负载Pt,Pd催化剂上NO—TPD和NO催化还原性能

负载Ｐｔ、Ｐｄ催化剂上ＮＯ－ＴＰＤ和ＮＯ催化还原性能１）钟依均（浙江师范大学化学系金华３２１００４）罗孟飞周碧袁贤鑫（杭州大学催化研究所杭州３１００２８）关键词负载Ｐｔ、Ｐｄ催化剂ＮＯ－ＴＰＤＣＯ－ＮＯ反应分类号Ｏ６４３．３２氮氧化物（ＮＯｘ）污染是...     

Pt／Al_2O_3，Pd／Al_2O_3催化剂上CO氧化与表面氧脱出－恢复性能

Ｐｔ／Ａｌ_２Ｏ_３，Ｐｄ／Ａｌ_２Ｏ_３催化剂上ＣＯ氧化与表面氧脱出－恢复性能周仁贤，郑小明（杭州大学催化研究所，杭州３１００２８）关键词铂，钯，氧化铝，氧化锆，负载型催化剂，一氧化碳，氧化，氧脱附ＡＩ。Ｏ。负载的贵金属（Ｐｔ，Ｐｄ或Ｒｈ等）催化剂对有...     

分子筛笼内铂羰基簇合物在CO＋NO反应中的催化研究

研究了ＮａＹ分子筛超笼内包容的Ｐｔ羰基簇合物催化剂在ＣＯ＋ＮＯ反应中的催化性能。「Ｐｔ１２（ＣＯ）２４」＾２－／ＮａＹ和「Ｐｔ９（ＣＯ）１３」＾２－／ＮａＹ在此反应中表现出比较高的活性。Ｎ２Ｏ被认为是ＣＯ＋ＮＯ反应的中间产物，同时笼内羰基簇合物还表现了比ＳｉＯ２负载的簇合物好的热稳定性，动力学研究表明，在「Ｐｔ１２（ＣＯ）２４」＾２－／ＮａＹ上，ＮＯ被还原和Ｎ２Ｏ生成的反应级数，相对于ＣＯ分压为小     

水滑石焙烧产物Mg（Al）O为载体的Pt催化剂的正己烷临氢反应性能

制备了以水滑石焙烧产物－Ｍｇ－Ａｌ复合氧化物为载体的Ｐｔ催化剂，并考察了它在氢存在下的烃类转化反应性能，表明此类催化剂具有比一般的Ｐｔ／Ａｌ２Ｏ３更好的正己烷脱氢环化和异构化反应活性和选择性，更低的氢解反应活性。分别制备了以Ｈ２ＰｔＣｌ６、Ｐｔ（ＮＨ３）４（ＯＨ）２和Ｐｔ（ＮＨ３）４Ｃｌ２为浸渍剂的催化剂，其中以用Ｐｔ（ＮＨ３）４Ｃｌ２和Ｐｔ（ＮＨ３）４（ＯＨ）２制备的催化剂的脱氢环化反应和异构化     

Dy对Pt－Dy／Al_2O_3催化剂表面吸附中心性质及其催化性能的影响

通过脉冲微型反应催化色谱装置，考察了正己烷在Ｐｔ／Ａｌ２Ｏ３和Ｐｔ－Ｄｙ／Ａｌ２Ｏ３催化剂上的转化反应；用ＴＰＤ、ＴＰＲ和ＨＯＴ技术研究了Ｐｔ－Ｄｙ／Ａｌ２Ｏ３催化剂的表面性质．结果表明，Ｄｙ和Ｐｔ之间存在相互作用，并发生电子效应和几何效应，但Ｄｙ的掺入未改变Ｐｔ／Ａｌ２Ｏ３催化剂表面固有的吸附中心性质     

甲烷部分氧化制合成气反应Pt/Al_2O_3和Pt/CeO2/Al_2O_3催化剂的研究(英文)

研究了Ｐｔ／Ａｌ２Ｏ３和Ｐｔ／ＣｅＯ２／Ａｌ２Ｏ３催化剂对甲烷部分氧化制合成气反应的催化活性，发现Ｐｔ／ＣｅＯ２／Ａｌ２Ｏ３显示了比Ｐｔ／Ａｌ２Ｏ３更高的甲烷转化率和合成气选择性。用Ｈ２ＴＰＲ，Ｈ２ＴＰＤ，ＳＥＭ和ＸＲＤ等手段和技术对催化剂进行了表征。ＣｅＯ２与Ｐｔ之间存在较强的相互作用（ＳＭＳＩ），这种作用促进了Ｐｔ在催化剂表面的分散，抑制了Ｐｔ在催化剂表面的迁移，大大降低了催化剂在反应中的完全燃烧活性，提高了催化剂的部分氧化活性和选择性，避免了因催化剂床层局部温度过高而导致催化剂活性下降或失活，提高了催化剂的稳定性。同时，在反应过程中，ＣｅＯ２通过促进水蒸气变换反应（ＷＧＳＲ）的进行使反应体系迅速达到平衡，提高了催化剂对Ｈ２的选择性。     

Dy对Pt—Dy／Al2O3催化剂表面吸附中心性质及其催化性能的影响

通过脉冲微型反应催化色谱装置，考察了正己烷在Ｐｔ／Ａｌ２Ｏ３和Ｐｔ－Ｄｙ／Ａｌ２Ｏ３催化剂上的转化反应：用ＴＰＤ、ＴＰＲ和ＨＯＴ技术研究了Ｐｔ－Ｄｙ／Ａｌ２Ｏ３催化剂的表面性质。     

金属羰基络合物制备的Pt-Re/Al2O3催化剂的性能Ⅰ.不同方法制备的Pt-Re/Al2O3催化剂上正庚烷的转化

考察了由［Ｐｔ３（ＣＯ）６］５［ＮＥｔ４］２与Ｒｅ２（ＣＯ）１０共浸或分浸制备的一系列催化剂在接近工业运转的压力下的正庚烷转化反应。以羰基金属原子簇化合物作为前身物制备的Ｐｔ－Ｒｅ／Ａｌ２Ｏ３催化剂的活性、芳构化选择性和稳定性等明显地优于常规的以Ｈ２ＰｔＣｌ６与ＨＲｅＯ４溶液共浸制备的催化剂。常规Ｐｔ－Ｒｅ／Ａｌ２Ｏ３催化剂的活性和稳定性比Ｐｔ／Ａｌ２Ｏ３好，但芳构化选择性降低，若引入Ｒｅ２（ＣＯ     

甲基环戊烷在铂催化剂上氢解的动力学研究

研究了甲基环戊烷在负载型铂催化剂上的氢解动力学，建立了新的动力学模型，在Ｐｔ／ＳｉＯ２上，两个平行反应（一个生成正己烷，另一个生成甲基戊烷）在甲基环戊烷吸附脱氢过程中存在显著的焓变差异，而Ｃ－Ｃ键断裂活化能则相近，在Ａｌ２Ｏ３负载铂催化剂上，反应的表现活经能仅是在Ｐｔ／ＳｉＯ２上的一半，这是由于Ｃｌ离子的存在，改变了铂的催化性能，导致缺电子铂颗粒的形成，使反应速率的控制步骤从在Ｐｔ／ＳｉＯ２上的Ｃ     

铁助剂对Pd／Al2O3催化剂抗硫性能的影响

借助ＣＯ探针分子原位红外（ｉｎ－ｓｉｔｕＩＲ）、ＴＥＭ（ＥＤＳ）、ＸＰＳ和ＸＲＤ对一系列Ｐｄ－Ｆｅ／Ａｌ_２Ｏ_３、Ｐｄ－Ｐｔ／Ａｌ_２Ｏ_３和Ｐｄ（或Ｐｔ）／Ａｌ_２Ｏ_３模型催化剂进行了表征，结果表明，硫在中毒Ｐｄ（或Ｐｔ）／Ａｌ_２Ｏ_３时，毒物Ｈ_２Ｓ优先吸附于催化剂的多位活性中心上，主要以电子效应影响催化剂的活性．铁的引入，提高了活性组分Ｐｄ的分散度，多位活性中心的减少不利于Ｈ_２Ｓ在催化剂上的吸附；Ｐｄ－Ｆｅ协同作用的结果，增强了催化剂对吸附Ｓ~（２－）氧化成毒性较小的Ｓ~（６＋）或可逸出系统的ＳＯ_２的能力，从而明显地提高了催化剂的抗硫中毒能力．     

Pt/HM,Pd/HM催化剂上NO-TPSR和CO-NO反应

消除NO对大气的污染，人们进行了广泛的研究，其中选择性催化还原是常用的方法[1]．众所周知，分子筛是常用的NO选择性还原催化剂载体，熊金保等[2]考察了Cu-ZSM-5催化剂表面NO的程脱产物，认为NO只吸附在Cu上，载体ZSM-5不吸附NO，Alvarez等[3]认为Na－ZSM-5和NaY表面有少量吸     

Cyclohexene Reactivity Using Catalysts Containing Pt,Re and PtRe Supported on Na‐ and H‐Mordenite

The reactivity of cyclohexene (CHE) over catalysts containing 0.3 wt% Pt, 0.3 wt% Re or 0.3 wt% Pt + 0.3 wt% Re supported on Na‐ and H‐mordenite has been studied in an atmospheric flow‐type reactor at a temperature range of 100–400 °C, using a flow of hydrogen (20 cm³/min). The catalysts were characterized for acid sites strength‐distribution, using desorption of ammonia in DSC. The acidity of H‐mordenite (HM) is attributed to strong acid sites, whereas the acidity of Na‐mordenite (NaM) is due to weak acid sites which are not involved in the catalytic reaction under study. The catalysts containing HM enhance the reactivity of CHE for isomorization reactions. However, the reactivity of CHE on NaM catalysts enhances only the hydrogenation and dehydrogenation reactions. Pt/HM is the most selective catalyst for isomerization of CHE, whereas Pt/NaM and PtRe/NaM catalysts are the most selective for hydrogenation and dehydrogenation reactions, respectively. The hydroisomorization of CHE seems to depend only on the acidity of the catalysts, whereas both hydrogenation and dehydrogenation reactions were controlled by metallic function of the catalysts.     

氢钼青铜对铂催化氧还原反应的促进作用

采用循环伏安法在玻碳电极上和硫酸溶液中电沉积制备出铂催化剂(Pt)及铂-氢钼青铜复合催化剂(Pt-HxMoO3), 用旋转圆盘电极研究并比较了它们对硫酸溶液中氧还原反应的催化活性. 研究结果表明, HxMoO3能明显地提高Pt对氧还原反应的电催化活性. 通过对静态电极上氧还原的峰电流与扫描速度的关系以及旋转圆盘电极上氧还原电流与旋转速度的关系的分析发现, HxMoO3提高了铂电极氧还原反应电荷传递步骤的传递系数, 因此加快了氧还原的动力学过程.     

中温镍水蒸汽转化催化剂积碳动力学与机理研究

研究了833-948K和常压下, C7H16在镍催化剂上进行水蒸汽转化过程中的积碳反应动力学, 获得了相应的动力学方程。并探讨了相应的反应机理, 提出在镍表面同时进行的水蒸汽转化和积碳反应是两个相对独立的反应。指出在较高温度下, 水蒸汽会从简单非解离吸附转变为解离吸附, 这一变化不仅改变了反应级数, 更重要的是它提高了水蒸汽参与表面反应的能力, 特别是加强了氢对积碳反应的作用; 同时庚烷的吸附热也随之产生相当大变化。分析了出现在本温度区内积碳反应负表观活化能的来源。     

光催化降解丙酮的原位红外研究

对催化剂.Pt/V2O5/MgF2在反应温度为120～150℃之间进行了光催化降解丙酮的研究,研究在可见光下进行,发现反应温度对光催化反应有明显的影响.在排除热反应的情况下,温度升高能加速丙酮的光催化反应.丙酮的光催化反应是从它的甲基上开始的,可能先生成了CH3COCH2O-吸附物,它进一步被氧化成丙酮醛、丙酮酸以及碳二醛、乙酸和碳一吸附物种,最终氧化成CO2和水.在没有光和较低的反应温度下,有CO生成,但是在可见光的照射下CO被迅速转化成CO2.研究表明,V2O5/MgF2与Pt/V2O5/MgF2为可见光条件下具备活性的光催化剂.     

Catalysis by Using TiO2 Nanoparticles and Nanotubes

TiO2 has attracted considerable attention due to its stability, non-toxicity, low cost, and great potential for use as a photocatalyst in environmental applications. Since strong metal-support interaction (SMSI) of titania-supported noble metals was first reported in 1978, titania supported catalyst has been intensively studied in heterogeneous catalysis. However, the effective catalytic activity was restricted due to the low surface area of TiO2. Recently, TiO2-based nanotubes were extensively investigated because of their potentials in many areas such as highly efficient photocatalysis and hydrogen sensor.In the present study, formation of titanium oxide (TiO2) nanotubes was carried out by hydrothermal method, with TiO2 nanoparticle-powders immersed in concentrated NaOH solution in an autoclave at 110 ℃. Preparation of nano-size Pt on TiO2-nanoparticles or TiO2-nanotubes was performed by photochemical deposition method with UV irradiation on an aqueous solution containing TiO2 and hexachloroplatinic acid or tetrachloroauric acid. The TEM micrographs show that TiO2-nanotubes exhibit ～300 nm in length with an inner diameter of ～ 6 nm and the wall thickness of ～ 2 nm, and homogeneous nanosize Pt particles (～ 2 nm) were well-dispersed on both nanoparticle- and nanotube- titania supports. It also shows the nanotube morphology was retained up2o n Pt-immobilization. Nitrogen adsorption isotherm at 77K resulted a high surface area (～ 200m/g) of TiO2-nanotubes, which is about 40 times greater than that of "mother" TiO2 nanoparticles (～5 m/g). All the spectroscopic results exhibited that the nanotube structure was not significantly affected by the immobilized Pt particles. Ti K-edge XANES spectra of TiO2 nanotube and Pt/TiO2-nanotube represent that most titanium are in a tetrahedral coordination with few retained in the octahedral structure.In the in-situ FT-IR experiments, an IR cell was evacuated to a pressure of 10-5 torr at room temperature as soon as the catalyst-pellet, Pt/TiO2 or Pt/TiO2-nanotube, was placed inside the cell.Then, 60 torr of hydrogen was introduced into the cell and subsequently the temperature was programmed to increase from room temperature to 300℃ at a constant heating rate of 5℃/min.For Pt/TiO2, an IR peak at 2083 em-1 started to appear at 200℃ with a maximum intensity at 250℃ and then decreasing as temperature increased. The 2083 em-1 IR peak corresponds to the linearly adsorption of CO on the well-dispersed Pt sites. Simultaneously, the IR bands of gaseous methane at 3016 em-1 started to appear at 225℃ and the peak intensity increased with temperature. The results reveal that Pt/TiO2 can adsorb gaseous CO2 and further catalyzes the reduction of CO2 by H2 through the intermediate CO, which further produces gaseous methane. While for the Pt/TiO2-nanotube catalyst, methane was produced at relatively low temperature, 100℃, and it catalyzed the direct conversion of CO2 to CH4. The absence of intermediate CO-adsorption signals durinng the temperature programmed process indicates that the prepared TiO2 nanotube-supported nanosize Pt possesses a potent capability for CO2 adsorption and highly catalytic activity in the hydrogenation of CO2, and was superior to the conventional Pt/TiO2 catalyst. The catalytic activity of Pt/TiO2-nanotube was indeed significantly enhanced by the high surface area of TiO2-nanotubes.Details will be discussed.     

浆态床二甲醚合成中V2O5、Sm2O3对脱水组分γ-Al2O3的修饰作用

采用等容浸渍法制备改性脱水催化剂,通过H2-TPR、Pyridine-IR、还原态NH3-TPD、XRD等表征手段,以及目标反应浆态床CO+H2合成二甲醚,研究了催化剂的还原性能以及酸中心分布与反应性能之间的关系。H2-TPR结果表明,在脱水催化剂γ-Al2O3、V2O5/γ-Al2O3和Sm2O3/γ-Al2O3上不出现还原峰,V2O5、Sm2O3的加入改善了复合催化剂中Cu的还原性能,促进了甲醇催化剂的还原。Pyridine-IR表明,V2O5和Sm2O3的加入对L酸、B酸的量影响不大。还原态NH3-TPD说明V2O5和Sm2O3的加入改变了酸中心的分布,增加了弱酸中心的比率。XRD结果发现,V2O5和Sm2O3均匀分散在γ-Al2O3上,没有新的物种生成。二甲醚合成目标反应的结果表明,改性后催化剂的反应活性增强,合成反应中CO转化率、二甲醚的选择性都得到提高。V2O5和Sm2O3的添加增加了弱酸中心数量,促进了脱水活性,从而提高了复合催化剂合成二甲醚的活性和选择性。     

Photochemical preparation of poly(N-vinyl-2-pyrrolidone)-stabilized platinum colloids and their deposition on titanium dioxide

Preparation processes for Pt-deposited TiO(2) (Pt/TiO(2)) by the synthesis of Pt nanoparticles and their deposition were pursued by transmission electron microscopy, extended X-ray absorption fine structure, UV-vis spectroscopy, and Fourier transform infrared spectroscopic studies. Colloidal dispersions of Pt particles stabilized by poly(N-vinyl-2-pyrrolidone) (PVP) were photochemically synthesized in aqueous ethanol solution. The average diameter of Pt particles was estimated to be 2.0 +/- 0.5 nm, which was almost unchanged by changing the reducing agent from ethanol to methanol and 2-propanol. The PVP-stabilized Pt particles were distributed over a TiO(2) surface only by mixing the Pt colloidal dispersions and TiO(2). CO was chemically coordinated on the Pt particles on a TiO(2) surface after heat treatment was carried out in an O(2) flow at 673 K to completely remove the residual PVP on Pt/TiO(2). Hydrogen reduction at 473 K did not increase the amount of CO adsorbed on Pt sites. The Pt/TiO(2) catalyst after the oxidation treatment showed higher activity for CO photooxidation than that obtained for pure TiO(2) catalyst. The CO photooxidation rate was not unchanged by the H(2) reduction.     

Study of Hydrogen Adsorption on Pt/WO3-ZrO2 through Pt Sites

The rate determining step and the energy barrier involved in hydrogen adsorption on Pt/WO_3- ZrO_2 were studied based on the assumption that the hydrogen adsorption occurs only through Pt sites. The rate of hydrogen adsorption on Pt/WO_3-ZrO_2 was measured in the adsorption temperature range of 323-573 K and an initial hydrogen pressure of 50 Torr.The rates of hydrogen uptake were very high for the initial few minutes and the adsorption continued for more than 5 h below 523 K.The hydrogen uptake far exceeded the H/Pt ratio of unity for all adsorption temperatures,indicating that the adsorption of hydrogen involved the dissociative adsorption of hydrogen on Pt sites to form hydrogen atoms,the spillover of hydrogen atoms onto the surface of the WO_3-ZrO2 catalyst,the diffusion of spiltover hydrogen atom over the surface of the WO_3-ZrO_2 catalyst,and the formation of protonic acid site originated from hydrogen atom by releasing an electron in which the electron may react with a second hydrogen atom to form a hydride near the Lewis acid site.The rate determining step was the spillover with the activation energy of 12.3 kJ/mol.The rate of hydrogen adsorption cannot be expressed by the rate equation based on the assumption that the rate determining step is the surface diffusion.The activity of Pt/WO_3-ZrO_2 was examined on n-heptane isomerization in which the increase of hydrogen partial pressure provided positive-effect on the conversion of n-heptane and negative-effect on the selectivity towards iso-heptane.     

Effects of pretreatment and reduction on the Co/Al2O3 catalyst for CO hydrogenation

The purpose of this study was to investigate the effect of preadsorbed CO at different temperatures, calcination temperatures, the combined influence of reduction temperature and time, and pretreatment using hydrogen or syngas as reduction agents on the F-T synthesis （FTS） activity and selectivity of Co/Al2O3 catalyst. The reactivity of the carbon species at higher preadsorption temperature with H2 in TPSR decreased, whereas the carbon-containing species showed higher reactivity over Co/Al2O3 catalyst with low calcination temperature. This agreed well with the order of catalytic activity for F-T synthesis on this catalyst. The catalytic activity of the catalyst varied with reduction temperature and time remarkably. CODEX optimization gave an optimum reduction temperature of 756 K and reduction time of 6.2 h and estimated C5＋ yield perfectly. The pretreatment of Co/Al2O3 catalyst with different reduction agents （hydrogen or syngas） showed important influences on the catalytic performance. A high CO conversion and C5＋ yield were obtained on the catalyst reduced by hydrogen, whereas methane selectivity on the catalyst reduced by syngas was much higher than that on the catalyst reduced by hydrogen.