CN1051735A - 生产半等规聚丙烯的催化剂 - Google Patents

生产半等规聚丙烯的催化剂 Download PDF

Info

Publication number
CN1051735A
CN1051735A CN90109215A CN90109215A CN1051735A CN 1051735 A CN1051735 A CN 1051735A CN 90109215 A CN90109215 A CN 90109215A CN 90109215 A CN90109215 A CN 90109215A CN 1051735 A CN1051735 A CN 1051735A
Authority
CN
China
Prior art keywords
compound
cyclopentadienyl
softening agent
formula
metallocenic compound
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN90109215A
Other languages
English (en)
Other versions
CN1028532C (zh
Inventor
约翰·尤恩
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fina Technology Inc
Original Assignee
Fina Technology Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=23661315&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=CN1051735(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Fina Technology Inc filed Critical Fina Technology Inc
Publication of CN1051735A publication Critical patent/CN1051735A/zh
Application granted granted Critical
Publication of CN1028532C publication Critical patent/CN1028532C/zh
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10Homopolymers or copolymers of propene
    • C08L23/12Polypropene
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F17/00Metallocenes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F10/04Monomers containing three or four carbon atoms
    • C08F10/06Propene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F110/00Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F110/04Monomers containing three or four carbon atoms
    • C08F110/06Propene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/65904Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with another component of C08F4/64
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/65912Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/6592Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
    • C08F4/65922Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not
    • C08F4/65927Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not two cyclopentadienyl rings being mutually bridged
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S526/00Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S526/943Polymerization with metallocene catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

本发明是关于能用于生产半等规聚合物的催化 剂体系中的一种金属茂化合物,该化合物是具有不同 的环戊二烯基基团及不具有双侧面对称性的一种桥 接的金属茂化合物,该化合物的一种实例是异亚丙基 (3-甲基环戊二烯基-1-芴基)二氯化锆。本发明的 催化剂可以通过一种离子化试剂,例如甲基铝氧烷被 转变成离子金属茂催化剂。用该催化剂所制备的聚 合物,其特征在于具有只对每隔一个的不对称碳原子 有效的等规结构。

Description

本发明一般涉及一种催化剂体系,特别是涉及半等规催化剂。
烯烃,特别是丙烯,可以聚合成多种形式的聚烯烃:等规,间规和无规。等规聚丙烯链中,主要是具有相同构型的重复单元和只有很少的无定的、简单的变型,等规聚丙烯其结构可以用弗歇尔投影,如式(1)来表示:
按照Bovey的NMR(核磁共振)命名原则,由于其5个连续的甲基是彼此为内消旋的,则该等规结构表示为…mmmm…,即在弗歇尔投影平面的同一侧。
等规聚丙烯是可以具有高熔点和其它所需物理性质的高结晶的聚合物,与无定形(非结晶的)状态聚合物有显著不同。
间规聚合物主要含有完全交替的立体异构体单元,并按弗歇尔投影,用结构式(2)来表示:
按照Bovey的NMR命名原则,由于其5个连续的甲基是彼此为外消旋的,则该间规结构表示为…rrrr…,即在弗歇尔投影平面上更迭一侧。
显示无规则次序的重复单元构型的聚合物链的是一种无规聚合物。商业上使用的一定百分比的无规聚合物一般是与等规形式一起生产的。
聚合物的结构形式有其它的变化,由M.  Farina,G.Disilvestro及P.Sozzani著的题目为“半有规立构聚丙烯:一种新型聚合物立构规整度的实例“中公开了半等规或半有规立构聚丙烯(Macromolecules,Vol.15,1451-1452,1982)。该半等规聚合物的结构用弗歇尔投影,表示如下:
Figure 901092150_IMG4
该聚合物的链节为如下所示的结构
Figure 901092150_IMG5
其中,RS为烃基或非烃基,在式(4)中的第二个碳原子为不对称碳原子,即不是由相同基团所连接的碳原子,因此,称之为“不对称”。
该聚合物结构的特征在于,RS基团连接到每隔一个的不对称碳原子上,处于用弗歇尔投影来表示的聚合物主链的相同的一侧及RS基团还连接到剩余的不对称碳原子上,处于与已经连接到每隔一个的不对称碳原子上的RS基团的相同一侧,或者在相反的一侧,当RS基团在聚合物主链的同一侧时,该结构是等规的,由于仅仅是每隔一个的符合等规结构,因此称之为“半”,该材料是一种非结晶的聚合物。
烯烃的聚合反应主要是用齐格勒-纳塔型催化剂,齐格勒-纳塔型催化剂是用第Ⅳ族的金属茂化合物与甲基铝氧烷作为助催化剂,西德专利申请号2608863公开了一种乙烯聚合的催化剂体系,它由双(环戊二烯基)二烃基钛、三烷基铝和水组成。西德专利申请号2608933公开了一种由通式为(环戊二烯基)nZrY4-n′的锆金属茂(式中Y代表R1CH2AlR2,CH2CH2AlR2和CH2CH(AlR22,其R为烷基或金属烷基,及n为1-4数,与三烷基铝助催化剂和水结合在一起所组成的乙烯聚合催化剂体系。
在乙烯和其它α-烯烃的共聚合中,使用金属作为催化剂在现有技术中是已知的,Kaminsky等人在美国专利号4542199中公开了一种烯烃聚合方法,特别是用于制备聚乙烯及聚乙烯与其它α-烯烃的共聚物的方法,所公开的催化剂体系包括一种分子式为(环戊二烯基)2MeRHal的催化剂,分子式中的R是卤素、环戊二烯基或C1-C6烷基、Me是过渡金属,特别是金属锆、及Hal是卤素,特别是氯。该催化剂体系还包括一种通式为Al2OR4(Al(R)-O)n的线型分子和/或为(Al(R)-O)n+2的环状分子的铝氧烷,其中,n是4-20的数,R是甲基或乙基。在美国专利号4404344中公开了一种类似的催化剂体系。
美国专利号4530914公开了一种将乙烯聚合成具有宽分子量分布及特别是具有双峰或多峰分子量分布的聚乙烯的催化剂体系,该催化剂体系含有至少二种不同的金属茂和铝氧烷,该专利公开了具有在二个环戊二烯基环之间的桥接的,用该桥接来使那些环为主体刚性的金属茂。
欧洲专利公开号0185918公开了一种烯烃聚合的立体刚性的、手性锆金属茂催化剂,该申请没有表示可以用铪来代替锆并被用来生产有用的聚合物产品。在环戊二烯基之间的桥接,被公开为1-4个碳原子的直链烃或为3-6个碳原子的环状烃。
欧洲专利申请0-277003涉及由Turner所进行的、通过质子化作用的方法制备的催化剂的工作。为一种双(环戊二烯基)金属化合物与一种具有能给予质子的阳离子及具有许多硼原子的阴离子的化合物相结合,例如,用下列反应来说明此发明:
双(环戊二烯基)二甲基铪十N,N-二甲基苯胺双(7,8-二氨癸烷硼酸盐)钴酸盐(Ⅲ)→
[CP2HfMe][B]+CH4+N,N-二甲基苯胺
其中[B]为7,8-二氨癸烷硼烷。
欧洲专利申请0-277-004也涉及由Turner所进行的、用质子化作用的方法制备的一种催化剂的工作,为一种双(环戊二烯基)金属化合物与一种离子化合物相结合,该离子化合物具有阳离子和阴离子,该阳离子可以与金属化合物上的配位体进行不可逆反应;而该阴离子在金属或准金属离子周围有许多亲脂基团,例如,可用下列反应来说明此发明:
三(正丁基)胺四(五氟苯基)硼+双(环戊二烯基)二甲基锆→[CP2ZrMe][Bph4]+CH4+(正丁基)3N
在“用可溶性4B族的金属茂/甲基铝氧烷催化剂进行丙烯聚合反应中的立体化学控制机理”(J.Am.Chem.Soc.,Vol.106,pp.6355-64,1984)的文章中,介绍了一种用钛或锆金属催化剂及铝氧烷助催化剂生产等规聚丙烯的体系,该文章揭示:由乙烯桥接的茚基衍生物的外消旋对映体所得到的手性催化剂,通过由立体化学控制模式的对映(结构)体-模型新预示的通常的结构可以生成等规聚丙烯,然而,乙烯桥接的钛茚基非对映体的内消旋非手性形式及非手性锆衍生物,生产出完全是无规结构的聚丙烯。
按照本发明,提供了一种通式为
的金属茂化合物,式中每个R和R′是1-20个碳原子的烃基,可相同或不同,并且要进行选择以使该CPR′m与CPRn是在空间不同的环,从而导致化合物中的双侧面对称的缺乏。R″是给予化合物以立体刚性的桥接的结构,M是第4族金属,n是0至4,m是0至4,及Hal是卤素。这种化合物的一种实例是异丙基(3-甲基环戊二烯基-1-芴基)二氯化锆,该化合物是一种具有不同环戊二烯基及没有双侧面对称的桥接的金属茂化合物。
这些化合物的一种用处是用在金属茂催化剂体系中,上述定义的金属茂化合物可通过任意已知的金属茂催化剂制备方法,被活化以用作催化剂。
用本发明的催化剂生产的聚合物具有被称之为“半等规”的结构,半等规聚丙烯的特征为用弗歇尔投影所表示的其甲基每隔一个地处于聚合物主链的同一侧,其剩余的甲基或者在聚合物主链的同一侧或在相反一侧。
聚合物链的增长导致丙烯链节由头-尾键合以这种方式形成下列结构:
在费歇尔投影中表示,该奇数次甲基单元就其相互间来说,是内消旋的,偶数次甲基碳具有无规空间(排列)的构型,半等规聚丙烯是非结晶的,这是由于这些无规基团的无序和不规则性所致。
本发明是有关一种新型的金属茂化合物,它是用来生产称之为半等规聚合物催化剂的催化剂前体。用一种离子化试剂将该金属茂化合物转变成金属茂催化剂,该离子化试剂将中性的金属茂化合物转化成起催化剂作用的金属茂阳离子。该离子化试剂可以是一种助催化剂化合物例如甲基铝氧烷(MAO)。
本发明的较好的应用是可用下列分子式表示的单体的半等规聚合,
式中R3是烃基或非烃基取代基。本发明中可以使用的单体是C+3α-烯烃、1-丁烯、1-二烯类,例如1,3-丁二烯、取代的乙烯化合物,例如乙烯、及苯乙烯,优选应用是乙烯的不饱和单体,此处用“乙烯的不饱和单体”是指其特征为其未端为乙烯基的(CH2=CH-)一种烃或取代烃化合物,在本发明中所使用的最好的乙烯的不饱和化合物为至少具有3个碳原子的,一个特殊的实例是丙烯。
用于生产半等规烯烃的催化剂是具有下列通式的金属茂化合物,R″(CPRn)(CPR′m)MeHal2,式中CP为环戊二烯基或取代的环戊二烯基、每个R和R′是1-20个碳原子的烃基、可相同或不同,并且要进行选择以使该CPR′m与CPRn是在空间不同的环,从而导致化合物的双侧面对称的缺乏,R″是给予化合物以立体刚性的桥接的结构,M是第4族金属,优选是钛、锆、铪。n是0至4,m是0至4,Hal是卤素,优选是氯。
化合物双侧面对称的缺点是按照以下的条件来定义的,一种金属茂化合物具有一个没有取代基的非环戊二烯基配位位置的、或者在环戊二烯基环一侧上有一个或多个取代基都在配位位置的上面和下面,以及在环戊二烯基环的另一侧上有一个或多个取代基,它在其配位位置的上面或者下面。这种化合物的一种实例是异亚丙基(3-甲基环戊二烯基-1-芴基)二氯化锆、简写为ipr(3MeCP-1-Flu)ZrCl2,该化合物的配位体的说明如下所示:
该双侧面对称的缺乏可通过以下情况来说明,由于一个甲基在环戊二烯基环的右侧,并在同一环戊二烯基环的左侧上没有取代基,则图示的右侧不同于左侧。
该ipr(3MeCP-1-Flu)ZrCl2化合物可以通过以下步骤来制备:裂解甲基环戊二烯二聚体,制备3,6,6-三甲基亚甲基环戊二烯,用异亚丙基桥接二个环戊二烯化合物并与锆和氯形成配位化合物,最后在四氢呋喃(THF)和在二氯甲烷(MeCl2)中进行反应,使用MeCl2以使ipr(3MeCP-1-Flu)ZrCl2以纯的形式而被离析出来。
烯烃的聚合可以通过用金属茂催化剂使烯烃聚合的任意已知的方式来完成,例如:本体聚合、淤浆聚合或气相中聚合。对于聚丙烯,聚合温度的范围为从-80℃到150℃,优选是25℃到90℃,最优选是从50℃到80℃。
非结晶的半等规聚丙烯用作间规或等规聚丙烯的增塑剂,增塑剂是掺入到塑料中以增加可加工性及挠曲性或伸长性的一种材料,添加增塑剂可以降低熔体粘度、二次转化温度,或塑料的弹性模量。将塑料与增塑剂紧密的混合(这是最普通的作法),混合是通过加热直至将塑料溶入增塑剂中,反之亦然。另外,塑料和增塑剂可以通过溶解于普通溶剂中,不必加热而加以混合,随之,通过蒸发而除去溶剂。
半等规聚合物是非结晶的,并且是具有增塑剂性质的部分有规立构的结构。半等规聚合物作为增塑剂的一种特殊的实例是将通过由丙烯同时与ipr(3MeCP-1-Flu)ZrCl2和异亚丙基(环戊二烯基-1-芴基)二氯化锆(简写为ipr(CP-1-Flu)ZrCl2或任何其它的简规催化剂前体进行聚合所制备的半等规聚丙烯和间规聚丙烯的一种反应器混合物可以通过将丙烯同时与ipr(3MeCP-1-Flu)ZrCl2和亚乙基双(四氢茚基)二氯化锆(简写为Et(IndH42ZrCl2或任何其它的等规的催化剂前体进行聚合而得到。半等规聚丙烯与等规或间规聚丙烯的混合的用量可以在1-90%(重量)的范围内,但要取决于被增塑的塑料所需的物理性质,优选是半等规聚丙烯在混合物中与等规或间规聚丙烯的用量在5-50%(重量)的范围内,而更优选是与等规或间规聚丙烯一起在混合物中的半等规聚丙烯的用量大约为10%(重量)。
已对本发明作了一般性的说明,下列实施例将给出本发明的部分实施方案及实施实例及其优点,通过说明,可理解所给出的这些实例,并且不意味着以任何方式的对说明书或其后的权利要求的限制。
实施例1
A.制备3,6,6-三甲基亚甲基环戊二烯
150毫升的甲基环戊二烯二聚体与100毫升矿物油在60℃进行分级蒸馏,并在0℃加以收集。在0℃,将500毫摩尔的甲基锂(1.4M;在乙醚中)逐滴加入到500毫摩尔的新蒸馏的甲基环戊二烯和137毫升的干燥丙酮中。将此溶液在25℃搅拌1小时,在用100毫升的饱和的NH4Cl水溶液萃取,并在MgSO4进行干燥之后,由通过真空蒸馏而得有机层中收集8℃(收率为85%)的3,6,6-三甲基亚甲基环戊二烯。
B.制备ipr(3-MeCP-1-Flu)
将1摩尔3,6,6-三甲基亚甲基环戊二烯溶于100毫升的四氢呋喃中,并将其逐滴地加到含有1摩尔的溶于大约100毫升四氢呋喃和714毫升的乙醚中的芴基阴离子的锂盐冷(-78℃)溶液中。将混合物加热至室温,通过用NH4Cl水溶液进行萃取、在MgSO4上进行干燥。在真空下过滤浓缩得到一油状物,再溶于氯仿中,沉淀,并用过量甲醇洗涤,从所得有机层中得到作为单一异构件的18克的白色粉末。1HNMR(核磁共振)CD2Cl2,Int.ref.Me4Si δ=0ppm:7.7d,7.3t,7.2d和7.1t(8)(Flu C6环);6.5t和5.6d(2)(CP乙烯基);4.1S(1)(Flu C5环次甲基);2.95S(2)(CP亚甲基);2.2d(3)(CP甲基);1.0S(6)(异丙基甲基)。(1立体异构体:CP亚甲基作为单一的信号出现,因为该亚甲基同时在ipr桥接和CP甲基的α位上)。
Cl在二氯甲烷中制备异亚丙基(3-甲基环戊二烯基-1-芴基)二氯化锆。
将2当量的甲基锂(1.4M,在乙醚中)在-78℃,逐滴加入到溶于100毫升的四氢呋喃中的5克异亚丙基(3-甲基环戊二烯-1-芴)中,加热至25℃,搅拌12小时,通过在真空下蒸发溶剂而分离出红色的二锂盐,然后通过用每分150毫升的干的、脱氧的戊烷(该戊烷随之被除去)洗涤二次以加以纯化,将二阴离子在-78℃溶于二氯甲烷中,并将等当量的在-78℃、125毫升CH2Cl2中成淤浆的ZrCl4快速加入到含有可溶性二阴离子的烧瓶中,搅拌混合物并慢慢地加热至25℃,并搅拌12小时。一种白色的固体物被过滤出来。通过在真空下浓缩二氯甲烷、冷却至-20℃,冷却时间为12小时,并取走浮在上层的部分,而得到对空气有一定程度的敏感性的、3克橙色粉末。将该产品用二氯甲烷进行重结晶而加以纯化,其ZrCl2C22H20理论值为:C,59;H,4.5。测定值为:C,56;H,4.4。1HNMR(核磁共振)(δ,ppm)CD2Cl2,Int.ref.TMSδ=0ppm:8.15-8.10 2d(2),7.87-7.78 2d(2),7.55-7.48 2t(2),7.27-7.21m(2)(Flu C6环);5.93t(1),5.63t(1),5,42t(1)(CP乙烯基);2,4d(6)(异丙烯甲基);2.0S(3)(CP甲基)。C2,在四氢呋喃中制备异亚丙基(3-甲基环戊;烯-1-芴基)二氯化锆。
在搅拌下于25℃,将34毫摩尔在乙醚(1.4摩尔)中的甲基锂,逐滴地加入到5克异亚丙基(3-甲基环戊二烯基-1-芴)配位体中,然后将其溶于75毫升的四氢呋喃中(它预先装在被装有侧臂和滴液漏斗的园底烧瓶中),当气体停止放出之后,将此暗橙色/红色的溶液搅拌数小时。将6.41克的ZrCl4·2四氢呋喃在40℃溶于100毫升的四氢呋喃中,在25℃,将上述的二阴离子装入含有ZrCl4·2四氢呋喃的烧瓶中,将该混合物搅拌18小时。然后再将该溶液装入一烧瓶中,并冷却到-20℃,以得到结晶产品,另外,在真空下蒸发出四氢呋喃。将5毫升的LiCl/ipr[3MeCP-1-Flu] ZrCl2混合物加到甲基铝氧烷中,用于聚合试验。
实施例Ⅱ
将1.4毫升的甲基铝氧烷(MAO)与5毫克如按实施例1在四氢呋喃中制备的ipr(3MeCP-1-Flu)ZrCl2混合,并溶于10-20毫升甲苯中。该MAO为37%(重量)(Scherring)。把1.2升的丙烯加入反应器中,将此混合物搅拌10分钟,反应温度保持在60℃。
将催化剂溶液加到50毫升不锈钢钢瓶中,把200毫升丙烯通过钢瓶泵入反应器中,将反应器中的内装物被搅拌60分钟。
反应产物在真空下干燥。称重聚合物,并进行分子量分布分析,其结果示于表1中。
实施例Ⅲ
重复实施例Ⅱ的程序,用1.4毫升的甲基铝氧烷、1.2升的丙烯、5毫升的ipr(3MeCp-1-Flu)ZrCl2反应温度为30℃,反应运行时间为60分钟,所得结果示于表1中。
实施例Ⅳ
重复实施例Ⅱ的程序,用1.4毫升的甲基铝氧烷、1.2升的丙烯、5毫克按实施例Ⅰ在MeCl2中所制得的ipr(3MeCP-1-Flu)ZrCl2,反应器温度为65℃,运行时间为60分钟,所得结果示于表1中。
由本实验的聚合物、得到C-13核磁共振谱按“半有规立构聚丙烯(一种新型立构规整度聚合物的实例)的方法为基础计算半等规聚丙烯的内消旋和外消旋聚合物结构的特定序列所出现的几率。
把计算值与观察值作为核磁共振谱的相对强度的函数的结果示于表Ⅱ中。
实施例Ⅴ
将5.0毫升的甲基铝氧烷与5毫克如按上述实施例在二氯甲烷中制备的ipr(3MeCP-1-Flu)ZrCl2混合,并溶于10-20毫升的甲苯中。该甲基铝氧烷为10%(重量)(SCherring)。将1.4升的丙烯加到反应器中,搅拌混合物10分钟,反应器温度被保持在60℃。
将0.4毫克的异亚丙基(环戊二烯基-1-芴基)二化锆(简写为ipr(CP-1-Flu)ZrCl2),单独地溶于10-20毫升的甲苯中,再把二种催化剂溶液混合在一起,并加到50毫升的不锈钢钢瓶中,将200毫升的丙烯经钢瓶泵入到反应器中。将反应器的内容物搅拌60分钟。
将反应产物在真空下干燥,称重聚合物并测定其熔点,其结果示于表1中。
所有一般合成程序都在惰性气氛下,使用真空气氛手套箱或Schlenk技术设备来进行的。甲苯、戊烷、及四氢呋喃溶剂都是在氮气氛下,在红紫钠/二苯甲酮一羰游基的存在下进行蒸馏的,二氯甲烷是在氮气氛下从新鲜的氢化钙中蒸馏出来。
下列结果是使用本发明的方法,由上述进行的实验中所得到的结果。
表1
实施例  金属茂化合物  甲基铝氧烷  丙烯  温度
毫克  毫升数  升  ℃
ipr(3MeCP-1-Flu)ZrCl2
2  5  1.4  1.2  60
3  5  1.4  1.2  30
4  5  1.4  1.2  65
ipr(3MeCP-1-Flu)ZrCl2/
ipr(CP-1-Flu)ZrCl2
5  5/0.4  5.0  1.4  60
时间  收率  重均分子量/数均分子量
实施例  分钟  克
2  60  184  1.9
3  60  32
4  60  297  3.4
5  60  162
表Ⅱ
序列  计算值  测量值
mmmm  0.15  0.14
mmmr  0.11  0.12
rmmr  0.07  0.06
mmrr  0.25  0.21
xmrx  0.00  0.05
mrmr  0.00  0.00
rrrr  0.23  0.19
rrrm  0.14  0.14
mrrm  0.06  0.08
本发明已经采用一种已知的具有双侧面对称性的间规催化剂前体,并在一个环戊二烯基基团上引入一个甲基以消除其双侧面对称性。由于聚丙烯中的甲基每隔一个的处于上述的弗歇尔投影平面的上部,则该新的催化剂制备出了被称之为半等规聚丙烯结构,半等规聚丙烯是非结晶的,并可以与间规和等规聚丙烯一起用作增塑剂。
显然,借助于上述的介绍,对本发明进行许多改进和其他是可能的。应该理解,在本发明权利要求的范围内,除了本文所作的特殊说明之外,本发明是可以实施的。

Claims (14)

1、一种包括通式为下式的金属茂化合物:
式中CP是环戊二烯基或取代的环戊二烯基,每个R和R′是具有1-20个碳原子的烃基,可相同或不同,并且要进行选择以使CPR′m是在空间上与CPRn不同的环,从而导致该化合物缺乏双侧面对称性,R″是给予化合物以立体刚性的桥接的结构,M是第4族金属,n为0至4,m为0至4及Hal是卤素。
2、一种按照权利要求1所述的金属茂化合物,其中,M是钛、锆和铪。
3、一种按照权利要求1所述的金属茂化合物、其中Hal是氯。
4、一种按照权利要求1所述的金属茂化合物,其中,该化合物是异亚丙基(3-甲基环戊二烯基-1-芴基)二氯化锆。
5、一种金属茂催化剂,包括:
(a)一种金属茂化合物;和
(b)一种离子化试剂;
其中,该金属茂化合物包括下列的通式:
式中CP是环戊二烯基,每个R和R′是具有1-20个碳原子的烃基,可相同或不同,并且要进行选择以使CPR′m与CPRn是在空间上是不同的环,从而导致该化合物缺乏双侧面对称性,R″是给予化合物立体刚性的桥接结构,M是第3族、第4族、第5族或第6族金属,n为0至4,m为0至4,及Hal是卤素。
6、一种按照权利要求5所述的金属茂化合物,其中M选自钛、锆、铪。
7、一种按照权利要求5所述的金属茂化合物,其中,Hal是氯。
8、一种按照权利要求5所述的金属茂化合物,其中,该化合物是异亚丙基(3-甲基环戊二烯基-1-芴基)二氯化锆。
9、一种包括一种聚合物的增塑剂,该聚合物具有由下列分子式为特征的取代的乙烯基化合物的单体所得链节:CH2=CHRS式中RS是烃基或非烃基取代基,及其中,在下列结构式中,聚合物的特征在于RS基团每隔一个连接到聚合物主链的同一侧的不对称碳原子上,及RS基团还连接到剩余的不对称碳原子上,处于与已经每隔一个地连接到不对称碳原子的RS基团在相同一侧,或者在相反一侧。
Figure 901092150_IMG1
10、一种按照权利要求9所述的增塑剂,其中,单体是丙烯,并且,该增塑剂与选自等规聚丙烯和间规聚丙烯塑料一起使用。
11、一种按照权利要求10所述的增塑剂,其中,塑料是间规聚丙烯。
12、一种按照权利要求11所述的增塑剂,其中,增塑剂的用量是1-90%(重量)。
13、一种按照权利要求12所述的增塑剂,其中,增塑剂的用量是5-50%(重量)。
14、一种按照权利要求13所述的增塑剂,其中,增塑剂的用量大约是10%(重量)。
CN90109215A 1989-10-10 1990-10-10 生产半等规聚丙烯的催化剂 Expired - Fee Related CN1028532C (zh)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US419.221 1989-10-10
US07/419,221 US5036034A (en) 1989-10-10 1989-10-10 Catalyst for producing hemiisotactic polypropylene
US419,221 1989-10-10

Related Child Applications (1)

Application Number Title Priority Date Filing Date
CN94108568A Division CN1058022C (zh) 1989-10-10 1994-08-16 制备反应器混合物的方法

Publications (2)

Publication Number Publication Date
CN1051735A true CN1051735A (zh) 1991-05-29
CN1028532C CN1028532C (zh) 1995-05-24

Family

ID=23661315

Family Applications (2)

Application Number Title Priority Date Filing Date
CN90109215A Expired - Fee Related CN1028532C (zh) 1989-10-10 1990-10-10 生产半等规聚丙烯的催化剂
CN94108568A Expired - Fee Related CN1058022C (zh) 1989-10-10 1994-08-16 制备反应器混合物的方法

Family Applications After (1)

Application Number Title Priority Date Filing Date
CN94108568A Expired - Fee Related CN1058022C (zh) 1989-10-10 1994-08-16 制备反应器混合物的方法

Country Status (11)

Country Link
US (2) US5036034A (zh)
EP (2) EP0742227B1 (zh)
JP (1) JPH03193796A (zh)
KR (1) KR0181495B1 (zh)
CN (2) CN1028532C (zh)
AT (2) ATE199722T1 (zh)
CA (1) CA2027124C (zh)
DE (2) DE69033435T3 (zh)
DK (2) DK0423101T4 (zh)
ES (2) ES2155909T3 (zh)
GR (2) GR3033307T3 (zh)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7241848B2 (en) 2002-10-30 2007-07-10 Mitsui Chemicals, Inc. Process for preparing low molecular weight olefin (CO)polymer and polymerization catalyst used therefor

Families Citing this family (244)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5324800A (en) * 1983-06-06 1994-06-28 Exxon Chemical Patents Inc. Process and catalyst for polyolefin density and molecular weight control
US5225500A (en) * 1988-07-15 1993-07-06 Fina Technology, Inc. Process and catalyst for producing syndiotactic polyolefins
US4892851A (en) 1988-07-15 1990-01-09 Fina Technology, Inc. Process and catalyst for producing syndiotactic polyolefins
DE3916553A1 (de) * 1989-05-20 1990-11-22 Hoechst Ag Syndio- isoblockpolymer und verfahren zu seiner herstellung
US5117020A (en) * 1989-10-30 1992-05-26 Fina Research, S.A. Process for the preparation of metallocenes
US5387568A (en) * 1989-10-30 1995-02-07 Fina Technology, Inc. Preparation of metallocene catalysts for polymerization of olefins
US6294625B1 (en) 1990-03-20 2001-09-25 Exxonmobil Chemical Patents Inc. Catalyst system of enhanced productivity and its use in polymerization process
ES2071888T3 (es) * 1990-11-12 1995-07-01 Hoechst Ag Bisindenilmetalocenos sustituidos en posicion 2, procedimiento para su preparacion y su utilizacion como catalizadores en la polimerizacion de olefinas.
US5206197A (en) * 1991-03-04 1993-04-27 The Dow Chemical Company Catalyst composition for preparation of syndiotactic vinyl aromatic polymers
EP0503422B1 (de) * 1991-03-09 1998-06-03 TARGOR GmbH Verfahren zur Herstellung chemisch einheitlicher Cycloolefincopolymere
CA2067525C (en) 1991-05-09 1998-09-15 Helmut G. Alt Organometallic fluorenyl compounds, preparation and use
US5436305A (en) * 1991-05-09 1995-07-25 Phillips Petroleum Company Organometallic fluorenyl compounds, preparation, and use
US5571880A (en) * 1991-05-09 1996-11-05 Phillips Petroleum Company Organometallic fluorenyl compounds and use thereof in an alpha-olefin polymerization process
US5391789A (en) * 1991-08-08 1995-02-21 Hoechst Aktiengesellschaft Bridged, chiral metallocenes, processes for their preparation and their use as catalysts
US5416228A (en) * 1991-10-07 1995-05-16 Fina Technology, Inc. Process and catalyst for producing isotactic polyolefins
GB9125645D0 (en) * 1991-12-03 1992-01-29 Smithkline Beecham Plc Novel compounds
US6245870B1 (en) * 1992-03-20 2001-06-12 Fina Technology, Inc. Process for producing syndiotactic/isotactic block polyolefins
US5302733A (en) * 1992-03-30 1994-04-12 Ethyl Corporation Preparation of metallocenes
US5434116A (en) * 1992-06-05 1995-07-18 Tosoh Corporation Organic transition metal compound having π-bonding heterocyclic ligand and method of polymerizing olefin by using the same
JP3398381B2 (ja) * 1992-07-01 2003-04-21 エクソンモービル・ケミカル・パテンツ・インク 遷移金属オレフィン重合触媒
DE4313413A1 (de) * 1993-04-23 1994-10-27 Basf Ag 3-(Het)aryloxy(thio)-Carbonsäurederivate, Verfahren und Zwischenprodukte zu ihrer Herstellung
CA2120315C (en) * 1993-04-30 2001-05-15 Joel L. Williams Medical articles and process therefor
US5372980A (en) * 1993-06-03 1994-12-13 Polysar Bimetallic metallocene alumoxane catalyst system and its use in the preparation of ethylene-alpha olefin and ethylene-alpha olefin-non-conjugated diolefin elastomers
US5486585A (en) * 1993-08-26 1996-01-23 Exxon Chemical Patents Inc. Amidosilyldiyl bridged catalysts and method of polymerization using said catalysts.
US5459117A (en) * 1993-08-27 1995-10-17 Ewen; John A. Doubly-conformationally locked, stereorigid catalysts for the preparation of tactiospecific polymers
US5631202A (en) 1993-09-24 1997-05-20 Montell Technology Company B.V. Stereospecific metallocene catalysts with stereolocking α-CP substituents
US5420320A (en) * 1994-06-08 1995-05-30 Phillips Petroleum Company Method for preparing cyclopentadienyl-type ligands and metallocene compounds
ES2164774T3 (es) * 1994-08-03 2002-03-01 Exxonmobil Chem Patents Inc Composicion catalitica ionica soportada.
US6143686A (en) * 1994-08-03 2000-11-07 Exxon Chemical Patents, Inc. Supported ionic catalyst compositions
DE4431838A1 (de) * 1994-09-07 1996-03-14 Basf Ag Geträgerte Metallocen-Katalysatorsysteme
IT1272924B (it) * 1995-01-23 1997-07-01 Spherilene Srl Procedimento per la preparazione di composti ciclopentadienilici e composti cosi' ottenibili
US5883278A (en) * 1995-04-24 1999-03-16 Albemarle Corporation Enhanced synthesis of racemic metallocenes
US5556997A (en) * 1995-04-24 1996-09-17 Albemarle Corporation Enhanced synthesis of racemic metallocenes
US6403772B1 (en) * 1995-09-11 2002-06-11 Montell Technology Company, Bv Open-pentadienyl metallocenes, precursors thereof and polymerization catalysts therefrom
US5709921A (en) * 1995-11-13 1998-01-20 Kimberly-Clark Worldwide, Inc. Controlled hysteresis nonwoven laminates
US5679814A (en) * 1995-12-11 1997-10-21 Albemarle Corporation Purification of metallocenes
DE69720823T2 (de) 1996-01-25 2004-01-22 Tosoh Corp., Shinnanyo Verfahren zur Olefinpolymerisierung unter Verwendung eines Übergangsmetallkatalysators.
US5914289A (en) * 1996-02-19 1999-06-22 Fina Research, S.A. Supported metallocene-alumoxane catalysts for the preparation of polyethylene having a broad monomodal molecular weight distribution
US6225426B1 (en) * 1996-04-10 2001-05-01 Uniroyal Chemical Company, Inc. Process for producing polyolefin elastomer employing a metallocene catalyst
US6313242B1 (en) 1996-05-20 2001-11-06 Fina Technology, Inc. Stereorigid bis-fluorenyl metallocenes
US5945365A (en) * 1996-05-20 1999-08-31 Fina Technology, Inc. Stereorigid bis-fluorenyl metallocenes
US5710299A (en) * 1996-06-27 1998-01-20 Albemarle Corporation Production of bridged metallocene complexes and intermediates therefor
US6759499B1 (en) * 1996-07-16 2004-07-06 Exxonmobil Chemical Patents Inc. Olefin polymerization process with alkyl-substituted metallocenes
US5760262A (en) * 1996-09-17 1998-06-02 Albemarle Corporation Enhanced production of bridged hafnocenes
JPH10101727A (ja) * 1996-09-24 1998-04-21 Shell Internatl Res Maatschappij Bv オレフィン又はポリマーを水素化するための触媒及び方法
US5936108A (en) * 1996-10-17 1999-08-10 Albemarle Corporation Metallocene synthesis
US5780660A (en) * 1996-11-07 1998-07-14 Albemarle Corporation Zirconocene ismerization process
PL188107B1 (pl) * 1996-11-15 2004-12-31 Montell Technology Company Bv Metalocen, układ katalityczny do polimeryzacji, kationowe metaloceny, ligand oraz sposób polimeryzacji
US6177377B1 (en) * 1996-12-18 2001-01-23 Amherst Polymer Technology, Inc. Polymer blends and process for preparation
US5851945A (en) * 1997-02-07 1998-12-22 Exxon Chemical Patents Inc. Olefin polymerization catalyst compositions comprising group 5 transition metal compounds stabilized in their highest metal oxidation state
US5807800A (en) * 1997-02-11 1998-09-15 Fina Technology, Inc. Process for producing stereospecific polymers
US6160072A (en) * 1997-05-02 2000-12-12 Ewen; John A. Process for polymerizing tactioselective polyolefins in condensed phase using titanocenes
US6228795B1 (en) 1997-06-05 2001-05-08 Exxon Chemical Patents, Inc. Polymeric supported catalysts
US5905162A (en) * 1997-08-12 1999-05-18 Albemarle Corporation Enhanced production of bridged hafnocenes
US6265512B1 (en) 1997-10-23 2001-07-24 3M Innovative Company Elastic polypropylenes and catalysts for their manufacture
JP3559894B2 (ja) 1998-04-01 2004-09-02 日産自動車株式会社 樹脂製ウィンドウ及びその製法
KR100380018B1 (ko) 1998-04-09 2003-10-04 주식회사 엘지화학 메탈로센담지촉매및이를이용한올레핀중합방법
EP0965603A1 (en) * 1998-06-19 1999-12-22 Fina Research S.A. Polyolefin production
US5965759A (en) * 1998-09-23 1999-10-12 Albemarle Corporation Catalytic process for isomerizing metallocenes
US6225427B1 (en) 1998-10-15 2001-05-01 Uniroyal Chemical Company, Inc. Olefin polymerization process employing metallocene catalyst provided by cocatalyst activation of a metallocene procatalyst
US6469188B1 (en) 1999-01-20 2002-10-22 California Institute Of Technology Catalyst system for the polymerization of alkenes to polyolefins
US6270912B1 (en) 1999-02-25 2001-08-07 Mobil Oil Corporation Multi-layer films with core layer of metallocene-catalyzed polypropylene
EP1031582A1 (en) * 1999-02-26 2000-08-30 Fina Research S.A. Use and production of polypropylene
US6432860B1 (en) * 1999-03-22 2002-08-13 Fina Technology, Inc. Supported metallocene catalysts
US6410124B1 (en) 1999-03-30 2002-06-25 Exxonmobil Oil Corporation Films with improved metallizable surfaces
EP1059332A1 (en) 1999-06-10 2000-12-13 Fina Research S.A. Polypropylene with high melt strength and drawability
US6252098B1 (en) 2000-06-05 2001-06-26 Albemarle Corporation Enhanced synthesis of racemic metallocenes
EP1300423A1 (en) * 2001-09-27 2003-04-09 Atofina Research S.A. Catalyst system comprising a mixture of catalyst components for producing a polyolefin blend
EP1323747A1 (en) 2001-12-19 2003-07-02 Borealis Technology Oy Production of olefin polymerisation catalysts
ES2321806T3 (es) 2001-12-19 2009-06-12 Borealis Technology Oy Produccion de catalizadores soportados para la polimerizacion de olefinas.
US7998579B2 (en) 2002-08-12 2011-08-16 Exxonmobil Chemical Patents Inc. Polypropylene based fibers and nonwovens
US8003725B2 (en) 2002-08-12 2011-08-23 Exxonmobil Chemical Patents Inc. Plasticized hetero-phase polyolefin blends
AU2003272213A1 (en) 2002-08-12 2004-02-25 Exxonmobil Chemical Patents Inc. Plasticized polyolefin compositions
US7531594B2 (en) 2002-08-12 2009-05-12 Exxonmobil Chemical Patents Inc. Articles from plasticized polyolefin compositions
US7271209B2 (en) 2002-08-12 2007-09-18 Exxonmobil Chemical Patents Inc. Fibers and nonwovens from plasticized polyolefin compositions
US6773818B2 (en) 2002-09-06 2004-08-10 Exxonmobil Oil Corporation Metallized, metallocene-catalyzed, polypropylene films
US8008412B2 (en) 2002-09-20 2011-08-30 Exxonmobil Chemical Patents Inc. Polymer production at supersolution conditions
US7223822B2 (en) 2002-10-15 2007-05-29 Exxonmobil Chemical Patents Inc. Multiple catalyst and reactor system for olefin polymerization and polymers produced therefrom
US7541402B2 (en) 2002-10-15 2009-06-02 Exxonmobil Chemical Patents Inc. Blend functionalized polyolefin adhesive
US7700707B2 (en) 2002-10-15 2010-04-20 Exxonmobil Chemical Patents Inc. Polyolefin adhesive compositions and articles made therefrom
US7550528B2 (en) 2002-10-15 2009-06-23 Exxonmobil Chemical Patents Inc. Functionalized olefin polymers
US7524910B2 (en) 2002-10-15 2009-04-28 Exxonmobil Chemical Patents Inc. Polyolefin adhesive compositions and articles made therefrom
KR101087179B1 (ko) 2003-03-28 2011-11-25 미쓰이 가가쿠 가부시키가이샤 폴리올레핀 수지 조성물
US6855783B2 (en) 2003-04-11 2005-02-15 Fina Technology, Inc. Supported metallocene catalysts
ES2377948T3 (es) 2003-06-20 2012-04-03 Borealis Polymers Oy Procedimiento para la preparación de una composición de un catalizador para la polimerización de olefinas
US8192813B2 (en) 2003-08-12 2012-06-05 Exxonmobil Chemical Patents, Inc. Crosslinked polyethylene articles and processes to produce same
US7211536B2 (en) * 2004-10-22 2007-05-01 Fina Technology, Inc. Supported metallocene catalysts and their use in producing stereospecific polymers
US20050182210A1 (en) 2004-02-17 2005-08-18 Natarajan Muruganandam De-foaming spray dried catalyst slurries
US7601666B2 (en) 2004-07-08 2009-10-13 Exxonmobil Chemical Patents Inc. Olefin polymerization catalyst system and process for use thereof
WO2006025540A1 (ja) * 2004-08-30 2006-03-09 Mitsui Chemicals, Inc. プロピレン系重合体の製造方法
GB0423555D0 (en) 2004-10-22 2004-11-24 Borealis Tech Oy Process
CN100390256C (zh) 2004-11-26 2008-05-28 三井化学株式会社 合成润滑油和润滑油组合物
US8389615B2 (en) 2004-12-17 2013-03-05 Exxonmobil Chemical Patents Inc. Elastomeric compositions comprising vinylaromatic block copolymer, polypropylene, plastomer, and low molecular weight polyolefin
US20060255501A1 (en) * 2005-05-11 2006-11-16 Shawcor Ltd. Crosslinked chlorinated polyolefin compositions
WO2006126608A1 (ja) * 2005-05-25 2006-11-30 Mitsui Chemicals, Inc. フルオレン誘導体、遷移金属化合物、オレフィン重合用触媒およびオレフィン系重合体の製造方法
US20090043057A1 (en) * 2005-05-25 2009-02-12 Mitsui Chemicals , Inc. Transition Metal Compound, Catalyst for Olefin Polymerization, and Process for Producing Olefin Polymer
DE112006001733T5 (de) 2005-07-01 2008-07-31 Albemarle Corporation Aluminoxanatsalzzusammensetzungen mit verbesserter Stabilität in aromatischen und aliphatischen Lösungsmitteln
EP1904576B1 (en) 2005-07-15 2012-04-25 ExxonMobil Chemical Patents Inc. Elastomeric compositions
ATE478921T1 (de) 2005-10-21 2010-09-15 Borealis Tech Oy Zusammensetzung
EP1795542A1 (en) 2005-12-07 2007-06-13 Borealis Technology Oy Polymer
EP1803743B1 (en) 2005-12-30 2016-08-10 Borealis Technology Oy Catalyst particles
US7517939B2 (en) 2006-02-02 2009-04-14 Chevron Phillips Chemical Company, Lp Polymerization catalysts for producing high molecular weight polymers with low levels of long chain branching
US7619047B2 (en) 2006-02-22 2009-11-17 Chevron Phillips Chemical Company, Lp Dual metallocene catalysts for polymerization of bimodal polymers
EP1834970B1 (en) * 2006-03-15 2014-05-14 Styrolution GmbH A process for producing polyolefin-polyvinylaromatic-block copolymers
EP1847555A1 (en) 2006-04-18 2007-10-24 Borealis Technology Oy Multi-branched Polypropylene
ATE480586T1 (de) 2006-07-14 2010-09-15 Borealis Tech Oy Polyethylen hoher dichte
US7601255B2 (en) 2006-09-06 2009-10-13 Chemtura Corporation Process for removal of residual catalyst components
US8242237B2 (en) 2006-12-20 2012-08-14 Exxonmobil Chemical Patents Inc. Phase separator and monomer recycle for supercritical polymerization process
EP1950243B1 (en) 2007-01-22 2010-03-24 Borealis Technology Oy Polypropylene composition with low surface energy
WO2008150572A1 (en) 2007-06-04 2008-12-11 Exxonmobil Chemical Patents Inc. Super-solution homogeneous propylene polymerization
EP2112175A1 (en) 2008-04-16 2009-10-28 ExxonMobil Chemical Patents Inc. Activator for metallocenes comprising one or more halogen substituted heterocyclic heteroatom containing ligand coordinated to an alumoxane
US20100280206A1 (en) 2007-11-09 2010-11-04 Borealis Technology Oy Polyethylene copolymer
US8318875B2 (en) 2008-01-18 2012-11-27 Exxonmobil Chemical Patents Inc. Super-solution homogeneous propylene polymerization and polypropylenes made therefrom
US8052822B2 (en) * 2008-02-15 2011-11-08 Exxonmobil Chemical Patents Inc. Blends of low crystallinity, low molecular weight propylene copolymers and styrenic block copolymers
US9938400B2 (en) * 2008-04-23 2018-04-10 Exxonmobil Chemical Patents Inc. Propylene copolymers in soft thermoplastic blends
EP2130860A1 (en) 2008-06-06 2009-12-09 Borealis Technology Oy Polymer
EP2133389A1 (en) 2008-06-12 2009-12-16 Borealis AG Polypropylene composition
US8765872B2 (en) 2008-07-10 2014-07-01 Mitsui Chemicals, Inc. 4-methyl-1-pentene polymer, resin composition containing 4-methyl-1-pentene polymer, masterbatch thereof, and formed product thereof
KR101312155B1 (ko) 2008-07-10 2013-09-26 미쓰이 가가쿠 가부시키가이샤 4-메틸-1-펜텐계 중합체 및 4-메틸-1-펜텐계 중합체 함유 수지 조성물, 및 그의 마스터배치 및 그들의 성형품
WO2010052264A1 (en) 2008-11-07 2010-05-14 Borealis Ag Solid catalyst composition
ES2392698T3 (es) 2008-11-10 2012-12-13 Borealis Ag Proceso para la preparación de un sistema catalizador metalocénico sólido, sin soporte, y su uso en la polimerización de olefinas
EP2186831B1 (en) 2008-11-10 2013-01-02 Borealis AG Process for the preparation of an unsupported, solid olefin polymerisation catalyst and use in polymerisation of olefins
EP2204410A1 (en) 2008-12-31 2010-07-07 Borealis AG Article coated with a composition comprising polyethylene prepared with a single site catalyst
WO2010080871A1 (en) 2009-01-08 2010-07-15 Univation Technologies, Llc Additive for gas phase polymerization processes
JP5661645B2 (ja) 2009-01-08 2015-01-28 ユニベーション・テクノロジーズ・エルエルシー ポリオレフィン重合プロセス用の添加剤
EP2275476A1 (en) 2009-06-09 2011-01-19 Borealis AG Automotive material with excellent flow, high stiffness, excellent ductility and low CLTE
DE102009027447A1 (de) 2009-07-03 2011-01-05 Evonik Degussa Gmbh Modifizierte Polyolefine mit besonderem Eigenschaftsprofil, Verfahren zu deren Herstellung und deren Verwendung
CN102482372B (zh) 2009-07-23 2013-09-04 尤尼威蒂恩技术有限公司 聚合反应系统
US8067652B2 (en) 2009-08-13 2011-11-29 Chemtura Corporation Processes for controlling the viscosity of polyalphaolefins
SI2308923T1 (sl) 2009-10-09 2012-08-31 Borealis Ag Kompozit iz steklenih vlaken z izboljšano obdelovalnostjo
KR101408423B1 (ko) 2009-11-06 2014-06-17 미쓰이 가가쿠 가부시키가이샤 4-메틸-1-펜텐·α-올레핀 공중합체, 이 공중합체를 포함하는 조성물 및 4-메틸-1-펜텐 공중합체 조성물
EP2330136B1 (en) 2009-12-07 2013-08-28 Borealis AG Process for the preparation of an unsupported, solid metallocene catalyst system and its use in polymerization of olefins
ES2535323T3 (es) 2009-12-22 2015-05-08 Borealis Ag Preparación de catalizadores de sitio único
EP2338920A1 (en) 2009-12-22 2011-06-29 Borealis AG Preparation of single-site catalysts
KR101424366B1 (ko) 2009-12-22 2014-07-31 보레알리스 아게 단일-위치 촉매 존재 하의 폴리프로필렌의 제조
WO2011078923A1 (en) 2009-12-23 2011-06-30 Univation Technologies, Llc Methods for producing catalyst systems
JP5798113B2 (ja) 2010-04-28 2015-10-21 三井化学株式会社 4−メチル−1−ペンテン系重合体からなる樹脂微粉末、およびそれを含む組成物、ならびにその製造方法
EP2386582B1 (en) 2010-05-07 2016-02-17 Borealis AG Preparation of a solid catalyst system
EP2386581B1 (en) 2010-05-07 2014-03-26 Borealis AG Preparation of a solid catalyst system
EP2386583A1 (en) 2010-05-07 2011-11-16 Borealis AG Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins
EP2385073A1 (en) 2010-05-07 2011-11-09 Borealis AG Process for the preparation of a solid metallocene catalyst system and its use in polymerisation of olefins
US20120135903A1 (en) 2010-05-11 2012-05-31 Mitsui Chemicals, Inc. Lubricating oil composition
EP2415598B1 (en) 2010-08-06 2014-02-26 Borealis AG Multilayer film
EP2632980B1 (en) 2010-10-28 2018-05-16 Borealis AG Single site polymer
JP6023069B2 (ja) 2010-11-22 2016-11-09 アルベマール・コーポレーシヨン 活性剤組成物、その製造及び触媒中でのその使用
EP2495264B1 (en) 2011-03-04 2013-05-08 Borealis AG Exterior automotive article with reduced paintability failure
US9153757B2 (en) 2011-08-01 2015-10-06 Mitsui Chemicals, Inc. Thermoplastic resin composition for reflective material, reflective plate, and light-emitting diode element
EP2554375B1 (en) 2011-08-03 2014-04-09 Borealis AG Film
EP2799488B1 (en) 2011-12-27 2016-07-20 Mitsui Chemicals, Inc. 4-methyl-1-pentene (co)polymer composition, and film and hollow molded body, each of which is formed from 4-methyl-1-pentene (co)polymer composition
US9328232B2 (en) 2012-02-24 2016-05-03 Japan Polypropylene Corporation Propylene-ethylene copolymer resin composition and moulded article, film and sheet thereof
EP2832755B1 (en) 2012-03-28 2017-10-11 Mitsui Chemicals, Inc. Propylene/alpha-olefin copolymer and application thereof
BR112014024333B1 (pt) 2012-04-04 2020-12-22 Borealis Ag composição de polipropileno reforçada com fibra de alto fluxo
EP2841471B1 (en) 2012-04-27 2020-05-06 W. R. Grace & Co. - Conn. Activator compositions, their preparation, and their use in catalysts
KR101720439B1 (ko) 2012-08-22 2017-03-27 미쓰이 가가쿠 가부시키가이샤 부직포 적층체
JP6033322B2 (ja) 2012-09-25 2016-11-30 三井化学株式会社 遷移金属化合物、オレフィン重合用触媒およびオレフィン重合体の製造方法
EP2902419B1 (en) 2012-09-25 2020-08-19 Mitsui Chemicals, Inc. Method for producing olefin polymer, and olefin polymer
ES2711081T3 (es) 2012-10-18 2019-04-30 Borealis Ag Catalizador para la polimerización de olefinas
EP2722344B1 (en) 2012-10-18 2017-03-22 Borealis AG Polymerisation process
EP2722346A1 (en) 2012-10-18 2014-04-23 Borealis AG Polymerisation process and catalyst
US8937139B2 (en) 2012-10-25 2015-01-20 Chevron Phillips Chemical Company Lp Catalyst compositions and methods of making and using same
US8895679B2 (en) 2012-10-25 2014-11-25 Chevron Phillips Chemical Company Lp Catalyst compositions and methods of making and using same
US9321914B2 (en) 2012-10-31 2016-04-26 Exxonmobil Chemical Patents Inc. Propylene copolymer compositions and processes to produce them
CN104755515B (zh) 2012-11-01 2017-08-25 尤尼威蒂恩技术有限责任公司 用于改进的聚合物产品的混合相容齐格勒‑纳塔/铬催化剂
EP2921525B1 (en) 2012-11-19 2017-07-19 Mitsui Chemicals, Inc. Polyester resin composition, manufacturing method therefor, and camera module containing said polyester resin composition
JP5805332B2 (ja) 2012-11-30 2015-11-04 三井化学株式会社 光学材料用組成物およびその用途
US9034991B2 (en) 2013-01-29 2015-05-19 Chevron Phillips Chemical Company Lp Polymer compositions and methods of making and using same
US8877672B2 (en) 2013-01-29 2014-11-04 Chevron Phillips Chemical Company Lp Catalyst compositions and methods of making and using same
WO2014142111A1 (ja) 2013-03-12 2014-09-18 三井化学株式会社 オレフィン重合体の製造方法およびオレフィン重合用触媒
CN105264026B (zh) 2013-06-07 2018-04-03 三井化学株式会社 含有丙烯·α‑烯烃共聚物的烯烃类涂料
ES2612627T3 (es) 2013-07-24 2017-05-17 Borealis Ag Proceso
ES2607378T3 (es) 2013-07-24 2017-03-31 Borealis Ag Proceso
EP3033389B1 (en) 2013-08-14 2017-10-11 Borealis AG Propylene composition with improved impact resistance at low temperature
EA031054B1 (ru) 2013-08-21 2018-11-30 Бореалис Аг Композиция полиолефина с высокой текучестью, жесткостью и ударной вязкостью
WO2015024891A1 (en) 2013-08-21 2015-02-26 Borealis Ag High flow polyolefin composition with high stiffness and toughness
ES2587781T3 (es) 2013-09-27 2016-10-26 Borealis Ag Películas adecuadas para procesamiento BOPP de polímeros con altos XS y alta Tm
ES2568615T3 (es) 2013-10-11 2016-05-03 Borealis Ag Película para etiquetas orientada en la dirección de la máquina
ES2574428T3 (es) 2013-10-24 2016-06-17 Borealis Ag Artículo moldeado por soplado basado en copolímero al azar bimodal
WO2015059229A1 (en) 2013-10-24 2015-04-30 Borealis Ag Low melting pp homopolymer with high content of regioerrors and high molecular weight
CN105722869B (zh) 2013-10-29 2017-09-12 北欧化工公司 具有高聚合活性的固体单点催化剂
TWI635100B (zh) 2013-11-05 2018-09-11 三井化學股份有限公司 改質丙烯.α-烯烴共聚合體與其製造方法、含有其之塗佈材、成形用樹脂組成物及熱熔性組成物
MX368147B (es) 2013-11-22 2019-09-20 Borealis Ag Homopolímero de propileno de baja emisión con alto flujo de masa fundida.
US9828698B2 (en) 2013-12-04 2017-11-28 Borealis Ag Phthalate-free PP homopolymers for meltblown fibers
WO2015091839A1 (en) 2013-12-18 2015-06-25 Borealis Ag Bopp film with improved stiffness/toughness balance
US10227427B2 (en) 2014-01-17 2019-03-12 Borealis Ag Process for preparing propylene/1-butene copolymers
WO2015117948A1 (en) 2014-02-06 2015-08-13 Borealis Ag Soft and transparent impact copolymers
JP2017508032A (ja) 2014-02-06 2017-03-23 ボレアリス エージー 高衝撃強さを有する軟質コポリマー
EP2907841A1 (en) 2014-02-14 2015-08-19 Borealis AG Polypropylene composite
ES2659731T3 (es) 2014-05-20 2018-03-19 Borealis Ag Composición de polipropileno para aplicaciones en interiores de automóviles
EP3192817B1 (en) 2014-09-11 2020-12-23 Mitsui Chemicals, Inc. Method for producing olefin (co)polymer containing constituent unit derived from 1-butene
EP2995631A1 (en) 2014-09-12 2016-03-16 Borealis AG Process for producing graft copolymers on polyolefin backbone
CA2974392C (en) 2015-01-21 2023-10-17 Univation Technologies, Llc Methods for controlling polymer chain scission
SG11201705576YA (en) 2015-01-21 2017-08-30 Univation Tech Llc Methods for gel reduction in polyolefins
ES2724011T3 (es) 2015-02-27 2019-09-05 Borealis Ag Estructura de película laminada basada solo en polietileno
KR20180094974A (ko) 2015-12-15 2018-08-24 보레알리스 아게 장벽 특성을 갖는 폴리에틸렌-기반 적층된 필름 구조체
KR102398733B1 (ko) 2016-03-25 2022-05-16 미쓰이 가가쿠 가부시키가이샤 신축성 구조체, 다층 신축 시트, 방적사 및 섬유 구조체
EP3241611B1 (en) 2016-05-02 2020-03-04 Borealis AG A process for feeding a polymerisation catalyst
KR102219390B1 (ko) 2016-06-03 2021-02-26 보레알리스 아게 다층 구조
EP3472237B1 (en) 2016-06-21 2021-05-26 Borealis AG Polymer composition for wire and cable applications with advantageous thermomechanical behaviour and electrical properties
EP3261096A1 (en) 2016-06-21 2017-12-27 Borealis AG Cable and composition
EP3261095A1 (en) 2016-06-21 2017-12-27 Borealis AG Cable with improved electrical properties
EP3261093B1 (en) 2016-06-21 2023-08-02 Borealis AG Cable with advantageous electrical properties
WO2017220724A1 (en) 2016-06-23 2017-12-28 Borealis Ag Process for catalyst deactivation
WO2018091653A1 (en) 2016-11-18 2018-05-24 Borealis Ag Catalyst
EP3564346A4 (en) 2016-12-27 2020-09-02 Mitsui Chemicals, Inc. LUBRICATING OIL COMPOSITION, LUBRICATING OIL VISCOSITY MODIFIER, AND LUBRICATING OIL ADDITIVE COMPOSITION
CN110234689A (zh) 2017-02-02 2019-09-13 三井化学株式会社 发泡体、聚烯烃系发泡片及复合体
JP6953543B2 (ja) 2017-10-20 2021-10-27 三井化学株式会社 皮膚用二酸化炭素徐放パックおよび二酸化炭素を皮膚に徐放する方法
WO2019122016A1 (en) 2017-12-21 2019-06-27 Borealis Ag Process for the preparation of solid catalyst
KR20200095577A (ko) 2017-12-28 2020-08-10 보레알리스 아게 촉매 및 이의 제조
EP3766927A4 (en) 2018-03-13 2021-11-17 Mitsui Chemicals, Inc. AIR BREATHABLE, LAMINATE AND COMPOSITE SHEET
EP3856837A1 (en) 2018-09-26 2021-08-04 Borealis AG Propylene copolymer composition with excellent optical and mechanical properties
WO2020064313A1 (en) 2018-09-26 2020-04-02 Borealis Ag Propylene random copolymer for use in film applications
US11827777B2 (en) 2018-09-26 2023-11-28 Borealis Ag Propylene copolymer with excellent optical properties
EP3883989B1 (en) 2018-11-23 2024-02-28 Borealis AG Polypropylene composition with improved optical properties and whitening resistance
CN113166292A (zh) 2018-11-30 2021-07-23 博里利斯股份公司 洗涤工艺
CN112969726A (zh) 2018-12-04 2021-06-15 三井化学株式会社 含有4-甲基-1-戊烯共聚物的树脂组合物及电容器用膜
EP3666804B1 (en) 2018-12-14 2023-04-05 Borealis AG Polypropylene composition with favourable combination of optics, softness and low sealing
CN113453899B (zh) 2019-03-28 2023-09-26 三井—陶氏聚合化学株式会社 密封剂用树脂组合物、层叠体、包装材料及包装容器
EP4023737A4 (en) 2019-08-29 2023-08-30 Mitsui Chemicals, Inc. LUBRICATING OIL COMPOSITION
CN112745433A (zh) * 2019-10-30 2021-05-04 中国石油化工股份有限公司 一种制备高立构规整度聚丙烯的方法
KR20220079644A (ko) 2019-11-15 2022-06-13 미쓰이 가가쿠 가부시키가이샤 수지 조성물 및 성형체
EP3825357A1 (en) 2019-11-25 2021-05-26 Borealis AG Propylene composition for foaming with improved mechanical properties
EP4122351A4 (en) 2020-03-19 2024-04-10 Mitsui Chemicals, Inc. SELF-ADHESIVE SHEET
WO2021193537A1 (ja) 2020-03-27 2021-09-30 三井化学株式会社 積層体、これを用いたロール体および梱包体
WO2021201112A1 (ja) 2020-03-31 2021-10-07 三井化学株式会社 組成物および成形体
EP3919529A1 (en) 2020-06-04 2021-12-08 Total Research & Technology Feluy Process to produce propylene copolymer, the polypropylene produced and articles made from this polypropylene
WO2022129409A1 (en) 2020-12-18 2022-06-23 Borealis Ag Modification of polyethylene terpolymer
EP4019582A1 (en) 2020-12-23 2022-06-29 Borealis AG Polyethylene film
US20240071647A1 (en) 2021-01-08 2024-02-29 Borealis Ag Composition
EP4036130B1 (en) 2021-01-29 2023-03-22 Borealis AG Modification of polyethylene copolymer
US20240123716A1 (en) 2021-03-02 2024-04-18 Mitsui Chemicals, Inc. Multilayer film, container, pack for cell culture and method for producing multilayer film
EP4053194B1 (en) 2021-03-03 2023-08-02 Borealis AG Monolayer blown film
EP4305075A1 (en) 2021-03-09 2024-01-17 Borealis AG Polyethylene composition for a film layer
ES2963967T3 (es) 2021-03-09 2024-04-03 Borealis Ag Composición de polietileno para una capa de película
EP4056598B1 (en) 2021-03-09 2023-09-13 Borealis AG Polyethylene composition for a film layer
EP4410933A1 (en) 2021-09-30 2024-08-07 Mitsui Chemicals, Inc. Lubricating oil composition
EP4163332A1 (en) 2021-10-10 2023-04-12 Borealis AG Polyethylene composition for a film layer
EP4166581A1 (en) 2021-10-12 2023-04-19 Borealis AG Propylene composition for foaming with high melt flow rate
WO2023198579A1 (en) 2022-04-11 2023-10-19 Borealis Ag Multilayer film
EP4389776A1 (en) 2022-12-20 2024-06-26 Borealis AG Process
EP4389783A1 (en) 2022-12-20 2024-06-26 Borealis AG Catalyst transition process
WO2024133045A1 (en) 2022-12-23 2024-06-27 Borealis Ag Process for producing a high-flow polypropylene homopolymer
WO2024133046A1 (en) 2022-12-23 2024-06-27 Borealis Ag Process for producing a polypropylene copolymer
WO2024133044A1 (en) 2022-12-23 2024-06-27 Borealis Ag Process for producing a polypropylene homo- or copolymer
EP4417629A1 (en) 2023-02-14 2024-08-21 Borealis AG Polyethylene blend for a film layer

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3127133A1 (de) * 1981-07-09 1983-01-27 Hoechst Ag, 6000 Frankfurt Verfahren zur herstellung von polyolefinen und deren copolymerisaten
US4530914A (en) * 1983-06-06 1985-07-23 Exxon Research & Engineering Co. Process and catalyst for producing polyethylene having a broad molecular weight distribution
US4937299A (en) * 1983-06-06 1990-06-26 Exxon Research & Engineering Company Process and catalyst for producing reactor blend polyolefins
DE3640924A1 (de) * 1986-11-29 1988-06-01 Hoechst Ag 1-olefin-stereoblockpolymer und verfahren zu seiner herstellung
DE3640948A1 (de) * 1986-11-29 1988-06-01 Hoechst Ag Verfahren zur herstellung eines 1-olefin-stereoblockpolymers
IL85097A (en) * 1987-01-30 1992-02-16 Exxon Chemical Patents Inc Catalysts based on derivatives of a bis(cyclopentadienyl)group ivb metal compound,their preparation and their use in polymerization processes
US4794096A (en) * 1987-04-03 1988-12-27 Fina Technology, Inc. Hafnium metallocene catalyst for the polymerization of olefins
KR900004932B1 (ko) * 1987-05-26 1990-07-12 주식회사 럭키 올레핀계 열가소성 수지 조성물의 제조 방법
DE3726067A1 (de) * 1987-08-06 1989-02-16 Hoechst Ag Verfahren zur herstellung von 1-olefinpolymeren
US4931417A (en) * 1987-11-09 1990-06-05 Chisso Corporation Transition-metal compound having a bis-substituted-cyclopentadienyl ligand of bridged structure
US4892851A (en) * 1988-07-15 1990-01-09 Fina Technology, Inc. Process and catalyst for producing syndiotactic polyolefins
DE3907965A1 (de) * 1989-03-11 1990-09-13 Hoechst Ag Verfahren zur herstellung eines syndiotaktischen polyolefins
DE3916553A1 (de) * 1989-05-20 1990-11-22 Hoechst Ag Syndio- isoblockpolymer und verfahren zu seiner herstellung

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7241848B2 (en) 2002-10-30 2007-07-10 Mitsui Chemicals, Inc. Process for preparing low molecular weight olefin (CO)polymer and polymerization catalyst used therefor

Also Published As

Publication number Publication date
DE69033435T2 (de) 2000-07-20
GR3036018T3 (en) 2001-09-28
ES2142303T5 (es) 2006-12-01
DE69033435T3 (de) 2006-10-19
EP0423101A2 (en) 1991-04-17
US5036034A (en) 1991-07-30
KR910007973A (ko) 1991-05-30
CN1058022C (zh) 2000-11-01
DE69033715D1 (de) 2001-04-19
ATE199722T1 (de) 2001-03-15
US6369175B1 (en) 2002-04-09
EP0742227B1 (en) 2001-03-14
ATE189226T1 (de) 2000-02-15
ES2142303T3 (es) 2000-04-16
CA2027124A1 (en) 1991-04-11
DK0423101T3 (da) 2000-07-17
EP0742227A2 (en) 1996-11-13
KR0181495B1 (ko) 1999-05-15
GR3033307T3 (en) 2000-09-29
CA2027124C (en) 2001-09-04
DK0742227T3 (da) 2001-06-05
DE69033435D1 (de) 2000-03-02
CN1028532C (zh) 1995-05-24
CN1100733A (zh) 1995-03-29
ES2155909T3 (es) 2001-06-01
JPH03193796A (ja) 1991-08-23
EP0423101B1 (en) 2000-01-26
EP0423101B2 (en) 2006-05-03
DK0423101T4 (da) 2006-08-21
DE69033715T2 (de) 2001-07-12
EP0742227A3 (en) 1997-01-22
EP0423101A3 (en) 1991-08-07

Similar Documents

Publication Publication Date Title
CN1028532C (zh) 生产半等规聚丙烯的催化剂
CN1069651C (zh) 乙烯聚合物的制备方法
CN1034125C (zh) 用含路易斯酸和烷基铝的金属茂催化剂聚合烯烃的方法
CN1061996C (zh) 由烯属不饱和单体制得的聚合物链的间同立构增长方法
US6403772B1 (en) Open-pentadienyl metallocenes, precursors thereof and polymerization catalysts therefrom
DE69631649T2 (de) Übergangsmetallverbindung, polymerisationskatalysator für olefine und verfahren zur herstellung olefinischer polymere
CN1247603C (zh) 用于烯烃聚合催化剂体系的取代的金属茂化合物、其中间体及制备方法
DE60213452T2 (de) Metallocene und verfahren zur herstellung von propylenpolymeren
Erker et al. Hydroboration of Bis (alkenylcyclopentadienyl) zirconium Dichlorides
US6180733B1 (en) Bridged bis-fluorenyl metallocenes, process for the preparation thereof and use thereof in catalysts for the polymerization of olefins
CN1117770C (zh) 在高压下制备乙烯共聚物的方法
CN1849346A (zh) 用于高分子量聚烯烃生产的氢硅烷添加剂
WO1998050440A1 (en) Process for producing tactioselective polyolefins in condensed phase using titanocenes
US6252019B1 (en) Process for polymerizing tactioselective polyolefins in condensed phase using hafnocenes
CN1756776A (zh) 丙烯聚合方法
CN1711288A (zh) 聚烯烃的生产
JP4131448B2 (ja) ヘテロ環式メタロセン類および重合触媒
JP4131448B6 (ja) ヘテロ環式メタロセン類および重合触媒

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C15 Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993)
OR01 Other related matters
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee