Au/ZrLa掺杂 CeO2催化剂在CO氧化反应中优异的催化活性：锆镧协同作用

在过去的25年,纳米金催化剂上 CO氧化反应得到广泛研究,但始终没有一致的结论。这是因为影响纳米金催化活性的因素很多,包括金的价态、载体的性质、氧空位、金属与载体之间的相互作用等,尤其是各影响因素之间相互牵制,增加了催化反应机理的研究难度。氧化铈载体表面氧缺陷的浓度较高,有利于活性金属组分在其表面的稳定和分散,因此氧化铈纳米晶负载的 Au催化剂受到广泛关注。此外,当 CeO2晶格中部分 Ce被化学性质不同的其它元素取代后,可以促进 CeO2晶格氧的活化,提高氧的储放能力,从而有利于催化反应进行。因此,本文采用水热法合成了组成均匀的 CeO2, CeZrOx和 CeZrLaOx三个载体,并通过沉淀-沉积法负载金。利用 X射线衍射(XRD)、拉曼光谱(Raman)、X射线光电子能谱(XPS)、高分辨透射电镜(HRTEM)、X射线吸收精细结构(XAFS)和氢气程序升温还原(H2-TPR)等技术分析了催化剂的物相结构、表面性质、形貌以及金纳米颗粒的大小和价态等性质,并结合其在 CO氧化反应中催化性能的差异,探讨影响金催化剂活性的关键因素。 XRD, TEM, HRTEM和 XAFS结果表明,三个载体上所得金纳米颗粒的平均尺寸都在2–4 nm,且分散较好; XPS结果表明,影响催化剂活性的关键因素不是金的价态,而是载体表面的活性氧物种。从Raman结果可知,掺杂后的氧化铈载体上氧空位浓度明显增加,因而催化剂活性都有所提高。 H2-TPR进一步探讨了三个载体以及负载金后其氧化还原能力的变化,结果表明,金和载体之间的相互作用可以增强载体的氧化还原性能以及表面氧空位浓度,进一步提高了催化剂活性,而负载金催化剂氧化还原性能的变化与载体的组成密切相关。由于锆的掺杂可使金与载体之间相互作用减弱,而镧则增强了二者间相互作用,因此 Au/CeZrLaOx催化剂上锆和镧的协同掺杂作用使其表面活性氧物种浓度最高,低温时表现出最高的催化活性。     

Catalytic Performance of Carbon Materials Supported Pd Nanoparticles in Selective Hydrogenation of Acetylene

Pd/C catalysts were prepared by deposited Pd nanoparticles (NPs) on different carbon supports including activated carbon (AC), graphite oxide (GO), and reduced graphite oxide (rGO) using sol-immobilization method. Through transmission electron microscopy, powder X-ray di raction, and X-ray photoelectron spectroscopy, the role of the carbon supports for the catalytic performances of Pd/C catalysts was examined in selective hydrogenation of acetylene. The results indicate that Pd/AC exhibited higher activity and selectivity than Pd/GO and Pd/rGO in the gas phase selective hydrogenation of acetylene. Thermal and chemical treatment of AC supports also have some effect on the catalytic performance of Pd/AC catalysts. The differences in the activity and selectivity of various Pd/C catalysts were partly attributed to the metal-support interaction.     

Structure‐activity relationship of supported Au catalysts with high catalytic activity by modifying the inactive supports

Three supported Au catalysts have been prepared by the deposition‐precipitation method by using the active carbon (AC), SiO₂‐AC, and SiO₂‐AC‐hollowed. The 3 supports were characterized by Brunauer‐Emmett‐Teller and scanning electron microscopy. Meanwhile, the supported Au nanoparticles were also characterized in detail by X‐ray powder diffraction, transmission electron microscopy, H₂‐TRP, and X‐ray photoelectron spectroscopy, and their catalytic activity and stability in CO oxidation was evaluated. The results demonstrated that Au supported on SiO₂‐AC‐hollowed exhibited much higher catalytic activity with acceptable stability for 72 hours than the other 2. We attributed to finer supported Au nanoparticles with abundant low‐coordinated Au atoms on the surfaces of hollowed supports with large special surface area and abundant pore structure. In summary, we successfully found an efficient and cheap method to prepare catalysts with high catalytic activity and acceptable stability by modifying the inactive supports.     

铝柱撑蒙脱石负载纳米金催化剂的结构表征及其CO催化活性研究

以铝柱撑蒙脱石为载体,用沉积沉淀法在其表面负载金属Au后制备了Au负载铝柱撑蒙脱石高效负载型催化剂。以XRD,TEM,XPS等手段对催化剂的结构进行了表征,并研究了铝柱撑蒙脱石负载前后CO催化氧化活性的变化规律。结果证明,Au是以高度分散的状态均匀分布在铝柱撑蒙脱石载体表面,且以Au0和Au3+的混合价态形式存在。CO催化氧化活性表征结果表明,负载后催化剂的催化活性有了显著提高,且其催化活性随着负载量的增加而不断增强,但当负载量增大到一定程度后,其催化活性不再继续增加,且有所下降。     

Gold nanoparticles deposited on mesoporous alumina for epoxidation of styrene: Effects of the surface basicity of the supports

Three kinds of mesoporous alumina (denoted as meso-Al₂O₃-x (x = a, b, c)) supports with different surface basicity were synthesized by different structure-direct agent and different assembly pathway, respectively. The surface basicity of the meso-Al₂O₃-x and the commercial γ-Al₂O₃ was measured by means of CO₂-TPD and IR spectroscopy. The profiles of CO₂-TPD and IR spectra indicated that the mesoporous alumina owned more abundant surface basic sites than that of γ-Al₂O₃. Au nanoparticles deposited on the above supports via the method of homogeneous deposition precipitation (HDP) using urea as the precipitation agent. The supported Au catalysts were characterized by N₂ adsorption–desorption isotherms, TEM, XPS and testing the catalytic performances in the epoxidation of styrene. The dispersion and average size of the gold particles are dependent of the number of surface basic sites on the supports. Transmission electron microscopy (TEM) observations show a homogeneous distribution of gold particles lower than 4 nm on meso-Al₂O₃-b and meso-Al₂O₃-c, which owned more basic sites on the surface. XPS spectra reveal that only metallic state of Au is presented on the supports, which is independent of surface properties. The different Al₂O₃ supported Au catalysts were employed as highly active/selective and reusable catalysts for the epoxidation of styrene by anhydrous t-butyl hydroperoxide (TBHP). Au nanoparticles as well as the surface basic sites of the support are responsible for the epoxidation.     

石墨烯负载MnOx催化剂的制备及其低温NH3-SCR活性

通过改进的Hummers法合成氧化石墨烯(GO), 随后采用水热法制备石墨烯负载锰氧化物(MnO_x/GR)催化剂. 考察了催化剂的低温NH₃选择性催化还原(NH₃-SCR)去除NO_x的性能, 并通过傅里叶变换红外(FTIR)光谱, 拉曼(Raman)光谱, X射线衍射(XRD), 透射电镜(TEM), N₂吸附-脱附, X射线光电子能谱(XPS)及H₂程序升温还原(H₂-TPR)等多种表征手段对催化剂的结构及NH₃-SCR性能进行分析. 结果显示, 不同MnO_x负载量的MnO_x/GR催化剂均展现了较好的低温SCR催化活性, 且在负载量为20%(w)时活性最优. 表征分析结果表明, 制备的GO表面含有丰富的含氧基团, 锰可以通过与含氧基团结合而负载到GO上; MnO_x/GR催化剂中MnO_x以纳米颗粒分散于石墨烯载体表面, 且以多种氧化物(MnO、Mn₃O₄和MnO₂)共同存在; 负载量为20%(w)的催化剂中高价锰和表面吸附氧含量增加, 低温区氧化还原能力增强及活性位点数量增加是其SCR活性提高的原因.     

以水热法合成的ZrO_2负载Au催化剂上的低温水煤气变换反应

采用一种简便的水热法合成了一系列ZrO2,并采用沉积-沉淀法制得相应1.0%Au/ZrO2催化剂,在模拟甲醇重整气气氛下评价了它们的低温水煤气变换(WGS)反应催化性能.结果发现,于150oC水热合成的ZrO2负载的Au催化剂活性最佳,240oC反应时CO转化率达87%,明显高于相同反应条件下Au负载量较高的Au/Fe2O3,Au/CeO2及Au/CeZrO4催化剂.采用X射线衍射、原子吸收光谱、N2物理吸脱附及扫描电子显微镜等手段对样品进行了表征.结果表明,Au/ZrO2催化剂的总孔体积及平均孔径越大、圆形片状形貌越规整,其低温WGS催化活性就越高.     

Synthesis of hierarchical Polystyrene/Polyaniline@Au nanostructures of different surface states and studies of their catalytic properties

We synthesized hierarchical Polystyrene/Polyaniline@Au(PS/PANI@Au) catalysts through a seeded swelling polymerization and in-situ reduction procedure. PS/PANI@Au catalysts possess a core of PS as seed and template, a PANI shell with fibers and uniform gold nanoparticles on the surface. The configuration changes of the PANI chains resulting from the doping/ dedoping procedure led to various loading amounts of Au nanoparticles. Reduction of 4-nitrophenol was chosen as the probe reaction to evaluate the catalytic activity of supported Au nanocatalysts. The catalytic results indicated that dedoping treatment of the PS/PANI supports provides stronger coordinative ability to metal nanoparticles as well as more –N= groups, which results in a better catalytic performance towards the reduction of 4-nitrophenol.     

等离激元共振光转热增强负载纳米金对丁二烯选择性加氢的催化性能

采用阳离子吸附法制备了氧化石墨烯负载纳米金(Au)催化剂(Au/GO), 通过调变Au的负载量(质量分数0.2%~2%), 实现了Au在10~21 nm粒径的可控制备. 室温下热红外测试显示0.2 W/cm²光照条件下, 随着金属负载量和粒径的增加, Au/GO光热温度可升高至110 ℃, 且光热转换效率高达88%. 研究发现, 以丁二烯的选择性催化加氢作为探针反应, 在0.2 W/cm²光照条件下, 丁二烯的转化率随Au负载量的增加先升高后降低, 丁烯选择性在90%以上; 当金负载量为0.5%(颗粒尺寸约15 nm), 光热转换温度为100 ℃时, 样品表现出较高的丁二烯转化率(99%)和丁烯选择性(90%), 且催化剂经过144 h稳定性测试无失活趋势. 与同等条件下的热催化反应相比, 光-热驱动的Au/GO的催化活性提高了5倍. 原位X射线光电子能谱测试分析表明, Au/GO催化性能的提升主要来源于等离子体光转热过程中激发纳米金表面产生了大量的Au ^δ+活性位点.     

控制CO选择氧化反应中金催化剂热点形成的新方法

采用沉积-沉淀法制备了Al2O3和MOx-Al2O3(M=Fe,Zn)负载型金催化剂.室温下对其CO氧化及富氢条件下CO选择氧化催化活性进行了广泛的研究.催化剂床层温度由热电偶直接测定.催化剂表面温度与O2/CO的体积比以及CO和H2的浓度密切相关.在CO氧化反应过程中Au/Al2O3催化剂的温度可高达170°C,添加FeOx可使其降至55°C.利用一系列仪器(X射线衍射仪,X射线光电子能谱仪和透射电镜等)对催化剂的结构进行了表征.结果显示Al2O3负载型金催化剂热点的形成可以通过添加合适的助剂很好地控制.助剂的添加能够使催化剂活性中心由金属态Au变为AuIII,从而导致了CO选择氧化反应机理不同.     

Direct gas-phase epoxidation of propylene to propylene oxide using air as oxidant on supported gold catalyst

Gold catalysts supported on SiO2, TiO2, TiO2-SiO2, and ZrO2-SiO2 supports were prepared by impregnating each support with a basic solution of tetrachloroauric acid. X-ray diffraction （XRD）, transmission electron microscopy （TEM）, and X-ray photoelectron spectroscopy （XPS） techniques were used to characterize their structure and surface composition. The results indicated that the size of gold particles could be controlled to below 10 nm by this method of preparation. Washing gold catalysts with water could markedly enhance the dispersion of metallic gold particles on the surface, but it could not completely remove the chloride ions left on the surface. The catalytic performance of direct vapor-phase epoxidation of propylene using air as an oxidant over these catalysts was evaluated at atmospheric pressure. The selectivity to propylene oxide （PO） was found to vary with reaction time on the stream. At the reaction conditions of atmosphere pressure, temperature 325 ℃, feed gas ratio V（C3H6）/V（O2）= 1/2, and GHSV =6000h^-1, 17.9% PO selectivity with 0.9% propylene conversion were obtained at initial 10 min for Au/SiO2 catalyst. After reacting 60 min only 8.9% PO selectivity were detected, but the propylene conversion rises to 1.4% and the main product is transferred to acrolein （72% selectivity）. Washing Au/TiO2-SiO2 and Aa/ZrO2-SiO2 samples with magnesium citrate solution could markedly enhance the activity and PO selectivity because smaller gold particles were obtained.     

不同组成和结构LaMnO_3钙钛矿负载Au催化剂的CO氧化活性

采用乙二醇溶胶-凝胶法制备了计量比LaMnO_3和非计量比LaMn_(1.2)O_3钙钛矿,并利用稀硝酸处理LaMnO_3制备得到LaMnO_3-AE,然后采用沉积沉淀法制备钙钛矿负载Au催化剂,以考察载体的结构和性质对Au的热稳定性以及催化剂活性的影响。通过X射线衍射(XRD)、透射电镜(TEM)、X射线光电子能谱(XPS)和H_2程序升温还原(H_2-TPR)等表征,发现LaMnO_3和LaMn_(1.2)O_3钙钛矿载体虽然有利于Au的分散,但是Au的热稳定性相对较差。相反,经稀硝酸刻蚀的LaMnO_3钙钛矿(LaMnO_3-AE)不利于Au的分散,但是有利于提高Au的热稳定性。在CO氧化反应中,当催化剂在低于500°C焙烧时,LaMn_(1.2)O_3钙钛矿负载Au催化剂的活性要显著高于LaMnO_3和LaMnO_3-AE负载Au催化剂的活性,而当催化剂焙烧温度升高至700°C以上时,LaMnO_3-AE负载Au催化剂却要显著优于LaMnO_3和LaMn_(1.2)O_3钙钛矿负载Au催化剂的活性。     

TiO2晶型对Au/TiO2上光催化分解臭氧的影响

以不同晶型TiO2为载体,采用沉积-沉淀法制备了Au/TiO2光催化剂,并用紫外-可见漫反射光谱、X射线光电子能谱(XPS)和表面光电压谱(SPS)等手段进行了催化剂表征,详细考察了Ti O2晶型对Au/TiO2光催化分解臭氧活性的影响.结果表明,光催化分解臭氧的活性顺序为Au/P25>Au/Anatase>Au/Rutile,这与不同的单一Ti O2对光催化臭氧分解的活性顺序是一致的.但在TiO2上沉积金后,其对光催化臭氧的分解活性有了显著的提高.由催化剂的Au4fXPS分析发现,不同晶型Ti O2上的电荷向金簇迁移的能力有明显差异,加之载体本身对光催化臭氧分解活性不同,两者协同作用导致负载金催化剂光催化分解臭氧活性的不同.SPS信号强度与催化剂光催化活性有很好的对应关系,SPS信号越强,光生电子和空穴分离效率越高,光催化活性越好.     

镍掺杂对氧化铝纳米片负载金催化剂在CO氧化反应中的促进作用（英文）

负载型金催化剂在CO氧化反应中具有良好的低温活性,受到了研究者的广泛关注,其催化性能与载体的性质密切相关.氧化铝具有廉价易得、比表面积大和热稳定性好等优点.然而,作为一种非还原性载体,氧化铝提供活性氧物种的能力差,与还原性载体相比催化剂的CO氧化活性较低.理论计算和实验结果表明,在金催化剂中引入过渡金属镍能够有效促进氧分子在催化剂表面的吸附和活化,从而提升金催化剂活性.此外,过渡金属的存在能够提高金的分散度,增加活性位数目,防止在高温预处理过程中金颗粒的烧结,从而提高催化剂的活性和稳定性.基于上述考虑,本文在氧化铝纳米片合成过程中原位引入硝酸镍,以实现对氧化铝载体的改性,然后负载金并应用于CO氧化反应.结果表明,当载体中的Ni/Al摩尔比为0.05,金负载量为1wt%时,采用还原性气氛对催化剂进行预处理可以得到具有CO氧化性能优良的金催化剂, 20 oC下CO转化率即可达100%.预处理气氛能够显著影响催化活性,采用还原性气氛预处理后催化剂活性明显优于氧化性气氛预处理.采用X射线衍射(XRD)、高分辨透射电镜(HRTEM)、氢气程序升温还原(H2-TPR)、氧气程序升温脱附(O2-TPD)、CO吸附原位红外光谱(CO-DRIFT)和X射线光电子能谱(XPS)等表征手段进一步研究了镍掺杂对Au/Al2O3催化剂上CO氧化反应的促进作用机制.XRD测试未观察到明显的金或镍衍射峰,表明金或镍物种均为高分散.HRTEM结果进一步证实,引入镍物种后金颗粒的粒径由3.6 nm减小为2.4 nm,表明镍掺杂有助于提高金的分散度.而XPS结果显示,镍掺杂催化剂中金与镍存在电子转移,而镍仍以Ni O为主.H2-TPR结果表明,镍掺杂的催化剂前驱体中的金物种更容易被还原.O2-TPD结果证实,镍掺杂催化剂能够引入更多的氧空位,促进氧分子的吸附和活化,从而促进CO氧化反应的进行.CO-DRIFT结果表明,相比于氧化性气氛,采用还原性气氛预处理后金物种的电子云密度增加, CO吸附增强.而对于镍掺杂的催化剂,金物种吸附CO分子的能力进一步提高,有利于CO氧化反应的进行.综上,镍掺杂能够有效提高催化剂中金的分散度,增强催化剂对CO的吸附,促进氧气分子的吸附和活化,从而提高了催化剂的CO氧化活性.     

负载型金催化剂催化乙醇选择氧化反应

选择不同氧化物(Al2O3,SiO2,TiO2,MgO)和H-ZSM-5分子筛作为载体,以尿素为沉淀剂,采用沉积-沉淀法制备了一系列负载型金催化剂.采用X射线衍射、电感耦合等离子体发射光谱、程序升温还原、NH3程序升温脱附和透射电镜等技术对催化剂样品进行了表征,并测定了催化剂对乙醇选择氧化反应的催化性能.选择Au/Al2O3催化剂,考察了金负载量、反应条件(温度、压力、时间)和添加剂对乙醇选择氧化反应的影响.结果表明,所制备的Au/Al2O3催化剂的金负载率较高,金粒子较小(3～4 nm)且分布均匀.载体对金催化剂催化乙醇氧化反应有显著影响,主要产物为乙醛、乙酸乙酯和缩醛.以TiO2为载体时,乙醇转化率较高.以Al2O3为载体时,乙酸乙酯选择性较高;少量碱性添加剂可抑制缩醛的生成,并可提高乙醇转化率和乙酸乙酯选择性.在优化的条件下,乙醇转化率可达4.7%,乙酸乙酯选择性可达93.5%.     

铁的化学形态对Au/Fe-O催化剂甲醛催化氧化性能的影响

采用溶胶沉积法、共沉淀法制备了负载型Au/Fe-O催化剂,运用X-射线粉末衍射(XRD)、透射电镜(TEM)、电感耦合等离子原子发射光谱(ICP-AES),比表面和X射线光电子能谱(XPS)技术对其进行了表征,考察了Au/Fe-O催化剂对甲醛的催化氧化活性.金负载量相同的条件下,溶胶沉积法制备的样品甲醛催化氧化活性好于共沉淀法制备的样品.实验结果表明:六面体的FeOOH载体担载了较多活性组分纳米金,是影响甲醛催化氧化活性的主要原因.     

Au/FeOx催化3-硝基苯乙烯加氢反应

采用沉积-沉降法制备了负载型Au/γ-Fe2O3、Au/α-Fe2O3和Au/Fe3-O4催化剂,并利用X射线粉末衍射技术对催化剂进行了表征。 在不同反应介质（水、乙醇和无溶剂）中,研究了Au/FeOx催化剂催化3-硝基苯乙烯加氢反应,考察了反应温度以及载体对催化剂活性的影响。 实验结果表明,在介质水中3-硝基苯乙烯的转化率要远高于乙醇中或无溶剂条件下的转化率,且随温度的升高而增大,而其加氢产物3-氨基苯乙烯的选择性无显著变化。 不同氧化铁载体负载的Au催化剂在水中的活性顺序为Au/γ-Fe2O3＞Au/α-Fe2O3＞Au/Fe3O4,其活性的差异被认为来自于不同氧化铁载体与Au之间的相互作用。     

Gold nanocatalysts supported on protonic titanate nanotubes and titania nanocrystals

Gold nanoparticles were first supported on protonic titanate nanotubes with the formation of Au/titanate nanocomposites. They were further transformed to Au/titania nanocomposites via an acetic acid treatment at 70 °C for 60 h. The porosity, crystal structure and morphology of those composites have been studied by X-ray diffraction (XRD), High-resolution transmission electron microscope (HRTEM), and low-temperature nitrogen adsorption. Catalytic tests for CO oxidation show that the Au/titanate nanocomposites had a promising activity with complete conversion of CO at 70 °C and that of Au/titania was at room temperature (25 °C). Both catalysts exhibited good thermal and long-term stabilities. The influence of the crystal vacancies and surface properties of the titanate and titania supports on the catalytic activities were evaluated.     

沉淀剂对AU/ZnO催化剂CO氧化性能及催化剂结构的影响

在25 C和进料中含水条件下,考察了由Na2CO3,(NH4)2CO3,NaOH和NH4OH等4种沉淀剂制备的Au/ZnO催化剂上CO氧化活性和稳定性.结果表明,沉淀剂影响Au/ZnO催化剂的前体组成、金粒子和ZnO粒子大小、比表面积及CO氧化性能.由NH4OH制备的Au/ZnO催化剂活性和稳定性较差,CO转化率只有15%;由其它3种沉淀剂制备的Au/ZnO催化剂的CO氧化活性和稳定性明显改善,可至少连续反应1 100 h,且保持CO完全氧化,其中Na2CO3是最佳沉淀剂.在反应过程中反应气氛可引起金粒子的聚集及在催化剂表面生成新的碱式碳酸锌物相.催化剂的稳定性与金粒子长大速度和碳酸根累积量有关.     

Relations between structure, acidity, and activity of WOx/TiO2: influence of the initial state of the support, titanium oxyhydroxide, or titanium oxide

Two series of WO(x)/TiO(2) catalysts, containing W surface densities up to 4.4 W atoms/nm(2), were prepared by pore volume impregnation of two different supports, titanium oxyhydroxide (amorphous) or titanium oxide (crystallized, 100% anatase). The influence of W surface density and the nature of the support on the surface structure, development of the acidity, and catalytic performances were examined. The texture and structure of the catalysts were investigated by Brunauer-Emmett-Teller measurements, X-ray diffraction (XRD), and Raman and infrared spectroscopy. The catalytic activity was tested for 2-propanol dehydration and n-hexane isomerization. For catalysts obtained by impregnation of titanium oxide, XRD and Raman results showed that W was present as a surface phase. Infrared spectra indicated an increase in the degree of polymerization of W species with increasing W surface density. CO and lutidine adsorption, followed by infrared spectroscopy, showed an increase in the strength and abundance of Br?nsted acid sites (measured after lutidine desorption at 573 K) with the W surface density above a threshold of 1.3 W atoms/nm(2). The development of Br?nsted acidity correlated with the evolution of the infrared bands attributed to polymerized W species. A direct relationship was observed between the concentration of Br?nsted acid sites and the catalytic activity for 2-propanol dehydration. Catalytic activity, for n-hexane isomerization, appears to be associated with the presence of highly condensed W species. The catalysts synthesized by impregnation of titanium oxyhydroxide exhibited a comparable behavior. Hence, for a given W surface density, the W surface structure, concentration of Br?nsted acid sites, and catalytic performances were similar. Thus, no significant effect of the initial form of the support (titanium oxyhydroxide versus titanium oxide; 100% anatase) was evidenced.