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    • 7. 发明申请
    • VESSEL FOR SEPARATING COMPONENTS OF A REACTION MIXTURE OBTAINED BY HIGH-PRESSURE POLYMERIZATION OF ETHYLENICALLY UNSATURATED MONOMERS WITH INTEGRATED BURSTING DISCS
    • 用于分离由具有整体冲击盘的乙烯基不饱和单体的高压聚合获得的反应混合物的组分的容器
    • WO2015091384A1
    • 2015-06-25
    • PCT/EP2014/077810
    • 2014-12-15
    • BASELL POLYOLEFINE GMBH
    • NEUMANN, ErichKHAYRULLIN, DanirFIBLA, Claudio
    • B01J3/00
    • C08F6/10B01D19/0036B01D19/0063B01J3/002B01J19/2415B01J2219/185B01J2219/1943B01J2219/1946C08F10/02Y02P20/582
    • Vessel for separating, at a pressure of from 10 MPa to 50 MPa, a composition comprising liquid components and gaseous components into a liquid fraction and a gaseous fraction, wherein the separation vessel has a cylindrical shape and is vertically arranged, the separation vessel has at its top a manhole, which is surrounded by a thickened part of the separation vessel wall; the separation vessel is equipped with means for introducing the composition into the separation vessel, with means for withdrawing a gaseous fraction from the top of the separation vessel, and with means for withdrawing a liquid fraction from the bottom of the separation vessel; and the separation vessel bears at least one bursting disc which is held by a bursting disc holder which is installed pressure-tight within a boring in the thickened part of the separation vessel wall, process for separating, at a pressure of from 10 MPa to 50 MPa, a composition comprising liquid components and gaseous components into a liquid fraction and a gaseous fraction, and process for preparing ethylene homopolymers or copolymers from ethylenically unsaturated monomers in the presence of free-radical polymerization initiators at temperatures from 100°C to 350°C and pressures in the range of from 1 10 MPa to 500 MPa in a polymerization reactor, wherein the separation of the reaction mixture obtained by the polymerization is carried out in such a separation vessel.
    • 用于在10MPa至50MPa的压力下将包含液体组分和气体组分的组合物分离成液体馏分和气体馏分的容器,其中分离容器具有圆柱形并且垂直布置,分离容器具有 其顶部是孔洞,其被分离容器壁的增厚部分包围; 分离容器配备有用于将组合物引入分离容器的装置,具有用于从分离容器的顶部排出气态馏分的装置,以及用于从分离容器的底部排出液体部分的装置; 并且分离容器承载至少一个破裂盘,该破裂盘由在压力较高的分离容器壁的增厚部分的镗孔内安装的爆破盘保持器保持,在10MPa至50℃的压力下分离 MPa,将包含液体组分和气态组分的组合物加入到液体馏分和气体馏分中,以及在自由基聚合引发剂存在下,在100℃至350℃的温度下由烯属不饱和单体制备乙烯均聚物或共聚物的方法 并且在聚合反应器中的压力范围为10MPa至500MPa,其中通过聚合获得的反应混合物的分离在这种分离容器中进行。
    • 8. 发明申请
    • PROCESS FOR THE GAS-PHASE POLYMERIZATION OF ETHYLENE OR ETHYLENE MIXTURES
    • 乙烯或乙烯混合物的气相聚合方法
    • WO2014184155A1
    • 2014-11-20
    • PCT/EP2014/059685
    • 2014-05-13
    • BASELL POLYOLEFINE GMBH
    • MEI, GabrieleBAITA, PietroMARTURANO, LorellaMAZZUCCO, AntonioPICA, RobertaMEIER, GerhardusSCHUELLER, Ulf
    • C08F2/34C08F110/02
    • C08F110/02C08F2/001C08F2/002C08F4/654C08F4/6543C08F4/6548C08F4/655C08F4/6565C08F10/02C08F2/34C08F2500/18C08F2500/24C08F4/6492C08F4/6425
    • A process for the gas-phase polymerization of ethylene or a mixture of ethylene and one or more 1-olefins in the presence of a polymerization catalyst system comprising the steps a) feeding a solid catalyst component, which was obtained by contacting at least a magnesium compound and a titanium compound, to a continuously operated apparatus and contacting the solid catalyst component with an aluminum alkyl compound at a temperature of from 0°C to 70°C in a way that the mean residence time of the solid catalyst component in contact with the aluminum alkyl compound is from 5 to 300 minutes; b) transferring the catalyst component formed in step a) into another continuously operated apparatus and prepolymerizing it with ethylene or a mixture of ethylene and one or more 1-olefins in suspension at a temperature of from 10°C to 80° forming polymer in an amount of from 0.2 to 25 g polymer/g of solid catalyst component in a way that the mean residence time of the solid catalyst component in the apparatus is from 5 minutes to 3 hours; and c) transferring the prepolymerized catalyst component formed in step b) into a gas-phase polymerization reactor and polymerizing ethylene or a mixture of ethylene and one or more 1-olefins in the presence of the prepolymerized catalyst component at temperatures of from 40°C to 120°C and pressures of from 0.1 to 10 MPa.
    • 一种在聚合催化剂体系存在下乙烯或乙烯与一种或多种1-烯烃的混合物进行气相聚合的方法,包括以下步骤:a)加入固体催化剂组分,所述固体催化剂组分通过使至少一种镁 化合物和钛化合物连接到连续操作的装置上,并使固体催化剂组分与烷基铝化合物在0℃至70℃的温度下接触,使得固体催化剂组分的平均停留时间与 铝烷基化合物为5〜300分钟; b)将步骤a)中形成的催化剂组分转移到另一个连续操作的装置中,并将其与乙烯或乙烯和一种或多种1-烯烃的混合物在10℃至80℃的温度下预聚合形成聚合物 以固体催化剂组分在设备中的平均停留时间为5分钟至3小时的方式,其量为0.2至25g聚合物/ g固体催化剂组分; 和c)将步骤b)中形成的预聚合的催化剂组分转移到气相聚合反应器中,并在预聚合的催化剂组分存在下在40℃的温度下聚合乙烯或乙烯和一种或多种1-烯烃的混合物 至120℃,压力为0.1至10MPa。
    • 10. 发明申请
    • PROCESS FOR MONITORING THE POLYMERIZATION OF ETHYLENE OR ETHYLENE AND COMONOMERS IN A TUBULAR-REACTOR AT HIGH-PRESSURES
    • 用于监测高压管状反应器中乙烯或乙烯和共聚物聚合的方法
    • WO2012084772A1
    • 2012-06-28
    • PCT/EP2011/073176
    • 2011-12-19
    • BASELL POLYOLEFINE GMBHWEIAND, SebastianGSELLA, WolfgangKUHNE, VictorSCHMIDT, Christian-UlrichZIMMERMANN, Tom
    • WEIAND, SebastianGSELLA, WolfgangKUHNE, VictorSCHMIDT, Christian-UlrichZIMMERMANN, Tom
    • C08F10/02C08F2/00
    • C08F10/02C08F110/02C08F210/02C08F210/16C08F2400/02G01N7/00C08F210/06C08F220/14C08F2/00C08F2/001
    • Process for monitoring the polymerization of ethylene or ethylene and comonomers in the presence of free-radical polymerization initiator at pressures in the range of from 160 MPa to 350 MPa and temperatures in the range of from 100°C to 350°C in a tubular reactor with one or more reaction zones, which is equipped with cooling jackets for cooling the tubular reactor with a cooling medium, comprising the steps of a) measuring as process parameters the temperature profile and the pressure of the reaction medium and the flow and temperature profile of the cooling medium along the reactor, b) monitoring the feeds of ethylene, if present comonomer, free-radical polymerization initiator and chain-transfer agent to all reaction zones, c) calculating, based on the measured process parameters and on a model for the polymerization process, concentrations for free-radical polymerization initiator, chain-transfer agent, ethylene and, if present, comonomers at at least so many positions along the reactor, that at least one calculation is carried out all 10 s for a volume unit flowing through the reactor, d) calculating, based on the measured process parameters and the calculated concentrations, the cooling power, the generation of heat, and the concentration of radicals, e) calculating, based on the calculated data of the cooling power, of the generation of heat, and of the concentration of radicals, the potential of a thermal runaway of the reaction mixture at the positions along the reactor which have the highest temperatures, and f) outputting an alarm signal if the calculated value for the potential of a thermal runaway exceeds a predefined value and process for polymerizing ethylene or ethylene and comonomers comprising such a monitoring process.
    • 在自由基聚合引发剂的存在下,在管状反应器中在160MPa至350MPa的压力范围和温度范围为100℃至350℃的范围内监测乙烯或乙烯和共聚单体聚合的方法 具有一个或多个反应区,其配备有用于用冷却介质冷却管式反应器的冷却夹套,包括以下步骤:a)测量作为工艺参数的温度分布和反应介质的压力以及流动和温度分布 沿着反应器的冷却介质,b)监测乙烯(如果存在的共聚单体),自由基聚合引发剂和链转移剂到所有反应区的进料,c)基于测量的工艺参数和对于 聚合过程,自由基聚合引发剂,链转移剂,乙烯的浓度,以及(如果存在)共聚单体在沿着至少这么多位置的共聚单体 反应器中,对于流经反应堆的体积单位进行至少一次计算,d)基于测量的工艺参数和计算的浓度,计算冷却功率,产生热量和浓度 自由基,e)基于计算的冷却功率的数据,计算出热的产生和自由基的浓度,反应混合物在具有最高温度的反应器的位置处的热失控的可能性 并且f)如果热失控潜力的计算值超过预定值,则输出报警信号,以及用于聚合包含这种监测过程的乙烯或乙烯和共聚单体的方法。