铁系催化剂上乙苯与CO2氧化脱氢反应

采用浸渍法和溶胶-凝胶法制备了三种含Mg,Fe和Al量相同的Fe2O3-MgO/γ-Al2O3,Fe2O3/MgAl2O4和MgFe0.1Al1.9O4催化剂,在580°C考察了它们催化乙苯与CO2氧化脱氢反应性能,并采用X射线衍射,表面元素分析,H2-程序升温还原和CO2-程序升温脱附等技术对催化剂体相及表面性质进行了表征.结果表明,催化剂制备方法影响Fe物种的存在形态,进而影响催化剂的稳定性和活性.采用浸渍法制备的Fe2O3/MgAl2O4催化剂含有高度分散的Fe2O3活性物种,该物种具有较好的初活性,但是稳定性较差;而采用溶胶-凝胶法制备的MgFe0.1Al1.9O4催化剂中,Fe物种主要以同晶取代的形式存在于尖晶石骨架中,因而具有较高的乙苯与CO2氧化脱氢催化活性和稳定性.     

二氧化硅负载氧化锌催化剂的溶胶-凝胶和浸渍法制备及对仲丁醇分解反应的催化性能

分别采用溶胶-凝胶法和浸渍法制备了ZnO-SiO₂催化剂和ZnO/SiO₂催化剂并进行了表征, 以仲丁醇脱氢为探针反应, 研究了不同制备方法对催化剂表面ZnO物种存在状态及其催化性能的影响. 结果表明, 2种方法均可制备高分散的负载型ZnO催化剂. 在ZnO-SiO₂和ZnO/SiO₂催化剂上, 仲丁醇分别以脱水和脱氢反应为主. 经过分析, 催化剂上ZnO物种的存在状态是影响产物选择性的关键因素, 而2种催化剂表面的粒径、 比表面积和表面酸碱性不是影响该反应选择性的根本原因.     

介孔纳米 MoPO-AlPO4 的制备及其对异丁烯选择氧化的催化性能

 分别采用溶胶-凝胶法和等体积浸渍法制备了 MoPO-AlPO4 催化剂, 考察了钼物种存在状态对催化剂晶格氧活性以及异丁烯选择氧化反应性能的影响. N2 吸附-脱附、X 射线衍射、高分辨透射电镜、X 射线光电子能谱、傅里叶变换红外光谱、程序升温还原和微反实验结果表明, 与浸渍法制备的催化剂相比, 溶胶-凝胶法制备的 MoPO-AlPO4 催化剂为介孔纳米材料, 其比表面积和孔数量均有较大程度的提高. 在浸渍法制备的催化剂中, 钼物种以四面体 MoO42− 和八表面体 MoO66− 形式存在; 而在溶胶-凝胶法制备的催化剂中钼物种主要以四面体 MoO42− 的形式存在, 并有部分钼物种嵌入到了 AlPO4 骨架中. 钼物种的种类对异丁烯选择氧化反应的活性和选择性有较大影响, 溶胶-凝胶法制备的催化剂由于嵌入 AlPO4 骨架中钼物种的存在, 异丁烯选择氧化反应性能得到较大提高.     

Cu/SiO2催化剂制备方法对其草酸二甲酯催化氢解性能的影响

以化学吸附水解法、蒸氨法和浸渍法制备了Cu/SiO2催化剂, 并用于草酸二甲酯氢解制备乙二醇的反应. 发现用化学吸附水解法制备的催化剂具有最高的催化活性和乙二醇选择性, 乙二醇得率可达92.6%. 对还原前后不同方法制备的催化剂进行表征发现, 浸渍法制备的催化剂中Cu物种不能很好地得到分散, 因此活性较差. 蒸氨法和化学吸附水解法能较好地分散Cu物种. 由于化学吸附水解法制备的催化剂的Cu0表面积较蒸氨法的大, 且Cu＋表面积相当, 故活性高于蒸氨法制备的催化剂.     

在仲丁醇脱氢反应中负载型铜催化剂的研究

采用浸渍法制备Cu/SiO₂和Cu-ZnO/SiO₂催化剂.研究了活性物种Cu和助剂ZnO的担载量对催化剂的结构和性能的影响,同时考察该催化剂对仲丁醇脱氢活性和选择性的影响.借助XRD和TPR对催化剂进行了表征,结果表明,高分散的Cu⁰为反应的活性中心,ZnO起到分散和稳定铜物种的作用.铜-锌之间的某种相互作用导致了缩合产物增加.     

蒸氨法制备铜硅催化剂的二甲醚水蒸气重整制氢性能

采用蒸氨法制备出不同Cu负载量的xCu/SiO_2-AE催化剂,并将其用于二甲醚水蒸气重整制氢反应。当Cu负载量为30%(w)时,30Cu/SiO_2-AE催化剂表现出最佳的催化性能。结果显示,该方法制备的催化剂表面具有高度分散的CuO和层状硅酸铜物相,经还原后分别形成Cu~0和Cu~+物种。与常规浸渍法制备的30Cu/SiO_2-IM催化剂相比,蒸氨法制备的30Cu/SiO_2-AE催化剂具有优异的催化稳定性和活性,这与其独特的层状结构和表面Cu~0与Cu~+之间的协同作用相关。     

氧化镁负载钼钒磷酸铜催化剂上正己醇氧化脱氢制正己醛

 采用乙醇溶液浸渍法制备了MgO负载的Cu2PMo11VO40催化剂,考察了催化剂对正己醇氧化脱氢生成正己醛的催化性能,确定了最佳反应条件. 催化剂经50 h反应后活性没有下降,生成正己醛的选择性保持在96.0%以上. IR光谱和TPR结果表明,在反应条件下催化剂上不断有V5+从Keggin结构中移出,与Cu2+一起作为抗衡离子存在于Keggin结构单元之外,形成缺位的Keggin型结构,使催化剂处于活化状态; Cu2+的存在使催化剂的还原温度降低,Keggin结构之外的V5+与Cu2+之间存在相互作用,可使催化剂活性提高.     

负载于二氧化硅上的小尺寸氧化亚铜物种促进丙烯选择性氧化生成丙烯醛

氧化物负载的含铜材料是丙烯选择性氧化制备丙烯醛的理想催化剂,一直以来都受到人们的广泛关注.然而,对于该催化体系的结构与性能之间的关系仍不是很清楚.因此,我们以碳酸钠为沉淀剂,通过沉积沉淀法将铜负载于高比表面的二氧化硅载体上,从而得到了均匀分散且小尺寸的Cu/SiO2催化剂.另外,采用浸渍法制得了相同负载量的分散不均匀、大尺寸的Cu/SiO2催化剂.丙烯选择性氧化反应活性测试发现,沉积沉淀法制备的催化剂比浸渍法制备的更有利于丙烯醛的生成,表现出了优异的催化性能:在300℃反应时,丙烯的转化率达到25.5%,丙烯醛的选择性达到66.8%,对应的丙烯醛的生成速率高达10.5 mmol·h^-1·gcat.^-1或111.2 mmol·h^-1·gCu^-1,远远超出了浸渍法制备的催化剂性能(1.7 mmol·h^-1·gcat.^-1或17.2mmol·h^-1·gCu^-1)和文献中报道的结果.结合高角度环形暗场扫描透射电子显微镜(HAADF-STEM)和X射线吸收精细结构(XAFS)技术,对沉积沉淀法制备的催化剂进行表征,发现在反应后铜物种的结构发生了明显的变化,由小尺寸的氧化铜(CuO)团簇转变为氧化亚铜(Cu2O)团簇,并且铜物种的尺寸没有明显的增大.为了进一步探索铜物种在预处理(氢气还原)以及催化反应时(丙烯+氧气)的结构变化,对不同方法合成的两种催化剂进行了原位X射线粉末衍射测试,发现不同尺寸的铜物种在还原和反应时都经历了从氧化铜(CuO)变为金属Cu再到Cu2O的结构变化,并且Cu2O在320 min的反应过程中可以稳定存在,说明它是该催化反应的活性物种.另外,通过原位双光束傅里叶变换红外光谱追踪反应时气体分子在催化剂表面的吸脱附状态,发现丙烯可以有效地吸附在小尺寸Cu/SiO2催化剂表面,随着Cu2O的形成,检测到了烯丙基中间体(CH2=CHCH2*)的产生,该物种可以与邻近Cu2O上的一个氧发生反应,从而生成丙烯醛,因此结合N2O滴定实验,我们可认为,高度分散的小尺寸的Cu2O物种是丙烯进行高效选择性氧化反应生成丙烯醛的活性物种.     

水热老化对不同方法制备的Fe-ZSM-5用于NH_3选择性催化还原NO_x的影响

采用液体离子交换、等体积浸渍和固相离子交换制备了一系列Fe-ZSM-5催化剂,并将其用于NH3选择性催化还原NOx(NH3-SCR)反应.运用X射线衍射、紫外-可见漫反射吸收光谱和原位漫反射傅里叶变换红外光谱对催化剂进行了表征.结果表明,Fe-ZSM-5催化剂表面Fe物种可分为孤立Fe3+物种、低聚Fe氧化物团簇和Fe2O3,各催化剂上NH3-SCR反应活性不同的根本原因是其表面Fe物种分布不同.水热老化后,Fe-ZSM-5催化剂上400oC以下反应时NOx转化率降低,而高温活性略有提高,各催化剂活性差异减小;同时NH3氧化活性和NO氧化活性均明显降低.这可归因于水热老化使Fe-ZSM-5催化剂表面的孤立Fe3+物种相对浓度降低,低聚Fe氧化物团簇和Fe2O3相对浓度增加,以及催化剂表面Br?nsted酸性位显著减少所致.     

制备方法对CuO—Ce0．7Zr0．3O2催化剂的氧缺位和CO氧化活性的影响

采用溶胶-凝胶法和溶胶-凝胶 浸渍法两种方法制备了CuO-Ce0.7Zr0.3O2催化剂,并对催化剂进行了XRD、Raman等表征,考察了催化剂的CO氧化性能.研究结果表明,溶胶-凝胶法制备的CuO-Ce0.7Zr0.3O2催化剂的CO氧化活性明显高于溶胶-凝胶 浸渍法制备的CuO/Ce0.7Zr0.3O2催化剂,CuO-Ce0.7Zr0.3O2催化剂容易形成氧缺位和表面高分散CuO的颗粒较大,从而提高催化活性.     

Characterization and catalytic behavior of silica-supported copper catalysts prepared by impregnation and ion-exchange methods

Two kinds of Cu/SiO₂ catalysts were prepared by impregnation (IM) and ion-exchange (IE) methods, and tested in dehydrogenation of 2-butanol to methyl-ethyl-ketone. Some kinds of Cu²⁺ on the IE catalyst could not be reduced during the reaction, and it produced the butene. The copper oxide over the IM catalyst could be reduced during the reaction, and showed stable dehydrogenation activity for 2-butanol.     

Characterization of Cu-ZnO-Cr2O3/SiO2 catalysts and application to dehydrogenation of 2-butanol to 2-butanone

The Cu-ZnO-Cr₂O₃/SiO₂ catalysts were prepared by impregnation method, which exhibited high activity for the dehydrogenation of 2-butanol to 2-butanone. These catalysts were characterized by means of XRD, EPR and BET. The experimental results indicated that (i) the valence states of copper play a key role, (ii) groups of copper atoms were the main active sites in this reaction, and (iii) copper oxide would lead to the condensation product of 5-methyl-3-heptanone.     

Characterization and catalytic functionalities of copper oxide catalysts supported on zirconia

A series of zirconia supported copper oxide catalysts with varying copper loadings (1.2-19.1 wt %) were prepared by impregnation method. The catalysts were characterized by X-ray diffraction, UV-visible diffuse reflectance spectroscopy, X-ray photoelectron spectroscopy (XPS), temperature-programmed reduction (TPR), and temperature-programmed desorption of CO2. Copper dispersion and metal area were determined by N2O decomposition method. X-ray diffraction patterns indicate the presence of crystalline CuO phase beyond 2.7 wt % of Cu on zirconia. UV-visible diffuse reflectance spectra suggest the presence of two types of copper species on the ZrO2 support. XPS peaks intensity ratio of Cu 2p3/2 and Zr 3d5/2 was compared with Cu dispersion calculated from N2O decomposition. TPR patterns reveal the presence of highly dispersed copper oxide at lower temperatures and bulk CuO at higher temperatures. The basicity of the catalysts was found to increase with Cu loading, and the activity of the catalysts was also found to increase with the increase in Cu loading up to 2.7 wt % Cu loading. The catalytic properties were evaluated for the dehydrogenation of cyclohexanol to cyclohexanone and were related to surface properties of the copper species supported on zirconia.     

Dehydrogenation of ethylbenzene with nitrous oxide in the presence of mesoporous silica materials modified with transition metal oxides

The novel mesoporous templated silicas (MCM-48, SBA-15, MCF, and MSU) were used as supports for transition metal (Cu, Cr, or Fe) oxides. The catalysts were synthesized using the incipient wetness impregnation, and characterized by low-temperature N2 sorption, DRIFT, photoacoustic IR spectroscopy, UV-vis diffuse reflectance spectroscopy, and temperature-programmed desorption of ammonia. It was shown that the preparation method used results in different distributions and dimensions of the transition metal oxide clusters on the inert support surface. The prepared catalysts were tested in the reaction of oxidative dehydrogenation of ethylbenzene in the presence of nitrous oxide. The iron-containing catalysts showed the highest catalytic activity. The presence of isolated Fe3+ was found to be the most important factor influencing the ethylbenzene conversion. The undesirable effect of the increase in selectivity toward CO2 was observed for the samples with the highest concentrations of acidic surface sites.     

Nanostructured Cu(x)Ce1-xO2-y mixed oxide catalysts: characterization and WGS activity tests

Cu(x)Ce(1-x)O(2-y) mixed oxide catalysts were prepared by different preparation procedures: co-precipitation, the sol-gel peroxide route, and the sol-gel citric acid-assisted route. The resulting solids were investigated by means of XRD, BET, H(2) and CO temperature-programmed reduction (TPR), oxidation (TPO) and desorption (TPD) analyses, and N(2)O pulse selective reaction. It was confirmed that H(2) (CO) consumed for complete reduction of well-dispersed and bulk-like CuO phases to Cu(0), reduction of surface ceria and H(2) (CO) adsorption on the catalyst surface contribute to the total H(2) (CO) consumption. Among catalysts examined, the Cu(0.15)Ce(0.85)O(2-y) mixed oxide sample prepared by means of co-precipitation method exhibits the highest activity and stability for water-gas shift (WGS) pulse reaction in the range of employed operating conditions. WGS activity of copper-ceria mixed oxide catalysts is determined by the extent of surface ceria reduction and dispersion of copper species.     

铜锆复合氧化物的结构对其催化选 择还原－氧化氮性 能的影响

用浸渍法和共沉淀法分别制得CuO---ZrO~2复合氧化具物有不同的选择还原NO~x的催化性能,采用XRD,BET,EXAFS和H~2---TPR等手段对样品进行了表征,发现浸渍法制备的样品具有的比表面较大,氧化锆被稳定在四方相。EXAFS实验表明,浸渍法制得样品的铜离子填入氧化锆表面空穴中,并以Cu^2+形式存在;500℃焙条件下用共沉淀法引入的铜离子可部分取代锆离子,在氧化锆体相高度分散形成均匀的无定形固溶体,铜离子在氧化锆体相的高度分散是形成表面弧立铜物种的关键。溶入氧化锆体相的铜离子在取代部位由于局部负电荷而使氧化性降低,是共沉淀法制备样品具有较高催化活性的主要原因。     

溶胶凝胶法制备甲醇裂解铜系催化剂

甲醇具有能量密度高、易于储存运输及价格低廉等优点,以甲醇作为氢气载体裂解制H2,可以解决氢气难以储存运输的困难。用于该反应的催化剂较多,铜系催化剂以其价格便宜、毒性小等特点而受到研究者的广泛关注。但是该催化剂在低温下活性不高。本文用溶胶一凝胶法制备技术研制了一系列加助剂的铜系催化剂,进行热重和TPR表征,讨论其在甲醇裂解制氢模型反应中的应用。     

担载Na对Cu-ZnO/SiO2催化剂结构及催化仲丁醇脱氢反应活性的影响

采用金属Na对SiO2进行预处理,之后用浸渍法制备Cu-ZnO/Na-SiO2催化剂。 研究了Na的加入方式和含量对催化剂的结构和性能的影响,采用XRD和TPR等测试技术对催化剂进行表征。 结果表明,与未经Na预处理SiO2制备的Cu-ZnO-Na/SiO2催化剂对比,Na的加入提高了Cu物种的分散度,并增强了Cu物种与载体的相互作用。 通过调节Na的加入量可获得性能较佳的仲丁醇脱氢催化剂。     

Characterization and reactivity of copper oxide catalysts supported on TiO2-ZrO2

A series of copper catalysts supported on TiO2-ZrO2 with copper loading varying from 1.0 to 21.6 wt % were prepared by a wet impregnation method. The catalysts were characterized by X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), UV-vis diffuse reflectance spectroscopy, electron spin resonance (ESR), temperature programmed reduction (TPR), and Brunauer-Emmett-Teller specific surface area measurements. Copper dispersion and metal area were determined by N2O decomposition by the passivation method. XRD results suggest that the copper oxide is present in a highly dispersed amorphous state at copper loadings <16.8 wt % in the sample and as a crystalline CuO phase at higher Cu loadings. Copper dispersion increases with Cu loading up to 5.1 wt % and levels off at higher loadings. The XPS peak intensity ratios of Cu 2p(3/2)/Ti 2p(3/2) and Cu 2p(3/2)/Zr 3d(5/2) were compared with the copper dispersion calculated from N2O decomposition. ESR results suggest the presence of two types of copper species on the TiO2-ZrO2 support. TPR profiles reveal the presence of highly dispersed copper oxide at lower temperatures and bulk CuO at higher temperatures. The catalytic properties were evaluated for the vapor-phase dehydrogenation of cyclohexanol to cyclohexanone and related to the dispersion of Cu on TiO2-ZrO2.