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公开(公告)号：EP2534119A1
公开(公告)日：2012-12-19
申请号：EP10784929.1
申请日：2010-11-23
IPC分类号： C07C5/02 , C07C5/03 , C07C29/20 , C07C37/08 , C07C45/00 , C07C45/53 , C07C39/04 , C07C49/403 , C07C13/19 , C07C7/148 , C07C7/163
摘要： The present invention relates to a hydrogenation process that may be used in connection with the production of phenol. In the process, a composition comprising: (i) cyclohexylbenzene; and (ii) a hydrogenable component are contacted with hydrogen in the presence of a hydrogenation catalyst under hydrogenation conditions. The hydrogenable component can be one or more of an olefin, a ketone or phenol. The hydrogenation catalyst has hydrogenation component and a support.
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32.发明公开METHOD OF CIRCULATING CATALYST BETWEEN A CATALYST REGENERATOR AND AN EXTERNAL CATALYST COOLER 有权方法KATALYSATORZIRKULIERUNG之间的催化剂再生器和外部催化剂冷却器
公开(公告)号：EP2238216A1
公开(公告)日：2010-10-13
申请号：EP08871660.0
申请日：2008-12-16
发明人： BEECH, JR., James, H. , CAO, Chunshe , NICOLETTI, Michael, P. , LATTNER, James, R. , GOELLNER, Jesse, F. , PATEL, Rutton, D. , HEALY, Timothy, M.
CPC分类号： C07C1/20 , B01J29/90 , B01J38/30 , B01J38/32 , C07C2529/40 , C07C2529/70 , C07C2529/83 , C07C2529/85 , C10G3/49 , C10G3/62 , C10G2300/802 , C10G2400/20 , Y02P20/584 , Y02P30/20 , C07C11/02
摘要： This invention relates to efficiently regenerating catalyst particles by minimizing the formation of localized “hot spots” and “cold spots” in a regeneration zone. Specifically this invention relates to a method for controlling regenerator temperature in an oxygenates-to-olefins system, comprising the steps of: contacting an oxygenate feed in a reactor with a catalytically effective amount of molecular sieve-containing catalyst under conditions effective for converting said oxygenate to a product containing light olefins and forming a coked catalyst; contacting a portion of the coked catalyst in a regenerator, having a catalyst bed height (Hc), an inlet height (Hi), and an outlet height (Ho), with an oxygen-containing regeneration medium under conditions effective to at least partially regenerate the coked catalyst; and conducting a portion of the catalyst from the regenerator to a catalyst cooler to form a cooled catalyst portion, wherein Ho is greater than Hi.
摘要翻译： 本发明涉及通过在再生区最小化局部“热点”和“冷点”的形成，有效地再生催化剂颗粒。 具体地，本发明涉及一种方法，用于在含氧化合物向烯烃的系统在控制再生器的温度，包括以下步骤：条件下与催化有效量的含分子筛催化剂的含氧化合物进料接触在反应器中有效，用于将所述含氧化合物 到一个产品包含轻质烯烃和形成结焦催化剂; 在的条件下含氧再生介质接触在再生器中的结焦的催化剂的一部分，具有一个催化剂床层高度（Hc）的至入口高度（您好），并且在出口的高度（HO），以有效地至少部分地再生 结焦的催化剂; 并进行从再生器的催化剂的部分，以催化剂冷却器以形成冷却的一部分催化剂，worin Ho大于您好更大。
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公开(公告)号：EP2160419A1
公开(公告)日：2010-03-10
申请号：EP08733148.4
申请日：2008-04-07
IPC分类号： C08F110/06 , C08F2/06
CPC分类号： C08F10/06 , C08F4/65912 , C08F4/65927 , C08F110/06 , C08L21/00 , C08F4/65908 , C08F2/06 , C08F2/14 , C08F2500/03 , C08F2500/17 , C08F2500/09 , C08F2500/12 , C08F2500/20
摘要： Processes for polymerizing propylene. About 40 wt% to about 80 wt% propylene monomer, based on total weight of propylene monomer and diluent, and about 20 wt% to about 60 wt% diluent, based on total weight of propylene monomer and diluent, can be fed into a reactor. The propylene monomer can be polymerized in the presence of a metallocene catalyst and an activator within the reactor at a temperature of about 800C or more and a pressure of about 13 MPa or more to produce a polymer product in a homogenous system. About 20 wt% to about 76 wt% (preferably About 28 wt% to about 76 wt%) propylene monomer, based on total weight of the propylene monomer, diluent, and polymer product, can be present at the reactor exit at steady state conditions.
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34.发明授权An oxygenate to olefin conversion process by means of a multiple riser reactor 有权含氧化合物转化为在多提升管反应器烯烃
公开(公告)号：EP1299504B1
公开(公告)日：2008-05-14
申请号：EP01932739.4
申请日：2001-04-27
CPC分类号： B01J8/26 , B01J8/0055 , B01J8/1845 , B01J8/1872 , C10G3/49 , C10G3/62 , C10G11/18 , C10G2300/4093 , C10G2400/20 , Y10S585/921 , Y10S585/922 , Y10S585/923 , Y10S585/926
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公开(公告)号：EP1556461B1
公开(公告)日：2007-10-03
申请号：EP03751954.3
申请日：2003-08-22
发明人： KUECHLER, Keith, H. , LATTNER, James, R. , COUTE, Nicholas, P. , SMITH, Jeffrey, S. , KRIEGER, Justin, L.
CPC分类号： C07C51/252 , B01J8/0055 , B01J8/388 , C07C1/20 , C10G3/45 , C10G3/49 , C10G3/62 , C10G11/18 , C10G2300/1011 , C10G2300/1022 , C10G2300/1037 , C10G2300/4056 , C10G2400/02 , C10G2400/20 , Y02P30/20 , Y10S585/921 , Y10S585/922 , Y10S585/923 , Y10S585/924 , Y10S585/926 , C07C57/04
摘要： The present invention is directed to a hydrocarbon conversion apparatus and process. The apparatus comprises the following: a plurality of riser reactors, each having a first end into which a catalyst is fed, a second end through which the catalyst can exit, and optionally a center axis extending there between. The apparatus also includes a separation zone having a plurality of inlets, each inlet not being oriented along the center axes of the riser reactors, the separation zone being provided to separate the catalyst from products of a reaction conducted in the hydrocarbon conversion apparatus. A plurality of deviating members are also provided, each deviating member being in fluid communication between the second end of a respective riser reactor and a respective inlet of the separation zone. The apparatus also includes a catalyst retention zone provided to contain catalyst, which is fed to the riser reactors. A catalyst return is in fluid communication between the separation zone and the catalyst retention zone.
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36.发明公开FLUID BED OXYGENATES TO OLEFINS REACTOR APPARATUS AND PROCESS OF CONTROLLING SAME 审中-公开器具，用于产生OLEPHINEN OFF含氧烃及其控制方法本设备
公开(公告)号：EP1556316A1
公开(公告)日：2005-07-27
申请号：EP03754528.2
申请日：2003-09-12
发明人： LATTNER, James, R.
CPC分类号： C10G11/187 , B01J29/90 , B01J38/30 , C07C1/20 , C10G3/49 , C10G3/62 , C10G9/007 , C10G11/16 , C10G11/18 , C10G11/182 , C10G2300/4006 , C10G2300/4018 , C10G2300/708 , C10G2400/20 , Y02P20/584 , Y02P30/20 , C07C11/02
摘要： A reactor apparatus and related method for controlling at least one process variable in a circulating fluid bed oxygenates to olefins reactor system comprising a riser are provided. The process variable is selected from at least one of (i) space velocity, (ii) average reaction temperature, (iii) conversion of reactant, and (iv) average coke level on catalyst. Typically, a corresponding set point for at least one process variable is selected from (1) reactant feed rate, (2) feed enthalpy, (3) reactor temperature-related function, e.g., mid-temperature or rate of temperature rise along a portion of the reactor, and (4) catalyst hold-up in the riser of the reactor. A corresponding manipulated variable is selected from (a) feed flow control valve(s), (b) feed preheat rate, (c) activity of the catalyst in the reactor, and (d) amount of catalyst in the reaction zone. The combination of measured and manipulated variables described here allows for smooth, stable control of the reactor at the optimum performance level.
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公开(公告)号：EP1319055B1
公开(公告)日：2004-09-29
申请号：EP00978681.5
申请日：2000-11-16
发明人： LATTNER, James, R. , VAUGHN, Stephen, N. , KUECHLER, Keith, H. , SKOUBY, David, C. , SUN, Hsiang-ning
IPC分类号： C10G3/00
CPC分类号： C10G3/62 , C10G3/49 , C10G2300/4006 , C10G2300/4018 , C10G2300/4081 , C10G2300/802 , C10G2400/20 , Y02P30/20 , Y02P30/42
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公开(公告)号：EP1392626A1
公开(公告)日：2004-03-03
申请号：EP02769432.2
申请日：2002-03-15
发明人： COUTE, Nicolas, P. , KUECHLER, Keith, H. , CHISHOLM, Paul, N. , VAUGHN, Stephen, N. , LATTNER, James, R. , KUECHLER, W., L., Sr.
CPC分类号： C10G3/57 , B01J29/90 , B01J38/30 , C07C1/20 , C07C2529/85 , C10G3/49 , C10G2300/4006 , C10G2300/4018 , C10G2400/20 , Y02P20/52 , Y02P20/582 , Y02P20/584 , Y02P30/42 , C07C11/04 , C07C11/06
摘要： Disclosed is a method for converting an oxygenate feedstock to an olefin product. In particular, the method incorporates the use of a silicoaluminophosphate molecular sieve catalyst in the manufacture of ethylene and propylene. The method includes contacting an oxygenate-containing feedstock with a silicoaluminophosphate molecular sieve catalyst to form the olefin-containing product in a fluidized bed reactor apparatus including at least a reaction zone and a recirculation zone. Certain ratios of the mass of catalyst in the reaction zone to that of the sum of the mass of catalyst in both the reaction zone and the recirculation zone within the reactor apparatus are specified.
摘要翻译： 公开了一种将含氧化合物原料转化成烯烃产物的方法。 具体而言，该方法结合使用硅铝磷酸盐分子筛催化剂来制造乙烯和丙烯。 该方法包括使含氧化合物的原料与硅铝磷酸盐分子筛催化剂接触以在包括至少反应区和再循环区的流化床反应器装置中形成含烯烃的产物。 规定了反应区中催化剂质量与反应器装置内反应区和再循环区中催化剂质量总和的比值。
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公开(公告)号：EP0923511B1
公开(公告)日：2001-10-24
申请号：EP97940688.1
申请日：1997-08-29
CPC分类号： B01J8/20 , B01J8/003 , B01J8/006 , B01J2208/00132 , B01J2208/00176 , B01J2208/00194 , B01J2208/003 , B01J2219/00033 , C07C5/2556 , C07C2521/04 , C07C2523/04 , C07C2602/20 , C07C2602/42 , Y10S585/921 , Y10S585/924 , Y10S585/925 , C07C13/43
摘要： The present invention is directed to a continuous process for producing a desired hydrocarbon product using a heterogeneous slurry catalyst, to the product of said process, and to the reactor utilized in such process.
摘要翻译： 本发明涉及使用非均相淤浆催化剂，所述方法的产物和在该方法中使用的反应器生产所需烃产物的连续方法。
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公开(公告)号：EP0929502B1
公开(公告)日：2001-08-01
申请号：EP97940865.5
申请日：1997-09-05
IPC分类号： C07C2/00
CPC分类号： C10G29/205 , C07C2/66 , C07C15/02 , C07C15/073 , C07C2529/70 , Y02P20/127 , Y10S203/06
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