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1.
采用MgCl2负载TiCl4及1,3-二氯-2-丙醇给电子体(XROH),与三乙基铝助催化剂组成的催化剂体系,合成了1-己烯共聚率高且宽分子量分布的乙烯/1-己烯共聚物。讨论了催化体系的组成、配比和聚合条件对乙烯/1-己烯共聚合行为,共聚物结构、分子量及分子量分布的影响。结果表明,n(Ti):n(Mg)=10:1,n(XROH):n(MgCl2)=2.6:1,n(Al):n(Ti)=100:1,乙烯压力0.45MPa,聚合温度80℃,聚合时间2h,共聚单体(1-hexene)浓度0.25mol/L时,催化效率达23.2kg/gcat。采用13CNMR、X-ray、SEM、WAXD、DSC、GPC等测试技术对催化剂、共聚物的结构进行了表征。结果表明,在Zieglar-Natta(Z-N)催化体系中,给电子体多卤代醇与TiCl4结合,载体MgCl2的晶体结构发生了变化。结晶度降低,有利于催化剂负载量的提高(ω(Ti)=4.8%)和催化效率增大。催化体系产生了多种活性中心,使聚烯烃分子量分布变宽(15~20)。多卤代醇还可增强1-己烯与乙烯的共聚能力,在共聚物中1-己烯的摩尔分数达5.1%。  相似文献   

2.
合成了5个不同结构的苯氧亚胺配体L1~L5,用Et_3N,Me_3SiCl或HNa处理后与TiCl_4·2THF或CpZrCl_3·DME进行配位反应得到不同取代基结构的化合物C1~C6,经过~1H NMR,~(13)C NMR,IR和元素分析等表征,确认了化学结构.以甲基铝氧烷(MAO)为助催化剂,化合物C1~C6为催化剂催化乙烯聚合,考察了聚合温度、乙烯压力、铝钛或铝锆比对催化剂活性及聚合物分子量的影响.聚合实验结果表明,刚性桥基结构提高了双核化合物(LMCl_3)_2的稳定性,催化剂的活性基本都能达到10~5~10~~6g/(mol M·h),其中C5的催化活性最高,达到1. 23×10~6g/(mol Zr·h); C4在Al/Ti摩尔比为50∶1时也具有较好的催化活性[5. 89×10~5g/(mol Ti·h)],聚合物分子量1. 11×10~6.该类催化剂还可以有效催化乙烯与1-辛烯共聚,1-辛烯插入率达到10. 65%(摩尔分数).  相似文献   

3.
合成了新型催化剂8-苯胺-1-萘磺酸钛配合物, 并应用于乙烯与降冰片烯的共聚合反应中. 分别考察了助催化剂种类[甲基铝氧烷(MAO)和三乙基铝(TEA)]、 降冰片烯浓度、 Al/Ti摩尔比、 聚合温度和聚合压力对催化活性与共聚性能的影响. 通过核磁共振、示差扫描量热和凝胶渗透色谱等对所制备的共聚物进行了表征. 结果表明, 在相同条件下, 以MAO为助催化剂时, 共聚催化活性更高, 催化剂为单活性中心, 可得到分子量分布较窄(PDI≈3)的共聚产物, 其共聚反应机理为加成聚合. 另外, 随着降冰片烯浓度的升高, 共聚物中降冰片烯单元的摩尔比呈线性上升趋势, 所得共聚物的熔点随之降低.  相似文献   

4.
α-萘基丁二亚胺氯化镍/MAO制备双(宽)峰聚乙烯   总被引:5,自引:0,他引:5  
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 .  相似文献   

5.
以甲基铝氧烷(MAO)为助催化剂的茂金属催化剂虽然具有催化活性高、分子量分布窄、聚合物化学组成均匀等优点,但其极高的Al/Zr比和聚合物颗粒形态差等缺点限制了其工业化应用,因此对茂金属催化剂的负载化成为近年来的研究热点.在众多的载体中,球形MgCl2是研究得很少的一类载体,文献中曾采用先负载主催化剂茂金属配合物,聚合时再加入助催化剂MAO的方法[1],由于加入的MAO与主催化剂的络合能力很强,会使部分载上的主催化剂溶解下来,成为均相聚合[2,3],导致聚合物颗粒形态差,且粘釜现象严重.我们则采用相反的思路,即先将助催化剂MAO负载在球形MgCl2上,制得MgCl2/MAO,在聚合前再将MgCl2/MAO与Et[Ind]2ZrCl2混合陈化,并立即在少量烷基铝活化下引发乙烯聚合[4],实验结果表明,该催化剂聚合活性高、聚合物的颗粒形态好、且不粘釜,是一种新型的载体催化剂.由于烷基铝的加入可使催化剂的活性大幅度提高,所以本文将烷基铝也称作助催化剂,来研究其对该载体催化剂催化乙烯聚合的影响.  相似文献   

6.
短链支化聚乙烯的合成与表征   总被引:1,自引:0,他引:1  
合成了两类结构明确的乙烯共聚物, 通过FTIR, GPC, 1H NMR和13C NMR表征了产物的分子结构, 分别研究了分子量和短链支化含量对两类共聚物结晶性能的影响. 采用阴离子聚合制备分子量(Mw)20000~110000、分子量分布为1.1的1,2-结构摩尔分数为7%左右的聚丁二烯. 加氢反应后得到乙烯/1-丁烯模型共聚物的熔点和结晶度随着分子量的增加而下降. 采用茂金属催化剂Et[Ind]2ZrCl2催化乙烯与1-己烯共聚合, 制备分子量为100000左右, 共聚单体摩尔分数为0~5.5%的乙烯/1-己烯共聚物, DSC结果表明其熔点和结晶度随着共聚物中1-己烯含量的升高而降低.  相似文献   

7.
将后过渡金属配合物{[2,6-ArN=C(Me)2C5H3N]FeCl2} ( Ar=2,6-iPr2C6H3) Ⅰ负载于SiO2上, 并与三乙基铝(AlEt3)组成催化剂体系并催化乙烯聚合. 考察了Al/Fe比(AlEt3/催化剂摩尔比)、聚合温度对催化剂活性、聚乙烯(PE)分子量、熔融温度以及结晶度的影响. 在Al/Fe比为750、聚合温度为40 ℃时, 催化剂活性达到7.07×105g PE·(mol Fe·h)-1. 实验所得聚合物的分子量为1.05×105~2.33×105 g/mol, 熔融温度高达132 ℃左右,结晶度在44.2%~77.8%之间.  相似文献   

8.
采用2种分别具有Cs对称性和C1对称性的异双桥联茂金属催化剂(Me_2C)(Me_2Si)Cp_2TiCl_2、[(CH_2)_5C](Me_2Si)Cp_2TiCl_2,在助催化剂甲基铝氧烷(MAO)的作用下用于丙烯聚合.通过对聚合温度、助催化剂用量和聚合时间的研究,详细考察了这些因素对聚合活性和聚合物结构的影响.由核磁共振碳谱(13CNMR)、示差扫描量热分析(DSC)和凝胶渗透色谱法(GPC)表征了所得聚合物的结构和分子量及分子量分布.这2种催化剂催化丙烯常压聚合活性最高可达10~6g PP/mol·h,重均分子量可达7×10~5,分子量分布在2.0左右,所得聚丙烯为高分子量的无规聚丙烯.这两种异双桥联茂金属催化体系在低温下表现出良好的聚合活性;但聚合温度升高,聚合活性和聚丙烯的分子量呈现明显的下降趋势.随铝钛比的增加,聚合活性和聚合物分子量均呈现先上升后降低的趋势.聚合时间增加活性下降,聚合物分子量有所增加.研究表明,这2种催化剂具有的大二面角(71.0°,70.3°)结构对催化性能和聚合物的结构有较大影响.  相似文献   

9.
通过双(环戊二烯基)二氯化锆(Cp2ZrCl2)催化剂和改良的甲基铝氧烷(MMAO)助催化剂, 合成了无机-有机杂化共聚物. 研究了2种具有不同单乙烯基反应基团的笼型倍半硅氧烷(POSS)与乙烯的聚合. 对共聚产物的结构、 热力学性质、 分子量及其分布等进行了研究. 共聚单体(POSS)的插入率在0.01%~0.30%之间, 随着共聚单体在共聚物中摩尔分数的增大, 聚合物的熔点和熔解热降低. 共聚物的热重分析结果显示, 乙烯-POSS共聚物拥有更高的热分解温度以及较高的热分解残留量. 随着POSS的加入, 聚合物的分子量明显提高, 聚合物的分子量分布变宽.  相似文献   

10.
以球形高效负载的TiCl4/MgCl2/邻苯二甲酸二异丁酯(DIBP)为催化剂,采用本体聚合方法进行丙烯与1-丁烯共聚合研究.考察了共单体效应对共聚活性及聚合物立构规整性的影响;表征了共聚物的结构.结果表明,随着1-丁烯/丙烯投料比的增加,聚合活性呈先升高后降低的趋势,在1-丁烯/丙烯摩尔投料比为0.26条件下聚合活性达到最高,并随着共聚物中1-丁烯含量的增加,共聚物的熔点明显下降,分子量降低,分子量分布变窄,同时共聚物力学性能有明显提高,透明度逐渐增加.  相似文献   

11.
Distribution of active centers(ACD)of ethylene or 1-hexene homopolymerization and ethylene-1-hexene copolymerization with a MgCl_2/TiCl_4 type Z-N catalyst were studied by deconvolution of the polymer molecular weight distribution into multiple Flory components.Each Flory component is thought to be formed by a certain type of active center. ACD of ethylene-1-hexene copolymer with very low 1-hexene incorporation was compared with that of ethylene homopolymer to see the effect of introducingα-olefin on eth...  相似文献   

12.
以乙烯、醋酸乙烯酯和α-烯烃为原料,以偶氮二异丁腈为引发剂,通过高压本体聚合制备三元聚合物.考察了聚合条件对共聚物数均分子量和醋酸乙酯(VA)质量分数的影响.结果表明:在引发剂用量为1.1g,反应压力为6 MPa,反应温度95℃,醋酸乙烯酯和α-烯烃的质量比为2:1的条件下能得到数均分子量为8 600和VA质量分数为0.35的产物.实验证明该产物性能优良,可作为蜡的添加剂.  相似文献   

13.
We describe the synthesis of [bis(N-(3-tert-butylsalicylidene)anilinato)] titanium (IV) dichloride (Ti-FI complex) and examine the effects of comonomer (feed concentration and type) on its catalytic performance and properties of the resulting polymers. Ethylene/1-hexene and ethylene/1-octene copolymers were prepared through copolymerization using Ti-FI catalyst, activated by MAO cocatalyst at 323 K and 50 psi ethylene pressure at various initial comonomer concentrations. The obtained copolymers were characterized by DSC, GPC and 13C-NMR. The results indicate that Ti-FI complex performs as a high potential catalyst, as evidenced by high activity and high molecular weight and uniform molecular weight distribution of its products. Nevertheless, the bulky structure of FI catalyst seems to hinder the insertion of α-olefin comonomer, contributing to the pretty low comonomer incorporation into the polymer chain. The catalytic activity was enhanced with the comonomer feed concentration, but the molecular weight and melting temperature decreased. By comparison both sets of catalytic systems, namely ethylene/1-hexene and ethylene/1-octene copolymerization, the first one afforded better activity by reason of easier insertion of short chain comonomer. Although 1-hexene copolymers also exhibited higher molecular weight than 1-octene, no significant difference in both melting temperature and crystallinity can be noticed between these comonomers.  相似文献   

14.
Cyclopentadienyl-titanium complexes containing -OC6H4X ligands (X = Cl,CH3) activated with methylaluminoxane (MAO) were used in the homo-polymerization of ethylene, propylene, 1-butene, 1-pentene, 1-butene, and 1-hexene, and also in co-polymerization of ethylene with the alpha-olefins mentioned. The -X substituents exhibit different electron donor-acceptor properties, which is described by Hammett's factor (sigma).The chlorine atom is electron acceptor, while the methyl group is electron donor. These catalysts allow the preparation of polyethylene in a good yield. Propylene in the presence of the catalysts mentioned dimerizes and oligomerizes to trimers and tetramers at 25 degrees C under normal pressure. If the propylene pressure was increased to 7 atmospheres,CpTiCl2(OC6H4CH3)/MAO catalyst at 25 degrees gave mixtures with different contents of propylene dimers, trimers and tetramers. At 70 degrees C we obtained only propylene trimer.Using the catalysts with a -OC(6)H(4)Cl ligand we obtained atactic polymers with M(w) 182,000 g/mol (at 25 degrees C) and 100,000 g/mol (at 70 degrees C). The superior activity of the CpTiCl2(OC6H4Cl)/MAO catalyst used in polymerization of propylene prompted us to check its activity in polymerization of higher alpha-olefins (1-butene, 1-pentene, 1-hexene)and in co-polymerization of these olefins with ethylene. However, when homo-polymerization was carried out in the presence of this catalyst no polymers were obtained. Gas chromatography analysis revealed the presence of dimers. The activity of the CpTiCl2(OC6H4Cl)/MAO catalyst in the co-polymerization of ethylene with higher alpha-olefins is limited by the length of the co-monomer carbon chain. Hence, the highest catalyst activities were observed in co-polymerization of ethylene with propylene (here a lower pressure of the reagents and shorter reaction time were applied to obtain catalytic activity similar to that for other co-monomers). For other co-monomers the activity of the catalyst decreases as follows: propylene >1-butene > 1-pentene > 1-hexene. In the case of co-polymerization of ethylene with propylene, besides an increase in catalytic activity, an increase in the average molecular weight M(w) of the polymer was observed. Other co- monomers used in this study caused a decrease of molecular weight. A significant increase in molecular weight distribution (M(w)/M(n)) evidences a great variety of polymer chains formed during the reaction.  相似文献   

15.
采用溶胶-凝胶法,将苯乙烯-丙烯酸共聚物(PSA)包覆于955 Davison硅胶上得到无机/有机复合微球载体,并在2,6-二[1-(2-异丙基苯基亚胺基)乙基]吡啶/Fe(acac)3均相催化剂中浸渍后得到负载型双亚胺基吡啶铁催化剂.该催化剂在生产高结晶度(72%)聚乙烯的同时,还能生产一定量的α-烯烃.考察了不同膜材料以及聚合条件(不同助催化剂,压力,温度,Al/Fe摩尔比)对聚合活性以及聚合产物性能的影响,发现温度对聚合产物的α-烯烃与聚乙烯的质量比影响最大,助催化剂类型既影响催化剂的活性,也对最终产物的性质有着很大的影响.氯化镁处理的PSA作为膜材料时,负载2,6-二[1-(2-异丙基苯基亚胺基)乙基]吡啶/Fe(acac)3所得到聚乙烯分子量较低(Mw=11.9×104),结晶度较大(72%),熔融指数MI较高(2.35 g/10min),可作为双峰聚乙烯中的低分子量部分加以利用.  相似文献   

16.
采用合成的催化剂五甲基环戊二烯基三烯丙氧基钛 [Cp Ti(OAllyl) 3]与改性甲基铝氧烷 (mMAO)组成新型催化体系进行乙烯 /丙烯共聚合 ,考察了助催化剂 (mMAO)中TMA含量、气体配比、聚合温度、助催化剂和主催化剂浓度等因素对共聚合活性及产物分子量的影响 ,研究其变化规律 .结果表明 ,Cp Ti(OAllyl) 3/mMAO催化体系中钛的价态分布为Ti(Ⅳ )时对共聚合更为有利 ,制得了乙烯 /丙烯无规共聚物弹性体  相似文献   

17.
The new binuclear phenoxyiminato zirconium complex {1,7-(O)2C10H4-2,7-[CH=N(2,6-iPr2C6H3)]2}Zr2Cl6(THF)2 (FI2-Zr2) polymerizes ethylene with greater activity (approximately 8x) than the mononuclear analogue. Also, this catalyst produces high molecular weight ethylene + 1-hexene copolymers, while the mononuclear analogue yields only traces of copolymer under identical conditions. This ability to produce copolymers suggests cooperativity between the two Zr centers which promotes 1-hexene co-enchainment.  相似文献   

18.
The kinetic features of ethylene polymerization on ten methylalumoxane-activated self-immobilized bis(phenoxyimine) complexes of titanium chloride of various structure containing oxyallyl functional groups were studied. The catalytic activity of the systems was determined in the temperature range 20–60 °C under ethylene pressure 0.4 MPa. The positions and structures of the oxyallyl group and substituents in the phenoxy groups of the complexes substantially change the activity of the catalytic systems based on these complexes, the rate of the self-immobilization of the catalysts on the polymer, and molecular weights and molecular weight distributions of the obtained polyethylenes.  相似文献   

19.
A number of metallocene/methylaluminoxane (MAO) catalysts have been compared for ethylene/propylene copolymerizations to find relationship between the polymerization activities, copolymer structures, and copolymerization reactivity ratio with the catalyst structures. Stereorigid racemic ethylene bis (indenyl) zirconium dichloride and the tetrahydro derivative exhibit very high activity of 10 7 g (mol Zr h bar)?1, giving copolymers having comonomer compositions about the same as the feed compositions, molecular weights increasing with the increase of ethylene in the feed, random incorporation of comonomers, and narrow molecular weight distribution indicative of a single catalytic species. Nonbridged bis (indenyl) zirconium behaved differently, favoring the incorporation of ethylene over propylene, producing copolymers whose molecular weight decreases with the increase of ethylene in the feed, broad molecular weight distribution, and a methanol soluble fraction. This catalyst system contains two or more active species. Simple methallocene catalysts have much lower polymerization activities. CpTiCl2/MAO produced copolymers with tendency toward alternation, whereas Cp2HfCl2/MAO gave copolymer containing short blocks of monomers.  相似文献   

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