Ru系双贵金属催化同时去除碳颗粒和NO_x

用等体积浸渍法制备了一系列Ru系双贵金属催化剂(Ru-M/Zr O2,M为Rh、Ir、Pd、Au、Pt),采用程序升温表面反应(TPSR)技术研究了其催化同时去除碳颗粒和NOx的活性,并考察了含硫含水条件对其活性的影响.结果表明,Ru系双贵金属催化同时去除碳颗粒和NOx的活性受贵金属组合的影响较为明显,Ru-Rh/Zr O2、Ru-Ir/Zr O2和Ru-Pd/Zr O2对碳颗粒和NOx同时去除表现了较高的协同活性,Tpeak低于510℃,η高于35%,其协同催化路径为:Ru催化NO氧化成NO2,Rh、Pd或Ir催化NO2与碳颗粒反应,使碳颗粒迅速氧化,同时NOx迅速还原.含硫含水条件对Ru系双贵金属催化去除碳颗粒具有促进作用,对Ru系双贵金属催化去除NOx具有抑制作用.与其他双贵金属催化剂相比,Ru-Rh/Zr O2和Ru-Ir/Zr O2表现了较强的抗硫抗水性能,而Ru-Pd/Zr O2的抗硫抗水性能最差.     

Pd/WO3-ZrO2催化剂的结构对乙烯直接氧化制乙酸的影响

利用浸渍法制备了一系列具有不同W/Zr比和不同WO3-ZrO2焙烧温度的1%pd/WO3-ZrO2催化剂.通过X射线衍射、N2吸附、氨程序升温吸附、吡啶吸附红外光谱和程序升温还原方法表征了催化剂的晶体结构、表面状态以及酸性.结果表明,制备条件对W和Pd的表面状态具有很人的影响.随着W/Zr比的增加和焙烧温度的提高,催化剂表而的WOx经历了从聚钨酸物种到聚钨酸/WO3晶体共存再到WO3品体颗粒的转化.W/Zr比为0.2且焙烧湍度为1073K的催化剂具有最多的聚钨酸物种,而该催化剂具有最好的活性.因此,聚钨酸物种的最决定了催化剂的活性.Pd的分散状态只依赖于WO3-ZrO2的焙烧温度.Pd物种分散性好,则乙酸选择性高,而分散性差的人颗粒Pd会导致乙烯的燃烧反应.     

负载型Pd/TiO2和Pd-Ag/TiO2催化剂的乙炔选择性加氢催化性能

利用程序升温还原(TPR)、X-射线衍射(XRD)、CO吸附-红外光谱(CO-IR)、电子顺磁共振(EPR)和微型催化反应评价等手段, 研究了负载Pd/γ-Al2O3, Pd/TiO2和Pd-Ag/TiO2催化剂的结构和乙炔选择性加氢催化性能. 结果表明, Pd/TiO2催化剂具有较Pd/γ-Al2O3催化剂更优良的乙炔选择性加氢催化性能, 这与Pd-TiO2之间的强相互作用密切相关. Pd-TiO2之间的强相互作用不仅使负载型钯金属催化剂具有较高的乙炔加氢催化选择性, 而且具有较高的乙炔加氢催化活性. Pd/TiO2催化剂中添加Ag 组分后, Pd金属可促进Ag+的还原并可能形成Pd-Ag合金, 催化剂的乙烯选择性虽有所增加, 但乙炔转化率和乙烯收率下降.     

制备过程对 Pd-SiW12/SiO2 催化剂在乙烯选择氧化制乙酸反应中催化性能的影响

 采用不同负载顺序或制备过程制备了 Pd-SiW12/SiO2 催化剂, 考察了它们在乙烯直接氧化制乙酸反应中的催化性能. 结果表明, Pd 和 SiW12 的负载顺序与 Pd 负载后的处理条件对 Pd-SiW12/SiO2 催化剂上 Pd 的分散度影响较大, 但对催化剂表面 B 酸量影响不大, 而 Pd 分散度较高时, 相应催化剂活性较高. 将 Pd 和 SiW12 同时负载于 SiO2 上时, 催化剂表现出较高的催化乙烯直接氧化制乙酸反应活性.     

添加WO3提高铈锆固溶体的氨选择性催化还原NOx反应活性

采用程序升温氨脱附、程序升温还原和X射线光电子能谱分析手段表征了加入WO3前后CeO2-ZrO2颗粒催化剂的表面性能变化.结果表明,WO3一方面增加了催化剂的酸性,另一方面略微提高了催化剂的氧化还原性能.在氨选择性催化还原氮氧化物反应中,当NH3/NO=1,空速为90000h-1的条件下,CeO2-ZrO2催化剂上氮氧化物转化率低于65%,而10%WO3/CeO2-ZrO2催化剂催化活性大于80%,所对应的温度区间为220～420℃.通入10%CO2和10%H2O后,由于竞争吸附,CeO2-ZrO2催化剂上的氮氧化物转化率低于46%,而10%WO3/CeO2-ZrO2催化剂上的氮氧化物转化率大于80%的温度区间移至230～500℃.     

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%.     

二甲醚部分氧化重整制氢中的部分氧化催化剂的考察

采用浸渍法制备了一系列负载型贵金属催化剂,与Ni/Al2O3构成双床层催化剂,在连续流动固定床反应器中,进行了二甲醚(DME)部分氧化重整制氢的研究,系统地考察了贵金属类型及其负载量、载体以及还原温度与反应温度的影响.结果表明,Pd/Al2O3催化性能不及Pt/Al2O3和Rh/Al2O3,而Pt/Al2O3和Rh/Al2O3催化性能相当,考虑到价格因素,选择了Pt/Al2O3作为本反应催化剂.对Pt负载量的考察表明,0.5%Pt/Al2O3催化性能最佳,且Al2O3又比MgO和ZrO2更适合作载体.通过对工艺条件的考察,确定适当的还原温度与反应温度均为700℃.在上述最佳催化剂与反应条件下,DME转化率保持在100%,H2收率可达80%.     

添加贵金属的Ni/α-Al2O3催化剂甲烷部分氧化制合成气的研究

甲烷部分氧化制合成气因其高空速、高转化率、低H2/CO比而引起人们的重视[1～5].本文研究了在Ni/α-Al2O3催化剂中添加的Rh、Ru、Pt和Pd等贵金属在甲烷部分氧化制合成气反应中的催化作用,重点研究了添加Pt对Ni/α-Al2O3催化剂反应性能的影响.     

负载型Pd/SBA-15催化剂的双烯选择性加氢催化性能

用微型反应器评价体系结合程序升温还原CO、化学吸附、BET比表面积测试和高分辨率透射电子显微镜等多种表征方法研究了负载型Pd/SBA-15催化剂的长链正构双烯选择性加氢的催化性能.结果表明,与Pd/-γAl2O3工业催化剂相比,Pd/SBA-15催化剂双烯选择性加氢的催化性能更优良,且Pd/SBA-15催化剂双烯选择性加氢催化性能与Pd负载量密切相关.随Pd负载量增加,Pd/SBA-15催化剂的金属分散度和长链正构双烯加氢选择性急剧下降.     

不同表面修饰石墨烯载Pd催化剂对甲酸氧化的电催化性能

采用对氨基苯磺酸对氧化石墨烯（GO）进行表面功能化,进而负载贵金属Pd,解决了Pd团聚和不易在载体表面负载的问题,从而提高了Pd基催化剂对于甲酸的催化能力。 实验研究了相同实验条件下,Pd在氧化石墨烯、还原石墨烯（RGO）和磺化处理的石墨烯（SGO）表面的分散和负载量以及得到的复合催化剂的催化性能。 实验结果表明,SGO更容易负载贵金属,得到的催化剂对O2气的电催化还原能力优于Pd/GO和Pd/RGO,此外Pd/SGO催化剂对CO的耐受力也明显提升,这可能是苯环上的π-π键和-SO3H的范德华力协同作用更有利于Pd的固定与分散。 对Pd/SGO催化氧还原的机理也进行了分析,该氧还原为2电子反应过程。     

Effect of Structure of Pd/WO3-ZrO2 Catalyst on Its Activity for Direct Oxidation of Ethylene to Acetic Acid

A series of 1%Pd/WO₃-ZrO₂ catalysts with different W/Zr ratios and calcination temperatures of WO₃-ZrO₂ were prepared by an impregnation method. Their crystal structure, surface state, and acidity were determined using X-ray diffraction, N₂ adsorption, NH₃ temperature-programmed desorption, pyridine infrared spectroscopy, and temperature-programmed reduction. Special attention was paid to the surface states of tungsten and palladium under different preparation conditions. The results revealed that WO_x surface species underwent a transformation from polytungstate species to coexistent polytungstate/crystalline WO₃ and further to crystalline WO₃ particles with increase of W/Zr ratio and calcination temperature. The W/Zr = 0.2 sample calcined at 1 073 K showed the maximum amount of polytungstates, which were responsible for the excellent activity. Moreover, the state of palladium was only dependent on the calcination temperature. Well-dispersed Pd species were responsible for high selectivity to acetic acid, and large metallic Pd particles were favorable for ethylene combustion.     

Preparation of Pd/C catalyst for formic acid oxidation using a novel colloid method

A novel colloid method using (WO₃)_n·xH₂O as colloidal source was developed to prepare Pd/C catalyst for formic acid oxidation. Transmission electron microscopy image shows that the Pd/C nanoparticles have an average size of 3.3 nm and a narrow size distribution. Electrochemical measurements indicate that the Pd/C catalyst exhibits significantly high electrochemical active surface area and high catalytic activity with good stability for formic acid oxidation compared with that prepared by common method. The colloid method is very simple and has great potentials for mass-producing Pd/C and others noble metal catalysts.     

Selective photocatalytic oxidation of alcohols to aldehydes in water by TiO2 partially coated with WO3

Semiconductor TiO₂ particles loaded with WO₃ (WO₃/TiO₂), synthesized by impregnation of tungstic acid followed by calcination, were used for photocatalytic oxidation of alcohols in water with molecular oxygen under irradiation at λ>350 nm. The WO₃/TiO₂ catalysts promote selective oxidation of alcohols to aldehydes and show higher catalytic activity than pure TiO₂. In particular, a catalyst loading 7.6 wt % WO₃ led to higher aldehyde selectivity than previously reported photocatalytic systems. The high aldehyde selectivity arises because subsequent photocatalytic decomposition of the formed aldehyde is suppressed on the catalyst. The TiO₂ surface of the catalyst, which is active for oxidation, is partially coated by the WO₃ layer, which leads to a decrease in the amount of formed aldehyde adsorbed on the TiO₂ surface. This suppresses subsequent decomposition of the aldehyde on the TiO₂ surface and results in high aldehyde selectivity. The WO₃/TiO₂ catalyst can selectively oxidize various aromatic alcohols and is reusable without loss of catalytic activity or selectivity.     

Oxidation of ethanol on carbon-supported oxide-rich Pd–W bimetallic nanoparticles in alkaline media

Carbon-supported oxide-rich Pd–W bimetallic nanoparticles were prepared by chemical reduction methods. The existence of oxides in the electrocatalysts is confirmed by X-ray photoelectron spectrum (XPS) and high resolution transmission electron microscopy. XPS analysis indicates that the oxygen atoms account for about 50% of all the atoms in Pd–W bimetallic nanoparticles. Compared to Pd/C catalyst, the carbon-supported oxide-rich Pd–W bimetallic nanoparticles exhibit a better catalytic activity for the anode oxidation of ethanol in alkaline media. The onset potential of the as prepared oxide-rich Pd_0.8W_0.2/C catalyst (Pd: W = 8: 2, metal atom ratio) for ethanol oxidation is negative shifted about 90 mV comparing to Pd/C catalyst. The oxide-rich Pd–W/C electrocatalysts provide a new model of noble-metal/promoter system as an extreme case of making the promoter (WO₃) closely adjacent to the noble metal (Pd) by fabricating nanoparticles containing both atom-clusters of oxides and the noble metal atoms.

     

The influence of hydrogen-containing molybdenum and tungsten bronzes on the catalytic activity of palladium composite catalysts for the oxidation of H<Subscript>2</Subscript>, CO,and CH<Subscript>4</Subscript>

The influence of hydrogen-containing molybdenum and tungsten bronzes on the catalytic activity of palladium composite catalysts for the oxidation of H₂, CO, and CH₄ was studied. It was found that the composite catalysts containing H _x MO₃ phases (M = W or Mo), which were formed by the reduction of MoO₃ and WO₃ oxides with hydrogen in the presence of deposited Pd, showed higher catalytic activity in the oxidation of small molecules (H₂, CO, and CH₄) with excess oxygen than the traditional Pd/Al₂O₃ deposited catalyst with the same content of the deposited metal. It was shown that the thermal stability of the H _x MO₃ phases was the limiting factor influencing the activity of these composite catalysts.     

WO3/C hybrid material as a highly active catalyst support for formic acid electrooxidation

The hybrid material based on WO₃ and Vulcan XC-72R carbon has been used as the support of Pd nanocatalysts. The resultant Pd–WO₃/C catalysts in a large range of WO₃ content exhibit excellent catalytic activity and stability for formic acid electrooxidation. The great improvement in the catalytic performance is attributed to the uniform dispersion of Pd with less particle sizes on the WO₃/C support and the hydrogen spillover effect which greatly accelerates the dehydrogenation of HCOOH on Pd.     

Noble metal loaded zeolites for the catalytic oxidation of chlorinated hydrocarbons

Summary A series of metal loaded zeolite catalysts (Pd/H-ZSM-5, Pd/H-BETA, Pt/H-ZSM-5, and Pt/H-BETA) were investigated for their activity and selectivity during oxidation of different chlorinated hydrocarbons, namely dichloromethane and trichloroethylene, at constant gas space velocity (15,000 h^-1) and constant chlorohydrocarbon concentration (1,000 ppm in dry air). It was observed that the two noble metals played a major role in influencing the catalytic performance for complete oxidation of both chlorinated compounds. The acidic properties of the zeolite support in combination with increased oxygen activation owing to the noble metal were responsible for the high chlorocarbon destruction activity exhibited by this type of catalysts.     

合成方法对Rh/CeO2-ZrO2-La2O3催化剂的结构、表面性能及DeNOx活性的影响

用沉积沉淀法合成两种不同系列的CeO2-ZrO2-La2O3混合氧化物(ZrO2和La2O3沉积CeO2粒子(标记为A-x)以及CeO2和La2O3沉积ZrO2粒子(标记为B-x)),并用作Rh催化剂的载体。XRD、拉曼、TPR、XPS和O2脉冲等表征结果显示出不同的沉积顺序将导致不同的结构和氧化还原性能,且B-x具有更高的氧迁移性、储氧能力和表面Ce浓度。当其负载Rh后,Rh/B-x催化剂具有更高的NO和CO转化率及N2选择性,且Ce的最佳含量为50at%。这可能归因于Rh负载于富铈表面形成更多有利于NO分解的表面Ce3+活性位。     

Effect of Pt,Pd, and Cs<Superscript>+</Superscript> Additives on the Surface State and Catalytic Activity of WO<Subscript>3</Subscript> in Oxidation of Hydrogen

We have shown that additions of Pt(Pd) and Cs⁺ to WO₃ significantly increase its specific surface area and catalytic activity in H₂ oxidation. After reduction, the promoted specimens contain the phases WO₃, WO_2.9, H_xWO₃; and in the case of Cs⁺ additions, Cs_xWO₃. According to X-ray photoelectron spectroscopy (XPS), the Pt and Pd have an oxidation state close to 0, while tungsten has a +5 oxidation state. The W:O ratio indicates the content of oxygen vacancies in the surface layer. The data are explained taking into account hydrogen spillover from Pt(Pd) to the support.__________Translated from Teoreticheskaya i Eksperimental’naya Khimiya, Vol. 41, No. 2, pp. 126–129, March– April, 2005.