Effects of Titania on the Adsorptive and Catalytic Properties of Silica-Supported Cobalt Catalyst

A series of Ti-promoted (6 wt%) Co/SiO₂ catalysts with titania content of 0 to 10 wt% were sequentially prepared by incipient wetness impregnation, and characterized with X-ray diffraction, thermogravimetric analysis, chemisorption, temperature-programmed desorption and infrared spectroscopy. The influences of Ti addition and reduction temperature (400–700 °C) on the adsorptive behavior and the catalytic properties for CO hydrogenation were investigated. The presence of Ti decreases the adsorption capacity of the cobalt surface for H₂, but enhances activity per gram cobalt. In addition, the turnover frequency increases 2–4 times upon Ti addition at reduction temperatures of 400–700 °C. The promotion in activity is accompanied by an enhanced selectivity for higher hydrocarbons and olefins. These modifications can be rationalized by the creation of active sites for CO dissociation. The desorption of CO₂ at 100 °C during temperature-programmed desorption of CO indicates the formation of active sites for CO disproportionation. Infrared spectroscopy indicates an increase in the relative absorbance of 2060–2075 cm^?1 bands upon Ti addition, which are attributed to CO adsorbed on the defect sites of the cobalt surface. Therefore, the promotion effect of Ti may be directly related to the formation of defect sites on the cobalt surface induced by the decorated titania moieties.     

Interfacial Impregnation Chemistry in the Synthesis of Cobalt Catalysts Supported on Titania

The interfacial chemistry of the impregnation step involved in the synthesis of cobalt catalysts supported on titania was investigated with regard to the mode of interfacial deposition of the aqua complex [Co(H₂O)₆]²⁺ on the “titania/electrolyte solution” interface, the structure of the inner‐sphere complexes formed, and their relative interfacial concentrations. Several methodologies based on the application of deposition experiments and electrochemical techniques were used in conjunction with diffuse‐reflectance spectroscopy and EPR spectroscopy. These suggested the formation of mononuclear/oligonuclear inner‐sphere complexes on deposition of the [Co(H₂O)₆]²⁺ ions at the “titania/electrolyte solution” interface. The joint application of semiempirical quantum‐mechanical calculations, stereochemical considerations, and modeling of the deposition data revealed the exact structure of these complexes and allowed their relative concentrations at various Co^II surface concentrations to be determined. It was found that the interface speciation depends on the Co^II surface concentration. Mononuclear complexes are formed at the compact layer of the “titania/electrolyte solution” interface for low and medium Co^II surface concentrations. Formation of mono‐hydrolyzed Ti₂O–TiO and the dihydrolyzed TiO–TiO disubstituted configurations is very probable. In the first configuration one water ligand of the [Co(H₂O)₆]²⁺ ion is substituted by a bridging surface oxygen atom and another by a terminal surface oxygen atom. In the second configuration two water ligands of the [Co(H₂O)₆]²⁺ ion are substituted by two terminal surface oxygen atoms. Binuclear and trinuclear inner‐sphere complexes are formed, in addition to the mononuclear ones, at relatively high Co^II surface concentrations.     

Selective Hydrogenation of CO2 to Ethanol over Cobalt Catalysts

Methods for the hydrogenation of CO₂ into valuable chemicals are in great demand but their development is still challenging. Herein, we report the selective hydrogenation of CO₂ into ethanol over non‐noble cobalt catalysts (CoAlO_x), presenting a significant advance for the conversion of CO₂ into ethanol as the major product. By adjusting the composition of the catalysts through the use of different prereduction temperatures, the efficiency of CO₂ to ethanol hydrogenation was optimized; the catalyst reduced at 600 ° gave an ethanol selectivity of 92.1 % at 140 °C with an ethanol time yield of 0.444 mmol g^?1 h^?1. Operando FT‐IR spectroscopy revealed that the high ethanol selectivity over the CoAlO_x catalyst might be due to the formation of acetate from formate by insertion of *CH_x, a key intermediate in the production of ethanol by CO₂ hydrogenation.     

Cu/SiO_2气凝胶催化剂上CO的催化氧化性能

如何消除 CO对环境造成的污染 ,是当前人们所关心的课题之一 .催化氧化是消除 CO的一种有效方法 .常用的 CO氧化催化剂多以贵金属为基础 .目前 ,对非贵金属催化剂的研究也正在进行 ,其中 ,过渡金属 Cu、Co、Fe等对 CO的氧化有较好的催化作用 .传统的过渡金属催化剂多以氧化铝为载体 ,并发展了多种制备方法 ,如化学浸渍法、溶胶凝胶法[1] 等 ;催化剂的金属活性组分也由微米级颗粒发展到纳米级超细粒子[2 ] .但对载体的研究仍集中于氧化铝 .近几年发现 ,过渡金属交换的ZSM- 5分子筛具有较高的活性和稳定性 [3 ] .二氧化硅气凝胶是一种新…     

Design and Synthesis of Copper–Cobalt Catalysts for the Selective Conversion of Synthesis Gas to Ethanol and Higher Alcohols

Combining quantum‐mechanical simulations and synthesis tools allows the design of highly efficient CuCo/MoO_x catalysts for the selective conversion of synthesis gas (CO+H₂) into ethanol and higher alcohols, which are of eminent interest for the production of platform chemicals from non‐petroleum feedstocks. Density functional theory calculations coupled to microkinetic models identify mixed Cu–Co alloy sites, at Co‐enriched surfaces, as ideal for the selective production of long‐chain alcohols. Accordingly, a versatile synthesis route is developed based on metal nanoparticle exsolution from a molybdate precursor compound whose crystalline structure isomorphically accommodates Cu²⁺ and Co²⁺ cations in a wide range of compositions. As revealed by energy‐dispersive X‐ray nanospectroscopy and temperature‐resolved X‐ray diffraction, superior mixing of Cu and Co species promotes formation of CuCo alloy nanocrystals after activation, leading to two orders of magnitude higher yield to high alcohols than a benchmark CuCoCr catalyst. Substantiating simulations, the yield to high alcohols is maximized in parallel to the CuCo alloy contribution, for Co‐rich surface compositions, for which Cu phase segregation is prevented.     

高分散锰氧化物催化剂的结构、性能及载体效应

用浸渍法制备了A l2O3,S iO2和MgO等不同性质载体负载的锰氧化物催化剂,考察了其对CO氧化反应的性能,并用XRD、XPS、TPR和XAFS等方法对催化剂进行了详细表征.活性测试结果表明,不同载体负载的样品的活性次序为:MnOx/A l2O3>MnOx/MgO>MnOx/S iO2.XRD结果表明,在S iO2和A l2O3上,负载量为15%的催化剂中没有检测到Mn氧化物的衍射峰,说明Mn物种在载体表面分散性很好,而在MgO上检测到Mg6MnO8物种.XAFS等表征结果表明,A l2O3和S iO2负载的样品中Mn主要以高分散的Mn2O3形式存在,MgO负载的样品中Mn的分散性相对较差,且与载体发生强相互作用.结合XPS和TPR结果,Mn氧化物与载体相互作用强弱的顺序为:MnOx/MgO>MnOx/A l2O3>MnOx/S iO2.负载Mn氧化物催化剂的活性与分散度没有直接对应关系,而是显示了明显的载体效应.     

Characteristics of Active Site Formation in Co-Containing Catalysts for CO Oxidation on Chemically Different Supports

We have studied the catalytic activity in CO oxidation for cobalt-containing (1.2 mass % Co) catalysts on different supports: ZSM-5, Al₂O₃, SiO₂, and ERI. Using X-ray photoelectron spectroscopy (XPS), diffuse reflection electronic spectroscopy, and thermal programmed reduction we have established that the differences in the activity of Co-containing catalysts are due to different localization of the cobalt cations, the nature of their distribution in the surface layer of the catalyst, and the presence of cobalt ions Co_Oh in an environment of intralattice oxygen which have high reducibility.     

负载型镧锰钙钛矿催化剂上甲烷催化燃烧的研究

研究了甲烷在负载型镧锰钙钛矿催化剂(LCFM／α-Al2O3)上的低温催化燃烧反应．考察了制备方法、焙烧温度列催化剂结构和活性的影响．并进行了100h稳定性实验．实验结果表明用浸渍法、焙烧温度高于800℃就能在载体上生成良好的钙钛矿结构，催化剂具有较低的起燃温度并且在高温条件下具有与非负载型镧锰钙钛矿催化剂相当的活性；100h稳定性实验表明LCFM／a-Al2O3催化剂经历了100h．800℃的连续高温燃烧反应，催化剂仍保持了原有结构和催化活性．并且没有明显积碳．     

CO在Pd系双金属及其单金属催化剂上的吸脱附红外光谱

红外光谱表明吸附在担载于Al_2O_3上的Pd-Cu、Pd-Ag、Pd-Co和Pd-Pt 双组分催化剂上的CO仍保持其在单金属上的主要吸附物种,但其部分CO吸收带发生位移,吸附的CO易于脱附.CO在还原态Pd-Cu和Pd-Ag双金属催化剂上以吸附于Pd上者为主,其吸收带明显变弱而更易脱附.在Pd- Pt和Pd-Co氧化和还原态催化剂上CO桥式和线式吸收带强度比发生显著变化.似乎在这二类双金属催化剂上的几何结构效应比电子配位效应更为明显.     

Pt/C催化剂对乙醇电氧化的粒径效应

利用有机溶胶方法, 通过控制溶剂挥发温度制备了具有不同粒径大小的Pt/C催化剂. 制得的Pt/C催化剂中, Pt粒子具有非常优异的均一性和良好的分散度. 电化学研究表明, 对于乙醇的电催化氧化, Pt/C催化剂存在着明显的粒径效应. 当Pt粒子粒径为3.2 nm时, Pt/C催化剂对乙醇的电催化氧化的质量比活性最佳. X射线光电子能谱(XPS)的研究显示, Pt/C催化剂对乙醇氧化的粒径效应与其零价Pt含量以及Pt粒子的比表面积密切相关.     

SMAI法制备的Cu催化剂的CO加氢催化

用溶剂化金属原子浸渍（SMAI）法制备了SiO2、Cr2O3负载Cu催化剂.XPS测定表明三种载体上的Cu几乎全部以零价态存在．X射线增宽法测定表明随着Cu含量增加Cu颗粒增大．Cu催化剂在CO加氢中的催化活性与载体、Cu颗粒大小和Cu价态有关．Cr2O3对Cu催化活性有促进效应．Cr2O3负载Cu催化剂活性随Cu颗粒减小而增大，而SiO2作载体时，颗粒大小对活性无影响，零价Cu0为催化活性中心     

合成醇Cu—Co催化剂中第Ⅲ组分对其催化性能的影响

在一般金属催化剂上,由CO和H_2选择合成高级醇是合成气化学的重要研究方向。IFP在1982年提出的Cu-Co催化剂至今还是重要的体系,对合成C_2醇有较好的选择性,但这类催化剂存在热稳定性差、活性低的缺点,为改善催化剂的性质需添加热稳定性高的载体和助剂。有关Cu-Co催化剂体系的研究已有不少报道,但加入第Ⅲ组分对其性质的影     

溶剂化金属原子浸渍法制备高分散负载型催化剂——ⅩⅣ.Pd催化剂的表面组成及CO_2甲烷化催化性能

用元素分析、热脱附和H_2还原脱附等方法分析了Pd/γ-Al_2O_3、Pd/MgO、Pd/TiO_2溶剂化金属原子浸渍(SMAI)催化剂的表面组成和孔结构。结果表明Pd颗粒表面覆盖着一些有机碎片,这些碎片主要由C_1和少量C_2,C_3及C_3以上物种组成。SMAI催化剂的比表面积均高于相应纯载体的比表面积。而平均孔径均小于后者,CO_2甲烷化反应中,SMAI催化剂的活性均高于相应的普通浸渍法(CI)催化剂,而活化能却低于后者。在SMAI催化剂上CO_2甲烷化反应机理与Solymosi机理相同。     

焙烧条件对金催化剂的结构及其催化CO氧化性能的影响

采用共沉淀法和金属有机配合物固载法,分别制备了负载型金催化剂,并考察了焙烧条件对其催化CO氧化性能的影响。实验结果表明,焙烧温度和时间对催化剂的结构和活性的影响显著,不同的金属氧化物负载的金催化剂具有不同的最佳焙烧温度。DTA-TG分析结果确定了催化剂稳定结构的形成温度;XRD测试结果显示,在最佳焙烧条件下得到的催化剂,其载体为具有一定结晶度的金属氧化物。     

Hydrocarbon Molecular Weight Distribution and Mechanism of the Fischer — Tropsch Synthesis on Cobalt Catalysts

We have carried out a quantitative analysis of the molecular weight distribution of hydrocarbons formed at different pressures. We have shown that a change in the distribution of hydrocarbons formed at elevated pressures occurs as a result of a change in the ratio between the rates of the individual reactions with preservation of the mechanism as a whole, while the difference between the distributions obtained at high and low pressures is explained by a change in mechanism for secondary reactions.__________Translated from Teoreticheskaya i Eksperimental’naya Khimiya, Vol. 41, No. 2, pp. 115–120, March–April, 2005.     

BaO对Pd/Al2O3催化性能的影响

以 Pd(C2 H3O2 ) 2 为前身 ,制备了系列 Ba O- Al2 O3复合氧化物负载钯的催化剂 .用质量滴定法 ,测定了复合载体的零电荷点 (pzc) .结果表明 ,体系的 pzc随 Ba O含量的增加而增大 ,在 5 %～ 10 %之间存在一拐点 ,并与XRD所测 Ba O在 Al2 O3上的单层分散阈值相对应 .复合载体在制备中发生固相反应 ,所生成的 Ba Al2 O4可以阻止 Al2 O3的相变 ,并极大地提高载体的热稳定性 ,其中 5 % Ba O的作用最为明显 .Ba O的引入 ,增强了 Pd/Al2 O3对 CO的氧化能力 ,同时 ,提高了其热稳定性     

酸化膨润土负载金催化剂用于CO氧化

用盐酸和硫酸对膨润土（Ben）进行改性处理,采用浸渍法（IMP）、沉积-沉淀法（DP）和阳离子吸附法(CA)制备改性膨润土负载的金催化剂,以CO氧化作为探针反应对催化剂的催化性能进行了研究,采用BET、XRD、TEM和TPD等对催化剂进行表征。 结果表明,经过简单的酸处理后的膨润土比表面积和孔体积有了大幅度的提高,硫酸酸化的膨润土作为载体较之盐酸酸化土更容易得到活性较高的金催化剂,XRD粒径计算结果和TEM观察结果证明,硫酸酸化的膨润土作为载体相比盐酸酸化土可以得到Au颗粒度更小的催化剂。 不同制备方法中,阳离子吸附法能较好的将Au负载于膨润土载体上,得到小颗粒的金催化剂,且在吸附48 h、450 ℃焙烧、150 ℃下H2还原的预处理条件下得到的催化剂活性最好。     

Co/Fe催化剂乙醇裂解和部分氧化制氢研究

采用共沉淀法制备的Co/Fe催化剂催化乙醇裂解和部分氧化制氢反应，考察了反应温度对两种途径反应的影响。结果发现，Co/Fe催化剂对乙醇部分氧化制氢显示出较高的氢选择性，且稳定性较好；该催化剂对乙醇裂解制氢也具有较高的氢选择性，但其稳定性很很差。XRD表征结果表明，在催化乙醇部分氧化反应后，Co70Fe30催化剂中存在CoFe合金和CoO相；而催化乙醇裂解反应后，Co70Fe30催化剂中仅存在CoFe合金，即CoFe合金可能是裂解反应的活性组分。     

CuO/CeO2催化剂的催化氧化性能及其表征

用CO流动反应法 ,程序升温还原 (TPR) ,光电子能谱 (XPS)和X射线衍射Rietveld分析等技术研究了CuO ,CeO2 及CuO/CeO2 各组分催化剂。结果表明 :单组分的CuO和CeO2 对CO的氧化活性较低 ,但CuO与CeO2 形成复合氧化物后 ,其CO氧化活性明显提高 ,这可能与铜物种在CeO2 表面的价态 (Cu2 + 和Cu+ ) ,分散状态和还原性能有关。CuO在CeO2 上的负载量对铜物种在CeO2 表面形成的价态 (Cu2 + 和Cu+ )至关重要 ,CuO的负载量为 1 0 %时 ,XPS检测不到Cu2p3/2 (eV)结合能 ;当CuO的负载量为 5 0 %时 ,CuO主要以Cu2 + 和Cu+ 形式存在 ,而负载量大于 5 0 %时 ,CuO则以Cu2 + 形式存在。由于形成了CuO/CeO2 复合氧化物 ,使离子半径小于Ce4 + 的CuO进入了CeO2 晶格 ;当CuO的负载量达到 5 0 %时 ,CuO的晶粒尺寸值为最小 ( 6 1nm) ,而晶格畸变值为最大 ( 2 86× 10 - 3) ,此时 ,催化剂具有较高的表面能和最佳的CO氧化活性     

Interaction between metallic gold and support and its influence on catalysis

The interaction between gold particles and support in Au/TiO₂ and Au/Al₂O₃ catalysts prepared by immobilizing colloidal gold on the support was evidenced by X-ray photoelectron spectroscopy. The reducibility of the support is more responsible than the interaction between the nanogold particles and support for the activity of catalysts.