高分子多糖载体对四苯基金属卟啉催化性能影响

在壳聚糖四苯基金属卟啉中, 氨基或羟基可能对金属卟啉的稳定性和催化活性起重要作用. 为探索这两类基团的作用效果差异, 并调查具有类似壳聚糖结构的纤维素作为载体, 对金属卟啉的保护以及羟基的协助催化作用, 制备了纤维素四苯基铁、钴和锰卟啉. 研究了纤维素四苯基铁、钴和锰卟啉催化空气氧化环己烷的能力, 并与相应的壳聚糖金属卟啉比较. 在418 K和0.8 MPa的空气压力下, 纤维素四苯基铁(钴或锰)卟啉均只能作一次性催化而耗尽; 所获得的醇酮选择性均低于相应的壳聚糖四苯基金属卟啉. 研究结果表明: 纤维素对四苯基铁、钴和锰卟啉没有明显的保护作用, 羟基对其催化环己基过氧化氢的协助分解作用也比较小. 壳聚糖对金属卟啉有很强的保护作用, 氨基有较强的协助金属卟啉催化环己基过氧化氢分解的能力, 使醇酮选择性提高.     

金属卟啉存在下芳醛氧化反应的研究

本文研究了在金属四苯基卟啉[Co(II)TPP,Fe(III)TPPCl,Mn(III)TPPCl,Zn(II)TPP,Cu(II)TP.TPP=四苯基卟啉]存在下,用氧气氧化芳醛的过程.测定了反应体系的吸氧动力学曲线;观察了氧化过程中金属卟啉的可见光谱的变化;研究了底物,金属卟啉在反应体系中的浓度以及溶剂等因素对反应的影响.结果发现,除能可逆键合分子氧的Co(II)TPP外,不具此种功能的Fe(III)TPPCl和Mn(III)TPPCl也能加速芳醛的氧化反应.然而,它们的催化作用是在金属四苯基卟啉与反应过程中积累起来的过酸作用,卟啉环遭到破坏后观察到的,此时可能形成了某种新的催化活性中心.金属卟啉本身对反应起抑制作用,它只是表观上的催化剂,其催化作用看来不应归结为对分子氧的活化.     

金属卟啉催化环己烷羟基化反应中环己酮的形成机理研究

单金属卟啉和双金属卟啉催化下PhIO常温氧化环己烷的羟基化反应中金属卟啉结构和反应溶剂、反应温度、反应时间等环境因素对产物酮含量及酮形成反应动力学的影响进行了系统研究, 并与金属卟啉催化下PhIO氧化环己醇的反应进行了对比, 提出了金属卟啉催化下环己烷羟基化反应中产物酮的形成机理。     

金属卟啉催化环己烷羟基化反应中环己酮的形成机理研究

单金属卟啉和双金属卟啉催化下PhIO常温氧化环己烷的羟基化反应中金属卟啉结构和反应溶剂、反应温度、反应时间等环境因素对产物酮含量及酮形成反应动力学的影响进行了系统研究, 并与金属卟啉催化下PhIO氧化环己醇的反应进行了对比, 提出了金属卟啉催化下环己烷羟基化反应中产物酮的形成机理。     

超临界二氧化碳中卟啉与钴(II)、镍(II)、锌(II)配合物反应动力学

用紫外-可见光谱研究了钴(II)、镍(II)、锌(II)的1,1,1,5,5,5-六氟-2,4-戊二酮-二水配合物[M(hfac)2(H2O)2,M=Co、Ni、Zn]与5,10,15,20-四(五氟苯基)卟啉[H2tpfpp]在超临界二氧化碳中反应生成金属卟啉[M(tpfpp)]的反应动力学.在金属配合物大大过量时,反应对卟啉为一级.其表观一级速率常数随钴(II)、镍(II)配合物的浓度增加先增加、而后趋于稳定,而表观一级速率常数随锌(II)配合物的浓度增加线形增加.根据实验事实,讨论了反应的机理,得到了相应的热力学和动力学参数.     

苯环上氯取代位对四苯基金属卟啉催化烯烃环氧化性能的影响

以苯乙烯、环己烯和反式二苯乙烯为烯烃底物,以双氧水、叔丁基过氧化氢和异丙苯过氧化氢为氧化剂,以苯环上对位和邻位氯取代的四苯基金属卟啉为仿生催化剂,对烯烃的催化环氧化反应进行了对比研究.讨论了不同氯取代位的四苯基金属卟啉对烯烃环氧化性能的影响.实验结果表明,在没有助催化剂存在下,邻位氯代的四(2,6-二氯苯基)铁(锰)卟啉对烯烃的环氧化具有优异的催化性能,烯烃底物的转化率和环氧选择性都比对位氯代的四苯基铁(锰)卟啉高,且反应条件温和.其中FeⅢ(TDCPP)Cl的催化性能最好,环氧化选择性最高,催化氧化苯乙烯时,环氧苯乙烷的选择性达到了90.4%.相同金属离子不同配体的金属卟啉传递氧原子的能力为TDCPP>T(p-Cl)PP>TPP.氧化剂的结构对环氧化物的选择性有较大影响.过氧键连有吸电子基团的异丙苯过氧化氢对环氧化物的选择性最高.根据实验结果,对金属卟啉催化环氧化机理进行了分析.     

金属卟啉自氧化反应研究

金属卟啉能在温和条件下催化PhIO、H_2O_2和NaClO等氧化剂对烷烃和烯烃的单充氧反应,但在这些氧化剂存在下,金属卟啉本身存在自毁灭现象而失去催化活性,关于金属卟啉的自毁灭现象,尚无文献详细报道,我们发现,这一现象实际上是金属卟啉在氧化剂作用下发生的自氧化反应,为了系统地研究并控制金属卟啉的自氧化反应,我们合成了9种不同结构的金属卟啉(图1),从动力学上对它们的自氧化反应进行了考察,研究发现,铁和铬卟琳的自氧化反应在动力学上为二级反应,锰卟啉为一级反应;卟啉环上的取代基,无论是吸电子基还是供电子基都使反应速度加快;但在反应体系中加入中性有机配体,能抑制金属卟啉的自氧化速度,氧化剂的能力越强,反应速度越快;溶剂的极性越小,反应速度越慢。     

超临界二氧化碳中卟啉与钴(II)、镍(II)、锌(II)配合物反应动力学

用紫外-可见光谱研究了钴(II)、镍(II)、锌(II)的1, 1, 1, 5, 5, 5-六氟-2, 4-戊二酮-二水配合物[M(hfac)2(H₂O)₂, M=Co、Ni、Zn]与5, 10, 15, 20-四(五氟苯基)卟啉[H2tpfpp]在超临界二氧化碳中反应生成金属卟啉[M(tpfpp)]的反应动力学. 在金属配合物大大过量时, 反应对卟啉为一级. 其表观一级速率常数随钴(II)、镍(II)配合物的浓度增加先增加、而后趋于稳定, 而表观一级速率常数随锌(II)配合物的浓度增加线形增加. 根据实验事实, 讨论了反应的机理, 得到了相应的热力学和动力学参数.     

钴(Ⅱ)配合物与卟啉在超临界二氧化碳中的反应动力学研究

用紫外-可见光谱研究了1,1,1,5,5,5-六氟-2,4-戊二酮-钴(Ⅱ)二水[Co(hfac)2(H2O)2]与5,10,15,20-四(五氟苯基)卟啉(H2tpfpp)在超临界二氧化碳中反应生成钴卟啉[Co(tpfpp)]的反应动力学.在钴(II)配合物大大过量时,此反应对卟啉为一级,且其表观一级速率常数随钴(Ⅱ)配合物的浓度增加先增加、而后趋于稳定.根据实验事实,讨论了此反应的机理,得到了相应的热力学和动力学参数.     

次卟啉二甲酯钴络合物均相选择性催化氧化环己烷

以次卟啉二甲酯钴[Co(DPDME)]为仿生催化剂,分子氧（空气）为氧给体,无其它辅助催化剂的条件下研究了催化氧化环己烷的反应。考察了反应温度、空气压力、催化剂用量和卟啉配体结构对醇酮的产率及选择性的影响。结果表明,在相同条件下,次卟啉二甲酯钴的催化活性明显高于其它的钴卟啉催化剂。以次卟啉合钴为催化剂,浓度为0.015 mmol/L,反应温度423 K,在空气压强为0.8 MPa的条件下反应5 h,环己烷的转化率达到18.17％,选择性为87.43％。温度对次卟啉钴的催化活性影响较大,温度高于443 K时,催化剂的稳定性降低,但是其转化数仍达到了66 646。对次卟啉二甲酯钴催化空气氧化环己烷的反应路径作了初步探讨。     

Co-Mg/Al类水滑石衍生复合氧化物上N2O催化分解的研究

恒定二价与三价阳离子比为3((nCo+nMg)/nAl=3), 采用共沉淀法制备不同Co含量的系列类水滑石前驱物CoxMg3-xAl-HT(x=0, 0.5, 1, 1.5, 2, 2.5, 3), 经焙烧得到其衍生复合氧化物催化剂CoxMg3-xAlO. 采用XRD、BET、TG-DSC和TPR等表征手段考察了Co含量对材料前驱物及其衍生复合氧化物组成和结构等方面的影响, 研究了系列CoxMg3-xAlO催化剂的催化N2O分解性能; 同时探讨了反应条件, 如N2O浓度、空速、O2和H2O等因素对催化剂活性的影响. 结果表明, 所有前驱物材料均能形成完整的层状水滑石结构；经高温焙烧后形成了以Co-Al尖晶石为主相的复合氧化物, 且Co掺杂有助于尖晶石相的生成； Co含量对材料的热稳定性、比表面、可还原性和催化分解活性有显著的影响；含Co复合氧化物催化材料存在两个还原峰, 还原过程为Co3+→Co2+→Co；Mg有助于提高催化剂的热稳定性；随着Co含量增加, 催化剂比表面下降, 但比表面不是影响催化剂活性的主要因素； 500 ℃焙烧后的Co2.5Mg0.5AlO催化剂具有较好的N2O催化分解活性；提高前驱物的焙烧温度导致催化剂的活性下降；N2O浓度、空速及O2对催化剂活性的影响较小, 而H2O则对催化剂的活性有较大的影响.     

碳纳米管负载的钴催化剂在费托合成反应中的粒子尺寸效应（英文）

The effect of Co particle size on the Fischer-Tropsch synthesis(FTS) activity of carbon nanotube(CNT)-supported Co catalysts was investigated. Microemulsion(using water-to-surfactant molar ratios of 2 to12) and impregnation techniques were used to prepare catalysts with different Co particle sizes. Kinetic studies were performed to understand the effect of Co particle size on catalytic activity. Size-dependent kinetic parameters were developed using a thermodynamic method, to evaluate the structural sensitivity of the CNT-supported Co catalysts. The size-independent FTS reaction rate constant and size-independent adsorption parameter increased with increasing reaction temperature. The Polani parameter also depended on catalyst particle size, because of changes in the catalyst surface coverage.     

Heterogeneous Fenton degradation of azo dye 4BS over Co–Mn–Fe ternary hydrotalcites

This work described the application of Co–Mn–Fe hydrotalcites (Co–Mn–Fe LDHs) as heterogeneous catalysts for Fenton reaction process. The Co–Mn–Fe LDHs were synthesized by the co-precipitation method and were characterized by X-ray diffractometry (XRD), infrared spectroscopy (IR), zeta potential, and BET surface area measurement. The catalytic activity of different kinds of hydrotalcites was evaluated by the degradation of Direct Scarlet 4BS (4BS). The Co–Mn–Fe LDHs showed the best catalytic performance among four catalysts. The presence of the Mn²⁺/Mn³⁺ at surface of catalyst could accelerate the reduction of Co³⁺–Co²⁺, and then increased in the catalytic activity of the Co–Mn–Fe LDHs. The effect of initial pH, catalyst dosage, dye concentration, and reaction temperature on the degradation of 4BS had been investigated. Radical reaction mechanism was proposed by the addition of radical scavenger. The degradation kinetic followed pseudo-first-order model. The activation energy of Co–Mn–Fe LDHs was determined to be 37.3 kJ/mol. The catalytic activity of Co–Mn–Fe LDHs was maintained after four cycles of reaction, which proved the reusability of catalyst. Finally, the possible reaction mechanisms involved in the heterogeneous Fenton system were proposed.     

Particle size effects in Fischer-Tropsch synthesis by Co catalyst supported on carbon nanotubes

The effect of Co particle size on the Fischer-Tropsch synthesis (FTS) activity of carbon nanotube (CNT)-supported Co catalysts was investigated. Microemulsion (using water-to-surfactant molar ratios of 2 to12) and impregnation techniques were used to prepare catalysts with different Co particle sizes. Kinetic studies were performed to understand the effect of Co particle size on catalytic activity. Size-dependent kinetic parameters were developed using a thermodynamic method, to evaluate the structural sensitivity of the CNT-supported Co catalysts. The size-independent FTS reaction rate constant and size-independent adsorption parameter increased with increasing reac-tion temperature. The Polani parameter also depended on catalyst particle size, because of changes in the catalyst surface coverage.     

碳纳米管负载Co-Mo催化剂在孤岛减压渣油加氢裂化反应中的应用

采用等体积浸渍法制备了一系列不同Co/Mo原子比的碳纳米管（CNT）负载Co Mo催化剂。将该系列催化剂用于孤岛减压渣油加氢裂化反应，评价其催化效果，并在相同反应条件下与 γAl2O3负载Co-Mo催化剂的催化性能进行比较。结果表明，Co-Mo/CNT催化剂的催化效果略低于Co-Mo/γAl2O3催化剂。Co/Mo原子比对Co-Mo/CNT催化剂的催化效果有较大的影响。与相同载体的催化剂相比，当Co/Mo原子比为0.50时，Co-Mo/CNT催化剂具有最佳的催化效果，而Co-Mo/γAl2O3催化剂在Co/Mo原子比为0.35时具有最佳的催化效果。     

用不同前驱体制备的Co/SiO2催化剂的结构及其CO2/CH4重整反应性能

 分别采用硝酸钴、醋酸钴、硫酸钴和氯化钴为前驱体制备了Co／SiO2催化剂,用XRD,TPR,SEM和H2－TPD等实验技术考察了钴盐前驱体对催化剂结构和二氧化碳重整甲烷反应性能的影响,重点考察了硝酸钴和醋酸钴的作用．结果表明,由醋酸钴制备的Co／SiO2催化剂有最佳的催化活性和稳定性,它在钴物种的存在状态、金属－载体相互作用、钴金属晶粒度及抗烧结、抗积炭能力等方面,均与由硝酸钴制备的Co／SiO2催化剂存在显著的差别．Co／SiO2催化剂的反应活性和稳定性分别与其金属分散度和抗烧结、抗积炭能力密切相关．     

XPS characterization of the reduction and synthesis behaviour of Co/Mn oxide catalysts for Fischer-Tropsch synthesis

Summary The surface composition of Co/Mn oxide catalysts after calcination, reduction and during CO hydrogenation experiments were investigated by XPS. The bulk changes during reduction were studied by Temperature Programmed Reduction (TPR). The calcined catalysts showed Co/Mn oxides of different compositions in their surfaces. The Co surface concentration, of the catalysts with high Co content, decreased after calcination compared to the bulk composition, but after reduction the bulk concentration was almost reached again. The catalysts with low Co content showed no decrease in the surface concentrations after calcination. Significant differences in surface concentrations for the catalysts Co20 and Co5 were observed by analysing the Co 2p and 3p levels, respectively; these can be explained by an internal reduction model. After reduction the sample Co100 was completely reduced to metallic cobalt. In the manganese-containing catalysts, after in-situ reduction, Co³⁺ and Co²⁺ were found; all manganese was reduced to Mn²⁺. A comparison of the results of the in-situ reduction and the TPR profiles led to the development of a so called internal reduction model. This model assumes migration of the Co²⁺ ions to the reduction front in inner layers of the catalysts, where they will be reduced to metallic cobalt; this is enriched in the bulk and cannot be found at the surface. The manganese matrix stabilizes the surface oxide layer so that all catalysts exhibited Co/Mn spinels in the surface. Synthesis experiments in the reaction chamber of the XPS apparatus did not lead to changes of the catalyst surfaces as a function of the reaction pressure, synthesis time or synthesis gas composition. The differences in the synthesis behaviour observed for the catalysts must be due to other effects, (i.e. a change in adsorption of hydrogen connected with a change in hydrogenation activity or the different cobalt concentrations).     

Catalytic Combustion of Ethyl Acetate over Nanostructure Cobalt Supported ZSM-5 Zeolite Catalysts

Gas phase catalytic combustion of ethyl acetate, as one of volatile organic compounds (VOC), was studied on nanostructure ZSM-5, HZSM-5 and Co-ZSM-5 with different cobalt loadings. Nanostructure of ZSM-5 was determined by XRD, SEM and TEM. Catalytic studies were carried out under atmospheric pressure in a fixed bed reactor. Results showed that the Co-ZSM-5 catalysts had better activity than others and at temperatures below 350 ℃, amount of Co loading was more effective on catalytic activity. The order of conversion of ethyl acetate over different Co loading is as follows: Co-ZSM-5 (0.75 wt%)＜Co-ZSM-5 (1.5 wt%)＜Co-ZSM-5 (15 wt%)＜Co-ZSM-5 (2.8 wt%). Besides the higher the inlet concentration of ethyl acetate, the lower the conversion yield, and oxygen concentration in catalytic oxidation conditions has not so large influence on conversion. Furthermore, the presence of water vapor in inlet gaseous feed has an inhibitive effect on ethyl acetate conversion and at the temperatures above 400˚C, the effect decreases.     

聚合物固载Co-Pd 催化剂的结构与活性

采用溶剂化金属原子浸渍(SMAI)法制备了几种不同金属含量的Co Pd催化剂,用X射线衍射、X射线光电子能谱和磁测定对催化剂进行表征,并与普通浸渍法(CI)制得的相同金属含量的催化剂进行比较.结果表明SMAI法制备的催化剂金属粒度小于CI法制备的催化剂,且前者零价金属含量高于后者.SMAI法制备的催化剂Co在表面上富集,而CI法制备的催化剂Co在表面和体相的金属含量基本相同.在二丙酮醇加氢及电催化反应中, SMAI法催化剂比相同组成的CI法催化剂具有更高的催化活性.     

原位合成钴/还原氧化石墨烯纳米粒子催化氨硼烷制氢

采用简单的原位还原合成方法,利用具有温和还原性能的氨硼烷作为还原剂,在室温下一步还原氧化石墨烯和氯化钴混合溶液制备了还原氧化石墨烯负载钴纳米复合材料催化剂. 利用所制备的钴/还原氧化石墨烯催化剂催化氨硼烷水解制氢,发现钴/还原氧化石墨烯具有优异的催化性能. 相对于没有负载的钴纳米粒子以及采用硼氢化钠作为还原剂制备的钴/还原氧化石墨烯催化剂,采用氨硼烷还原制备的钴/还原氧化石墨烯催化剂表现出更加优越的催化性能. 动力学测试表明,钴/还原氧化石墨烯催化氨硼烷水解反应为零级反应,同时钴/还原氧化石墨烯催化剂催化氨硼烷水解反应的活化能为27.10 kJ·mol^-1,低于大部分已报道的其它催化剂,甚至一些贵金属催化剂的活化能. 钴/还原氧化石墨烯催化剂有着稳定的循环使用性,特别是其具有的磁性使得它能够直接从溶液中通过磁力回收,极具应用前景. 这种简单有效的合成方法有望推广到其它的金属-还原氧化石墨烯纳米复合材料体系.