LiMn(BH4)3/2LiCl复合物的反应球磨制备及其脱氢性能

以LiBH₄和MnCl₂为初始原料, 采用反应球磨法制备了LiMn(BH₄)₃/2LiCl复合物, 并系统地研究了该复合物的脱氢性能及含钛催化剂的掺杂对其脱氢性能的影响. 结果表明: LiMn(BH₄)₃/2LiCl复合物是由非晶态的LiMn(BH₄)₃和晶态的LiCl组成, 在135-190 °C分解, 分解反应的活化能为114.0 kJ·mol^-1; LiMn(BH₄)₃/2LiCl复合物分解失重约7.0% (w). 组分分析表明除H₂外, 释放的气体中还含有4.0% (摩尔分数, x)的B₂H₆. B₂H₆的生成是该复合物失重超过其理论储氢容量6.3% (w)的原因; 进一步研究发现, 含钛催化剂(TiF₃、TiC、TiN和TiO₂)中, 仅TiF₃能够催化LiMn(BH₄)₃/2LiCl复合物的分解反应, 使其起始分解温度和分解反应活化能分别降低至125 °C和104.0 kJ·mol^-1. 这主要归因于TiF₃中的Ti原子取代了LiMn(BH₄)₃中的部分Li原子, 并在局域形成了易于分解的Ti(BH₄)₃.     

1,4-丁炔二醇与4,4′-二乙炔联苯共聚物的合成及表征研究

 本文用(Ph₃P)₂PdCl₂为催化剂,合成了1,4-丁炔二醇(BD)与4,4-二乙炔联苯(DEBP)共聚物。对用不同比例的两种单体得到的共聚物测定了比重(d₄²⁵、溶胀度(θ_D)、最良溶剂及相邻两交联点之间的平均分子量(M_c)。实验表明,在两种单体摩尔比中,DEBP用量越多,共聚物中泡状微孔越多,颜色越淡,溶胀度和比重越小,交联度越大;DEBP/BD(摩尔比)大于1/5时,共聚物的最良溶剂为苯,溶度参数为9.15卡^0.5·cm^-1.5,是1/10时,其最良溶剂为乙醇,溶度参数是12.7卡^0.5·cm^-1.5。对共聚物还做了红外光谱表征。     

Cu、N共掺杂TiO2纳米管光催化重整甘油制备合成气

通过碱性水热-离子交换法制备了Cu、N共掺杂TiO₂纳米管(Cu/N-TNT),对其光催化重整甘油制备合成气性能进行了研究。结果表明,Cu/N-TNT具有富含氧空位(O_V)的管状结构,N以Ti-N形式取代部分O形成杂质能级,Cu以Cu²⁺形式掺杂在催化剂晶格间隙和表面,Cu、N共掺杂促进TiO₂表面电荷有效分离,有利于其光催化重整甘油制备合成气活性和选择性的提高。紫外光照射8 h时,掺Cu量为0.15%的Cu/N-TNT催化剂上CO和H₂产量分别为7.3和8.5 mmol·g^-1,是原始TiO₂的9.1和70.8倍,n_H2/n_CO从0.52提高为1.18,n_CO/n_CO2从0.21提高至0.42。Cu/N-TNT表面N和O_V为醛类脱羰和甲酸脱水生成CO提供反应活性位点,Cu作为浅势阱提高光生电子-空穴分离效率。光生空穴(h⁺)是光催化重整甘油制备合成气过程中的主要活性物种,大量羟基自由基(·OH)和超氧自由基(·O₂^-)会导致甘油过度氧化,使CO选择性降低。     

五元体系Li＋, K＋//, CO32- ,SO42- , B4O72- -H2O在288 K时的介稳相平衡研究

采用等温蒸发法研究了五元体系Li^＋, K^＋//, , -H₂O 在288 K时的介稳相平衡关系, 测定了该五元体系在288 K条件下的介稳平衡的溶解度和溶液密度, 根据实验数据绘制了相应的介稳平衡相图和水图. 相平衡研究结果表明该五元体系介稳相平衡中有复盐K₂SO₄•Li₂SO₄生成, 其介稳相图(Li₂CO₃饱和)有4个共饱和点, 9条单变量曲线, 6个Li₂CO₃饱和的结晶区分别为LiBO₂•8H₂O, K₂B₄O₇•4H₂O, K₂CO₃•3/2H₂O, K₂SO₄, Li₂SO₄•H₂O和复盐 K₂SO₄•Li₂SO₄.     

基于1, 1′-苯乙炔-3, 3′, 5, 5′-四羧酸微孔铜配位聚合物的合成和气体吸附性质

本文报道了配合物[Cu₂(EBTC)(H₂O)₂]·8H₂O·DMF·DMSO(1, EBTC=1, 1′-乙炔基苯-3, 3′, 5, 5′-四羧酸根;DMF=N, N-二甲基甲酰胺;DMSO=二甲基亚砜)的合成、晶体结构和吸附性质。1拥有内径为0.85 nm和0.85 nm×2.15 nm的两种孔洞, 分别被6个和12个四羧酸根桥联的[Cu₂(CO₂)₄]螺旋桨式结构围绕, 并被EBTC连接成三维超分子结构, 该结构拥有可容纳溶剂分子的一维孔道。1为(3, 4)-连接的fof(sqc1575)拓扑结构, 具有非常大的孔体积, 其值高达单位晶胞体积的72.8%。去除溶剂分子后的1a表现出永久孔性, 其Langmuir表面积为2844 m²·g^-1, BET 表面积为1 852 m²·g^-1。它对H₂、CO₂、CH₄和C²H₂具有可观的气体吸附量和相对较高的吸附焓。特别是, 在迄今所有已报道的孔性金属-有机材料中, 1a在273 K、1.0×10⁵ Pa下, 表现出最高的乙炔吸附量(252 cm³·g^-1)和很高的吸附焓(吸附量为1 mmol·g^-1时的吸附焓为34.5 kJ·mol^-1)。     

有机-无机杂化磷酸锆及胺插层化合物的MAS NMR 研究

The layered zirconium [N-(phosphonomethyl)iminodiacetic acid-phosphate] Zr(HPO₄)_1.34[O₃PCH₂N-(CH₂CO₂H)2]_0.66·H₂O can only be prepared in the series of the zirconium phosphonate-phosphates Zr(HPO₄)_2-x[O₃PCH₂N(CH₂CO₂H)₂]_x·H2O (ZPPMIDA) by the reaction of zirconium oxychloride with phosphonic acid and H₂O₃PCH₂N(CH₂CO₂H)₂ in the designed x range of 0 < x < 2, which had been monitored by using the phosphorus integration value ratio of HPO₄^2- and [O₃PCH₂N(CH₂CO₂H)₂]^2- group in the ³¹P MAS NMR spectra. After intercalation of n-butyl amine, the ³¹P chemical shift of HPO₄^2- group at -8.0~-10.0 ppm moved to 6.0 ppm with a change of 14.0~16.0 ppm and that of [O₃PCH₂N(CH₂CO₂H)₂]^2- group at -29.1 ppm changed only 0.5 ppm. Due to the pillared effect of [O₃PCH₂N(CH₂CO₂H)₂]^2- groups on the interlayer spacing, intercalated amines such as n-butylamine, n-hexyl amine and n-octyl amine easily reacted with HPO₄^2- group in ZPPMIDA (x=0.66) rather than that in α-ZrP, and carboxylic group (-CO₂H) in ZPPMIDA (x=0.66).     

KI/NH3协同催化CO2与环氧丙烷合成碳酸丙烯酯的反应机理

采用密度泛函理论(DFT)研究了NH₃/KI、KI及无催化剂条件下, CO₂与环氧丙烷(PO)合成碳酸丙烯酯(PC)的反应机理. 在B3LYP/6-311++G^**基组水平上(I采用MIDIX基组)优化了反应过程中的反应物、中间体、过渡态和产物, 通过振动分析及内禀反应坐标(IRC)确定中间体和过渡态的真实性. 同时, 在相同基组水平应用自然键轨道(NBO)理论和分子中的原子(AIM)理论分析了这些化合物的轨道间相互作用和成键特征. 研究结果表明: 在无催化剂条件下非协同反应通道PO+CO₂→M0a→TS0c→M0c→TS0c′→PC为最有利通道, 其活化能为200.65 kJ·mol^-1; KI催化下活化能降低至187.40 kJ·mol^-1, 反应速率较小; 在KI/NH₃协同催化下, 除KI的催化作用外, NH₃中的氢原子还能与CO₂或PO中的氧原子形成氢键, 活化反应, 活化能降低至154.64 kJ·mol^-1, 大幅度提高了PO与CO₂环合生成产物PC的反应速率, 理论计算与实验结果一致.     

偏硼酸锶催化剂光催化还原CO2合成CH4

采用溶胶-凝胶法制备出偏硼酸锶(SrB₂O₄)光催化剂. 紫外光催化还原CO₂合成CH₄(在液相水中)的实验证明: SrB₂O₄催化剂的光催化活性略高于TiO₂(P25). 利用X射线电子衍射谱(XRD)、傅里叶变换红外(FTIR)光谱、X射线光电子能谱(XPS)、透射电子显微镜(TEM)、荧光(PL)光谱和紫外-可见(UV-Vis)漫反射吸收光谱等技术, 研究了SrB₂O₄ 催化剂的晶体结构、形貌和能带结构. 结果表明: SrB₂O₄ 的价带为2.07 V (vs normalhydrogen electrode (NHE)), 低于(H₂O/H⁺)的氧化还原电位E_redox^o (0.82 V (vs NHE)); 而导带为-1.47 V (vsNHE), 高于(CO₂/CH₄)的氧化还原电位E_redox^o (-0.24 V (vs NHE)). 因此, SrB₂O₄催化剂可以有效地光催化还原CO₂生成CH₄. 与TiO₂(P25)相比, SrB₂O₄催化剂具有相对较高导带, 光生电子的还原能力强于TiO₂(P25), 更有利于CH₄的生成, 从而决定了SrB₂O₄催化剂光催化还原CO₂合成CH₄具有较高的光催化活性.     

两个闭式十一顶钌硼烷簇合物[(PPh3)(p-BrC6H4CO2)2RuB10H8]和[(PPh3)2Ru(p-BrC6H4CO2)(PPh3)RuB10H9]的合成与晶体结构

[RuCl₂(PPh₃)₃],B₁₀H₁₀^2-与p-BrC₆H₄COOH在CH₂Cl₂中回流, 得到两个闭式十一顶钌十硼烷簇合物: [(PPh₃)(p-BrC₆H₄CO₂)₂RuB₁₀H₈] (1) 和 [(PPh₃)₂Ru(PPh₃)(p-BrC₆H₄CO₂)RuB₁₀H₉] (2), 并进行了元素分析、红外光谱、¹H核磁共振谱、¹³C核磁共振谱、X-射线单晶衍射表征. 簇合物1属于单斜晶系，空间群为C2/c, a = 2.569(4) nm, b=1.546(2) nm, c=1.927(3) nm, β=95.11(2)°, Z=8, V=7.622(21) nm³, D_c=1.533 Mg/m³, F(000)=3472, S=1.009, R=0.0418, wR=0.0775; 簇合物2属于三斜晶系, 空间群为P-1, a = 1.3142(3) nm, b=1.3761(3) nm, c=1.8503(4) nm, α=90.445(4)°, β=105.950(4)°, g=108.980(4)°, Z=2, V=3.0251(12) nm³, D_c=1.434Mg/m³, F(000)=1316, S=1.007, R=0.0464, wR=0.1175. 单晶结构分析表明, 两个簇合物的中心都具有一个闭式1:2:4:2:2堆砌结构的十一顶{RuB₁₀}金属硼烷骨架, 硼笼开口处具有船式构象的环状的六个硼原子对Ru(1)原子呈h⁶船式配位. 在簇合物1中, 钌原子有三个簇外配体, 一个三苯基膦, 两个对溴苯甲酸根. 对溴苯甲酸根上另外的两个氧原子分别取代了B(2)和B(3)上的氢原子, 从而在簇合物的两侧形成两个对称的Ru-O-C-O-B五员环. 簇合物2是一个双金属钌硼烷簇合物, Ru(2)通过一个Ru-Ru键和两个{RuH_mB}桥键与簇合物中心{RuB₁₀}相连, 从而在簇外形成了一个变形的Ru(1)-Ru(2)-B(3)-B(6)四面体结构.     

以5-(6-羧酸-2-萘基)-间苯二羧酸为配体构筑的两个镉的金属-有机骨架化合物的合成、晶体结构及荧光性质

在溶剂热条件下,以不对称三羧酸5-(6-羧酸-2-萘基)-间苯二羧酸(H₃L)为配体合成了2个镉的金属-有机骨架化合物:{[Cd₃L₂(H₂O)₃]·6DMF}_n(1)和{[Cd₃L₂(H₂O)₄]·3DMA}_n(2)。通过X射线单晶衍射,粉末衍射,热重和红外光谱进行了结构表征。结构分析表明,1和2形成3,6-连接的三维结构,其拓扑符号分别为:(4⁵.6⁴.8⁶)(4³)₂和(6¹².8³)(6³)₂。此外,还对2个化合物进行了荧光分析。     

Synthesis of CO2-based functional poly(carbonate-co-lactide)

TPPAlCl-PPN⁺Cl⁻ binary catalyst (where TPPAlCl is 5,10,15,20-tetraphenylporphyrin aluminum chloride, PPN⁺Cl⁻ is bis[triphenylphosphine] iminium chloride, the molar ratio of TPPAlCl to PPN⁺Cl⁻ is 1 to 0.5) can initiate the effective one-pot/one-step ternary copolymerization of CO₂, lactide and 4-vinyl-1-cyclohexene-1,2-epoxide, and the quaternary copolymerization of CO₂, propylene oxide, lactide, 4-vinyl-1-cyclohexene-1,2-epoxide, to form multiblock poly(carbonate-co-lactide) products with pendant vinyl group. The ternary copolymerization product composes of polylactide (PLA) block and poy(vinylcyclohexylene carbonate) (PVCHC) block, and the quaternary copolymerization product composes of poy(propylene carbonate) (PPC) block, PLA block and PVCHC block, which are verified by ¹H NMR, ¹³C NMR, ¹H-¹H cosy, hetero-nuclear multiple bond correlation, DTG, and Gel permeation chromatography analysis. The functionality and glass-transition temperature of the products can be easily adjusted by the copolymerization variables, such as the molar ratio of comonomers, copolymerization temperature, pressure of CO₂, the concentration of the catalyst.     

High yield synthesis of biodegradable poly(propylene carbonate) from carbon dioxide and propylene oxide

A novel SalenCo^III (2,4‐dinitrophenoxy) (Salen = N,N'‐bis(3,5‐di‐tert‐butylsalicylidene)‐1,2‐cyclohexanediamino) and 1,10‐phenanthroline monohydrate catalyst system was designed and employed for the copolymerization of CO₂ and propylene oxide (PO). The perfectly alternating copolymerization of CO₂ and PO proceeds effectively under middle temperature and pressure to yield poly(propylene carbonate) with a high yield and a high number average molecular weight of polymer. The structure of polymer was characterized by the IR and NMR measurements. The perfectly alternating copolymer was confirmed. The MALDI‐TOF spectrum insinuates that the copolymerization of CO₂ and PO was initiated by H₂O. Copyright © 2016 John Wiley & Sons, Ltd.     

Terpolymerization of propylene oxide,carbon dioxide,and trimethylene carbonate

High-molecular-weight polymers with different contents of propylene carbonate (PC), and trimethylene carbonate (TMC) units in the polymer chain were synthesized by the coordination anionic copolymerization of carbon dioxide, propylene oxide (PO), and TMC in supercritical carbon dioxide (scCO₂). Zinc adipate (ZnAd) was used as a catalyst. The terpolymerization products were characterized by ¹H and ¹³C NMR, IR spectroscopy, GPC, and DSC. The effect of the reaction conditions on the yield, composition, structure, and molecular weight and thermal characteristics of the terpolymers was studied. The phase behavior of the synthesized polymers and mixtures of polypropylene carbonate with polytrimethylene carbonate was examined.

     

Copolymerization of carbon dioxide and propylene oxide using an aluminum porphyrin system and its components

The catalytic activities of tetraphenylporphinatoaluminum chloride (TPPAlCl) and its propylene oxide adduct (TPPAl(PO)₂Cl) were investigated in detail together with a quarternary salt Et₄NBr for the copolymerization of carbon dioxide and propylene oxide. In addition, for the components and starting raw materials of the catalyst systems, catalytic activities were examined for the copolymerization. The TPPAlCl catalyst delivered oligomers containing ether linkages to a large extent, regardless of its PO adduction. And cyclic propylene carbonate, as byproduct, was formed in a very small portion. Using the TPPAlCl coupled with Et₄NBr as a catalyst system, the formation of ether linkages was reduced significantly in the copolymerization; however, the obtained oligomer still contained ether linkages of 25.0 mol % in the backbone. On the other hand, the formation of cyclic carbonate was increased to 22.4 mol % relative to the oligomer product. The results indicate that the salt, which was coupled with the TPPAlCl catalyst, plays a key role in reducing the formation of ether linkage in the oligomer and, however, in enhancing the formation of cyclic carbonate. Similar results were obtained for the copolymerization catalyzed by the TPPAl(PO)₂Cl/Et₄NBr system. That is, the formation of ether linkages was not restricted further by the PO adduction of the TPPAlCl component in the catalyst system. Only oligomers with a relatively high molecular weight were produced. This indicates that the PO adduction of the TPPAlCl component contributes highly to the initiation and propagation step in the oligomerization, consequently leading to a relatively high molecular weight oligomer. In contrast, the Et₄NBr, as well as the Et₂AlCl, produced only cyclic carbonate in a very low yield. Furthermore, tetraphenylporphine exhibited no catalytic activity, regardless of using together with Et₄NBr. On the other hand, the Et₂AlCl coupled with Et₄NBr provided a low molecular weight oligomer having ether linkages of 92.3 mol % in addition to the cyclic carbonate. © 1999 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 37: 3329–3336, 1999     

Alternating copolymerization of propylene oxide and carbon dioxide with highly efficient and selective (salen)Co(III) catalysts: Effect of ligand and cocatalyst variation

Synthetic routes to a series of new (salen)CoX (salen = N,N′-bis(salicylidene)-1,2-diaminoalkane; X = Br or pentafluorobenzoate (OBzF₅)) species are described. Several of these complexes are active for the copolymerization of propylene oxide (PO) and CO₂, yielding regioregular poly(propylene carbonate) (PPC) without the generation of propylene carbonate byproduct. Variation of the salen ligand, as well as the inclusion of organic-based ionic or Lewis basic cocatalysts, has dramatic effects on the resultant (salen) CoX catalytic activity. Highly active (R,R)-(salen- 1 )CoOBzF₅ (salen- 1 = N,N′-bis(3,5- di-tert-butylsalicylidene)-1,2-diaminocyclohexane) catalysts with [Ph₄P]Cl or [PPN]Y ([PPN] = bis(triphenylphosphine)iminium; Y = Cl or OBzF₅) cocatalysts exhibited turnover frequencies up to 720 h⁻¹ for rac-PO/CO₂ copolymerization, yielding PPC with greater than 90% head-to-tail connectivity. Additionally, the (R,R)-(salen- 1 )CoOBzF₅/[PPN]Cl catalyst system demonstrated a k_rel of 9.7 for the enchainment of (S)- over (R)-PO when the copolymerization was carried out at low temperatures. © 2006 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 44: 5182–5191, 2006     

Fixation of carbon dioxide into aliphatic polycarbonate,cobalt porphyrin catalyzed regio‐specific poly(propylene carbonate) with high molecular weight

Cobalt porphyrin complex (TPPCo^IIIX) (TPP = 5, 10, 15, 20‐Tetraphenyl‐ porphyrin; X = halide) in combination with ionic organic ammonium salt was used for the regio‐specific copolymerization of propylene oxide and carbon dioxide. A turnover frequency of 188 h^?1 was achieved after 5 h, and the byproduct propylene carbonate was successfully controlled to below 1%, where the obtained poly(propylene carbonate) (PPC) showed number average molecular weight (M_n) of 48 kg/mol, head‐to‐tail content of 93%, and carbonate linkage of over 99%. When the polymerization time was prolonged to 24 h, PPC with M_n over 115 kg/mol and head‐to‐tail linkage maintaining 90% was prepared, whose glass transition temperature reached 44.5 °C. © 2008 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 46: 5959–5967, 2008     

A Novel [OSSO]-Type Chromium(III) Complex as a Versatile Catalyst for Copolymerization of Carbon Dioxide with Epoxides

A new chromium(III) complex, bearing a bis-thioether-diphenolate [OSSO]-type ligand, was found to be an efficient catalyst in the copolymerization of CO₂ and epoxides to achieve poly(propylene carbonate), poly(cyclohexene carbonate), poly(hexene carbonate) and poly(styrene carbonate), as well as poly(propylene carbonate)(cyclohexene carbonate) and poly(propylene carbonate)(hexene carbonate) terpolymers.     

Dicarboxylic acid promoted immortal copolymerization for controllable synthesis of low‐molecular weight oligo(carbonate‐ether) diols with tunable carbonate unit content

Low‐molecular weight oligo(carbonate‐ether) diols are important raw materials for polyurethane formation, which with tunable carbonate unit content (CU) may endow new thermal and mechanical performances to polyurethane. Herein, facile synthesis of oligo(carbonate‐ether) diols with number average molecular weight (M_n) below 2000 g mol^?1 and CU tunable between 40% and 75% are realized in high activity by immortal copolymerization of CO₂/propylene oxide (PO) using zinc‐cobalt double metal cyanide complex (Zn‐Co‐DMCC) in the presence of sebacic acid (SA). M_n of the oligomer is in good linear relationship to the mole ratio of PO and SA (PO/SA) and hence can be precisely controlled by adjusting PO/SA. Besides, the molecular weight distribution is quite narrow due to the rapid reversible chain transfer in the immortal copolymerization. High pressure and low temperature are favorable for raising CU. In all the reactions, the weight fraction of propylene carbonate (W_PC) can even be controlled as low as 2.0 wt %, and the catalytic activity of Zn‐Co‐DMCC is above 1.0 kgg^?1 cat. © 2012 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem, 2012     

Kinetics and mechanism of metallocene‐catalyzed olefin polymerization: Comparison of ethylene,propylene homopolymerizations,and their copolymerization

A series of ethylene, propylene homopolymerizations, and ethylene/propylene copolymerization catalyzed with rac‐Et(Ind)₂ZrCl₂/modified methylaluminoxane (MMAO) were conducted under the same conditions for different duration ranging from 2.5 to 30 min, and quenched with 2‐thiophenecarbonyl chloride to label a 2‐thiophenecarbonyl on each propagation chain end. The change of active center ratio ([C^*]/[Zr]) with polymerization time in each polymerization system was determined. Changes of polymerization rate, molecular weight, isotacticity (for propylene homopolymerization) and copolymer composition with time were also studied. [C^*]/[Zr] strongly depended on type of monomer, with the propylene homopolymerization system presented much lower [C^*]/[Zr] (ca. 25%) than the ethylene homopolymerization and ethylene–propylene copolymerization systems. In the copolymerization system, [C^*]/[Zr] increased continuously in the reaction process until a maximum value of 98.7% was reached, which was much higher than the maximum [C^*]/[Zr] of ethylene homopolymerization (ca. 70%). The chain propagation rate constant (k_p) of propylene polymerization is very close to that of ethylene polymerization, but the propylene insertion rate constant is much smaller than the ethylene insertion rate constant in the copolymerization system, meaning that the active centers in the homopolymerization system are different from those in the copolymerization system. Ethylene insertion rate constant in the copolymerization system was much higher than that in the ethylene homopolymerization in the first 10 min of reaction. A mechanistic model was proposed to explain the observed activation of ethylene polymerization by propylene addition. © 2016 Wiley Periodicals, Inc. J. Polym. Sci., Part A: Polym. Chem. 2017 , 55, 867–875     

New catalytic systems based on fluorine-containing titanium(iv) alkoxides for the synthesis of ultrahigh-molecular-weight polyethylene and olefin elastomers

The catalytic activity of the systems based on titanium(iv) alkoxides (Ti(OPrⁱ)₄, Ti(OPrⁱ)₂(OCH(CF₃)₂)₂, and Ti(OCH(CF₃)₂)₄) and mixtures of alkylaluminum chlorides (Et₂AlCl or Et₃Al₂Cl₃) with dibutylmagnesium in ethylene polymerization and ethylene copolymerization with propylene and 5-ethylidene-2-norbornene was studied. Ultrahigh-molecular-weight polyethylene with the molecular weight reaching 4.9 · 10⁶ Da was found to be formed in the homopolymerization reaction, whereas copolymerization gives ter-copolymers containing propylene (up to 35 mol.%) and 5-ethylidene-2-norbornene (4.3 mol.%) units.