed in a molar ratio of 6-30 : 1 : 0.5-5 : 0.01-1.0 : 0.1-15, to obtain an initial mixture for preparing the SAPO molecular sieves, wherein the molar ratio of water to the organic amine is less than 2.0; b) the initial mixture obtained in the step a) is maintained at 30-60 °C and aged with stirring for not more than 24 hours, to obtain an initial gel; c) the initial gel obtain in the step b) is crystallized at 150-250 °C for 0.5-15 days. The SAPO molecular sieves prepared thereby are used, after being calcined at 400 - 700 °C in air, as catalysts for acid-catalyzed reactions or for conversion reactions of oxygen-containing compounds to olefins.
    • 设置在SAPO分子筛,并由此制得的催化剂的溶剂热合成方法。 合成方法包括以下步骤:a)以有机胺铝源,磷源,硅源,水和在6-30的摩尔比混合的,:1:0.5-5:0.01〜1.0:0.1 -15,以获得在初始混合物用于制备SAPO分子筛,worin的水的摩尔比的有机胺是小于2.0; b)在步骤a)中获得的初始混合物保持在30-60℃并老化搅拌不超过24小时,以获得在初始凝胶; c)该初始凝胶获得在步骤b)在150-250℃下结晶为0.5〜15天。 由此制备的SAPO分子筛的使用,在400煅烧至700℃的空气中,作为催化剂用于酸催化的反应或反应为含氧化合物转化成烯烃后。
    • 2. 发明公开
    • METHOD FOR PREPARING A LIGHT OLEFIN USING AN OXYGEN-CONTAINING COMPOUND
    • VERFAHREN ZUR HERSTELLUNG EINES LEICHTEN OLEFINS MIT VERWENDUNG EINER SAUERSTOFFHALTIGEN VERBINDUNG
    • EP3078651A4
    • 2017-08-16
    • EP13898489
    • 2013-12-03
    • DALIAN INST CHEMICAL PHYSICS CAS
    • LIU ZHONGMINYE MAOZHANG TAOHE CHANGQINGWANG XIANGAOZHAO YINFENG
    • C07C1/20B01J29/90C07C11/04C07C11/06C07C11/08
    • C07C1/20B01J29/90B01J38/06B01J38/12C07C5/333Y02P20/52Y02P20/584Y02P30/42C07C11/04C07C11/06C07C11/08
    • The present invention relates to a method for improving the light olefin yield in the process of preparation of a light olefin using an oxygen-containing compound. More specifically, the present invention provides a method for preparing a light olefin using an oxygen-containing compound, in which, a multi-stage dense phase fluidized bed comprising k secondary pre-carbon deposition zones (k‰¥1) and n secondary reaction zones (n‰¥1) is used as a reactor, and a multi-stage dense phase fluidized bed regenerator comprising m secondary regeneration zones (m‰¥2) is used as a main equipment. By the method of re-refining the hydrocarbons with four or more carbons obtained in the separation section, or adding naphtha, gasoline, condensate oil, light diesel oil, hydrogenation tail oil or kerosene in the reaction zone, the invention primarily solves the problems in the prior art of the uniformity of carbon deposition amount and the carbon content of the catalyst being difficult to control, and the light olefin yield being low.
    • 本发明涉及在使用含氧化合物制备轻质烯烃的过程中提高轻质烯烃产率的方法。 更具体地说,本发明提供了一种使用含氧化合物制备轻质烯烃的方法,其中包括k个二级预碳沉积区(k≥1)和n次级反应的多级密相流化床 (1台)作为反应器,以m台二次再生区(m¥2台)为主要设备的多级密相流化床再生器。 本发明通过对分离段中得到的四种或更多种碳进行再精制或在反应区中加入石脑油,汽油,冷凝油,轻柴油,加氢尾油或煤油的方法,主要解决了 碳沉积量的均匀性和催化剂的碳含量难以控制的现有技术以及轻质烯烃收率低。
    • 3. 发明公开
    • METHOD FOR PREPARING NAY MOLECULAR SIEVE OF HIGH SILICA-ALUMINA RATIO AND PRODUCT THEREOF
    • 用于生产的NaY分子筛具有高硅铝-SHARE及其产品
    • EP3081532A4
    • 2017-05-10
    • EP13899055
    • 2013-12-09
    • DALIAN INST CHEMICAL PHYSICS CAS
    • YUAN DANHUADONG XINGLONGXU YUNPENGLIU ZHONGMINWANG KUNYUANHUANG WEI
    • C01B39/24
    • C01B39/24
    • The present invention relates to a method for preparing a NaY molecular sieve having a high silica-to-alumina ratio, wherein deionized water, a silicon source, an aluminum source, an alkali source, and ILs as a template agent are mixed to obtain an initial gel mixture; the initial gel mixture is maintained at a proper temperature and aged, then fed into a high pressure synthesis kettle for crystallization; the solid product is separated and dried, to obtain the NaY molecular sieve having a high silica-to-alumina ratio, wherein the ILs is a short-chain alkylimidazolium ionic liquid. The template agent used in the method of the invention is less volatile, and the resultant high-silicon Y molecular sieve has a high crystallinity and a silica-to-alumina ratio of 6 or more.
    • 本发明涉及一种用于制备具有高二氧化硅与氧化铝之比,worin去离子水,硅源与铝源,在碱性源的NaY分子筛,和离子性液体作为模板剂混合,以获得在 初始凝胶混合物; 初始凝胶混合物被维持在适当的温度和老化,然后送入高压釜合成结晶; 将固体产物分离并干燥,以获得具有高的二氧化硅与氧化铝比,worin离子液体是一种短链烷基咪唑鎓离子液体中的NaY分子筛。 在发明的方法中使用的模板剂是不易挥发,并且将所得的高硅分子筛Y具有高结晶度和二氧化硅与氧化铝之比为6以上。
    • 6. 发明公开
    • METHOD FOR PREPARING POLYOXYMETHYLENE DIMETHYL ETHER CARBONYL COMPOUND AND METHYL METHOXYACETATE
    • VERFAHREN ZUR HERSTELLUNG EINER多羟基甲基二甲基碳二亚胺甲基甲基氧化锡
    • EP3088381A4
    • 2017-05-31
    • EP13900195
    • 2013-12-23
    • DALIAN INST CHEMICAL PHYSICS CAS
    • NI YOUMINGZHU WENLIANGLIU HONGCHAOLIU YONGLIU ZHONGMINMENG SHUANGHELI LINALIU SHIPINGZHOU HUI
    • C07C67/37C07C67/38C07C69/708
    • C07C67/37C07C67/38C07C69/708
    • This invention provides a method for preparing a polyoxymethylene dimethyl ether carbonyl compound and/or methyl methoxyacetate as intermediates for producing ethylene glycol, which comprises passing a raw material: polyoxymethylene dimethyl ether or methylal together with carbon monoxide and hydrogen gas through a reactor carrying an acidic molecular sieve catalyst, and performing a reaction to prepare a corresponding product under an appropriate condition where no other solvent is added, wherein the process of the reaction is a gas-liquid-solid three-phase reaction. In the method of this invention, the raw material of polyoxymethylene dimethyl ether or methylal has a high conversion rate, each product has a high selectivity, the catalyst has a long service life, additional solvents are not required to be used, and reaction conditions are relatively mild. The method of this invention enables continuous production and has the potential for industrial application. Also, ethylene glycol may be produced by subjecting the resultant product to hydrolysis after hydrogenation or hydrogenation after hydrolysis.
    • 本发明提供一种制备聚甲醛二甲醚羰基化合物和/或甲氧基乙酸甲酯作为生产乙二醇的中间体的方法,其包括将原料:聚甲醛二甲醚或甲缩醛与一氧化碳和氢气一起通过携带酸性的反应器 分子筛催化剂,并在不添加其它溶剂的适当条件下进行反应以制备相应的产物,其中反应过程是气 - 液 - 固三相反应。 在本发明的方法中,聚甲醛二甲醚或甲缩醛的原料转化率高,每种产品都具有高选择性,催化剂使用寿命长,不需要额外的溶剂,反应条件为 比较温和 本发明的方法能够连续生产并具有工业应用的潜力。 此外,乙二醇可以通过在水解后氢化或氢化后使所得产物水解而制备。
    • 7. 发明公开
    • REACTION DEVICE FOR PREPARING LIGHT OLEFINS FROM METHANOL AND/OR DIMETHYL ETHER
    • REACHTIONSVORRICHTUNG ZUR HERSTELLUNG VON LEICHTEN OLEFINEN AUS METHANOL UND / ODER DIMETHYLETHER
    • EP3078414A4
    • 2017-06-07
    • EP13898849
    • 2013-12-03
    • DALIAN INST CHEMICAL PHYSICS CAS
    • ZHANG TAOYE MAOLIU ZHONGMIN
    • B01J8/26B01J8/34C07C1/20C07C11/04C07C11/06
    • B01J8/26B01J8/1827B01J8/1836B01J8/1872B01J8/34B01J2208/0015B01J2208/00902B01J2208/00938C07C1/20Y02P30/42C07C11/04C07C11/06
    • This present invention relates to a reaction device for preparing light olefins from methanol and/or dimethyl ether, and more specifically relates to a reaction device for preparing light olefins from methanol and/or dimethyl ether, which mainly comprises a dense phase fluidized bed reactor (2), a cyclone separator (3), a stripper (5), a lift pipe (7), a dense phase fluidized bed regenerator (10), a cyclone separator (11), a stripper (13), and a lift pipe (15), wherein the dense phase fluidized bed reactor (2) is separated into n (n‰¥2) secondary reaction zones by a material flow controller (17), and the dense phase fluidized bed regenerator (10) is separated into m (m‰¥2) secondary regeneration zones by the material flow controller (17). The use of the reaction device of this present invention solves the problems in the prior art that the distribution of carbon deposition on a catalyst is non-uniform and the selectivity for the light olefins is relatively low.
    • 本发明涉及由甲醇和/或二甲醚制备轻质烯烃的反应装置,更具体地说,涉及一种由甲醇和/或二甲醚制备轻质烯烃的反应装置,主要由密相流化床反应器 2),旋风分离器(3),汽提器(5),提升管(7),密相流化床再生器(10),旋风分离器(11),汽提器(13)和提升管 (15),其中密相流化床反应器(2)通过物料流量控制器(17)分离成n(n‰)个二级反应区,密相流化床再生器(10)分离为m (m‰2)次级再生区由物料流量控制器(17)控制。 本发明的反应装置的使用解决了现有技术中催化剂上碳沉积的分布不均匀并且轻质烯烃的选择性相对较低的问题。