Effect of pretreatment gases on the performance of WO3/SiO2 catalysts in the metathesis of 1-butene and ethene to propene

Different gases were employed to pretreat WO₃/SiO₂ for the metathesis of 1-butene and ethene to propene. Air-pretreated WO₃/SiO₂ was inactive, whereas N₂-, N₂/H₂-, and H₂-pretreated WO₃/SiO₂ exhibited high 1-butene conversion and propene selectivity. Tetragonal WO₃ and partially reduced WO_2.92 were found to be the active phases/species, whereas monoclinic WO₃ was inactive. N₂/H₂- and H₂-pretreated WO₃/SiO₂ contained both W⁶⁺ and W⁵⁺ species (i.e., nonstoichiometric WO_3−x). Air- and N₂-pretreated WO₃/SiO₂ only contained monoclinic W⁶⁺ species (WO₃) before the reaction. However, the used N₂-pretreated WO₃/SiO₂ contained both W⁶⁺ and W⁵⁺ species, suggesting that the N₂ pretreatment can facilitate the formation of some W⁵⁺ species during the reaction. This in situ partial reduction can activate the N₂-pretreated WO₃/SiO₂ for the metathesis.     

分子氧为氧化剂的Au?Ag/TS-1光催化剂协同光催化丙烯气相环氧化

近年来,丙烯环氧化已引起人们广泛的兴趣;然而,大多数过程仍面临分离困难等问题.此外,丙烯转化率和环氧丙烷(PO)的选择性仍然非常低.从环境和经济观点来看,分子氧是丙烯选择性环氧化的理想氧化剂.开发一种气相光催化环氧化方法,即在光能和多相光催化剂存在的情况下,用于化学品生产.因此,本文探讨了通过光催化O2选择氧化丙烯环氧化.传统的制备方法存在环境污染及能耗大等缺点,而利用氧气直接进行光催化丙烯环氧化制备环氧丙烷是相当具有前景的化学品生产途径.本文采用水热法制备了微球状TS-1载体,再通过浸渍还原法制备了不同Au/Ag质量比的Au–Ag/TS-1双金属催化剂.通过X射线衍射、扫描电镜、紫外-可见吸收光谱、透射电镜、X射线光电能谱、荧光光谱和N2吸脱附法等手段对合成的催化剂的组成、形貌和性质进行了研究,通过气相色谱在线分析得到光催化反应结果.结果表明,通过浸渍还原法可以很好的将贵金属分散到载体表面上.对于Au–Ag/TS-1双金属催化剂,当Au/Ag质量比为4/1时,反应温度为443 K时,环氧丙烷生成速率最大(68.3μmol/(g·h)),其选择性达52.3%.对于Au–Ag/TS-1光催化剂,双金属负载有利于O2吸附活化,同时促进了电子的传递,从而抑制电子空穴的复合,有利于氧自由基的形成.结果表明,Au,Ag双金属之间存在协同催化作用,根据实验现象提出了一种可能的反应机理.     

PREPARATION AND PERVAPORATION PROPERTIES OF PROPENE/1-DECENE COPOLYMER MEMBRANES

Propene/1-decene copolymers （P-co-D） were synthesized by means of slurry polymerization process under atmospheric pressure using Ziegler-Natta catalyst （MgCl2/TiCl4/AlEt3）. The random P-co-Ds were elastic, low-crystalline, thermally stable and therefore suitable to be used as membrane materials in organophilic pervaporation with chloroform/water mixture. Its mechanical strength is better than polydimethylsiloxane （PDMS）. The correlation between structural parameters （glass transition temperature and crystallinity） and properties of organophilic pervaporation were investigated.     

Regiochemistry of propene insertion with group 4 polymerization catalysts from a theoretical perspective

The regiochemistry of monomer insertion in propene polymerization promoted by group 4 metal catalysts has been investigated by using DFT methods. We calculated primary and secondary propene insertion on metallocenes, constrained geometry catalysts and post-metallocene systems analyzing the effects of ligand framework, growing chain and metal. Our study supports the concept that for metallocene-based catalysts the regiochemistry of propene is mainly originated by steric effects. Instead, for octahedral systems a delicate balance between steric and electronic effects is found. This allows to play with the electronic properties of the ligand framework to tune finely the regiochemistry of polymerization.     

Synthesis and structure of [Cp2Zr(OPr)(HOPr)] and its activity in the polymerisation of propene oxide

The reaction of Cp₂Zr(OPrⁱ)₂ with [H(OEt₂)₂][H₂N{B(C₆F₅)₃}₂] in dichloromethane at room temperature gives [Cp₂Zr(OPrⁱ)(HOPrⁱ)]⁺[H₂N{B(C₆F₅)₃}₂]⁻ · Et₂O in high yield. The crystal structure is reported. The complex contains a short Zr-alkoxide and a longer Zr-alcohol bond; the OH group of the coordinated isopropanol is hydrogen-bonded to a diethyl ether molecule. The complex initiates the polymerisation of propylene oxide, most probably via a cationic mechanism.     

金属Ir4 Cluster催化丙烯加氢反应势能面的密度泛函理论研究

用密度泛函理论(DFT)对金属Ir4 cluster催化丙烯Propene加氢反应的反应机理进行了理论研究. 在B3LYP理论水平下优化了反应通道上反应物、中间体、过渡态和产物各驻点物种的几何构型, 构建了该反应的基态势能面. 计算结果表明, Ir4 cluster催化丙烯加氢反应, 主要通过3条反应通道(c,d和e)进行. 主反应通道c 是H1原子先经过中间体1加成到丙烯的边端C上形成中间体3, 然后H2原子经过渡态TS3—5, 中间体5和过渡态TS5-P加成到中间C上生成产物P. c通道无论从动力学角度还是热力学角度都是最有利的; 反应通道d和e中的最高势垒和通道c上的相比差别不大, 具有一定的竞争性, 是次通道.     

Oxidative Dehydrogenation of Propane to Propene over Barium Promoted Ni-Mo-O Catalyst

Oxidative dehydrogenation of propane to propene was investigated over Ba- promoted Ni_0.9MoO₄ catalysts (molar ratio of Ba/Mo: 1%, 3%, 6%, 9%, 12%, 15%). The selectivity for propene increases with the increasing number of basic sites on the catalyst, and molybdenum ions play an important role in propane activation. No significant deactivation of the 6% Ba- Ni_0.9MoO₄ and Ni_0.9MoO₄ at 773 K for 80 h and for 40 h, respectively, appeared, indicating that the 6% Ba- Ni_0.9MoO₄ has great advantage over the Ni_0.9MoO₄. This revised version was published online in June 2006 with corrections to the Cover Date.     

镁改性对HZSM-5分子筛催化乙烯制丙烯的影响

采用等体积浸渍法制备了一系列不同Mg含量(0–1.0%)的HZSM-5分子筛。利用X射线衍射(XRD)、N_2吸附/脱附、铝魔角旋转固体核磁共振(~(27)AlMASNMR)、~(29)SiMASNMR、氨-程序升温脱附(NH_3-TPD)和吡啶吸附傅里叶变换红外(Pyridine-IR)光谱等技术对改性前后样品的结构和酸性进行了详细表征,在常压连续流动固定床反应器上考察其对乙烯转化制丙烯(ETP)反应的催化性能,评价了反应条件和Mg改性的影响。结果表明,在温度为550°C、乙烯体积空速GHSV=3000 h~(-1)的适宜反应条件下,0.5%适量镁改性HZSM-5导致乙烯转化率有所下降,但丙烯选择性增加到45%以上,而副产物芳烃的选择性降到8%以下。反应前样品的酸性表征和反应后积碳样品的TPO及~(13)CCP/MASNMR谱图分析表明适量镁改性使HZSM-5分子筛的总酸量和强B酸量减少而中强酸量增加,从而提高了丙烯的选择性,但是过量的镁改性使分子筛的总酸量明显减少,导致催化剂的活性显著下降。     

冲击波处理的结晶MgO催化剂上丙烷脱氢制丙烯的研究

冲击波处理的结晶ＭｇＯ催化剂上丙烷脱氢制丙烯的研究张菊，郑小明（杭州大学化学系，杭州，３１００２８）王立（浙江大学高分子科学与工程学系，杭州，３１００２７）冲击波及其在催化剂制备中的应用正越来越受到人们的关注［１］。丙烷是液化石油气的主要成份，催化工...     

介孔CeNiO催化剂的合成及其丙烷氧化脱氢制丙烯反应性能

以十二烷基硫酸钠（SDS）和三嵌段共聚物P123为混合模板剂,尿素为沉淀剂,采用均匀沉淀法制备了具有介孔结构的NiO和CeNiO催化剂.考察了催化剂的丙烷氧化脱氧反应性能,并利用用N₂吸附-脱附、透射电镜（TEM）、X射线粉末衍射（XRD）和H₂程序升温还原（H₂-TPR）等技术对催化剂进行了表征.活性测试结果表明,在400-450℃范围内NiO和CeNiO催化剂有相似的催化性能,但后者表现出较高的低温（<400℃）催化活性.325℃反应时,纯NiO上丙烯收率仅为3.1%,而5CeNiO(n_Ce/n_Ni=5%)催化剂上丙烯收率高达12.2%.N₂吸附-脱附和TEM结果表明,制备的NiO和CeNiO催化剂均有较大的比表面积且具有虫孔状介孔结构.H₂-TPR结果表明,CeNiO催化剂中由于Ce的存在使得得一部分氧物种的可还原性能明显增强,这可能是该催化剂具有较高催化活性的重要原因.