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    • 11. 发明申请
    • PROCATALYST FOR OLEFIN POLYMERIZATION
    • 烯烃聚合的方法
    • WO2011039152A1
    • 2011-04-07
    • PCT/EP2010/064299
    • 2010-09-28
    • BOREALIS AGJOHANSSON, SolveigGAROFF, ThomasWALDVOGEL, Päivi
    • JOHANSSON, SolveigGAROFF, ThomasWALDVOGEL, Päivi
    • C08F4/655C08F4/651C08F4/02C08F210/16
    • C08F210/16B01J27/135B01J31/0212B01J31/128B01J31/143B01J31/38B01J37/14C08F110/02Y02P20/52C08F4/6555C08F4/025C08F4/651C08F2500/12C08F2500/03C08F2500/18C08F2500/20C08F210/14
    • Process for preparing an improved solid procatalyst of a Ziegler-Natta catalyst system comprising the following steps: a) reacting an metal alkyl with the formula (I) Al(R 1 ) 3 , wherein each R 1 independently represents an alkyl group of 1 to 6 carbon atoms with an alkyl metal halide compound of the formula (II) Al(R 2 ) m X 3-m , wherein each R 2 independently represents an alkyl group of 1 to 6 carbon atoms; each X is independently a halogen; 0 ≤ m 2 ) or a gas containing oxygen (O 2 ) to give a second reaction product, c) either the first reaction product or the second reaction product is reacted with a magnesium compound of the formula (III) R 3 n (OR 4 ) 2-n Mg, wherein R 3 and R 4 independently represent a C 1 -C 20 alkyl group and 0≤ n ≤ 2 and n may or may not be an integer, yielding a procatalyst precursor d) optionally contacting the procatalyst precursor with an alkyl metal halide compound of the formula (II) and/or with a magnesium compound of the formula (III), and e) contacting either the procatalyst precursor or the reaction product of step d) with a titanium halide compound having the formula (IV) (OR 5 ) p TiX 2 4-p , wherein each R 5 independently represents a C 1 -C 20 alkyl group, each X 2 is independently a halogen; 0 ≤ p ≤ 3 and p may or may not be an integer, in order to yield the solid procatalyst and its use for the production of polyethylene homo- or copolymers with a PDI below 4 down to 3.
    • 制备齐格勒 - 纳塔催化剂体系的改进的固体前催化剂的方法,包括以下步骤:a)使烷基金属与式(I)Al(R 1)3反应,其中每个R 1独立地表示1至6个碳原子的烷基 原子与式(II)的烷基金属卤化物化合物Al(R2)mX3-m,其中每个R2独立地表示1至6个碳原子的烷基; 每个X独立地是卤素; 0 = m <3,并且m可以是或不是整数,由此式(I)的金属烷基或式(II)的烷基金属卤化物已经首先与惰性载体接触,以产生第一反应 产物b)用氧气(O 2)或含氧气(O 2)的气体处理第一反应产物以产生第二反应产物,c)将第一反应产物或第二反应产物与下式的镁化合物 III)R3 n(OR4)2-nMg,其中R3和R4独立地表示C1-C20烷基且0 = n = 2,n可以是或不是整数,得到前催化剂前体d)任选地使前催化剂前体 与式(II)的烷基金属卤化物和/或与式(III)的镁化合物反应,和e)使前催化剂前体或步骤d)的反应产物与具有式 (IV)(OR5)pTiX2 4-p,其中每个R 5独立地表示C 1 -C 20烷基 每个X 2独立地是卤素; 0 = p = 3,p可以为整数,以产生固体前催化剂及其用于生产低于4的PDI的聚乙烯均聚物或共聚物的用途。
    • 13. 发明申请
    • IMPROVED MULTI-STAGE PROCESS FOR PRODUCING MULTI-MODAL LINEAR LOW DENSITY POLYETHYLENE
    • 用于生产多模式线性低密度聚乙烯的改进的多级方法
    • WO2010125020A1
    • 2010-11-04
    • PCT/EP2010/055517
    • 2010-04-26
    • BOREALIS AGGAROFF, ThomasWALDVOGEL, PäiviKALLIO, KalleERIKSSON, VirginieAITTOLA, AkiKOKKO, Esa
    • GAROFF, ThomasWALDVOGEL, PäiviKALLIO, KalleERIKSSON, VirginieAITTOLA, AkiKOKKO, Esa
    • C08F210/16C08F2/00C08F4/655
    • C08F210/16C08F2/14C08F4/6555C08F2/001C08F2/34C08F210/08C08F2500/18C08F2500/12C08F2500/05C08F2500/07C08F2500/02C08F2500/08C08F2500/01C08F210/14
    • Multi-stage polymerization process for the production of a multi-modal linear low density polyethylene in at least two staged reactors connected in series comprising at least (i) polymerizing in a first slurry phase stage ethylene monomers and optionally one or more alpha- olefine comonomers, in the presence of a Ziegler-Natta polymerization catalyst system to obtain a first polyethylene fraction component (A) (ii) polymerizing in a second gas or slurry phase stage ethylene monomers and one or more alpha- olefine comonomers, in the presence of a Ziegler-Natta polymerization catalyst system to obtain a second polyethylene fraction component (B), whereby the Ziegler-Natta polymerisation catalyst system comprises C) a procatalyst, which procatalyst comprises a) an Al compound having the formula AI(alkyl) x CI 3-x (l), where alkyl is an alkyl group with 1 to 12 and 0 1 ) 2-n (R 2 ) n (II), wherein each R 1 and R 2 is independently a C 1-20 hydrocarbon residue which may optionally be substituted with halogen and O y Ti(OR 3 ) 4-y (III), wherein R 3 is a C 2-20 hydrocarbon residue and y is 1, 2, 3 or 4 and compounds a), b) and c) being deposited on a particulate inorganic support and D) a halogenated aluminium alkyl cocatalyst of the formula (IV) (C 1 -C 4 -alkyl) m -AI-X 3-m , wherein X is chlorine, bromine, iodine or fluorine and m is 1 or 2, and yielding a multimodal linear low density polyethylene with a narrow molecular weight distribution, whereby the process shows a higher comonomer conversion compared to multi-stage processes using non-halogenated cocatalysts.
    • 用于在串联连接的至少两个阶段反应器中生产多模式线性低密度聚乙烯的多级聚合方法,包括至少(i)在第一浆料相阶段聚合乙烯单体和任选的一种或多种α-烯烃共聚单体 在齐格勒 - 纳塔聚合催化剂体系的存在下,获得第一聚乙烯级分组分(A)(ⅱ)在第二气体或浆料相阶段聚合乙烯单体和一种或多种α-烯烃共聚单体,在 齐格勒 - 纳塔聚合催化剂体系,以获得第二聚乙烯级分组分(B),其中齐格勒 - 纳塔聚合催化剂体系包含C)前催化剂,其主催化剂包含a)具有式AI(烷基)xCI3-x( 其中烷基是具有1至12和0 1)2-n(R2)n(II)的烷基,其中每个R 1和R 2独立地为可任选被 卤素和O yTi(OR 3)4-y(III),其中R 3是C 2-20烃残基,y是1,2,3或4,并且化合物a),b)和c)沉积在颗粒状无机载体上 和D)式(Ⅳ)(C1-C4烷基)m-Al-X3-m的卤化烷基铝助催化剂,其中X是氯,溴,碘或氟,m是1或2,并产生多峰 具有窄分子量分布的线性低密度聚乙烯,由此与使用非卤化助催化剂的多阶段方法相比,该方法显示出更高的共聚单体转化率。
    • 14. 发明申请
    • IMPROVED MULTI-STAGE PROCESS FOR PRODUCING MULTI-MODAL ETHYLENE POLYMER COMPOSITION
    • 用于生产多模式乙烯聚合物组合物的改进的多阶段方法
    • WO2010097352A1
    • 2010-09-02
    • PCT/EP2010/052173
    • 2010-02-22
    • BOREALIS AGGAROFF, ThomasWALDVOGEL, PäiviKALLIO, KalleERIKSSON, VirginieAITTOLA, AkiKOKKO, Esa
    • GAROFF, ThomasWALDVOGEL, PäiviKALLIO, KalleERIKSSON, VirginieAITTOLA, AkiKOKKO, Esa
    • C08F10/00C08F4/685
    • C08F10/00C08F110/02C08F210/16Y02P20/52C08F4/6357C08F4/685C08F2/001C08F2500/07C08F2500/12C08F2500/05C08F2500/18C08F210/14C08F2500/08
    • Multi-stage polymerization process for the production of a multi-modal linear low density polyethylene in at least two staged reactors connected in series comprising at least (i) polymerizing in a first slurry phase stage ethylene monomers and optionally one or more alpha-olefine comonomers, in the presence of a Ziegler-Natta polymerization catalyst system to obtain a first polyethylene fraction component (A) (ii) polymerizing in a second gas or slurry phase stage ethylene monomers and one or more alpha-olefine comonomers, in the presence of a Ziegler-Natta polymerization catalyst system to obtain a second polyethylene fraction component (B), whereby the Ziegler-Natta polymerization catalyst system comprises 1) a solid procatalyst formed by contacting at least: a) a Mg-alcoholate complex of the formula (I): Mg(OR 1 ) 2-n (R 1 ) n , wherein each R 1 independently represents a C 1 -C 20 hydrocarbyl group and 0 ≤ n 2 ) m X 3-m , wherein each R 2 independently represents an alkyl of up to 6 carbon atoms; each X is independently a halogen; 0 ≤ m 1 -C 20 -alkyl group, 0 ≤ x ≤ 2; 1 ≤ y ≤ 3; 0 ≤ z ≤ 2 and x + y + z = 3; x, y and z may or may not be an integer, yielding a multi-modal polyethylene, whereby the process shows a reduced change of comonomer response with polymerization time and a more stable comonomer conversion with polymerization time compared to multistage processes using Ziegler-Natta catalysts with 100% Ti.
    • 用于在至少两个串联反应器中连续串联生产多模式线性低密度聚乙烯的多级聚合方法,包括至少(i)在第一浆料相阶段聚合乙烯单体和任选的一种或多种α-烯烃共聚单体 在齐格勒 - 纳塔聚合催化剂体系存在下,得到第一聚乙烯级分组分(A)(ⅱ)在第二种气相或淤浆相阶段中聚合乙烯单体和一种或多种α-烯烃共聚单体,在 齐格勒 - 纳塔聚合催化剂体系,得到第二聚乙烯组分(B),其中齐格勒 - 纳塔聚合催化剂体系包括:1)通过使至少与下列物质接触而形成的固体前催化剂:a)式(I)的Mg-醇化物络合物, :Mg(OR1)2-n(R1)n,其中每个R1独立地表示C1-C20烃基,0 = n2)mX3-m,其中每个R2独立地表示至多6个碳原子的烷基; 每个X独立地是卤素; 0 = m <3和m,并且可以是或不是整数,c)钒化合物和钛化合物,以提供V:Ti的摩尔比为10:90至90:10,以产生 固体前催化剂和2)式(III)的一种或多种有机金属助催化剂,其中每个R独立地为C 1 -C 20 - 烷基,0 = x = 2; 1 = y = 3; 0 = z = 2,x + y + z = 3; x,y和z可以是或不是整数,产生多峰聚乙烯,由此与使用齐格勒 - 纳塔(Ziegler-Natta)的多阶段方法相比,该方法显示了聚合时间下共聚单体响应的变化减小和聚合时间的更稳定的共聚单体转化 具有100%Ti的催化剂。