Ni基催化剂催化燃油重整耦合选择性催化还原NOx反应

分别以La₂O₂CO₃, CeO₂, ZrO₂和Al₂O₃为载体, 采用浸渍法制备了Ni基重整催化剂, 并以正十二烷模拟车载燃油进行催化重整反应以同时制备小分子碳氢化合物(HCs)和H₂, 考察了其在4wt%Ag/Al₂O₃上选择性催化还原(HC-SCR)氮氧化物(NO_x)的性能. 采用N₂吸附-脱附、X射线粉末衍射、H₂程序升温还原和热重等手段对Ni基催化剂进行了表征. 结果表明, 随着重整催化剂氧化还原性能增强, 产物中H₂浓度增加, 可参与SCR反应的HCs含量减少, 从而导致重整-SCR耦合体系上NO_x净化活性温度窗口向低温移动, NO_x最高转化率降低. Ni/ZrO₂+Ag/Al₂O₃耦合体系中H₂/HCs符合SCR反应所需的最优比例, 在柴油车典型排气温度范围内表现出良好的NO_x净化能力. 同时, 在Ni/ZrO₂+Ag/Al₂O₃耦合体系上考察了其燃油重整-SCR的活性稳定性. 结果显示, 重整催化剂的耐久性有待进一步提高.     

有序介孔氧化硅膜的制备及结构研究

本文介绍了在α-Al₂O₃中空纤维载体上制备担载有序氧化硅膜的方法。应用LXRD、HRTEM、TG-DTA、SEM、氮气吸附等测试手段对膜的结构、形貌进行了表征。LXRD和HRTEM结果显示所制备的非担载膜具有高度有序的二维六方结构。SEM分析发现担载膜表面完整、无缺陷。气体渗透实验表明中空纤维担载膜具有一定的气体选择性，在0.1 MPa下对H₂/N₂和CH₄/N₂的分离因子分别为2.80和1.65，气体透过膜孔的扩散由努森机制所控制。等温氮气吸附实验显示：500 ℃热处理后非担载膜的比表面积为548.84 m²·g^-1，孔容为0.57 mL·g^-1。     

T型分子筛膜的合成、表征与渗透汽化性能

采用二次生长法,在不锈钢、α-Al₂O₃和莫来石多孔管状支撑体上分别合成了高渗透汽化性能的T型分子筛膜。考察了合成条件如合成时间、n(SiO₂)/n(Al₂O₃)、n(H₂O)/n(Al₂O₃)和硅源等对T型分子筛膜形成和分离性能的影响。通过XRD和SEM表征了膜的晶相和形貌。     

在CeO2-ZrO2中加入La2O3对改善单Pd三效催化剂性能的作用

浸渍法制备了CeO₂-ZrO₂-La₂O₃复合氧化物，用XRD、热分析（TG-DTA，DSC）、BET表面积、H₂-TPR等对合成样品进行表征，研究了La₂O₃的加入对CeO₂-ZrO₂和单钯Pd/CeO₂-ZrO₂/γ-Al₂O₃/蜂窝陶瓷催化剂性能和热稳定性的影响。结果表明，在CeO₂-ZrO₂-La₂O₃中，La的存在能促进CeO₂-ZrO₂固溶体的还原，提高贮氧能力；在Pd/CeO₂-ZrO₂/γ-Al₂O₃中加入La有利于提高催化剂的耐热稳定性，阻止γ-Al₂O₃在高温下的晶相转变，进一步稳定Al₂O₃的结构，保持其高的表面积。在贵金属Pd的负载量为1 g·L^-1的条件下，测定了Pd/CeO₂-ZrO₂-La₂O₃/γ-Al₂O₃/蜂窝陶瓷催化剂对CO、C₃H₈和NOx的三效催化净化活性。结果表明，在Pd/CeO₂-ZrO₂/Al₂O₃/蜂窝陶瓷催化剂中加入La₂O₃后，能明显地改善催化剂的低温活性和三效催化性能，经1 000 ℃老化10 h后，CO、C₃H₈和NO_x净化的起燃温度（T₅₀）分别为330 ℃、350 ℃和380 ℃。     

Pt/MOx(M=Ni,Fe,Co,Ce)催化剂上CO氧化反应中抗H2O与CO2的性能研究

我们研究了4种负载型Pt催化剂（1Pt/NiO、1Pt/FeO_x、1Pt/Co₃O₄和Pt/CeO₂）上不同反应条件下CO氧化活性及抗H₂O和CO₂性能.发现反应气氛中CO₂的加入与CO形成了竞争吸附,并在催化剂表面形成了碳酸盐物种堵塞了活性位,从而导致催化剂失活.反应气氛中H₂O的加入对1Pt/CeO₂催化剂的活性有所抑制,但对1Pt/FeO_x、1Pt/NiO和1Pt/Co₃O₄催化剂的活性却有促进作用.在1Pt/FeO_x和1Pt/CeO₂催化剂上的分步反应实验和动力学研究表明,尽管H₂O的加入在两种催化剂上均与CO形成了竞争吸附,但在1Pt/FeO_x催化剂上H₂O在载体表面解离形成的羟基更易与CO反应,开辟了新的反应途径,从而提高了反应性能.此外,H₂O的加入能有效分解该催化剂上的碳酸盐物种,从而保持了其稳定性.     

Ni对单Pd型挥发性有机废气净化催化剂的助催化作用

本文以蜂窝状堇青石陶瓷为催化剂载体，用分步浸渍法制备了挥发性有机废气(VOCs)净化用Pd-Ni/La-Ce-Zr-Al₂O₃ /堇青石催化剂，考察了Ni助催化剂对单钯型VOCs净化催化剂性能的影响，并用H2-TPR、比表面、XRD、SEM等手段对催化剂进行了表征。研究表明，Ni的加入明显提高了催化剂的低温活性和热稳定性，经过800 ℃焙烧的Pd-Ni/La-Ce-Zr-Al₂O₃ /堇青石(m_Pd∶m_Ni=3∶20)催化剂的催化性能明显优于Pd/La-Ce-Zr-Al2O₃ /堇青石催化剂，甲苯起燃温度下降约25 ℃，经1 000 ℃高温处理后，仍能保持优良的催化性能。Ni的加入使Pd催化剂性能提高的原因应归结于活性组分分散度的提高和钯、镍与载体之间存在的强相互作用。     

K2CO3含量对Ni-Cu-Mn-K/Al2O3水煤气变换催化剂结构和性能的影响

以γ-Al₂O₃为载体，采用等体积浸渍法，制备了不同K₂CO₃含量的Ni-Cu-Mn-K/Al₂O₃水煤气变换催化剂，采用低温N₂吸附、XRD、TPD和TPR，考察了K₂CO₃含量对催化剂结构和性能的影响。结果表明:K₂CO₃的加入使催化剂的还原温度有所提高，适量的K₂CO₃能增加活性组分的电子密度，从而增强其给电子活化CO的能力，提高催化剂的活性。但过量的K₂CO₃使得催化剂比表面积和孔容降低，且导致催化剂对CO吸附过强，催化活性降低。当Ni-Cu-Mn-K/γ-Al₂O₃催化剂中K₂CO₃的添加量为7.5%时，且催化剂经530 ℃耐热15 h后，在350 ℃时水煤气变换反应中CO转化率达62.29%。     

Pt/ZrO2-Al2O3催化剂催化氧化C3H6和CO性能

采用共沉淀法合成了ZrO₂与Al₂O₃的不同质量比的ZrO₂-Al₂O₃复合氧化物,并以此为载体通过等体积浸渍法制备了1.5% Pt/ZrO₂-Al₂O₃（w/w）催化剂。以C₃H₆和CO为反应物的催化性能评价显示,在系列催化剂中以Pt/Zr（0.4）-Al催化剂催化氧化活性最为优异,其C₃H₆和CO的起燃温度（T₅₀）小于125℃,完全转化温度（T₉₀）小于150℃。采用XRD、低温N₂吸附、H₂-TPR、CO脉冲吸附等分析表征技术探索了催化剂物相结构、比表面积、颗粒尺寸等对催化活性的影响规律。结果发现,ZrO₂-Al₂O₃复合氧化物具有Al₂O₃材料的介孔织构和大比表面积特性,且产生了Al_xZr_1-xO_y固溶体新物相。适当的ZrO₂与Al₂O₃的质量比,是改善Pt与ZrO₂-Al₂O₃的相互作用强度,促进贵金属Pt的分散,提升Pt/ZrO₂-Al₂O₃催化剂的低温氧化活性的关键。     

固载Ru基催化剂上二氧化碳加氢合成甲酸的研究(IV): 反应机理

探讨了在CO₂加H₂合成HCOOH过程中原位合成的固载Ru基催化剂的可能结构、CO₂的活化方式以及可能的反应机理. 在反应中, 固载Ru配合物中的一个P配体首先解离, 被质子型溶剂ROH取代而生成循环活性物质, 然后CO₂正插入Ru—H键生成甲酸酯配合物, 之后甲酸酯配合物中的Ru—O₂CH键被H₂氢解生成HCOOH, 而本身重新转化为活性物质, 完成催化循环.     

固载Ru基催化剂上二氧化碳加氢合成甲酸的研究(IV): 反应机理

探讨了在CO₂加H₂合成HCOOH过程中原位合成的固载Ru基催化剂的可能结构、CO₂的活化方式以及可能的反应机理. 在反应中, 固载Ru配合物中的一个P配体首先解离, 被质子型溶剂ROH取代而生成循环活性物质, 然后CO₂正插入Ru—H键生成甲酸酯配合物, 之后甲酸酯配合物中的Ru—O₂CH键被H₂氢解生成HCOOH, 而本身重新转化为活性物质, 完成催化循环.     

Ni/Al2O3 catalysts for CO methanation: Effect of Al2O3 supports calcined at different temperatures

The correlation between phase structures and surface acidity of Al₂O₃ supports calcined at different temperatures and the catalytic performance of Ni/Al₂O₃ catalysts in the production of synthetic natural gas (SNG) via CO methanation was systematically investigated. A series of 10 wt% NiO/Al₂O₃ catalysts were prepared by the conventional impregnation method, and the phase structures and surface acidity of Al₂O₃ supports were adjusted by calcining the commercial γ-Al₂O₃ at different temperatures (600–1200 °C). CO methanation reaction was carried out in the temperature range of 300–600 °C at different weight hourly space velocities (WHSV = 30000 and 120000 mL·g^?1·h^?1) and pressures (0.1 and 3.0 MPa). It was found that high calcination temperature not only led to the growth in Ni particle size, but also weakened the interaction between Ni nanoparticles and Al₂O₃ supports due to the rapid decrease of the specific surface area and acidity of Al₂O₃ supports. Interestingly, Ni catalysts supported on Al₂O₃ calcined at 1200 °C (Ni/Al₂O₃-1200) exhibited the best catalytic activity for CO methanation under different reaction conditions. Lifetime reaction tests also indicated that Ni/Al₂O₃-1200 was the most active and stable catalyst compared with the other three catalysts, whose supports were calcined at lower temperatures (600, 800 and 1000 °C). These findings would therefore be helpful to develop Ni/Al₂O₃ methanation catalyst for SNG production.     

Influence of the Support on the Catalytic Characteristics of the Deposited Palladium in the Liquid-Phase Hydrogenation of Diphenylacetylene

Palladium catalysts on various types of supports were studied in the liquid-phase hydrogenation of diphenylacetylene. Samples of Pd/SiO₂–Al₂O₃, Pd/MgAl₂O₄, Pd/Al₂O₃, and Pd/TiO₂ were characterized by the chemisorption of the CO and IR spectroscopy of adsorbed CO. The use of n-hexane as the solvent increases the reaction rate, which can be explained by the better solubility of hydrogen in the liquid phase. It is established that the acid–base properties of the support do not affect the activity and selectivity of the catalysts in the reaction under study. However, they alter the electronic state of palladium. According to the catalytic tests, Pd/TiO₂ has the highest activity (turnover frequency) and selectivity to alkene. The comparison of the obtained catalytic data and the results of IR spectroscopy made it possible to conclude that this is due to the electron density redistribution between the palladium and TiO _x particles, which is caused by the strong metal–support interaction.     

Pd/Ga<Subscript>2</Subscript>O<Subscript>3</Subscript>–Al<Subscript>2</Subscript>O<Subscript>3</Subscript> catalysts for the selective liquid-phase hydrogenation of acetylene to ethylene

The structure of Ga₂O₃–Al₂O₃ supports and Pd/Ga₂O₃–Al₂O₃ catalysts and the performance of these catalysts in liquid-phase acetylene hydrogenation have been investigated. The deposition of Ga(NO₃)₃ onto Al₂O₃ by impregnation followed by calcination of the impregnated support at 600°C yields γ-Ga₂O₃–Al₂O₃ solid solutions containing up to 50 wt % Ga₂O₃. X-ray diffraction characterization of model palladium catalysts and their temperature-programmed reduction with hydrogen have demonstrated that, while palladium in Pd/Ga₂O₃ is in the form of a Pd₂Ga alloy, in the Pd/γ-Ga₂O₃–Al₂O₃ catalyst there is no direct interaction between PdО and Ga₂O₃ particles and palladium is in the monometallic state. The introduction of 10–20 wt % gallium oxide into Al₂O₃ lowers the activity of the supported palladium catalyst relative to that of the initial Pd/Al₂O₃ but increases the ethylene yield by enhancing the ethylene formation selectivity.     

Development of a Ni–Pd/CeZrO<Subscript>2</Subscript>/Al<Subscript>2</Subscript>O<Subscript>3</Subscript> catalyst for the effective conversion of methane into hydrogen-containing gas

The effects of the Pd content (0–1 wt %) and the synthesis method (joint impregnation with Ni + Pd and Pd/Ni or Ni/Pd sequential impregnation) on the physicochemical and catalytic properties of Ni–Pd/CeZrO₂/Al₂O₃ were studied in order to develop an efficient catalyst for the conversion of methane into hydrogen-containing gas. It was shown that variation in the palladium content and a change in the method used for the introduction of an active constituent into the support matrix make it possible to regulate the redox properties of nickel cations but do not affect the size of NiO particles (14.0 ± 0.5 nm) and the phase composition of the catalyst ((γ + δ)-Al₂O₃, CeZrO₂ solid solution, and NiO). It was established that the activity of Ni–Pd catalysts in the reaction of autothermal methane reforming depends on the method of synthesis and increases in the following order: Ni + Pd < Ni/Pd < Pd/Ni. It was found that, as the Pd content of the Ni–Pd/CeZrO₂/Al₂O₃ catalyst was decreased from 1 to 0.05 wt %, the ability for self-activation, high activity, and operational stability of the catalyst under the conditions of autothermal methane reforming remained unaffected: at 850°C, the yield of hydrogen was ~70% at a methane conversion of ~100% during a 24-h reaction.     

Study of properties of Al2O3 and TiO2 supported palladium catalysts in reactions of tetrachloromethane hydrogenation

Properties of Al₂O₃- and TuO₂-supported palladium catalysts modified with calcium oxide were studied. Catalyst samples 2% Pd/CaO-TiO₂ and 2% Pd/CaO-Al₂O₃ were examined by the methods of temperature-programmed reduction in a flow of hydrogen, temperature-programmed desorption of ammonia and carbon(IV) oxide, and X-ray diffraction analysis.     

CO2 Hydrogenation on Cu/Al2O3: Role of the Metal/Support Interface in Driving Activity and Selectivity of a Bifunctional Catalyst

Selective hydrogenation of CO₂ into methanol is a key sustainable technology, where Cu/Al₂O₃ prepared by surface organometallic chemistry displays high activity towards CO₂ hydrogenation compared to Cu/SiO₂, yielding CH₃OH, dimethyl ether (DME), and CO. CH₃OH formation rate increases due to the metal–oxide interface and involves formate intermediates according to advanced spectroscopy and DFT calculations. Al₂O₃ promotes the subsequent conversion of CH₃OH to DME, showing bifunctional catalysis, but also increases the rate of CO formation. The latter takes place 1) directly by activation of CO₂ at the metal–oxide interface, and 2) indirectly by the conversion of formate surface species and CH₃OH to methyl formate, which is further decomposed into CH₃OH and CO. This study shows how Al₂O₃, a Lewis acidic and non‐reducible support, can promote CO₂ hydrogenation by enabling multiple competitive reaction pathways on the oxide and metal–oxide interface.     

Adsorption-Induced Segregation as a Method for the Target-Oriented Modification of the Surface of a Bimetallic Pd–Ag Catalyst

The effect of palladium segregation was studied which resulted from the effect of CO and O₂ on the surface structure and catalytic characteristics of the Pd–Ag₂/Al₂O₃ catalyst. The IR-spectroscopic study of adsorbed CO showed that Pd₁ centers isolated from each other by silver atoms predominated on the surface of reduced Pd–Ag₂/Al₂O₃, as evidenced by the almost complete absence of absorption bands typical for the multicentred CO adsorption. In the course of catalyst treatment with CO and O₂, the intensity of absorption bands characteristic of the multicenter CO adsorption considerably increased due to the transformation of a portion of monatomic Pd₁ centers into multiatomic Pd_n ones as a result of the surface segregation of Pd. In this case, a substantial increase in the catalyst activity in the liquid-phase hydrogenation of diphenylacetylene was observed. It was established that, after treatment with CO, the catalyst selectivity for the formation of a target olefin (stilbene) remained almost constant, whereas the treatment with O₂ led to a decrease in the selectivity because of more considerable surface modification.     

Thermodynamic possibilities and constraints of pure hydrogen production by a chromium,nickel, and manganese-based chemical looping process at lower temperatures

The reduction of chromium, nickel, and manganese oxides by hydrogen, CO, CH₄, and model syngas (mixtures of CO + H₂ or H₂ + CO + CO₂) and oxidation by water vapor has been studied from the thermodynamic and chemical equilibrium point of view. Attention was concentrated not only on the convenient conditions for reduction of the relevant oxides to metals or lower oxides at temperatures in the range 400–1000 K, but also on the possible formation of soot, carbides, and carbonates as precursors for the carbon monoxide and carbon dioxide formation in the steam oxidation step. Reduction of very stable Cr₂O₃ to metallic Cr by hydrogen or CO at temperatures of 400–1000 K is thermodynamically excluded. Reduction of nickel oxide (NiO) and manganese oxide (Mn₃O₄) by hydrogen or CO at such temperatures is feasible. The oxidation of MnO and Ni by steam and simultaneous production of hydrogen at temperatures between 400 and 1000 K is a difficult step from the thermodynamics viewpoint. Assuming the Ni—NiO system, the formation of nickel aluminum spinel could be used to increase the equilibrium hydrogen yield, thus, enabling the hydrogen production via looping redox process. The equilibrium hydrogen yield under the conditions of steam oxidation of the Ni—NiO system is, however, substantially lower than that for the Fe—Fe₃O₄ system. The system comprising nickel ferrite seems to be unsuitable for cyclic redox processes. Under strongly reducing conditions, at high CO concentrations/partial pressures, formation of nickel carbide (Ni₃C) is thermodynamically favored. Pressurized conditions during the reduction step with CO/CO₂ containing gases enhance the formation of soot and carbon-containing compounds such as carbides and/or carbonates.     

Key Role of a-Top CO on Terrace Sites of Metallic Pd Clusters for CO Oxidation

Pd-based catalysts are the most widely used for CO oxidation because of their outstanding catalytic activity and thermal stability. However, fundamental understanding of the detailed catalytic processes occurring on Pd-based catalysts under realistic conditions is still lacking. In this study, we investigated CO oxidation on metallic Pd clusters supported on Al₂O₃ and SiO₂. High-angle annular dark-field scanning transmission electron microscopy revealed the formation of similar-sized Pd clusters on Al₂O₃ and SiO₂. In contrast, CO chemisorption analysis indicated a gradual change in the dispersion of Pd (from 0.79 to 0.2) on Pd/Al₂O₃ and a marginal change in the dispersion (from 0.4 to 0.24) on Pd/SiO₂ as the Pd loading increased from 0.27 to 5.5 wt %; these changes were attributed to differences in the metal-support interactions. Diffuse reflectance infrared Fourier-transform spectroscopy revealed that fewer a-top CO species were present in Pd supported on Al₂O₃ than those in Pd supported on SiO₂, which is related to the morphological differences in the metallic Pd clusters on these two supports. Despite the different dispersion profiles and surface characteristics of Pd, O₂ titration demonstrated that linearly bound CO (with an infrared signal at 2090 cm⁻¹) reacted first with oxygen in the case of CO-saturated Pd on Al₂O₃ and SiO₂, which suggests that a-top CO on the terrace site plays an important role in CO oxidation. The experimental observations were corroborated by periodic density functional calculations, which confirmed that CO oxidation on the (111) terrace sites is most plausible, both kinetically and thermodynamically, compared to that on the edge or corner sites. This study will deepen the fundamental understanding of the effect of Pd clusters on CO oxidation under reaction conditions.     

Bimetallic Pd—Pt/γ-Al<Subscript>2</Subscript>O<Subscript>3</Subscript> catalysts for complete methane oxidation: the effect of the Pt: Pd ratio

Alumina-supported bimetallic Pt—Pd catalysts proved to be more active in the complete oxidation of methane than monometallic systems (Pt/Al₂O₃, Pd/Al₂O₃). The maximum activity of the bimetallic catalysts was achieved at ~40 at.% Pt in Pd on the catalyst surface. After the oxidation reaction, redistribution of platinum and palladium was observed in the active component of the catalysts with the degree of redistribution depending on the initial Pt: Pd ratio.