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    • 4. 发明申请
    • Fluid Contact Tray Particularly for the use in an Offshore Fractionation Column
    • US20170348609A1
    • 2017-12-07
    • US15537811
    • 2015-08-17
    • Sulzer Chemtech AG
    • Stephen ShieldsSenthil KrishnamoorthyMarkus Duss
    • B01D3/24B01D3/20B01D1/00
    • B01D3/24B01D1/0005B01D3/20B01D3/22B01D3/225B01D3/30B01D3/324
    • A fluid contact tray (10) for a fractionation column (1), in particular a vapor-liquid contact tray suitable for the use in an offshore fractionation column, comprises: •a tray deck (12) comprising an active mass transfer surface (20) suitable for contacting two fluids (l, g) of different densities, wherein the active mass transfer surface (20) comprises one or more orifices (18) for the passage of a fluid/gas (g), and wherein at least two at least partially radially extending separation walls (22-1, 22-2, 22-3, 22-4) and/or at least one separation weir (42) are arranged on the active mass transfer surface (20), which divides the active mass transfer surface (20) into at least two sections (24-1, 24-2, 24-3, 24-4), •an annular channel (26) suitable for collecting fluids/liquids (l), which is arranged at the peripheral area of the active mass transfer surface (20) and at least partially embraces the mass transfer surface (20), •a central downcomer (34) for collecting and discharging a fluid/liquid (l) from the annular channel (26), wherein the central downcomer (34) has the form of a hollow body with an opening (36) in the bottom section thereof being suitable for the distribution of liquid vertically downwardly, and wherein the central downcomer (34) is non-rotatably fixed at the fluid contact tray (10), and •at least one conducting means (40) for transferring fluid collected in the annular channel (26) from the annular channel (26) to the central downcomer (34). This fluid contact tray (10) is in particular useable for offshore applications, such as for a fractionation column located on a FLNG or FPSO vessel.
    • 6. 发明申请
    • Method to Minimize the Transition Time From One Polymer Grade to Another Polymer Grade in a Polymerization Plant
    • US20170240699A1
    • 2017-08-24
    • US15510046
    • 2015-09-01
    • Sulzer Chemtech AG
    • Liborio Ivano CostaFabio Codari
    • C08G63/78C08G63/08
    • C08G63/785C08G63/08
    • The present invention relates to a method for reducing the transition time and/or the polymer waste being out of the specification during the change from a first polymer grade to a second polymer grade in a continuous polymerization process conducted in a polymerization plant, wherein the polymerization plant comprises at least one back-mixing reactor, at least one monomer and at least one processing agent selected from the group consisting of catalysts, co-catalysts, polymerization initiators, comonomers, chain-transfer agents, branching agents, solvents and arbitrary combinations of two or more of the aforementioned agents are added before and/or during the polymerization process into the at least one back-mixing reactor, wherein the concentration of one or more of the at least one added processing agent in the feed introduced into the at least one back-mixing reactor is varied as a function of time from a first value associated with the first polymer grade to a final value associated with the second polymer grade, —the first polymer grade and the second polymer grade are one or more parameters related to the molecular weight of the polymer to be produced and/or one or more parameters related to the composition of the polymer to be produced and/or one or more parameters related to the structure of the polymer to be produced and/or one or more parameters related to the amount of the polymer to be produced, wherein during the variation of the concentration of the at least one added processing agent from the first value to the final value one or more intermediate values are adjusted, wherein at least one, preferably the majority and more preferably all of the one or more intermediate values are closer to the final value than to the first value, wherein the absolute difference between the at least one, preferably each of the majority and more preferably each of all of the one or more intermediate values from the first value is greater than the absolute difference between the final and the first value, wherein the one or more intermediate values are maintained for a time which is calculated on the basis of only residence time in the at least one back-mixing reactor and steady-state correlations between input and output of the reactor and/or of the polymerization plant, and wherein the method is performed without performing dynamic modelling.
    • 8. 发明授权
    • Packing element, method to produce it and a column or reactor comprising said element
    • 包装元件,其制造方法和包括所述元件的柱或反应器
    • US09452412B2
    • 2016-09-27
    • US14388364
    • 2012-12-14
    • Sulzer Chemtech AG
    • Ilja AusnerFlorian Kehrer
    • B01F3/04B01J19/30B29C45/00B29L31/18
    • B01J19/30B01F3/04468B01F3/04496B01J2219/30207B01J2219/30211B01J2219/30276B01J2219/30408B01J2219/30416B01J2219/30466B01J2219/30483B01J2219/3083B01J2219/312B01J2219/318B01J2219/3183B29C45/00B29L2031/18Y10T29/49
    • A packing element (1) for use in mass and/or heat transfer processes through which at least one liquid may flow, wherein the packing element (1): has an outer surface (2) comprising three or more outer arched rib elements (21) and two outer connecting edge elements (22), optionally has an inner surface (3) comprising optional inner arched rib elements (31), wherein the element 1 is substantially spherical or substantially ellipsoidal, and wherein the outer connecting edge elements (22) and the outer arched rib elements (21) and optional inner arched rib elements (31) are embodied such that the total projected area (4) of the packing element (1) when viewed in any direction (7), preferably a radial direction (5) or optional axial direction (6), is partially open due to the presence of an open projected area (41), wherein it is open to an extent that ranges from about 15 to about 50, preferably about 17 to about 40, more preferably about 18 to about 35, most preferably about 20 to about 30% of the total projected area (4). The invention further relates to a method for producing said element (1). The present invention further relates also to a column or reactor comprising a bed of said elements (1), a method to prepare said bed, and the use of the element (1) or column or reactor in a mass transfer and/or heat transfer process and/or in a chemical reaction.
    • 一种用于质量和/或热传递过程的填料元件(1),至少一种液体可通过所述填料元件(1)流动,其中所述填料元件(1)具有包括三个或更多个外部拱形肋元件(21)的外表面(2) )和两个外部连接边缘元件(22),可选地具有包括任选的内部拱形肋元件(31)的内表面(3),其中元件1基本上是球形或基本上椭圆形的,并且其中外部连接边缘元件(22) 并且外部拱形肋元件(21)和可选的内部拱形肋元件(31)被实施为使得当从任何方向(7)观察时,包装元件(1)的总投影面积(4),优选地沿径向方向 5)或可选的轴向方向(6)由于存在开放的投影区域(41)而部分打开,其中其开口的范围为约15至约50,优选约17至约40,更大 优选约18至约35,最优选约20至约 占总预计面积的30%(4)。 本发明还涉及一种用于生产所述元件(1)的方法。 本发明还涉及包括所述元件(1)的床,制备所述床的方法以及在传质和/或传热中使用元件(1)或塔或反应器的塔或反应器 过程和/或化学反应。
    • 10. 发明申请
    • A Liquid-Liquid Extraction System and Process for use Thereof
    • 液 - 液萃取系统及其使用方法
    • US20150314217A1
    • 2015-11-05
    • US14650926
    • 2013-11-27
    • SULZER CHEMTECH AG
    • Jörg KochJuan Ramon Herguijuela
    • B01D11/04B01F3/08
    • B01D11/043B01D11/0434B01D11/0457B01D11/0488B01D21/0039B01D21/10B01D2011/002B01F3/0873
    • A liquid-liquid extraction system (1) adapted for the flow of two or more liquids therein is disclosed. The system comprises a mixer settler sub-system (100) and a counter-current liquid-liquid extraction column (200). The sub-system (100) comprises one or more mixer settlers (110) connected in series, and the column (200) comprises either a mixing section (260) comprising an agitation means (261) and/or a static section (280) comprising an internal (281). The first outlet (131) of the mixer settler sub-system (100) is in fluid communication with the first inlet (221) of the column (200) and the second inlet (112) of the mixer settler sub-system (100) is in fluid communication with the second inlet (222) of the counter-current liquid-liquid extraction column (200). The invention further relates to a counter-current liquid-liquid extraction process for using said system 1. The present invention further relates also to the use of the system (5) or process in removing aromatic compounds from organic streams, in treating an oil stream of a refinery, or in a liquid-liquid extraction process having at least two feed streams of different viscosity, similar density, or low interfacial tension.
    • 公开了一种适于在其中流动两种或多种液体的液体 - 液体萃取系统(1)。 该系统包括混合沉降器子系统(100)和逆流液 - 液萃取塔(200)。 子系统(100)包括串联连接的一个或多个混合器沉降器(110),并且塔(200)包括混合部分(260),其包括搅拌装置(261)和/或静止部分(280) 包括内部(281)。 混合器沉降器子系统(100)的第一出口(131)与混合器沉降器子系统(100)的塔(200)的第一入口(221)和混合器沉降器子系统(100)的第二入口(112)流体连通, 与逆流液 - 液萃取塔(200)的第二入口(222)流体连通。 本发明还涉及用于使用所述系统1的逆流液 - 液萃取方法。本发明还涉及系统(5)或方法在从有机物流中除去芳族化合物的过程中的用途,用于处理油流 炼油厂或具有至少两种不同粘度,相似密度或低界面张力的进料流的液 - 液萃取方法。