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    • 1. 发明申请
    • PROCESS FOR THE PREPARATION OF AN UNSUPPORTED, SOLID OLEFIN POLYMERISATION CATALYST AND USE IN POLYMERISATION OF OLEFINS
    • 制备不需要的固体烯烃聚合催化剂的方法及其在烯烃聚合中的应用
    • WO2010052237A1
    • 2010-05-14
    • PCT/EP2009/064606
    • 2009-11-04
    • BOREALIS AGSEVERN, JohnELO, PerttiVIJAY, SameerMUSTONEN, Marja
    • SEVERN, JohnELO, PerttiVIJAY, SameerMUSTONEN, Marja
    • C08F10/00C08F4/659C08F210/16
    • C08F10/00C08F4/65925C08F210/16C08F4/65912C08F210/14C08F2500/18C08F2500/03
    • Improved process for the preparation of an unsupported, heterogeneous olefin polymerisation catalyst, comprising an organometallic compound of a transition metal of Group 3 to 10 of the Periodic Table (IUPAC) or of an actinide or lanthanide in the form of solid particles comprising the steps of a) preparing a solution of an aluminoxane and an ionic complex M-X, M being an alkali or earth alkali metal and X being a halide or pseudo halide, in a molar ratio of Al of the aluminoxane to M of the ionic complex between 80:1 and 300:1, b) mixing said solution with an organometallic compound of a transition metal of Group 3 to 10 of the Periodic Table (IUPAC) or of an actinide or lanthanide lanthanide in a molar ratio of M of the ionic complex to the transition metal of the organometallic compound between 1:1 and 4:1, yielding a second solution, c) dispersing said second solution obtained in step b) in a solvent immiscible therewith to form an emulsion in which said second solution of step b) forms the dispersed phase in the form of droplets and the solvent immiscible with said solution forms the continuous phase, d) solidifying said dispersed phase to convert said droplets to solid particles and optionally recovering aid particles to obtain said catalyst, the catalysts itself and its use for olefin polymerisation.
    • 制备无支撑的非均相烯烃聚合催化剂的改进方法,其包含周期表(IUPAC)的第3至10族的过渡金属或固体颗粒形式的锕系元素或镧系元素的有机金属化合物,其包括以下步骤: a)制备铝氧烷和离子络合物MX的溶液,M是碱金属或碱土金属,X是卤化物或假卤化物,铝氧烷的Al与离子络合物的M的摩尔比为80:1 和300:1,b)将所述溶液与元素周期表(IUPAC)中第3至10族的过渡金属的有机金属化合物或离子络合物的摩尔比与过渡金属的锕系元素或镧系元素镧系元素M的摩尔比 有机金属化合物的金属在1:1至4:1之间,产生第二溶液,c)将步骤b)中获得的所述第二溶液分散在与其不混溶的溶剂中以形成乳液,其中步骤b)的所述第二溶液 以液滴的形式形成分散相,并且与所述溶液不混溶的溶剂形成连续相,d)固化所述分散相以将所述液滴转化为固体颗粒,并任选地回收助剂颗粒以获得所述催化剂,催化剂本身及其用途 用于烯烃聚合。
    • 2. 发明申请
    • PROCESS FOR OLEFIN POLYMERIZATION
    • 烯烃聚合方法
    • WO2011058091A1
    • 2011-05-19
    • PCT/EP2010/067268
    • 2010-11-11
    • BOREALIS AGAUMO, JeannetteMATIKAINEN, PasiBARTKE, MichaelELOVIRTA, TomVIJAY, SameerLYLYKANGAS, MikkoELO, PerttiHUHTANEN, Lauri
    • AUMO, JeannetteMATIKAINEN, PasiBARTKE, MichaelELOVIRTA, TomVIJAY, SameerLYLYKANGAS, MikkoELO, PerttiHUHTANEN, Lauri
    • C08F10/00C08F4/659
    • C08F10/00C08F110/06C08F2410/01C08F4/65912C08F4/65927C08F2/00C08F2500/12C08F4/6492
    • The present invention aims to provide a process for polymerizing at least one olefin in the presence of a polymerization catalyst comprising the steps of: (A) continuously introducing a first liquid comprising a transition metal compound, an organometallic compound of a metal of Group 13 of Periodic System of Elements and a solvent, and a second liquid which together with said first liquid is capable of forming an emulsion, into an emulsification stage to produce an emulsion comprising said first liquid dispersed in said second liquid; (B) continuously withdrawing an emulsion stream from said emulsification stage and directing it into a solidification stage to form a slurry comprising a solid polymerization catalyst component comprising said transition metal compound and said organometallic compound suspended in said second liquid; (C) continuously recovering said solid polymerization catalyst component from said solidification stage; (D) directing said solid polymerization catalyst component into a first prepolymerization stage together with a monomer and an amount of second liquid wherein the monomer is prepolymerized onto said solid polymerization catalyst component so that the ratio of the weight of the polymer to the weight of said solid polymerization catalyst component is from 0.1:1 to 20:1 to form a slurry of a prepolymerized solid polymerization catalyst component suspended in said second liquid; (E) recovering said prepolymerized solid polymerization catalyst component from said first prepolymerization stage; (F) continuously introducing said prepolymerized solid polymerization catalyst component into a second prepolymerization stage together with an olefin monomer to form a prepolymerized catalyst comprising in average 100 to 1000 g of polymer per 1 gram of said solid polymerization catalyst component; (G) continuously withdrawing said prepolymerized catalyst from said second prepolymerization stage and directing it into a subsequent polymerization stage together with at least one olefin monomer to effect polymerization of the at least one olefin monomer in the presence of said prepolymerized catalyst. The polymerization process produces polymers in high yield. The morphology of the polymer powder is good and the amount of fine particle polymer is low. The process can be operated for long a long period in a stable manner.
    • 本发明的目的在于提供一种在聚合催化剂存在下聚合至少一种烯烃的方法,包括以下步骤:(A)连续引入包含过渡金属化合物的第一液体,第13族金属的有机金属化合物 元素周期性系统和溶剂,以及与所述第一液体一起能够形成乳液的第二液体进入乳化阶段以产生包含分散在所述第二液体中的所述第一液体的乳液; (B)从所述乳化阶段连续抽出乳液流并将其导入固化阶段以形成包含悬浮在所述第二液体中的包含所述过渡金属化合物和所述有机金属化合物的固体聚合催化剂组分的浆料; (C)从所述固化阶段连续回收所述固体聚合催化剂组分; (D)将所述固体聚合催化剂组分与单体和一定量的第二液体一起引导到第一预聚合阶段,其中所述单体预聚合到所述固体聚合催化剂组分上,使得所述聚合物的重量与所述 固体聚合催化剂组分为0.1:1至20:1,以形成悬浮在所述第二液体中的预聚合固体聚合催化剂组分的浆液; (E)从所述第一预聚合阶段回收所述预聚固体聚合催化剂组分; (F)将所述预聚合的固体聚合催化剂组分连同烯烃单体一起连续引入第二预聚合阶段,以形成预聚合的催化剂,每克所述固体聚合催化剂组分平均含有100至1000克聚合物; (G)从所述第二预聚合阶段连续地抽出所述预聚合催化剂,并将其引导至随后的聚合阶段与至少一种烯烃单体,以在所述预聚合的催化剂存在下进行至少一种烯烃单体的聚合。 聚合过程以高产率生产聚合物。 聚合物粉末的形态好,微粒聚合物的量低。 该方法可以长时间稳定运行。
    • 4. 发明申请
    • PROCESS FOR PRODUCING A POLYMERIZATION CATALYST
    • 制备聚合催化剂的方法
    • WO2011058089A1
    • 2011-05-19
    • PCT/EP2010/067266
    • 2010-11-11
    • BOREALIS AGVIJAY, SameerRÄSÄNEN, JukkaLYLYKANGAS, Mikko
    • VIJAY, SameerRÄSÄNEN, JukkaLYLYKANGAS, Mikko
    • C08F4/00C08F110/06C08F4/6592C08F6/00B01J37/00
    • C08F10/06B01J31/143B01J31/1608B01J31/2295B01J37/0072B01J37/009B01J2531/94C07C17/38C07C17/383C08F4/65912C08F6/02C08F110/06C08L23/10C08F4/00C08F4/65927C08F2500/12
    • The present invention aims to provide a process for producing a solid polymerization catalyst component comprising the steps of (A) withdrawing a mixed stream comprising the solid polymerization catalyst component and a mixture of a first liquid comprising a hydrocarbon or halogenated hydrocarbon solvent and a second liquid comprising a liquid capable of forming an emulsion with said first liquid from a catalyst preparation stage; (B) separating said mixed stream into a liquid stream comprising a majority of said mixture of said first liquid and said second liquid and a product stream comprising a majority of said solid polymerization catalyst component; (C) dividing said liquid stream into a first liquid stream comprising a majority of said first liquid and a second liquid stream comprising a majority of said second liquid; (D) forming a purified second liquid stream and a disposable stream; and (E) returning at least a part of said purified second liquid stream into said catalyst preparation stage. The process offers an economical and environmentally attractive method of producing the solid catalyst component. The catalyst is active in polymerization and can be used in industrial processes.
    • 本发明的目的在于提供一种制备固体聚合催化剂组分的方法,包括以下步骤:(A)将包含固体聚合催化剂组分的混合物和包含烃或卤代烃溶剂的第一液体和第二液体 包括能够从催化剂制备阶段与所述第一液体形成乳液的液体; (B)将所述混合物流分离成包含大部分所述第一液体和所述第二液体的所述混合物的液体物流和包含大部分所述固体聚合催化剂组分的产物流; (C)将所述液体流分成包含大部分所述第一液体的第一液体流和包含大部分所述第二液体的第二液体流; (D)形成纯化的第二液体流和一次性流; 和(E)将至少一部分纯化的第二液体物流返回到催化剂制备阶段。 该方法提供了生产固体催化剂组分的经济且环境友好的方法。 催化剂在聚合反应中有活性,可用于工业过程。
    • 6. 发明申请
    • PROCESS FOR HYDRAULIC CONVEYING OF POLYOLEFIN PELLETS
    • 聚烯烃颗粒液压输送方法
    • WO2017194488A1
    • 2017-11-16
    • PCT/EP2017/060968
    • 2017-05-09
    • BOREALIS AG
    • RÄSÄNEN, JukkaZITTING, SamuliSLEIJSTER, HenryBERGSTRA, MichielVIJAY, Sameer
    • B29B9/06B29B9/12B29B9/16F26B17/00
    • B29B9/16B29B9/065B29B9/12B29B2009/163B29K2023/06B29K2023/12F26B17/00
    • Process for hydraulic conveying of polyolefin pellets comprising the steps of: (i) extruding molten polyolefin into strands and cutting the strands into pellets in an underwater pelletiser (A); (ii) withdrawing a first pellet suspension stream (1.1) from the pelletiser; (iii) concentrating the first pellet suspension stream in a first pellet separator (B); (iv) passing the concentrated pellet stream (1.4) to a hydraulic conveying line through a first vessel (D) and mixing it with water thereby producing a second pellet suspension stream (1.5); (v) withdrawing the second pellet suspension stream from the first vessel and passing it to a second pellet separator (E); (vi) separating the pellets from water in the second pellet separator thereby creating a second water stream (1.6) and a dry pellet stream (1.10) and passing the second water stream back to the first vessel; wherein any one of the first or second pellet suspension stream or the dry pellet stream comprises an antiblock.
    • 聚合物粒料的水力输送方法包括以下步骤:(i)将熔融聚烯烃挤出成股,并在水下造粒机(A)中将股绳切成粒料; (ii)从造粒机中取出第一颗粒悬浮液流(1.1); (iii)将第一颗粒悬浮液流浓缩在第一颗粒分离器(B)中; (iv)通过第一容器(D)将浓缩的粒料流(1.4)传送至液压输送管线并将其与水混合,从而产生第二粒料悬浮液流(1.5); (v)从第一容器中取出第二颗粒悬浮液流并将其送入第二颗粒分离器(E); (vi)将颗粒与第二颗粒分离器中的水分离,由此产生第二水流(1.6)和干颗粒流(1.10)并使第二水流返回第一容器; 其中第一或第二颗粒悬浮液料流或干颗粒料流中的任何一个包含防粘连剂。
    • 9. 发明申请
    • A PROCESS FOR RECOVERING HYDROCARBONS IN A SOLUTION POLYMERISATION PROCESS
    • 在溶液聚合过程中回收烃的方法
    • WO2017108963A1
    • 2017-06-29
    • PCT/EP2016/082199
    • 2016-12-21
    • BOREALIS AG
    • AL-HAJ ALI, MohammadERIKSSON, ErikMATHIVANAN, GuhanSLEIJSTER, HenryVIJAY, SameerWURNITSCH, ChristofZITTING, Samuli
    • C08F2/06C08F6/00C08J11/02C08F6/12
    • C08F6/003C08F2/06C08F6/12C08L23/00
    • The present invention relates to a process for producing a polymer composition comprising the steps of: (A) polymerising, in a first polymerisation reactor in a first solvent, - a first olefin monomer having two or more carbon atoms, - in the presence of a first polymerisation catalyst for producing a first solution comprising a first polymer of the first olefin monomer and the first solvent; (B) withdrawing a first stream of the first solution from the first polymerisation reactor; (C) passing the first stream of the first solution into a first separator wherein a first liquid phase comprising the polymer and a first vapour phase coexist; (D) withdrawing a first vapour stream and a first concentrated solution stream comprising the polymer from the first separator; (E) passing at least a part of the first vapour stream to a first fractionator; (F) withdrawing a first overhead stream and a first bottom stream from the first fractionator; (G) recovering at least a part of the first overhead stream as a first recycle stream and passing it to the first polymerisation reactor; (H) passing the first concentrated solution stream from the first separator (4) to a second separator (8) wherein a second liquid phase comprising the polymer and a second vapour phase coexist; (I) withdrawing a second vapour stream and a second concentrated solution stream comprising the polymer from the second separator; (J) passing at least a part of the second vapour stream to a second fractionator; (K) withdrawing a second overhead stream and a second bottom stream from the second fractionator; (L) recovering at least a part of the second overhead stream as a second recycle stream and passing it to the first polymerisation reactor; (M) passing the second concentrated solution stream from the second separator to a third separator wherein a third liquid phase comprising the polymer and a third vapour phase coexist; characterised in that the mass flow rate of the first recycle stream is at least 80 % of the mass flow rate of the first vapour stream and the mass flow rate of the second recycle stream is at least 70 % of the mass flow rate of the second vapour stream.
    • 本发明涉及生产聚合物组合物的方法,其包括以下步骤:(A)在第一聚合反应器中在第一溶剂中聚合 - 具有两个或更多个碳的第一烯烃单体 原子 - 在用于制备包含第一烯烃单体的第一聚合物和第一溶剂的第一溶液的第一聚合催化剂存在下进行; (B)从第一聚合反应器中取出第一种第一溶液流; (C)将所述第一溶液的第一流通入第一分离器,其中包含所述聚合物和第一气相的第一液相共存; (D)从第一分离器中取出包含聚合物的第一蒸气流和第一浓缩溶液流; (E)将第一蒸气流的至少一部分通入第一分馏器; (F)从第一分馏器中抽出第一顶部料流和第一底部料流; (G)回收至少一部分第一塔顶馏出物物流作为第一再循环物流并将其通入第一聚合反应器; (H)将来自第一分离器(4)的第一浓缩溶液流送至第二分离器(8),其中包含聚合物和第二蒸汽相的第二液相共存; (I)从第二分离器中取出第二蒸气流和包含聚合物的第二浓缩溶液流; (J)将第二蒸气流的至少一部分传送到第二分馏器; (K)从第二分馏器中取出第二塔顶料流和第二塔底料流; (L)回收作为第二循环物流的至少一部分第二塔顶馏出物料流并将其通入第一聚合反应器; (M)将来自第二分离器的第二浓缩溶液流送入第三分离器,其中包含聚合物和第三蒸汽相的第三液相共存; 其特征在于,所述第一再循环流的质量流率为所述第一蒸气流的质量流率的至少80%,并且所述第二再循环流的质量流率为所述第二再循环流的质量流率的至少70% 蒸气流。
    • 10. 发明申请
    • IN-LINE BLENDING PROCESS
    • 在线混合过程
    • WO2017108951A1
    • 2017-06-29
    • PCT/EP2016/082184
    • 2016-12-21
    • BOREALIS AG
    • SLEIJSTER, HenryAL-HAJ ALI, MohammadRÄSÄNEN, JukkaZITTING, SamuliBERGSTRA, MichielERIKSSON, ErikWURNITSCH, ChristofMATHIVANAN, GuhanVIJAY, SameerKANELLOPOULOS, VasileiosAHO, JaniTAKAKARHU, Jouni
    • C08F2/00C08F2/06C08F6/00C08F6/12C08J11/02
    • C08F6/003C08F2/001C08F2/06C08F6/12C08J11/02Y02P20/582C08L23/00
    • An in-line blending process for polymers comprising: (a) providing two or more reactor-low pressure separator units (1,7) in parallel configuration, each reactor-low pressure separator unit comprising one reactor (2,8) fluidly connected to one low pressure separator (3,9) downstream and further a recycling line (5,11) connecting the low pressure separator (3,9) back to the corresponding reactor (2,8); (b) polymerizing olefin monomers having two or more carbon atoms in each of the reactors (2,8) in solution polymerisation; (c) forming an unreduced reactor effluents stream including a homogenous fluid phase polymer-monomer-solvent mixture in each of the reactors (2,8), (d) passing the unreduced reactor effluents streams from each of the reactors (2,8) through the corresponding low pressure separators (3,9), whereby the temperature and pressure of the low pressure separators (3,9) is adjusted such that a liquid phase and a vapour phase are obtained, whereby yielding a polymer-enriched liquid phase and a polymer-lean vapour phase, and (e) separating the polymer-lean vapour phase from the polymer- enriched liquid phase in each of the low-pressure separators (3,9) to form separated polymer-lean vapour streams and separated polymer-enriched liquid streams; (f) combining the polymer-enriched liquid streams from step (e) in a further low-pressure separator and/or a mixer (13) to produce a combined polymer-enriched liquid stream (16); (g) reintroducing the polymer-lean vapour streams from step (e) via recycling lines (5,11) into the corresponding reactors (2,8).
    • 一种用于聚合物的在线共混方法,其包括:(a)提供两个或多个处于并联结构的反应器 - 低压分离器单元(1,7),每个反应器 - 低压分离器单元包括一个反应器 (2,8)流体地连接到下游的一个低压分离器(3,9),并且还包括将低压分离器(3,9)连接回到相应的反应器(2,8)的再循环管线(5,11); (b)在溶液聚合中在每个反应器(2,8)中聚合具有两个或更多个碳原子的烯烃单体; (c)在每个反应器(2,8)中形成包含均相流体相聚合物 - 单体 - 溶剂混合物的未还原的反应器流出物流,(d)使来自每个反应器(2,8)的未还原的反应器流出物流通过, 通过相应的低压分离器(3,9),由此调节低压分离器(3,9)的温度和压力,从而获得液相和气相,由此产生富含聚合物的液相并且 贫聚合物汽相和(e)在每个低压分离器(3,9)中将贫聚合物汽相与富聚合物液相分离以形成分离的贫聚合物蒸汽流和分离的聚合物 - 富集液体流; (f)在另外的低压分离器和/或混合器(13)中合并来自步骤(e)的富含聚合物的液体流以产生合并的富含聚合物的液体流(16); (g)通过循环管线(5,11)将来自步骤(e)的贫聚合物蒸气流再次引入相应的反应器(2,8)中。