Cu/ZrO2催化剂上乙醇水蒸气重整反应的研究Ⅰ催化剂性能及其制备参数的影响

研究了Cu/ZrO2催化剂在乙醇水蒸气重整反应中的催化性能。用常规沉淀法、醇凝胶法制备了ZrO2载体;用浸渍法或共沉淀法制备了Cu/ZrO2催化剂。考察了ZrO2载体的制备方法以及Cu/ZrO2的制备参数对催化剂性能的影响。采用BET、XRD、TEM及XRF等方法对催化剂的比表面积、孔容、晶相、表面形貌以及活性组分等进行了表征。同时,制备并比较了Ni/ZrO2、Cu/10MgO-90ZrO2和Cu/10CaO-90ZrO2催化剂的性能,考察了活性组分Cu、Ni的差异以及ZrO2载体的影响。在Cu/ZrO2催化剂(Cu的质量分数为8%)上,500 ℃~600 ℃乙醇转化率达到98%~100％、H2选择性为2.0~2.6（摩尔比）。 Cu/ZrO2与Ni/ZrO2机械混合有助于H2选择性的提高。在催化剂载体中添加MgO、CaO碱性物质可以使H2选择性提高1.3倍~2.0倍。浸渍法制备的Cu/ZrO2催化剂的性能优于共沉淀法。     

制备方法对负载型纳米ZrO2/Al2O3复合载体性能的影响

采用浸渍-沉淀法制备了负载型纳米ZrO2/Al2O3复合载体.采用X射线衍射、N2物理吸附、差示扫描量热(DSC)和程序升温脱附等技术考察了浸渍方式和干燥方法对复合载体的表面性能、热稳定性和晶相结构的影响.结果表明,ZrO2/Al2O3复合载体中没有生成ZrO2-Al2O3复合氧化物或固溶体,纳米ZrO2仅负载在Al2O3的表面.微波干燥法制备的ZrO2/Al2O3复合载体的比表面积(158.7 m2/g)较大,最可几孔径为19.4 nm,ZrO2的粒度为4.2 nm,晶相结构为四方相ZrO2.微波诱导作用使ZrO2/Al2O3复合载体表面产生了新的酸碱中心,微波干燥法制备的ZrO2/Al2O3复合载体具有较强的热稳定性,在873~1 073 K范围内DSC曲线没有出现吸热峰,而其它干燥方法制备的复合载体在903~1 023 K范围内出现了较明显的吸热峰,表明复合载体表面的部分四方相ZrO2转变为单斜相ZrO2(m-ZrO2).对超声波处理过的复合载体进行微波干燥能进一步提高纳米ZrO2与Al2O3之间的相互作用,纳米粒子的粒度(3.4 nm)更小,分布更均匀,但没有改变ZrO2的晶相结构.     

Effect of Crystallization of Zirconium Hydroxide on the Structure and Isomerization Performance for n-Heptane Hydroisomerization of Ni-WO3/ZrO2

采用XRD、BET、IR、SEM、NH3-TPD方法对以无定形Zr（OH）4和已晶化的ZrO2为载体制备的Ni-WO3/ZrO2催化剂进行了表征,考察了载体晶化对催化剂结构、酸性及催化性能的影响。结果表明,载体晶化减弱了W与Zr间的相互作用,抑制了四方相ZrO2的生成,减少了催化剂上强酸中心的数目,从而降低了Pt-WO3/ZrO2催化剂上正庚烷异构化反应活性.     

载体的晶化对Ni/WO3-ZrO2催化剂结构及催化正庚烷异构化活性的影响

采用XRD、BET、IR、SEM、NH3-TPD方法对以无定形Zr(OH)4和已晶化的ZrO2为载体制备的Ni-WO3/ZrO2催化剂进行了表征,考察了载体晶化对催化剂结构、酸性及催化性能的影响。结果表明,载体晶化减弱了W与Zr间的相互作用,抑制了四方相ZrO2的生成,减少了催化剂上强酸中心的数目,从而降低了Pt-WO3/ZrO2催化剂上正庚烷异构化反应活性.     

ZrO2及其含量对Pd/ZrO2-Al2O3催化剂加氢脱硫性能的影响

采用浸渍法制备了一系列Pd/ZrO2-Al2O3催化剂,并考察了ZrO2-Al2O3复合载体及其ZrO2含量对Pd基催化剂噻吩加氢脱硫(HDS)性能的影响,运用XRD和NH3-TPD等手段对催化剂进行了表征。结果表明,ZrO2-Al2O3复合载体及其ZrO2含量对Pd基催化剂的HDS性能有较大的影响,其中ZrO2含量为12wt%时Pd/ZrO2-Al2O3催化剂的活性最好。ZrO2-Al2O3复合载体及其ZrO2含量对Pd基催化活性的影响是通过增加Pd的分散度、H吸附量和催化剂的酸量、以及降低活性组分与载体的相互作用来实现。     

Re组分及ZrO_2载体制备方法对Ru-Re/ZrO_2催化丙三醇氢解反应的影响

分别采用沉淀法、水热合成法和不同气氛下焙烧的方式制备了ZrO2载体,采用浸渍法负载Ru及Ru-Re组分制备了Ru/ZrO2和Ru-Re/ZrO2催化剂.利用氮气吸附-脱附、X射线衍射、透射电镜及程序升温还原等方法对样品的比表面积、孔容、平均孔径、晶体结构、形貌及还原特性等进行了表征.考察了Re组分及ZrO2载体制备方法对催化剂在丙三醇氢解制丙二醇反应中的催化性能的影响.结果表明,不同方法制备的ZrO2载体对负载型Ru催化剂的催化性能有一定影响,其中以沉淀法在空气中焙烧制得ZrO2负载活性组分后得到的催化剂的活件相对较低(转化率18.7%),而以沉淀法在氮气中焙烧以及水热合成法制备的ZrO2负载活性组分后得到的催化剂的活性相对较高(转化率25.8%).Re组分的引入对Ru/ZrO2系列催化剂的催化性能有明显的促进作用.     

ZrO2前体的制备方法对WOX-/ZrO2

考察了ZrO2前体的制备方法对WOX-/ZrO2的性质及其正庚烷临氢异构化反应性能的影响,同时采用BET、XRD、Py-IR等手段对其进行了表征.结果表明,ZrO2前体的制备方法会明显影响ZrO2前体的比表面积及WOX-/ZrO2催化剂中四方ZrO2和单斜ZrO2晶型的比例,同时WO3的分散程度也有差异.单斜ZrO2太多及WO3晶型的出现会降低正庚烷临氢异构化反应活性;而ZrO2全部为四方晶型时,虽然有利于提高低温反应活性,但缺点是裂解选择性太高;而当单斜ZrO2和四方ZrO2共存,但以四方ZrO2为主,且没有WO3晶型出现时,既可保持较高的反应活性,同时又具有极高的异构化选择性.     

CO2重整甲烷反应高效稳定Ni/ZrO2催化剂的纳米结构特点

分别通过在常压流动N2气中加热处理ZrO(OH)2醇凝胶和在空气中焙烧ZrO(OH)2水凝胶制备了含不同晶相组成和不同尺寸ZrO2纳米粒子的Ni/ZrO2催化剂.Ni/ZrO2催化剂上CO2重整CH4反应的活性和稳定性以及多种催化剂表征(XRD,TEM,TPR及TPD等)数据表明,高效稳定的Ni/ZrO2催化剂必须具有“金属/氧化物”纳米复合物的特征.ZrO2纳米粒子的晶相组成对CO2重整甲烷反应中纳米复合物型Ni/ZrO2催化剂的稳定性没有明显影响.     

稀土氧化物掺杂对SO4^2-／ZrO2／Al2O3催化剂催化性能的影响

采用浸溃-沉淀法在具有较大比表面积的Al2O3上直接合成纳米ZrO2制备负载型纳米ZrO2/Al2O3复合载体,并将氧化钪、氧化钕、氧化错等稀土氧化物(RExOy)分别掺杂到负载型纳米ZrO2/Al2O3复合载体中以改善ZrO2的表面性能.同时以此复合载体负载SO42-制备SO42-/RExOy-ZrO2/Al2O3催化剂.运用XRD,BET,NH3-TPD,原位红外等技术与方法对催化剂的晶相结构、比表面积、孔径分布、酸中心种类等进行表征,并以α-蒎烯异构化反应为探针考察了催化剂的催化性能.结果表明,掺杂的稀土氧化物没有改变ZrO2的晶相结构,但ZrO2粒度有所减小,催化剂的比表面积增加,同时稀土氧化物的存在还会改变催化剂表面SO42-的配位方式,提高表面酸中心数和酸强度,增强催化剂的活性.催化剂的孔结构对选择性有较大的影响.     

固体强酸催化剂Pd/WO3-ZrO2的制备及其对正庚烷异构化反应的催化性能

 采用共沉淀方法制备了固体酸载体WO3-ZrO2,考察了W含量和焙烧温度等对WO3-ZrO2酸性和物相结构的影响,并且考察了Pd/WO3-ZrO2催化剂对正庚烷异构化反应的催化性能. 结果表明,Pd/WO3-ZrO2催化剂的催化性能与固体强酸的W含量及晶相结构密切相关. 在w(W)=13.2%～15.8%时,经700～800 ℃焙烧,WO3在ZrO2表面达到单层分散,且大部分ZrO2以四方晶相存在,所制备的0.5%Pd/WO3-ZrO2对正庚烷异构化反应的催化活性可达到70.4%,选择性可达到81.0%.     

载体对担载Ni催化剂甲烷与二氧化碳重整反应活性的影响

制备了 Zr O2 、Mg O改性的 Al2 O3、Ti O2 复合载体 ,并应用 X-射线粉末衍射 (XRD)、比表面积测定、扫描电镜 (SEM)等手段进行了表征 .结果表明 ,这些氧化物在 Al2 O3上的晶粒尺寸小、比表面积大 ,分散较好 ,而在Ti O2 上的分散性较差 .对经 10 73K焙烧的 Mg O/ Ti O2 ,还发现部分 Ti O2 载体由锐钛矿变为金红石 ,同时生成Mg Ti O3 新相 .考察了载体对 Ni催化剂的 CH4与 CO2 重整反应活性的影响 ,其次序为 :Mg O/ Al2 O3>Zr O2 /Al2 O3>Al2 O3>Mg O >Zr O2 >Ti O2 >Mg O/ Ti O2 . Ti O2 及 Mg O/ Ti O2 担载 Ni催化剂的低活性可能与 Ti O2 本身的还原性有关     

Effects of preparation conditions of Au/FeO_x /Al_2O_3 catalysts prepared by a modified two-step method on the stability for CO oxidation

Composite oxide FeO x /Al 2 O 3 -supported gold catalysts were prepared by a modified two-step method. The effects of preparation conditions on the initial catalytic activity and long-time stability were studied for CO oxidation. XRD, XPS and in situ FTIR were employed to investigate the state of FeO x and the species on the catalyst surface. The results showed that Au/FeO x /Al 2 O 3 catalysts prepared by this method exhibited high activity and high stability in a wide pH value range. Calcination pretreatm...     

MnOx/ZrO2催化剂表面氧性能

采用ＸＲＤ，ＴＰＤ和ＴＰＲ等技术研究了ＭｎＯｘ／ＺｒＯ２催化剂的表面特性，结果表明，ＺｒＯ２表面的ＭｎＯｘ物种主要以Ｍｎ２Ｏ３和ＭｎＯ２形态存在，经还原－氧化处理后，ＭｎＯｘ物种的分散状况趋好。Ｍｎ－Ｚｒ之间的相互作用促进ＭｎＯ２的分解，而抑制Ｍｎ２Ｏ３的分解。     

Facile synthesis of pure monoclinic and tetragonal zirconia nanoparticles and their phase effects on the behavior of supported molybdena catalysts for methanol-selective oxidation

Pure monoclinic (m) and tetragonal (t) zirconia nanoparticles were readily synthesized from the reaction of inorganic zirconium salts (e.g., hydrated zirconyl nitrate) and urea in water and methanol, respectively, via a facile solvothermal method. The role of the solvents was crucial in the formation of the pure ZrO(2) phases, whereas their purity was essentially insensitive to other variables, including reaction temperature, reactant concentration, pH, and zirconium salts. Water as the solvent led to the transformation of hydrous ZrO(2) precipitates initially formed with tetragonal structures to thermodynamically more stable m-ZrO(2) via the dissolution-precipitation process, whereas methanol favored the removal of water molecules from the precursors via their reaction with urea, consequently maintaining the tetragonal structures. The obtained tetragonal samples were found to possess superior hydrothermal stability compared to those reported previously, which provides the possibility for systematically studying the effects of ZrO(2) phases on many catalytic reactions involving water as a reactant or product. Using these pure m- and t-ZrO(2) phases as supports, dispersed MoO(x) catalysts were synthesized at MoO(x) surface densities of approximately 5.0 Mo/nm(2), which is close to one monolayer of coverage. Characterization by X-ray diffraction and Raman spectroscopy confirmed that the pure ZrO(2) phases remained unchanged in the presence of the MoO(x) domains and the MoO(x) domains existed preferentially as 2D polymolybdate structures. The catalysts were subsequently examined for selective methanol oxidation as a test reaction. m-ZrO(2) support led to 2-fold greater oxidation rates than for t-ZrO(2) support, reflecting the higher intrinsic reactivity of the MoO(x) domains on m-ZrO(2). This is consistent with their higher reducibility probed by temperature-programmed reduction with H(2) (H(2) TPR). These observed effects of the ZrO(2) phases provide the basis for designing catalysts with tunable redox properties and reactivity.     

焙烧温度对柴油车氧化催化剂Pt-Pd-（x）ZrO2/Ce0.3Zr0.7O2-Al2O3性能的影响

制备了氧化铝、铈锆固溶体复合氧化物负载铂、钯的双金属催化剂Pt-Pd/ Ce0.3Zr0.7O2-Al2O3,并添加3% ZrO2助剂改性,用于柴油车尾气中CO、HC和NO的催化氧化,其中贵金属负载量仅为0.68 wt%。考察了制备过程中焙烧温度对催化剂性能的影响。催化剂活性评价结果表明,与未添加ZrO2的催化剂比较。添加ZrO2明显提高了催化剂的低温氧化活性,而且焙烧温度对催化剂的氧化性能有较大影响。焙烧温度为800 ?C时,CO和C3H6的起燃温度最低,分别为168、189 ?C,焙烧温度为700 ?C时,NO转化为NO2的转化率最高,最大转化率为36%,具有较好的热稳定性。通过XRD、N2吸附-脱附、CO化学吸附、XPS、H2-TPR等表征手段考察了催化剂物理化学性质随焙烧温度的变化情况,并分析了与催化剂活性之间的关系,得到贵金属分散度、表面化学吸附氧含量、催化剂的还原性质对氧化性能有重要影响,发挥协同作用。进而可以通过优化焙烧温度提升柴油车氧化催化剂性能,对提高工业应用柴油车尾气后处理系统的净化效率有重要意义。     

Cu/ZnO and Cu/ZrO2 interactions studied by contact angle measurement with TEM

A technique of contact angle measurement was applied to the nano-scale oxide-supported metal particles. For Cu supported on ZnO and ZrO2 the angles were found to increase and the work of adhesion to decrease with increasing particle size. Such a trend is interpreted as an effect of negative contact line tension of 2.1 x 10(-9) J m(-1) and 1.0 x 10(-9) J m(-1) in the Cu/ZnO and Cu/ZrO2 system, correspondingly. For the small-sized Cu particles the apparent work of adhesion on ZnO support is higher than that on ZrO2.     

Structures and properties of zirconia-supported ruthenium oxide catalysts for the selective oxidation of methanol to methyl formate

The effects of RuO(x) structure on the selective oxidation of methanol to methyl formate (MF) at low temperatures were examined on ZrO(2)-supported RuO(x) catalysts with a range of Ru surface densities (0.2-3.8 Ru/nm(2)). Their structure was characterized using complementary methods (X-ray diffraction, Raman and X-ray photoelectron spectra, and reduction dynamics). The structure and reactivity of RuO(x) species change markedly with Ru surface density. RuO(x) existed preferentially as RuO(4)(2-) species below 0.4 Ru/nm(2), probably as isolated Zr(RuO(4))(2) interacting with ZrO(2) surfaces. At higher surface densities, highly dispersed RuO(2) domains coexisted with RuO(4)(2-) and ultimately formed small clusters and became the prevalent form of RuO(x) above 1.9 Ru/nm(2). CH(3)OH oxidation rates per Ru atom and per exposed Ru atom (turnover rates) decreased with increasing Ru surface density. This behavior reflects a decrease in intrinsic reactivity as RuO(x) evolved from RuO(4)(2-) to RuO(2), a conclusion confirmed by transient anaerobic reactions of CH(3)OH and by an excellent correlation between reaction rates and the number of RuO(4)(2-) species in RuO(x)/ZrO(2) catalysts. The high intrinsic reactivity of RuO(4)(2-) structures reflects their higher reducibility, which favors the reduction process required for the kinetically relevant C-H bond activation step in redox cycles using lattice oxygen atoms involved in CH(3)OH oxidation catalysis. These more reactive RuO(4)(2-) species and the more exposed ZrO(2) surfaces on samples with low Ru surface density led to high MF selectivities (e.g. approximately 96% at 0.2 Ru/nm(2)). These findings provide guidance for the design of more effective catalysts for the oxidation of alkanes, alkenes, and alcohols by the synthesis of denser Zr(RuO(4))(2) monolayers on ZrO(2) and other high surface area supports.     

ZrO2在Pd／Al2O3催化剂中的助剂作用

用流动反应法考察了富氧或贫氧气氛中添加ＺｒＯ２的Ｐｄ／Ａｌ２Ｏ３催化剂上ＣＯ的催化氧化反应，并用ＸＲＤ、ＴＰＲ和ＴＰＤ－ＭＳ等技术研究了助剂ＺｒＯ２与γ－Ａｌ２Ｏ３间的相互作用对催化剂上氧物种的还原和脱出－恢复行为的影响，结果表明，基质γ－Ａｌ２Ｏ３与ＺｒＯ２能发生相互作用，添加６％ＺｒＯ２的催化剂氧化活性最好，添加适量的ＺｒＯ２有利于催化剂上氧物种的脱出－恢复，从而促进ＣＯ氧化活性及表面活泼氧物     

Au/Ce1-xZrxO2催化剂的制备、表征及其在CO氧化和水煤气变换反应中的催化性能

采用共沉淀法制备了不同锆铈摩尔比的Ce1-xZrxO2(x=0,0.1,0.3,0.5,0.7,0.9和1.0)氧化物,并以改性的浸渍法制备了金担载量为1%(质量分数)的Au/Ce1-xZrxO2催化剂.考察了催化剂在低温CO氧化和水煤气变换反应中的催化性能.应用氮物理吸附、X射线衍射、透射电镜和H2程序升温还原等技术对氧化物载体及其负载金催化剂进行了表征,并与其催化性能进行了关联.结果表明,与纯CeO2和ZrO2相比,Ce1-xZrxO2的比表面积增大而孔径减小,孔分布更加集中.Zr的加入使表面Ce4 的还原更加困难,使体相Ce4 的还原更加容易.活性组分金的加入有利于铈锆氧化物的还原.ZrO2载体较大的孔径使金在载体表面分散均匀而粒子较小,因此与Au/CeO2和Au/Ce1-xZrxO2相比,Au/ZrO2具有更好的低温CO氧化活性和水煤气变换活性,而Au/CeZrO在高温下的水煤气变换反应中表现出更好的催化性能.     

Experimental and theoretical study of the structure and reactivity of Fe1-2O< or =6- clusters with CO

Synergistic studies employing experiments in the gas phase and theoretical first principles calculations have been carried out to investigate the structure, stability, and reactivity toward CO of iron oxide cluster anions, Fe(x)O(y)- (x = 1-2, y < or = 6). Collision-induced dissociation studies of iron oxide species, employing xenon collision gas, show that FeO3- and FeO2- are the stable building blocks of the larger iron oxide clusters. Theoretical calculations show that the fragmentation patterns leading to the production of O or FeO(n) fragments are governed both by the energetics of the overall process as well as the number of intermediate states and the changes in spin multiplicity. Mass-selected experiments identified oxygen atom transfer to CO as the dominant reaction pathway for most anionic iron oxide clusters. A theoretical analysis of the molecular level pathways has been carried out to highlight the role of energetics as well as the spin states of the intermediates on the oxidation reaction.