双功能催化剂体系催化乙烯原位聚合制备长链支化聚乙烯研究

以蒙脱土负载 β 二酮二氯化锆作为乙烯齐聚催化剂与Et(Ind) 2 ZrCl2 复合组成了原位双功能聚合催化体系 ,成功地以乙烯为唯一单体唯一反应釜制备长链支化聚乙烯 ,该催化剂体系具有乙烯共聚活性高 ,聚合物物性可调等优点     

双功能催化体系制备聚丙烯/蒙脱土复合材料

为了制备聚丙烯/蒙脱土纳米复合材料,将Brookhart型的乙烯齐聚催化剂负载于有机蒙脱土片层间,进一步与丙烯聚合茂金属催化剂进行复配得到双功能催化体系。采用这种双功能催化剂体系通过催化乙烯齐聚得到α-烯烃/蒙脱土的齐聚产物,进一步将丙烯与这种齐聚产物共聚,合成了一系列结构不同的聚丙烯/蒙脱土纳米复合材料。通过气相色谱、X射线衍射(XRD)分析得出蒙脱土负载的铁系催化剂催化乙烯齐聚产物是以C_4~C_(16)为主的α-烯烃,蒙脱土以片层形式分散于齐聚产物的甲苯溶液中。研究了蒙脱土负载的铁系催化剂与共聚催化剂复配催化乙烯齐聚以及丙烯与齐聚产物共聚合的情况。通过XRD、透射电镜、差示量热分析、凝胶渗透色谱分析表征可知,蒙脱土以纳米片层剥离的形式均匀分散于聚丙烯基体中,聚丙烯/复合材料的结晶温度比纯聚丙烯有所下降,所得聚丙烯基体分子量在8.1×10~4~17.1×10~4g/mo L。     

(2-Me-3-ClPh)_2PBIMe_2FeCl_2racC_2H_4(Ind)_2ZrCl_2/MAO双功能催化体系乙烯原位共聚制备LLDPE

合成了后过渡金属铁 (2 Me 3 ClPh) 2 PBIMe2 FeCl2 低聚催化剂 ,并与亚乙基桥茂金属共聚催化剂rac C2 H4 (Ind) 2 ZrCl2 共用 ,用MAO(1 4mol L甲苯溶液 )作为助催化剂 ,原位共聚合成线性低密度聚乙烯 (LLDPE) .结果发现 ,这种后过渡铁催化剂具有很高的低聚催化活性 [1 0× 10 7goligomer (molFe·h) ],双功能催化体系的催化活性保持在 10 6 gPE (molFe·h)以上 ;1 3C NMR分析表明 ,得到了线性低密度聚乙烯 ,当Fe Zr比为 1 2时 ,也没有出现α 烯烃残留现象 ,说明这两种催化剂具有好的匹配性 ;随Fe Zr比和反应温度的变化 ,聚合物的熔点、结晶度、熔点等均表现出很好的规律性 .     

双组分茂金属催化剂催化乙烯聚合的研究

选择能形成支链的不对称桥联茂金属化合物Me2 C[(Cp) (Ind) ]ZrCl2 和非桥联的不同结构的茂金属化合物二氯二 (烯基取代环戊二烯 )锆如 ( Cp) 2 ZrCl2 ,(Cp) 2 ZrCl2 和 (Cp) 2 ZrCl2 ,以MAO为助催化剂 ,分别组成三组双组分茂金属催化剂的催化体系 ,催化乙烯聚合 .结果表明 ,两类催化剂组成的双组分茂金属催化体系催化乙烯聚合能得到支化的宽分子量分布的聚乙烯 ;聚合温度和改变两种茂金属催化剂的摩尔比对催化活性和分子量有很大影响 .因此可以利用改变双组分茂金属催化剂的摩尔比例和聚合温度来调控聚合物的分子量和分子量分布 .改变两种茂金属催化剂的摩尔比和聚合温度也能使聚合物的结晶度发生改变     

α-萘基丁二亚胺氯化镍/MAO制备双(宽)峰聚乙烯

合成了一种新型α 二亚胺镍配合物———α 萘基丁二亚胺氯化镍 ,此配合物作为催化剂在MAO的活化下催化乙烯聚合得到支化聚乙烯 ,聚合活性高达 7 18× 10 5gPE molNi·h ,1 3C NMR、FTIR测试结果表明制备的聚乙烯含有末端双键 ;GPC结果表明所制备的聚乙烯分子量呈双 (宽 )峰分布 ,其原因有两个 ,一是此催化剂能产生分子量较低的α 烯烃 ,在聚合过程中一部分α 烯烃会“就地”与乙烯原位共聚形成分子量较高的聚合物 ,二是此催化剂存在立体异构体 ,而不同异构体在MAO活化下形成的活性中心的配位环境不同 ,因而得到的聚乙烯的分子量也不同 .研究了聚合温度、聚合压力、铝镍摩尔比 (nAl nNi)对催化活性、聚乙烯分子量、支化度的影响 .聚乙烯的分子量随聚合温度的升高而下降 ,支化度增大 ,熔点则降低 .     

蒙脱土负载（acac）2ZrCl2催化乙烯齐聚研究

利用蒙脱土（MMT）与(acac)2ZrCl2反应,制备了负载于H－蒙脱土层间的(acac)2ZrCl2催化剂,以AlEt2Cl为助催化剂时,该负载催化剂体系对乙烯剂聚具有很高的催化选择性,产物主要为α－烯径,如C6^=和C8^=。     

Ind2Zr（OC6H4Me—p）2和EtnAlCl3—n催化乙烯剂聚的研究

茂金属催化剂（Kaminsky催化剂）是80年代发展起来的烯烃聚合高效催化剂,有关其催化烯烃聚合的研究很多,近年来,Kaminsky型催化剂催化乙烯齐聚合成低碳α烯烃的研究已有报道。由乙烯齐聚得到的直链低碳α烯烃是生产线性低密度聚乙烯（LLDPE）和高密度聚乙烯（HDPE）的共聚单体。以茚基锆化合物与烷基铝组成的Ziegler-Natta催化体系催化乙烯齐聚尚未见报道,本文考察了Ind2Zr(OC6H4Me-p)2和各种乙基铝组成的二元催化体系对乙烯齐聚的催化性能。     

α-二亚胺镍(Ⅱ)配合物-TiCl4复合催化剂催化乙烯原位聚合制备支化聚乙烯

制备了α-二亚胺镍()配合物[C6H5—NC(CH3)—C(CH3)N—C6H5]NiBr2(NiL)-TiCl4负载在MgCl2-SiO2载体上的复合催化剂(NiL-TiCl4/MgCl2-SiO2),以AlR3为助催化剂(不用MAO)催化乙烯聚合.研究了NiL和TiCl4负载方法、NiL/TiCl4摩尔比、助催化剂种类及聚合反应温度等对催化剂性能的影响.用IR和13CNMR表征聚合产物支化度及支链结构;用GC-MS监测聚合反应.实验结果表明,NiL-TiCl4复合催化剂具有齐聚原位共聚特性,可催化乙烯原位聚合,合成支化聚乙烯.     

原位共聚制备的线性低密度聚乙烯的结构特征

采用{[(2-ArN=C(Me))2C5H3N]FeCl2}作为齐聚催化剂[其中Ar=2,4-C6H3(CH3)2和Ar=2-Cl-4-CH3C6H3],商品化的Ziegler-Natta催化剂作为共聚催化剂,分别组成双功能催化体系A[Ziegler-Natta/MAO/TEA/Fe-CH3]和B[Ziegler-Natta/MAO/TEA/Fe-Cl],催化乙烯原位共聚。通过调节不同的聚合条件制备了具有不同支化度、不同分子量及其分布的LLDPE,利用13 C-NMR、流变仪、GPC(示差/光散射)等表征手段,研究了所得高聚物的结构特征。结果表明,该催化体系制备LLDPE样品的支链含量和齐聚物的碳数分布规律是一致的,LLDPE中既有短支链也有较长的支链,聚合物的分子量分布较宽,为聚合物的力学性能和可加工性能提供了更大的调节余地。通过对样品的零剪切粘度、模量、交叉频率、损耗角以及剪切变稀特征等的考察,零剪切粘度与重均分子量的指数关系大于3.8,可以判断被分析的样品含有长支链。分别采用A和B催化剂体系制备的样品作比较,B组样品含有长支链组分,存在较多的高分子量尾端。     

桥联茂金属催化剂用于双功能催化体系制备LLDPE的研究

以四种取代基不同的桥联茂金属作为乙烯共聚催化剂 ,以Ti(OR) 4为二聚催化剂组成双功能原位聚合催化剂体系 ,在同一反应釜中 ,乙烯为唯一聚合单体 ,以阳离子助剂B(C6 F5 ) 3为唯一助催化剂 ,原位制备LLDPE .该聚合体系催化剂活性高、单体插入率高、得到的聚合物为熔点低、分子量可调的超低密聚乙烯     

Preparation of linear low‐density polyethylene by the in situ copolymerization of ethylene with an iron oligomerization catalyst and rac‐ethylene bis(indenyl) zirconium (IV) dichloride

An iron oligomerization catalyst, [(2‐ArN?C(Me))₂C₅H₃N]FeCl₂ [Ar = 2,6‐C₆H₃(F)₂], was combined with rac‐ethylene bis(indenyl)zirconium (IV) dichloride [rac‐Et(Ind)₂ZrCl₂] to prepare linear low‐density polyethylene (LLDPE) by the in situ copolymerization of ethylene. A series of LLDPEs with different properties were prepared by the alteration of the reaction temperature, Fe/Zr molar ratio, Al/(Fe + Zr) molar ratio, and reaction time. The structures of the polymers were characterized with differential scanning calorimetry, ¹³C NMR, gel permeation chromatography (GPC), and so forth. The melting points, crystallizations, and densities of the resulting products increased, and the average branching degree decreased, as the reaction temperature, Al/(Fe + Zr) ratio, and reaction time increased. The melting points, crystallizations, and densities of the polymers decreased, and the average branching degree increased, when the Fe/Zr ratio increased. The ¹³C NMR and GPC results showed that there were no unreacted α‐olefins remaining in the resulting polymers because the percentage of low‐molar‐mass sections (C₄–C₁₀) of the oligomers obtained with this catalyst was very high (>70%). In addition, the formation of polymers with two melting points under different reaction conditions was examined in detail, and the results indicated that the two melting points of the polymers could be attributed to polyethylene with different branches. © 2005 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 43: 984–993, 2005     

一种新型亚胺基吡啶铁配合物和茂金属复配催化乙烯原位共聚制备LLDPE

20世纪80年代中期,Kissin等人^[1]首先采用了乙烯二聚催化剂和传统Ziegler-Natta催化剂组成双功能催化体系,催化乙烯原位聚合制备短支链线性低密度聚乙烯(LLDPE)．由于该方法具有不需要另外加入α-烯烃的特点,近年来受到人们的重视．胡友良^[2-4]等人用乙烯二聚催化剂Ti-     

SYNTHESIS OF BRANCHED POLYETHYLENE USING (α-DIIMINE)NICKEL(Ⅱ)TiCl4 COMBINED AND SUPPORTED CATALYST*

(α-Diimine)nickel(Ⅱ) {[C6H5 -N = C(CH3)-C(CH3) = N -C6H5]NiBr2}-TiCl4 abbreviated as NiL-TiCl4 combined catalyst which is supported on MgCl2-SiO2 carrier has been prepared, by using alkyl aluminum (AIR3) as the cocatalyst in place of methylaluminoxane (MAO) to catalyze ethylene oligomerization and copolymerization in situ. The influences of procedure for supporting NiL-TiCI4, the molar ratio of NiL to TiCI4, cocatalyst type and polymerization temperature on the catalytic performance were studied. The degree of branching and the composition of the branched chain of polymers produced have been investigated by IR and ^13C-NMR spectra. The results show that the combined catalyst can synthesize the branched polyethylene with various banched chains .The polymerization reaction was monitored by gas chromatography and mass spectrometry (GC-MS). The results show that this catalyst promotes the oligomerization and copolymerization in situ for ethylene.     

SYNTHESIS OF BRANCHED POLYETHYLENE USING (α-DIIMINE)NICKEL(Ⅱ) -TiCl4 COMBINED AND SUPPORTED CATALYST

(a-Diimine)nickel(Ⅱ) {[C6H5 - N = C(CH3) - C(CH3) = N - C6H5]NiBr2}-TiCl4 abbreviated as NiL-TiCl4combined catalyst which is supported on MgCl2-SiO2 carrier has been prepared, by using alkyl aluminum (AlR3) as the cocatalyst in place of methylaluminoxane (MAO) to catalyze ethylene oligomerization and copolymerization in situ. The influences of procedure for supporting NiL-TiCl4, the molar ratio of NiL to TiCl4, cocatalyst type and polymerization temperature on the catalytic performance were studied. The degree of branching and the composition of the branched chain of polymers produced have been investigated by IR and 13C-NMR spectra. The results show that the combined catalyst can synthesize the branched polyethylene with various banched chains .The polymerization reaction was monitored by gas chromatography and mass spectrometry (GC-MS). The results show that this catalyst promotes the oligomerization and copolymerization in situ for ethylene.     

Researches on the In Situ Copolymerization of Ethylene with Catalysts Immobilized onto the Molecular Sieves

In this paper,the bi-functional catalyst system composed of molecular sieve(MCM-41) immobilized oligomerization catalyst(C25H17Cl2N3·FeCl2) and copolymerization catalyst(Et(Ind)2ZrCl2) was employed in the in situ copolymerization of ethylene aiming to prepare the Linear low density polyethylene(LLDPE).In this paper,we mainly argued the regular pattern of the in situ copolymerization of ethylene in limited nano-space and compared it with that happening in free space.The impact of variance of the reaction temperature,Fe/Zr value and the A1/(Fe+Zr) value on the activity of the in situ copolymerization of ethylene has also been introduced.Furthermore,the degree of branching,thermal properties and crystalline changes of the obtained polymerization products prepared from different reactivity were investigated.     

铁系亚胺基吡啶复配催化乙烯原位共聚产物的表征

Branched polyethylene from ethylene as single monomer was prepared by the tandem catalyst system of {2-[2-Me C6 H4 N=Me)]2 C5H3N} FeCl2 (1) and {2,6-[1-(2,6-Me2-4-Br-C6H4N=(Me)]2C5H3N} FeCl2 (2) activated with methylaluminoxane (MAO) . The products of polymerization were characterized by DSC, GPC and ^13C-NMR. The results revealed that the copolymer produced by in situ copolymerization of ethylene was a mixture of branched polyethylene and α-olefin. The content of α-olefin in the mixture was increased with increasing the molar ratio of catalysts 1/2. The MWD paramelers of polyethylene and copolymer were 28.6 and 7.9, respectively. ^13C-NMR spectra showed that there were ethyl groups, butyl groups and long chain alkyl groups in the copolymer. The average degree of branching of such branched polyethylene was less than 5C/1000C.     

铁系催化剂催化降冰片烯与丙烯酸甲酯共聚合

研究了Fe(acac)3-Al(i-Bu)3(acac=乙酰丙酮)催化降冰片烯(NB)与丙烯酸甲酯(MA)共聚反应条件影响、第三组份影响及催化剂铁铝比影响.并用核磁共振、红外光谱和元素分析方法研究了共聚物的组成,用热分析方法研究了共聚物的分解温度,并用电镜分析了共聚物的膜结构.结果表明,铁系催化剂在温和的反应条件下有较好的催化性能,并可获得能够形成有序多孔膜的共聚物.     

Novel polystyrene‐supported zirconocene catalyst for olefin polymerization and its catalytic kinetics

Through the Diels–Alder reaction between cyclopentadiene groups attached to polystyrene in the presence of zirconocene, novel polystyrene‐supported metallocene catalysts were prepared. A novel method for immobilizing metallocene catalysts was investigated, and the resultant polystyrene‐supported metallocene for olefin polymerization was studied. The results of olefin polymerization showed that different crosslinking degrees of support in the catalyst system had significant effects on the catalytic behavior. The influence of the [Al]/[Zr] molar ratio and the temperature on the (co)polymerization activity was studied. When 1‐hexene and 1‐dodecene were used for copolymerization with ethylene, an obvious positive comonomer effect was observed. © 2005 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 43: 2650–2656, 2005