专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

41. 发明申请

US20130006029A1 HYDROTREATING PROCESS 有权
标题翻译：加氢过程
公开(公告)号：US20130006029A1
公开(公告)日：2013-01-03
申请号：US13575849
申请日：2011-02-21
申请人： Gabor Kiss , Iulian Nistor , John Zengel , Sabato Miseo , Roman Krycak , Teh C. Ho
发明人： Gabor Kiss , Iulian Nistor , John Zengel , Sabato Miseo , Roman Krycak , Teh C. Ho
IPC分类号： C07C1/32
CPC分类号： C10G49/24 , B01J38/56 , C10G45/02 , C10G45/08 , C10G2300/1055 , C10G2300/1096 , C10G2300/202 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/04
摘要： A process for hydrotreating a first aromatics- and sulfur-containing hydrocarbon feed using a fresh supported CoMo catalyst, includes treating the fresh catalyst under first hydrotreating conditions with a second hydrocarbon feed having a lower aromatics content than the first feed.
摘要翻译：使用新鲜负载的CoMo催化剂加氢处理第一芳烃和含硫烃进料的方法包括在第一加氢处理条件下用比第一进料芳烃含量低的第二烃进料处理新鲜催化剂。

42. 发明申请

US20110196116A1 POLYMERIZATION PROCESSES FOR BROADENED MOLECULAR WEIGHT DISTRIBUTION 审中-公开
公开(公告)号：US20110196116A1
公开(公告)日：2011-08-11
申请号：US13088642
申请日：2011-04-18
申请人： Gabor Kiss , Robert Patrick Reynolds, JR. , John W. Chu , Patrick Brant , James Richardson Lattner
发明人： Gabor Kiss , Robert Patrick Reynolds, JR. , John W. Chu , Patrick Brant , James Richardson Lattner
IPC分类号： C08F4/00 , C08F4/42
CPC分类号： C08F10/00 , C08F110/06 , C08F2/06 , C08F2/01 , C08F2500/04
摘要： Provided are methods of producing polymers with broadened molecular weight and/or composition distribution in a continuous homogeneous polymerization system utilizing reactor temperature gradients, reactor polymer concentration gradients, monomer concentration gradients, catalyst concentration gradients, and combinations thereof in the polymerization reactor. Such methods are particularly suitable when utilizing metallocene catalysts and other single-site catalysts, which generally produce polymers with narrow molecular weight and composition distribution.

43. 发明授权

US07939610B2 Polymerization processes for broadened molecular weight distribution 有权
标题翻译：用于扩大分子量分布的聚合方法
公开(公告)号：US07939610B2
公开(公告)日：2011-05-10
申请号：US12454514
申请日：2009-05-19
申请人： Gabor Kiss , Robert Patrick Reynolds, Jr. , John W. Chu , Patrick Brant , James Richardson Lattner
发明人： Gabor Kiss , Robert Patrick Reynolds, Jr. , John W. Chu , Patrick Brant , James Richardson Lattner
IPC分类号： C08F2/00 , C08F4/00 , C08F110/06
CPC分类号： C08F10/00 , C08F110/06 , C08F2/06 , C08F2/01 , C08F2500/04
摘要： Provided are methods of producing polymers with broadened molecular weight and/or composition distribution in a continuous homogeneous polymerization system utilizing reactor temperature gradients, reactor polymer concentration gradients, monomer concentration gradients, catalyst concentration gradients, and combinations thereof in the polymerization reactor. Such methods are particularly suitable when utilizing metallocene catalysts and other single-site catalysts, which generally produce polymers with narrow molecular weight and composition distribution.
摘要翻译：提供了在聚合反应器中使用反应器温度梯度，反应器聚合物浓度梯度，单体浓度梯度，催化剂浓度梯度及其组合的连续均匀聚合体系中制备具有更宽分子量和/或组成分布的聚合物的方法。当使用茂金属催化剂和其它通常产生具有窄分子量和组成分布的聚合物的其它单中心催化剂时，这些方法是特别合适的。

44. 发明授权

US07910679B2 Bulk homogeneous polymerization process for ethylene propylene copolymers 有权
标题翻译：乙烯丙烯共聚物的均匀聚合方法
公开(公告)号：US07910679B2
公开(公告)日：2011-03-22
申请号：US12291898
申请日：2008-11-14
申请人： Gabor Kiss , Robert Patrick Reynolds, Jr. , John W. Chu , Steven P. Rucker , James Richardson Lattner
发明人： Gabor Kiss , Robert Patrick Reynolds, Jr. , John W. Chu , Steven P. Rucker , James Richardson Lattner
IPC分类号： C08F2/02 , C08F210/06 , C08F4/643
CPC分类号： C08F210/16 , C08F4/65908 , C08F4/65927 , C08F210/06 , Y10S526/902 , C08F2/02 , C08F2/14 , C08F2500/03 , C08F2500/12
摘要： Provided are bulk homogeneous polymerization processes for producing ethylene propylene random copolymers. The process includes contacting in a reactor or in a series of reactors propylene monomer, ethylene comonomer with one or more catalyst systems and optional solvent (present at less than 40 wt %), wherein the reactor train is at a temperature of between 65° C. and 180° C. and at a pressure no lower than 10 MPa below the cloud point pressure of the polymerization system and less than 1500 MPa, and wherein the polymerization system for the reactor train is in its dense fluid state to form a polymer reactor effluent including a homogeneous fluid phase polymer-monomer mixture in the reactor train; and wherein the resultant copolymer product comprises between 10 wt % and 20 wt % randomly distributed ethylene and the concentration of total region defects in the continuous propylene segments of the random EP copolymer is between 40 and 150% greater than in a copolymer of equivalent melt flow rate and wt % ethylene polymerized by a solution polymerization process.
摘要翻译：提供用于生产乙烯丙烯无规共聚物的本体均相聚合方法。该方法包括使反应器或一系列反应器中的丙烯单体，乙烯共聚单体与一种或多种催化剂体系和任选的溶剂（以小于40wt％存在）接触，其中反应器系在65℃ 并且在低于聚合体系的浊点压力不低于10MPa的压力下低于1500MPa，并且其中反应器系列的聚合系统处于其致密的流体状态以形成聚合物反应器流出物包括在反应器系列中的均相流体相聚合物 - 单体混合物; 并且其中所得共聚物产物包含10重量％至20重量％的随机分布的乙烯，并且随机EP共聚物的连续丙烯链段中总区域缺陷的浓度比当量熔体流动的共聚物中的区域间缺陷的浓度高40至150％速率和wt％乙烯通过溶液聚合方法聚合。

45. 发明申请

US20090076214A1 In-line blending of plasticizers with a base polymer 有权
标题翻译：增塑剂与基础聚合物的在线共混
公开(公告)号：US20090076214A1
公开(公告)日：2009-03-19
申请号：US12283046
申请日：2008-09-09
申请人： Gabor Kiss , Alan Anthony Galuska
发明人： Gabor Kiss , Alan Anthony Galuska
IPC分类号： C08L23/00
CPC分类号： C08F10/00 , C08F210/16 , C08F2/001 , C08F2/01 , C08F210/14 , C08F2500/12 , C08F2500/08 , C08F2500/20
摘要： A process for in-line blending of plasticizers and polymers is provided. The process includes providing a single reactor train including one or more serially configured reactors, a high-pressure separator downstream fluidly connected to the reactor train, and one or more storage tanks, wherein the reactor train produces one or more base polymer components and the one or more storage tanks store one or more off-line produced plasticizers; contacting in the reactor train olefin monomers, catalyst systems, optional comonomers, optional scavengers, and optional diluents or solvents, at a temperature above the solid-fluid phase transition temperature of the polymerization system and a pressure no lower than 10 MPa below the cloud point pressure of the polymerization system and less than 1500 MPa, forming a reactor effluent including a homogeneous fluid phase polymer-monomer mixture; passing the reactor effluent through the separator to separate a monomer-rich phase from a polymer-rich phase; and feeding the plasticizers to the process after the reactor train and while the base polymer still has a substantial quantity of light components to form a plasticized polymer blend with improved blend quality.
摘要翻译：提供了一种用于在线共混增塑剂和聚合物的方法。该方法包括提供包括一个或多个串联配置的反应器，流体连接到反应器列的下游的高压分离器和一个或多个储罐的单个反应器系列，其中反应器系统产生一个或多个基础聚合物组分，或更多储存罐存储一个或多个离线生产的增塑剂; 在高于聚合体系的固体 - 流体相转变温度的温度和不低于浊点10MPa的压力下，在反应器中与烯烃单体，催化剂体系，任选的共聚单体，任选的清除剂和任选的稀释剂或溶剂接触聚合体系的压力小于1500MPa，形成包含均相流体相聚合物 - 单体混合物的反应器流出物; 使反应器流出物通过分离器以将富单体相与富聚合物相分离; 并且在反应器列车之后将增塑剂进料到工艺中，而基础聚合物仍然具有大量的轻组分以形成具有改进的混合质量的增塑聚合物共混物。

46. 发明申请

US20060025545A1 Polymer production at supercritical conditions 审中-公开
公开(公告)号：US20060025545A1
公开(公告)日：2006-02-02
申请号：US11177004
申请日：2005-07-08
申请人： Patrick Brant , Francis Rix , Gabor Kiss , Robert Reynolds
发明人： Patrick Brant , Francis Rix , Gabor Kiss , Robert Reynolds
IPC分类号： C08F2/00
CPC分类号： C08F110/06 , C08F4/65912 , C08F10/00 , C08F10/06 , C08F210/06 , Y02P20/544 , C08F4/65927 , C08F2/06 , C08F2/00 , C08F2/14 , C08F2500/23 , C08F2500/15 , C08F2500/20 , C08F2500/09 , C08F2500/12 , C08F2500/01 , C08F2500/03 , C08F2500/17 , C08F210/14
摘要： This invention relates to a process to polymerize olefins comprising contacting, in a polymerization system, olefins having three or more carbon atoms with a catalyst compound, activator, optionally comonomer, and optionally diluent or solvent, at a temperature above the cloud point temperature of the polymerization system and a pressure no lower than 10 MPa below the cloud point pressure of the polymerization system, where the polymerization system comprises any comonomer present, any diluent or solvent present, the polymer product, where the olefins having three or more carbon atoms are present at 40 weight % or more, wherein the metallocene catalyst compound is represented by the formula: where M is a transition metal selected from group 4 of the periodic table; each R1 is independently selected from the group consisting of hydrogen, hydrocarbyl, substituted hydrocarbyl and functional group, and any two R1 groups may be linked, provided that if the two R1 groups are linked, then they do not form a butadiene group when M is Zr; each R2 is independently selected from the group consisting of hydrogen, hydrocarbyl, substituted hydrocarbyl or a functional group, and two or more R2 groups may be linked together to form an aliphatic or aromatic ring; R3 is carbon or silicon; R4 is hydrogen, hydrocarbyl, substituted hydrocarbyl or a functional group; a is 0, 1, or 2; R5 is hydrogen, hydrocarbyl, substituted hydrocarbyl or a functional group, R4 and R5 may be bound together to form a ring, and R5 and R3 may be bound together to form a ring; b is 0, 1, or 2; R6 is carbon or silicon; and R4 and R6 may be bound together to form a ring; each R7 is independently selected from the group consisting of hydrogen, hydrocarbyl, substituted hydrocarbyl and a functional group; each R8 is independently selected from the group consisting of hydrogen, hydrocarbyl, substituted hydrocarbyl and a functional group, and R7 and R8 may be linked together to form an aliphatic or aromatic ring; each R9 is independently selected from the group consisting of hydrogen, hydrocarbyl, substituted hydrocarbyl and a functional group, and two R9 groups may be linked together to form a ring, R9 and R8 may be linked together to form a ring, R9 and R16 may be linked together to form a ring, R9 and R11 may be linked together to form a ring; c is 0, 1 or 2; R10 is -M2(R16)h- where M2 is B, Al, N, P, Si or Ge, h is an integer from 1 to 2, such that the valence of M2 is filled, and R16 is hydrogen, hydrocarbyl, substituted hydrocarbyl or a functional group, and two R16 groups may be linked together to form a ring; d is 0, 1, or 2; each R11 is independently selected from the group consisting of hydrogen, hydrocarbyl, substituted hydrocarbyl and a functional group, and two R11 groups may be linked together to form a ring. R11 and R8 may be linked together to form a ring. R11 and R16 may be linked together to form a ring; e is 0, 1, or 2; where the sum of c, d, and e is 1, 2 or 3; R12 is carbon or silicon; R13 is hydrogen, hydrocarbyl, substituted hydrocarbyl or a functional group, and R13 and R14 may be bound together to form a ring, and R13 and R15 may be bound together to form a ring, when g is 0; f is 0, 1, or 2; R14 is hydrogen, hydrocarbyl, substituted hydrocarbyl or a functional group, and R14 and R12 may be bound together to form a ring, when f is 0; g is 0, 1, or 2; and R15 is carbon or silicon.

47. 发明申请

US20050114541A1 Scalable and dynamic quality of service control 有权
标题翻译：可扩展和动态的服务质量控制
公开(公告)号：US20050114541A1
公开(公告)日：2005-05-26
申请号：US10706796
申请日：2003-11-12
申请人： Andrei Ghetie , Harshad Tanna , John Unger , Gabor Kiss , Vincent Massa
发明人： Andrei Ghetie , Harshad Tanna , John Unger , Gabor Kiss , Vincent Massa
IPC分类号： G06F15/16 , G06F15/173 , H04L12/56 , H04L29/08
CPC分类号： H04L67/322 , H04L47/10 , H04L47/20 , H04L47/22 , H04L47/2408 , H04L47/2425 , H04L47/2491 , H04L47/781 , H04L47/805 , H04L67/327
摘要： Applications and users dynamically make QoS provisioning requests for individual traffic flows traversing client and server hosts. A traffic flow provisioning request is conveyed to a services manager, which determines a set of traffic attributes for the flow and determines the networks the flow traverses between the client and server hosts. The services manger then oversees the admission of the flow to appropriate traffic classes in each determined network and the obtaining of a DSCP value for each network. Lastly, the services manger conveys the DSCP value of the first network traversed back to the client or server host, depending on the direction of the flow, which host is then configured to appropriately mark the DSCP field of the traffic flow packets. In a further embodiment, the services manager also instructs the client or server host to perform packet policing and shaping for the flow.
摘要翻译：应用程序和用户动态地为穿过客户端和服务器主机的各个流量动态地提供QoS配置请求。业务流量配置请求被传送到服务管理器，服务管理器确定流的一组业务属性，并确定流在客户端和服务器主机之间的网络。然后，服务管理员将流量接纳到每个确定的网络中的适当流量类别并获得每个网络的DSCP值。最后，服务管理器将第一个网络的DSCP值传送回客户端或服务器主机，具体取决于流的方向，然后将哪个主机配置为适当地标记业务流分组的DSCP字段。在另一实施例中，服务管理器还指示客户端或服务器主机对流进行分组管理和整形。

48. 发明授权

US5675041A Direct hydroformylation of a multi-component synthesis gas containing carbon monoxide, hydrogen, ethylene, and acetylene 失效
标题翻译：含有一氧化碳，氢气，乙烯和乙炔的多组分合成气的直接加氢甲酰化
公开(公告)号：US5675041A
公开(公告)日：1997-10-07
申请号：US573052
申请日：1995-12-15
申请人： Gabor Kiss , Frank Hershkowitz , Harry W. Deckman , Michael Gerard Matturro , Istvan T. Horvath , Anthony M. Dean , Raymond A. Cook
发明人： Gabor Kiss , Frank Hershkowitz , Harry W. Deckman , Michael Gerard Matturro , Istvan T. Horvath , Anthony M. Dean , Raymond A. Cook
IPC分类号： C07C45/50
CPC分类号： C07C45/50 , Y02P20/582
摘要： The invention is a process for production of C.sub.3 to C.sub.6 aldehydes by hydroformylating a mixture containing: (a) C.sub.2 to C.sub.5 olefins and mixtures thereof, and (b) (i) C.sub.2 to C.sub.5 alkynes and mixtures thereof or (ii) C.sub.3 to C.sub.5 cumulated dienes and mixtures thereof or (iii) mixtures of (i) and (ii), with CO, H.sub.2 and a solution of a rhodium complex catalyst produced by complexing Rh and an organophosphorus compound at a concentration of Rh in solution from 1 to 1000 ppm by weight. Alternatively, the solution of rhodium complex catalyst can have a P/Rh atom ratio of at least 30. Alternatively, the solution of rhodium complex catalyst can have a P/Rh atom ratio greater than the value R.sub.L defined by the formula: ##EQU1## in which R.sub.B is the P/Rh ratio sufficient for a catalytically active Rh complex, pKa.sub.TPP is the pKa value for triphenylphosphine, pKa.sub.L is the pKa value for the triorganophosphorus compound, R is the gas constant, and .DELTA.S.sub.B is 35(N-1) cal/mole/.degree.K., N is the number of P-Rh attachments per ligand molecule. The process has utility for the hydroformylation of streams that contain olefins and alkynes.
摘要翻译：本发明是通过加氢甲酰化含有：（a）C 2〜C 5烯烃及其混合物的混合物，和（b）（ⅰ）C2〜C5炔烃及其混合物或（ⅱ）C3〜C5 累积的二烯及其混合物，或（iii）（ⅰ）和（ⅱ）的混合物与CO，H 2和铑络合物催化剂的溶液形成，所述铑配合物催化剂是通过使Rh和溶液中Rh浓度为1〜1000的有机磷化合物重量ppm。或者，铑络合物催化剂的溶液的P / Rh原子比可以至少为30.另外，铑络合物催化剂的溶液可以具有大于由下式定义的值RL的P / Rh原子比：其中RB是催化活性Rh配合物的P / Rh比，pKaTPP是三苯基膦的pKa值，pKaL是三有机磷化合物的pKa值，R是气体常数，DELTA SB是35（N-1 ）cal / mole / DEGK，N是每个配体分子的P-Rh附着物的数目。该方法可用于含有烯烃和炔烃的物流的加氢甲酰化。

49. 发明授权

US5276226A Low temperature halogenation of alkanes 失效
标题翻译：低温卤化烷烃
公开(公告)号：US5276226A
公开(公告)日：1994-01-04
申请号：US956706
申请日：1992-10-05
申请人： Istvan T. Horvath , Raymond A. Cook , Gabor Kiss
发明人： Istvan T. Horvath , Raymond A. Cook , Gabor Kiss
IPC分类号： C07C17/10 , C07C17/00 , C07C19/00
CPC分类号： C07C17/10
摘要： The invention relates to a process for selectively producing alkyl halides from alkanes, such as methane and ethane at relatively mild temperatures and pressures in an organic liquid phase in the presence of halogen and transition metal complex. The alkane may be neat if in a liquid form, or may be solubilized with a suitable organic solvent, if the alkane not a liquid at reaction conditions. The reaction is for a time, under conditions of temperature and pressure and in effective amounts that will permit the formation of alkyl halides. Optional hydrolysis to the corresponding alcohols may follow. The alkyl halides have utility as precursors for alternative fuels, such as methanol.
摘要翻译：本发明涉及在卤素和过渡金属络合物存在下，在有机液相中相对温和的温度和压力下从烷烃如甲烷和乙烷中选择性地制备烷基卤的方法。如果在反应条件下烷烃不是液体，则烷烃可以是纯的，如果是液体形式，或者可以用合适的有机溶剂溶解。在温度和压力的条件下反应一段时间，并且有效量可以形成烷基卤。可以按照相应的醇进行任选的水解。烷基卤化物可用作替代燃料（例如甲醇）的前体。

50. 发明授权

US09061974B2 Process for producing phenol 有权
标题翻译：苯酚生产工艺
公开(公告)号：US09061974B2
公开(公告)日：2015-06-23
申请号：US14110266
申请日：2011-12-15
申请人： Kun Wang , Roberto Garcia , Gabor Kiss
发明人： Kun Wang , Roberto Garcia , Gabor Kiss
IPC分类号： C07C37/08 , C07C45/53 , C07C2/74 , C07C407/00 , C07C249/08 , C07C51/31 , B01J29/08 , B01J29/90 , B01J29/06
CPC分类号： C07C37/08 , B01J29/06 , B01J29/08 , B01J29/90 , C07C2/74 , C07C45/53 , C07C51/31 , C07C249/08 , C07C407/00 , C07C2529/89 , C07C2601/14 , Y02P20/52 , Y02P20/584 , Y02P20/588 , C07C55/14 , C07C39/04 , C07C49/403 , C07C13/28 , C07C409/14 , C07C251/44
摘要： A process for producing phenol is described in which a feed comprising cyclohexylbenzene hydroperoxide is contacted with a cleavage catalyst comprising an aluminosilicate zeolite of the FAU type having a unit cell size less than 24.50 Å under cleavage conditions effective to convert at least part of the cyclohexylbenzene hydroperoxide into phenol and cyclohexanone.
摘要翻译：描述了一种生产苯酚的方法，其中包含环己基苯氢过氧化物的进料与裂解催化剂接触，裂解催化剂包含具有小于24.50埃的单元电池尺寸的FAU型铝硅酸盐沸石，在有效地转化至少部分环己基苯氢过氧化物转化成苯酚和环己酮。

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