催化乙烯醛化的钌羰基原子簇新体系

发现了乙烯醛化的一个有效的新催化体系,它由钌原子簇H_4Ru_4(CO)_(12)或Ru_3(CO)_(12),卤化物和碱金属阳离子促进剂组成。在碱性的四氢呋喃-水溶液中,C_2H_4,H_2和CO的分压为1:2:2(总压小于75kg/cm~2)及125～175℃的条件下,其催化活性正比于反应温度、C_2H_4、H_2和CO的分压。添加卤化物和碱金属阳离子极大地提高了催化活性并得到如下顺序:NaI/NaOH 相似文献   

铁化合物-Al(i-Bu)3卤化物系催化剂的ESR研究

用ESR法研究了Fe(naph)2-Al(i-Bu)3-烯丙基氯和Fe(acac)3-Al(i-Bu)3-AlEt2Cl两个反应体系.以了解这类含铁催化剂的催化机理.结果表明,不管它们的起始铁化合物中的铁离子是II价还是III价,由它们和Al(i-Bu)3及卤化物反应组成的活性催化剂,其活性中心铁离子均是II价.这一结果为进一步确定铁系催化剂活性中心的结构提供了重要依据.     

BF_3·OEt_2对钼体系催化合成1,2-聚丁二烯的影响

在以加氢汽油为溶剂,MoCl_3(C_7H_(15)COO)_2(Mo)为主催化剂,(i-Bu)_2AlO〈O〉(Al)为助催化剂合成1,2-聚丁二烯的二元催化体系中,添加BF_3CH3·OEt_2等,对体系的催化活性影响显著。以的混合物为第三组份加入催化体系,较大幅度提高了钼系催化体系的活性。在Mo/Bd=8.0×10~(-5)(摩尔比),聚合5小时,丁二烯转化率可达到70％。初步搞清了钼催化体系合成的1,2-聚丁二烯中产生凝胶的条件,推测了凝胶的生成原因,考察了聚合条件对催化活性、分子量及微观结构含量的影响。     

~(19)F-NMR研究镍系催化丁二烯聚合中氟的存在状态

<正> Ziegler-Natta型Ni(naph)_2-Al(i-Bu)_3-BF_3OEt_2(简称Ni-Al-B)催化体系在丁二烯(Bd)聚合过程中,活性中心络合物上氟的状态和数量控制着单体配位、引发、增长和链转移等步骤。文献[1—6]曾指出该体系显高催化活性的Al/B(mol比)范围在0.5—1.0之间,即F/Al=6—3.Al/B>1或F/Al<3时,聚合活性显著降低。最近,我们采用了添加酸、醇、酚和酯类等方法来改进体系中B组分的分散及氟的反应性,Al/B显著拓宽为0.3—3,氟的利用率得到提高。在此基础上,本文将讨论用~(19)F-NMR法研究氟     

稀土-其它过渡金属混合催化剂用于共轭双烯烃的聚合——Ⅲ.关于两种活性中心及其聚合机理的探讨

研究了(NdCl_3+FeCl_3)r phen-HA_2(i-Bu)_2体系聚合丁二烯。通过固定催化剂中稀土(或铁)含量而改变铁(或稀土)含量的方法,证明了此聚合体系中存在两种不同的对丁二烯聚合有很高催化活性的活性中心,即能使丁二烯聚合成高顺式产物的Nd活性中心,和使丁二烯聚合成几乎是等二元(cis-1,4和1,2构型),聚合物的Fe活性中心。所得产物具确两个T_g和产物分级后可得到cis-1,4为92％和1,2含量为54％的级分,为以上结论也提供了旁证。两种活性中心的催化活性受铝比、聚合温度等的影响,稀土活性体对聚合条件比过渡金属活性体有较宽的适应范围。对其聚合机理进行了探讨,认为两种活性中心分别按各自的聚合机理进行聚合反应。     

聚合物载体-稀土金属络合物的研究 Ⅸ.聚(苯乙烯-丙烯酰胺)载体-钕络合物的合成、表征及其催化活性

本文介绍了一种新的聚合物载体-稀土金属络合物,聚(苯乙烯-丙烯酰胺)载体-钕络合物的合成,表征和讨论了络合物的IR光谱,由此络合物与烷基铝组成的二元体系对丁二烯聚合具有良好的催化活性和定向效应。不同烷基铝的催化活性顺序为Al(i-Bu)_3>Al(i-Bu)_2H>AlEt_3。     

有机钼、钨化合物研究 ⅩⅢ六羰基钼、钨体系催化炔烃聚合及其聚合物的性质

本文首次报导M(CO)_6 CX_4(M=Mo,W;X=Cl,Br)和AlCl_3(无水)组成的体系,在光照下对各种取代炔烃的聚合催化作用.发现AlCl_3能明显地提高M(CO)_6 CX_4 hv体系的催化活性.研究了不同聚合条件对聚合反应的影响,提出和讨论了该体系催化炔烃聚合反应的机理:金属卡宾活性中心的产生、金属卡宾稳定化,催化炔烃歧化聚合反应,以及最佳聚合条件.     

铁体系催化丁二烯聚合的研究——Ⅱ.FeCl_3-(i-C_4H_9)_3Al-含氮配位体系聚合丁二烯

本文研究了FeCl_3-(i-C_4H_9)_3Al-含氮配位体系对丁二烯聚合的催化活性。含一个氮的化合物对该体系聚合丁二烯的催化活性没有显著的提高。能与Fe形成五员螯合环的含氮化合物对活性提高有以下次序:邻啡啰啉>2,2′-联吡啶>>乙二胺或四甲基乙二胺。详细研究了FeCl_3-(i-C_4H_9)_3Al-邻啡啰啉体系聚合丁二烯的规律,该体系可以得到中乙烯基聚丁二烯。提出了丁二烯聚合的反应机理。     

活性阴离子聚合定量“开-关”聚合机理研究

在链增长聚合过程中,有效控制聚合活性中心的"开"、"关"能够对特定结构和功能的聚合物合成实现"定制裁剪"。当活性中心能够进行"锁闭(Locked)"和"解锁(Unlocked)"状态便捷可控的转换,即可在特定位置实现特定单元的插入。近期,大连理工大学马红卫等在活性阴离子聚合领域开展了活性中心定量"开-关"聚合机理研究。基于烷氧硅基DPE(DPE-Si(O-iPr)_3,DPE:1,1-二苯基乙烯)以及醇钠(NaODP)来实现活性阴离子聚合体系活性中心的定量"开-关",在活性阴离子聚合机理方面取得的这一进展能够为阴离子聚合理论研究带来新的发展,同时也为高分子链结构的精密调控提供了更广阔的前景。     

丙烯选择氧化铋钼铁复氧化物催化剂组成,结构及性能的研究

采用XRD、Raman、XPS及催化剂性能评价等手段,考察了Bi_3(FeO_4)(MoO_4)_2和Fe_2(MoO_4)_3分别存在及两者共存时对Bi-Mo复氧化物体系催化性能的影响.结果表明,这两种含Fe物种的存在都有助于改善Bi-Mo系复氧化物催化剂对丙烯选择氧化反应的催化性能.但两者在作用机理上有所不同.Fe_2(MoO_4)_3本身无催化活性,但在反应条件下可部分还原为FeMoO_4形成Fe~(3+)/Fe~(2+)氧化还原对;且其地结构上与α-Bi_2(MoO_4)_3相匹配,这些因素都有助于促进催化体系中电子和氧物种的传递及催化剂表面活性中心的再生,从而提高催化性能.Bi_3(FeO_4)(MoO_4)_2在反应条件下也可形成Fe~(3+)/Fe~(2+)氧化还原对,但由于其Fe~(3-)所处的化学环境与Fe_2(MoO_4)_3很不相同,且Fe的含量也不及Fe_2(MoO_4)_3,因此它在促进催化体系中电子和氧物种的传递及催化剂表面活性中心的再生等方面的性能较差,但它对提高催化剂表面的活性中心(Bi-Mo对)数目有贡献.     

Organoaluminum–cyclic ether-cyclic imide catalysts for the polymerization of epoxides

A catalyst for the polymerization of epoxides consisting of trialkylaluminums, cyclic ethers, and cyclic imides has been investigated. Various catalyst components were examined to reveal that the combination of triisobutylaluminum, dioxane, and succinimide gives the most active catalyst. The catalytic activity is greatly enhanced with aging in which the change in color from pale yellow to dark red takes place. The polymerization data show that the dioxane provides a pathway for the catalyst components to form an active species. The dioxane-containing catalyst is likely to be different in structure from that of the dioxane-free catalyst. It was shown that the catalyst solution is electrically conductive. A parallel correlation seems to exist between the electrical conductivity and the catalytic activity, suggesting that the catalytic species may be of an ionic character.     

Ni/SiO2催化剂上甲烷催化裂解制氢

研究了固定床反应器上甲烷在Ni/SiO2催化剂上的裂解反应，并分别用O2、H2O进行催化剂失活/活化循环实验，并对催化剂用XRD进行分析。结果表明,Ni/SiO2催化剂具有良好的催化性能,甲烷转化率～40%，并能在150 min的时间内保持其活性，无论是用空气氧化还是水蒸气汽化，都能有效地活化已失活的催化剂。XRD实验显示，多次裂解－再生循环过程，对催化剂结构没有明显破坏。     

原位负载稀土三元催化剂催化环氧丙烷和二氧化碳的共聚合研究

采用2种方法制备了原位负载稀土三元催化剂,即先将均相的Y(CCl3OO)3-Glycerin体系负载在载体上,后逐滴加入ZnEt2(标记为Y(CCl3OO)3-Glycerin/γ-Al2O3/ZnEt2);或先将ZnEt2与载体反应,再与均相的Y(CCl3OO)3-Glycerin体系反应(标记为ZnEt2/γ-Al2O3/Y(CCl3OO)3-Glycerin).研究发现原位负载催化剂催化环氧丙烷和二氧化碳共聚合反应的活性比未负载前低24%～36%,通过分析催化剂制备过程中所生成的乙烷量的变化,证明原位负载时催化剂组分如Y(CCl3OO)3、Glycerin或ZnEt2发生了向载体孔隙内的扩散渗透,使得催化剂各组分配比与未负载催化剂相比发生了偏差,从而降低了催化活性;另一方面,表面羟基与ZnEt2反应形成了低效率的活性种,也是原位负载催化剂活性不高的原因之一.提出了影响原位负载稀土三元催化剂活性的2个主要因素,即活性种的反应活性和活性种的数量.通过调节催化剂组分配比、负载化阶段的振荡研磨时间、原位负载时的活性种状态、载体的表面状态等,可使负载催化剂的活性比未负载的稀土三元催化剂提高3.5%.     

超微粒La-Co氧化物催化剂对柴油机尾气碳黑催化燃烧性能的研究

用有机酸络合法制备了Co3O4，NiCo2O4和LaCo2O43种催化剂。通过程序升温氧化反应(TPO)技术对这3种催化剂进行模拟柴油碳黑催化燃烧反应的活性评价。研究发现以Co3O4为活性成分的催化剂能显著降低碳黑燃烧的温度。以Ni和La部分取代Co3O4后形成的复合氧化物NiCo2O4和混合氧化物LaCo2O4能改进Co3O4的氧化活性。但是NiCo2O4不能改进碳黑在松散接触时的燃烧活性；而混合氧化物LaCo2O4由于形成了超微粒含缺陷的LaCoO3钙钛矿型结构，它具有良好的低温氧化活性和表面原子移动性，因而能显著改进碳黑在松散接触时的燃烧活性。     

In-situ Synthesis of Gallium-Containing SAPO-11 Molecular Sieves and Superior Catalytic Performance of Their NiWS Supported Catalysts for Hydroisomerization of n-Hexadecane

In order to prepare a high-performance SAPO-11 (silicoaluminophosphate-11) based non-noble metal supported catalyst for the hydroisomerization of long-chain n-alkanes, gallium-modified SAPO-11 molecular sieve was successfully synthesized by the in-situ synthesis method, and the NiWS supported catalyst was prepared for the hydroisomerization of n-hexadecane. The effects of Ga-modification on the physicochemical properties of SAPO-11 molecular sieve, the active phase properties, and the catalytic performance of the catalyst were studied. Through a series of physicochemical characterizations, it was found that the introduction of Ga increased the mesoporous volume of SAPO-11 molecular sieve, reduced their acid density and strength, but improved the amount of medium-strong Brønsted acid. The Ga-modification weakened the interaction between the active metals and the support, increased the sulfidation degree of active metals, and increased the stacking number and dispersion of active phase. The results of catalytic performance evaluation showed that the catalytic activity and isomerization selectivity of the Ga-modified SAPO-11 molecular sieve based catalysts were improved, and the yield of i-hexadecane of NiW/2Ga-SAPO-11 was the highest, which was 40.30 % higher than that of NiW/SAPO-11. By analyzing the distribution of isomeric products, it was found that the Ga-modified SAPO-11 molecular sieve was helpful in improving the hydroisomerization depth of n-hexadecane over the catalyst.     

负载型双金属催化剂的制备及其等离子体催化氨分解制氢性能

利用等体积浸渍法制备了Fe-Co、Fe-Ni、Mo-Co、Mo-Ni双金属催化剂(总金属含量均为10%(w,质量分数),双金属摩尔比均为1:1),考察了其在等离子体条件下氨分解活性,结果表明Fe-Ni双金属催化剂表现出较好的协同作用。在此基础上,进一步考察了Fe/Ni摩尔比对其活性的影响。结果表明:当Fe/Ni摩尔比为6/4时,氨分解活性最好,而且该双金属催化剂稳定性良好。采用N_2物理吸附、X射线衍射(XRD)、H_2-程序升温还原(H_2-TPR)和高分辨透射电子显微镜(HRTEM)对催化剂的物化性质、还原性能、微观形貌等进行了研究。结果表明:活性较好的Fe-Ni双金属催化剂中,Fe与Ni形成尖晶石结构NiFe_2O_4,该结构有利于Fe和Ni的还原,即活性组分易恢复金属态,这可能是其活性较高的原因。     

Growth of carbon nanotubes on the novel FeCo-Al2O3 catalyst prepared by ultrasonic coprecipitation

FeCo-Al_2O_3 catalyst was prepared by an ultrasonic coprecipitation (UC) method for the growth of carbon nanotubes (CNTs) from catalytic decomposition of methane. Its catalytic performance was compared with that of the FeCo-Al_2O_3 catalyst counterparts prepared by stepwise impregnation (I) and conventional coprecipitation (C) methods, respectively. The structure and properties of the catalysts and the CNTs as produced thereon were investigated by means of XRD, XPS, TEM and N_2 adsorption techniques. It was found that the catalyst prepared by the ultrasonic coprecipitation method was more active, and the yield and purity of the synthesized CNTs were promoted evidently. The XPS results revealed that there were more active components on the surface of the catalyst prepared by the ultrasonic coprecipitation method. On the other hand, N_2 adsorption demonstrated that the catalyst prepared by the ultrasonic coprecipitation method conferred larger specific surface area, which was beneficial to dispersion of active components. TEM images further confirmed its higher dispersion. These factors could be responsible for its higher activity for the growth of CNTs from catalytic decomposition of methane.     

Growth of carbon nanotubes on the novel FeCo-Al_2O_3 catalyst prepared by ultrasonic coprecipitation

FeCo-Al2O3 catalyst was prepared by an ultrasonic coprecipitation (UC) method for the growth of carbon nanotubes (CNTs) from catalytic decomposition of methane.Its catalytic performance was compared with that of the FeCo-Al2O3 catalyst counterparts prepared by stepwise impregnation (I) and conventional coprecipitation (C) methods,respectively.The structure and properties of the catalysts and the CNTs as produced thereon were investigated by means of XRD,XPS,TEM and N2 adsorption techniques.It was found that the catalyst prepared by the ultrasonic coprecipitation method was more active,and the yield and purity of the synthesized CNTs were promoted evidently.The XPS results revealed that there were more active components on the surface of the catalyst prepared by the ultrasonic coprecipitation method.On the other hand,N2 adsorption demonstrated that the catalyst prepared by the ultrasonic coprecipitation method conferred larger specific surface area,which was beneficial to dispersion of active components.TEM images further confirmed its higher dispersion.These factors could be responsible for its higher activity for the growth of CNTs from catalytic decomposition of methane.     

含锌尖晶石型ZnM_2O_4(M=Cr,Al,Fe)催化剂上二氯甲烷高效催化燃烧

采用溶胶凝胶法制备出一系列的含锌尖晶石型ZnM_2O_4(M=Cr,Al,Fe)催化剂并测试其对二氯甲烷催化燃烧性能,并对催化剂进行了XRD,H_2-TPR,NH_3-TPD和XPS等表征.制备出的催化剂都具有较高的反应活性,其中ZnCr_2O_4尖晶石活性最佳,其T50为277℃.表征结果表明,催化剂的性能受到表面酸性和氧化还原性的协同作用.ZnCr_2O_4尖晶石催化剂具有较小的中等酸强度的表面酸性和最佳的低温还原性能,因此反应性能最佳.     

Cooperative Catalysis for Selective Alcohol Oxidation with Molecular Oxygen

The activation of dioxygen for selective oxidation of organic molecules is a major catalytic challenge. Inspired by the activity of nitrogen‐doped carbons in electrocatalytic oxygen reduction, we combined such a carbon with metal‐oxide catalysts to yield cooperative catalysts. These simple materials boost the catalytic oxidation of several alcohols, using molecular oxygen at atmospheric pressure and low temperature (80 °C). Cobalt and copper oxide demonstrate the highest activities. The high activity and selectivity of these catalysts arises from the cooperative action of their components, as proven by various control experiments and spectroscopic techniques. We propose that the reaction should not be viewed as occurring at an ‘active site’, but rather at an ‘active doughnut’–the volume surrounding the base of a carbon‐supported metal‐oxide particle.