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98 条记录 (耗时 0.032 秒)

    Polymerisation process
    63.
    发明授权
    Polymerisation process 有权
    聚合过程

    公开(公告)号：US09255162B2

    公开(公告)日：2016-02-09

    申请号：US14419552

    申请日：2013-08-01

    申请人： INEOS EUROPE AG

    发明人： Guillaume Lajus ,  Rupert Parkinson ,  Leslie William Bolton

    IPC分类号： C08F2/00 ,  C08F110/06 ,  C08F110/02 ,  C08F10/06 ,  C08F10/00 ,  C08F10/02

    CPC分类号： C08F10/06 ,  C08F10/00 ,  C08F10/02 ,  C08F2/34 ,  C08F210/16 ,  C08F210/08

    摘要： Process for the polymerization of olefins in a gas phase fluidized bed reactor, by i) passing a fluidizing gas to the reactor to fluidize a bed of polymer particles therein, ii) withdrawing the fluidizing gas from the reactor, iii) cooling all or a portion of the fluidizing gas withdrawn from the reactor to a temperature at which a portion of the components of the fluidizing gas condense to form condensed liquid, and iv) passing condensed liquid and non-condensed components of the fluidizing gas back to the reactor. A reservoir of condensed liquid downstream of the cooling step is provided, and variations in the inventory of the condensed liquid are made in order to control the temperature in the reactor.

    摘要翻译： 在气相流化床反应器中烯烃聚合的方法，i）将流化气体通入反应器以使其中的聚合物颗粒床流化，ii）从反应器中排出流化气体，iii）冷却全部或部分 从所述反应器排出的流化气体至所述流化气体的一部分部分冷凝以形成冷凝液体的温度，以及iv）将所述流化气体的冷凝液体和未冷凝的组分送回所述反应器。 提供在冷却步骤下游的冷凝液体的储存器，并且制造冷凝液体的库存变化以便控制反应器中的温度。

    Catalyst activator
    65.
    发明授权
    Catalyst activator 有权
    催化剂活化剂

    公开(公告)号：US09192906B2

    公开(公告)日：2015-11-24

    申请号：US14686956

    申请日：2015-04-15

    申请人： INEOS EUROPE AG

    发明人： Alex King ,  Stephen Kevin Lee ,  Brent R. Walworth

    IPC分类号： B01J2/16 ,  B01J8/44 ,  B01J23/26 ,  B01J37/08 ,  C08F4/24 ,  C08F10/00 ,  C08F4/78

    CPC分类号： B01J8/24 ,  B01J8/44 ,  B01J23/26 ,  B01J37/08 ,  B01J2208/00212 ,  B01J2208/00415 ,  B01J2208/00884 ,  B01J2208/00991 ,  C08F4/24 ,  C08F4/78 ,  C08F10/00

    摘要： The invention relates generally to a catalyst activator, and in particular to a catalyst activator for heat conditioning a catalyst, comprising: a) a vessel for containing a catalyst charge having an internal diameter of at least 1.2 meters and/or an internal volume of at least 5 m3; b) a fluidization grid plate disposed in said vessel, said fluidization grid plate and having an upper major surface and a lower major surface; c) an array of generally conical depressions in said upper major surface that overlap by less than 17%; and d) an array of holes perforating said fluidization grid plate, said holes extending from at least some of said generally conical depressions through said lower surface.

    摘要翻译： 本发明一般涉及一种催化剂活化剂，特别涉及一种用于加热调节催化剂的催化剂活化剂，该催化剂活化剂包括：a）用于容纳内径至少为1.2米和/或内部体积为 至少5立方米; b）设置在所述容器中的流化栅格板，所述流化栅格板具有上主表面和下主表面; c）在所述上主表面中大致锥形凹陷的阵列重叠小于17％; 以及d）穿孔所述流化栅格板的孔阵列，所述孔从至少一些所述大致圆锥形的凹陷穿过所述下表面延伸。

    Polymer degassing process control
    66.
    发明授权
    Polymer degassing process control 有权
    高分子脱气工艺控制

    公开(公告)号：US09181367B2

    公开(公告)日：2015-11-10

    申请号：US14348953

    申请日：2012-10-03

    申请人： Ineos Europe AG

    发明人： Jean-Louis Chamayou ,  Luc Girardot

    IPC分类号： C08F110/02 ,  C08F6/00 ,  C08F10/02

    CPC分类号： C08F110/02 ,  C08F6/005 ,  C08F6/006 ,  C08L23/04

    摘要： Process for operating a vertical fixed bed degasser which is continuously fed with an active polymer powder produced by a catalytic olefin polymerization process in a polymerization reactor. The polymerization conditions in the degasser are such that there is produced an additional amount of polymer corresponding to between 0.001 and 0.015 times the amount which entered the degasser. The degassing process includes introducing into the degasser a stripping gas containing principal monomer, with the temperature inside the degasser being the polymerization reactor temperature plus or minus 20° C.

    摘要翻译： 用于操作在聚合反应器中连续加入通过催化烯烃聚合方法生产的活性聚合物粉末的垂直固定床脱气机的方法。 脱气器中的聚合条件使得产生相当于进入脱气器的量的0.001至0.015倍的附加量的聚合物。 脱气过程包括将含有主要单体的汽提气体引入脱气机中，脱气器内的温度为聚合反应器温度加或减20℃。

    PROCESS FOR THE PRODUCTION OF A POLYMER IN A GAS PHASE FLUIDISED BED REACTOR
    67.
    发明申请
    PROCESS FOR THE PRODUCTION OF A POLYMER IN A GAS PHASE FLUIDISED BED REACTOR 有权
    在气相流化床反应器中生产聚合物的方法

    公开(公告)号：US20150252128A1

    公开(公告)日：2015-09-10

    申请号：US14433919

    申请日：2013-10-07

    申请人： INEOS EUROPE AG

    发明人： Damien Disanto ,  Jean-Louis Chamayou ,  Arnaud Soulage

    IPC分类号： C08F210/16 ,  C08F2/00

    CPC分类号： C08F210/16 ,  C08F2/001 ,  C08F2/34 ,  C08F10/02 ,  C08F210/02 ,  C08F2400/02 ,  C08F110/02 ,  C08F2500/07 ,  C08F2500/12

    摘要： The present invention relates to a method for the operation of a process for the production of a polymer by polymerisation of a monomer and an optional comonomer in a gas phase fluidised bed reactor during steady-state and non-steady-state conditions. In particular, the present invention relates to a process for the continuous production of a medium and/or high density ethylene (co-)polymer in a gas phase fluidised bed reactor comprising improved non-steady-state conditions.

    摘要翻译： 本发明涉及通过在稳态和非稳态条件下在气相流化床反应器中聚合单体和任选的共聚单体来生产聚合物的方法的操作方法。 特别地，本发明涉及在气相流化床反应器中连续生产介质和/或高密度乙烯（共）聚合物的方法，该方法包括改进的非稳态条件。

    PROCESS AND APPARATUS FOR PRODUCING OLEFINS WITH HEAT TRANSFER FROM STEAM CRACKING TO ALCOHOL DEHYDRATION PROCESS
    69.
    发明申请
    PROCESS AND APPARATUS FOR PRODUCING OLEFINS WITH HEAT TRANSFER FROM STEAM CRACKING TO ALCOHOL DEHYDRATION PROCESS 有权
    用于从蒸汽破碎转移到酒精脱水过程中生产烯烃的方法和装置

    公开(公告)号：US20140114104A1

    公开(公告)日：2014-04-24

    申请号：US14124757

    申请日：2012-06-26

    申请人： Laurent Caranoni ,  Bernard Descales ,  Neil Turnbull ,  Vaughn Clifford Williams

    发明人： Laurent Caranoni ,  Bernard Descales ,  Neil Turnbull ,  Vaughn Clifford Williams

    IPC分类号： C07C2/06 ,  C07C1/24 ,  C07C4/04

    CPC分类号： C07C2/06 ,  C07C1/24 ,  C07C4/04 ,  C10G9/26 ,  C10G2300/807 ,  C10G2400/20 ,  Y02P30/10

    摘要： A method of producing ethylene and, optionally, propylene comprising: a) subjecting a feedstock to steam cracking to produce a first olefin containing stream; b) heating an ethanol containing stream with heat from a steam cracker; c) passing the heated ethanol containing stream over a dehydration catalyst at a temperature between 200 C to 500 C preferably 250 C to 450 C to produce a second olefin containing stream; d) combining the first and second olefin containing streams to give an initial product stream comprising ethylene and optionally propylene; and e) subjecting the initial product stream to purification comprising at least i) water content reduction ii) hydrogen content reduction iii) reduction of content of molecules containing 4 or more carbon atoms and iv) ethane content reduction.

    摘要翻译： 一种生产乙烯和任选的丙烯的方法，包括：a）使原料进行蒸汽裂化以产生含第一烯烃的料流; b）用来自蒸汽裂解器的热量加热含乙醇的流; c）在200℃至500℃，优选250℃至450℃的温度下将经过加热的含乙醇的料流通过脱水催化剂，以产生第二烯烃流; d）将第一和第二烯烃流合并，得到包含乙烯和任选的丙烯的初始产物流; 和e）对初始产物流进行纯化，包括至少i）含水量降低ii）氢含量降低iii）减少含有4个或更多个碳原子的分子的含量和iv）乙烷含量降低。