MCM-41负载型过氧磷钨杂多酸季胺盐催化剂的制备和结构性能的考察

合成了以MCM-41为载体的过氧磷钨杂多酸季胺盐系列催化剂,并用XRD,FTIR,BET等方法测定了催化剂的体表结构.发现不同晶化时间合成的MCM-41具有不同的孔结构和比表面,负载过氧磷钨杂多酸季胺盐以后的催化剂对18醇催化氧化成18酸表现了不同的催化性能,与无载体的过氧磷钨杂多酸季胺盐催化剂相比显示了更高的活性和选择性.     

过氧铌取代钨磷杂多配合物的稳定性

过氧铌取代钨磷杂多配合物的稳定性龚剑，魏永慧瞿伦玉（吉林医学院预防医学系吉林１３２００１）（东北师范大学化学系长春）关键词杂多配合物，过氧铌取代，Ｄａｗｓｏｎ结构，稳定性近年杂多配合物在新型催化剂的开发［１，２］，抗病毒［３］以及作为无机离子交换剂［...     

Dawson结构过氧钛、锆-取代钨磷杂多配合物的合成及催化活性

过氧型钨磷杂多酸盐;环氧化作用;Dawson结构过氧钛、锆-取代钨磷杂多配合物的合成及催化活性     

单铌和单过氧铌杂多配合物的合成、表征及催化性能

过氧铌钨磷杂多酸盐;催化活性;单铌和单过氧铌杂多配合物的合成、表征及催化性能     

磷钨杂多化合物催化H2O2氧化十八醇制十八酸

合成了磷钨杂多化合物,考察了其对十八醇经过氧化氢催化氧化制十八酸的反应活性,探讨了温度,催化剂用量、反应时间以及Ｈ２Ｏ２与底物的摩尔比等一系列条件对反应的影响,确定了最佳反应条件。通过ＩＲ,ＩＣＰ,ＵＶ和ＮＭＲ等技术对催化剂进行了表征,考察了反应前后催化剂的变化情况,讨论了活性中心。     

过氧锆杂多化合物的合成、表征及催化活性

过氧锆钨硅杂多化合物;异构体;环氧化反应;催化活性;过氧锆杂多化合物的合成、表征及催化活性     

Keggin结构过氧铌钨磷杂多配合物的合成、表征及催化性能

钼钨的杂多化合物（HPC）在催化、电催化、分子材料、药物等诸多领域中已显示出独特的功能。含过氧金属离子取代的杂多阴离子在催化以过氧化氢为氧化剂的烯烃环氧化反应中具有很高的活性和选择性。近年来,含铌的杂多配合物由于良好的催化活性和抗病毒性,引起了人们的重视。本文合成了8种Keggin结构过氧铌钨磷杂多配合物,并用红外、紫外吸收光谱、极谱-循环伏安、及^183W NMR谱等测试手段对其结构和性质进行了确定和比较,考察了它们对烯烃环氧化反应的催化活性。     

过氧铌杂多钨酸盐热分解动力学参数的测定

钼和钨的杂多配合物由于其高催化活性及抗病毒性吸引着人们的关注［１］。杂多配合物的组成改变能调变其酸性、氧化性、反应性等,因此,混配型杂多配合物的研究近二十年来十分活跃。铌取代的杂多配合物在催化方面具有很独特的性质,其催化的工业应用及其机理已引起广泛的兴趣［２］。我们发现,过氧铌杂多配合物比非过氧杂多配合物具有更高的催化活性［３］。杂多酸盐的热稳定性是影响多相催化活性的重要性质,迄今有关过氧杂多配合物的热性质和热分解反应动力学参数的研究未见报道。本文用ＴＧ、ＤＴＡ、ＤＳＣ溶解度试验,变温红外和Ｘ一…     

含钼四元杂多磷钨酸盐的电化学研究

含钼四元杂多磷钨酸盐的电化学研究张恒彬，齐兴义，郑军伟，李树家（吉林大学化学系，长春，１３００２３）关键词磷钨杂多酸，氧化还原，电催化，循环伏安Ｋｅｇｇｉｎ结构钼或钨的杂多酸有良好的氧化还原性质和电催化作用［１～３］．其中钼或钨被其它过渡金属元素取代...     

磷钨杂多酸盐／SiO2可逆负载催化剂催化氯丙烯环氧化制环氧氯丙烷

通过原位负载法合成了一种新的具有可逆负载特性的磷钨杂多酸盐/SiO2催化剂,并应用于氯丙烯环氧化反应.在反应温度65℃的条件下,系统研究了原位负载过程中反应时间、调节剂Na2HPO4用量、烯烃/H2O2摩尔比和硅烷化硅胶粒度大小等因素对环氧化反应的影响,并考察了催化剂的循环使用效果.实验结果表明,在适宜的反应条件下,初始反应环氧氯丙烷的产率达86·5%,催化剂循环使用3次,催化活性基本保持不变.     

Studies on the Performance and Structure of Supported Catalysts for the Partial

The catalytic properties of several supported metal catalysts on different carriers were studied in the partial oxidation of methane (POM) to syngas. In our experiment, supported noble metal catalysts exhibited better performance than the other supported transition metal catalysts. The catalyst performances were significantly influenced by the d-electron configuration of the active metal components and the dispersion of active metal components on the support. A catalyst with a moderate number of unpaired electrons in the d-orbital of the active metal support without obvious acidity or redox activity (e.g. MgO) was suitable for POM performance. The Rh/SiO2 catalyst was the best in the POM reaction, among those investigated. Reaction conditions apparently also affected the POM performance of the catalyst. The conversion of methane and the selectivity for CO increased with the reaction temperature, and a high CH4/O2 ratio was not beneficial for POM performance.     

Studies on the Performance and Structure of Supported Catalysts for the Partial Oxidation of Methane to Syngas

The catalytic properties of several supported metal catalysts on different carriers were studied in the partial oxidation of methane (POM) to syngas. In our experiment, supported noble metal catalysts exhibited better performance than the other supported transition metal catalysts. The catalyst performances were significantly influenced by the d-electron configuration of the active metal components and the dispersion of active metal components on the support. A catalyst with a moderate number of unpaired electrons in the d-orbital of the active metal support without obvious acidity or redox activity (e.g. MgO) was suitable for POM performance. The Rh/SiO2 catalyst was the best in the POM reaction, among those investigated. Reaction conditions apparently also affected the POM performance of the catalyst. The conversion of methane and the selectivity for CO increased with the reaction temperature, and a high CH4/O2 ratio was not beneficial for POM performance.     

Selective Oxidation of Isobutane to Methacrylic Acid over Supported V-Mo-P Based

Heteropolyacid, the most popular catalyst for the direct oxidation of isobutane, exhibits high catalytic activity, poor thermal stability and a short lifetime. Therefore, the catalyst requires further research to improve its performance. Catalysts composed of mixed oxides (V2O5, P2O5, or MoO3) supported on silica were prepared by the sol-gel method to catalyze the reaction. Results of XRD, IR, and BET corroborated that the mixed oxides were dispersed homogeneously on the surface of support. The activity of lattice oxygen in the catalysts was studied by TPR, and the chemisorption property of isobutane on the surface of the catalysts was investigated by the TPD method. H2-TPR of the catalysts revealed that the lattice oxygen of the vanadium-based catalysts is more active than that of the molybdenum-based catalysts. The rcdox property of V or Mo species is slightly affected by other compositions of the series catalysts. The TPD curves illustrate that there are two kinds of adsorptive species of isobutane on the surface of the V and Mo based catalysts. The adsorbing species on the VMoP/SiO2 catalyst are identical to the main adsorbing species on VP/SiO2 and MoP/SiO2. The catalyst VMoP/SiO2 is more active than others in the selective oxidation of isobutane.     

Selective Oxidation of Isobutane to Methacrylic Acid over Supported V-Mo-P Based Composite Oxide Catalysts

Heteropolyacid, the most popular catalyst for the direct oxidation of isobutane, exhibits high catalytic activity, poor thermal stability and a short lifetime. Therefore, the catalyst requires further research to improve its performance. Catalysts composed of mixed oxides (V2O5, P2O5, or MoO3) supported on silica were prepared by the sol-gel method to catalyze the reaction. Results of XRD, IR, and BET corroborated that the mixed oxides were dispersed homogeneously on the surface of support. The activity of lattice oxygen in the catalysts was studied by TPR, and the chemisorption property of isobutane on the surface of the catalysts was investigated by the TPD method. H2-TPR of the catalysts revealed that the lattice oxygen of the vanadium-based catalysts is more active than that of the molybdenum-based catalysts. The redox property of V or Mo species is slightly affected by other compositions of the series catalysts. The TPD curves illustrate that there are two kinds of adsorptive species of isobutane on     

P(4VP-co-St)/SiO2固载的取代钴卟啉对乙苯的催化氧化性能

通过轴向配位法将不同结构的钴卟啉(CoTXPP(X=H, Cl, NO2))分别固载到接枝微粒聚(4-乙烯基吡啶-co-苯乙烯)/SiO2(P(4VP-co-St)/SiO2)上, 室温下分别制备了P(4VP-co-St)/SiO2固载的金属卟啉催化剂CoTPP-P(4VP-co-St)/SiO2, CoTClPP-P(4VP-co-St)/SiO2和CoTNPP-P(4VP-co-St)/SiO2, 利用傅立叶变换红外(FTIR)光谱和电子吸收光谱对其结构及轴配过程进行了表征. 在无溶剂、无助催化剂和还原剂的体系中, 研究对比了其催化分子氧氧化乙苯为苯乙酮的性能, 考察了不同反应条件对苯乙酮产率的影响. 研究发现, 其催化活性随着环外取代基吸电子能力的增强而提高. CoTNPP-P(4VP-co-St)/SiO2的催化活性和选择性最好, 在120 ℃常压下其催化乙苯反应12 h, 苯乙酮收率达到25.53%, 产物α-甲基苄醇的含量则极少. 与普通的催化剂不同, 在催化氧化体系中, CoTNPP-P(4VP-co-St)/SiO2存在最适宜用量, 过量的CoTNPP-P(4VP-co-St)/SiO2反而会使其催化活性降低; P(4VP-co-St)/SiO2表面CoTXPP的固载密度存在一最佳值. 此外, 固载化以后, 催化剂具有较好的重复使用性. 结果表明, 接枝微粒P(4VP-co-St)/SiO2对金属卟啉不仅有明显的保护作用, 而且能提高其稳定性.     

结构助剂SiO2、Al2O3对铁基催化剂浆态床F-T合成性能的影响

采用连续共沉淀与喷雾干燥成型技术相结合的方法制备了微球状Fe/Cu/K/SiO2和Fe/Cu/K/Al2O3催化剂，研究SiO2和Al2O3作为结构助剂对铁基催化剂吸附行为、炭化行为及F-T合成反应性能的影响。表征结果表明,与Al2O3相比较，SiO2抑制了H2的吸附，但促进了CO的吸附，有利于催化剂的炭化。催化剂在260℃、1.5MPa、H2/CO=0.67和2000h-1下的浆态床F-T合成反应评价表明，Fe/Cu/K/SiO2催化剂具有较高的F-T合成活性、高的水煤气变换反应（WGS）活性，且其烃产物选择性明显向高炭数方向偏移，而Fe/Cu/K/Al2O3催化剂则表现出较低的F-T合成活性、低的水煤气变换反应（WGS）活性和高的轻质烃选择性。但Fe/Cu/K/Al2O3催化剂比Fe/Cu/K/SiO2催化剂具有更好的运行稳定性。     

不同前驱体制备的Mn-H4SiW12O40/SiO2 催化剂对二甲醚催化氧化制取甲缩醛反应性能的影响

采用浸渍法分别用硫酸锰、醋酸锰、氯化锰和硝酸锰为原料制备了Mn-H4SiW12O40/SiO2 杂多酸催化剂。在常压连续流动固定床反应器中，考察了二甲醚选择氧化制取甲缩醛的反应活性。实验结果表明，催化剂的催化活性顺序为Mn-Cl2H4SiW12O40/SiO2>Mn(NO3)2H4SiW12O40/SiO2>MnSO4H4SiW12O40/SiO2>Mn(AC)2H4SiW12O40/SiO2。并进一步考察了反应温度对不同锰盐前驱体催化剂性能的影响。结果表明，随温度的升高，硫酸锰修饰的H4SiW12O40/SiO2 催化剂催化氧化比较剧烈，在613K时二甲醚转化率高达42.4%，但此时甲缩醛选择性仅为0.9%。采用氯化锰修饰的H4SiW12O40/SiO2催化剂，二甲醚催化氧化反应较缓和，并且甲缩醛的选择性明显高于分别采用硫酸锰、醋酸锰和硝酸锰改性的催化剂，在593K反应1h时，二甲醚转化率为8.6%，甲缩醛选择性达到37.5%。H2-TPR结果显示，硫酸锰改性的催化剂高温氧化性能明显强于另外三种催化剂，氯化锰的修饰使得催化剂的低温氧化性能变强。XRD结果表明，MnCl2 H4SiW12O40/SiO2催化剂的衍射特征峰明显强于其他三种催化剂，并且发现了MnO2衍射特征峰。     

M-Na-P-Mo-V/SiO2系列催化剂对异丁烯氧化反应的催化性能

 以浸渍法制备了M－Na－P－Mo－V／SiO2系列催化剂,并用FT－IR和TPR对催化剂进行了表征,考察了催化剂上的异丁烯化反应．结果表明,在空速900h－1和345℃的反应条件下,过渡金属的引入可提高甲基丙烯醛的选择性．其中Cu对催化性能的改善最佳,甲基丙烯醛选择性可达65．7％;而在Na－P－Mo－V／SiO2催化剂上,乙酸选择性可达50％,但甲基丙烯醛选性仅为4．1％．在催化剂中引入过渡金属时,Cu在提高甲基丙烯醛选择性的同时,也抑制了完全氧化产物COx的生成;Fe提高双键断裂产物和完全氧化产物选择性的同时,使甲基丙烯醛选择性下降;Zn对反应的影响不很大．TPR结果表明,在入Cu的催化剂中,Cu与杂多酸阴离子之间可能存在“溢流”作用．     

金催化顺丁烯二酸酐的选择加氢反应

采用溶胶-凝胶法制备了一系列担载纳米金催化剂,用以催化顺丁烯二酸酐(简称顺酐,MA)的选择加氢反应．模板剂的引入改变了催化剂载体的结构,从而提高了其催化活性和对加氢产物丁二酸酐(SA)以及丁二酸二乙酯(DFAS)的选择性．同时考察了反应温度、溶剂、催化剂制备方法对顺酐选择加氢反应的影响以及催化剂的重复使用性能．实验结果表明,以焙烧处理除去模板剂十八胺的Au／SiO2-O(C)为催化剂时,顺酐选择加氢制取丁二酸酐和一步加氢酯化制取丁二酸二乙酯的效果最佳,其转化率以及产物选择性均大于99．5％．     

丙烷选择氧化制丙烯醛MoVTeO/SiO2催化剂结构与性能研究

考察了MoVTeO/SiO₂系列催化剂对丙烷选择氧化制丙烯醛反应的催化性能,结合XRD,Raman和TPD等表征结果研究了催化剂结构、表面性质与催化性能之间的关系.结果表明,以Mo为主要活性组分的催化剂(MoV_0.2Te_0.1/SiO₂)具有较好的催化性能.在V,Te组分存在下,Mo物种的分散度和MoO₃的可还原性能提高.以表面钼酸盐和多钼酸盐类形态存在的高分散Mo物种有助于提高催化活性,而催化剂较弱的表面酸性对丙烯醛的生成有利.