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1.
分别以Pd(NO3)2,Pd(NH3)4(NO3)2和H2Pd Cl4为钯前驱体制备了Pd/Ce0.67Zr0.33O2(CZ)催化剂.以硝酸钯为钯前驱体制得的Pd/CZ(NO)催化剂具有较高的储氧量,存在较多的小的钯簇,其钯与载体间相互作用较强,因此在三种新鲜催化剂中对HC和CO的消除表现出了最好的催化活性.以硝酸四氨钯为钯前驱体制得的Pd/CZ(NH)催化剂具有较高的钯分散度,存在较多的大的钯簇,同时存在金属态和氧化态的钯,从而对NO和NO2的消除表现出了较好的催化活性.以氯钯酸为钯前驱体制得的Pd/CZ(Cl)催化剂由于钯分散度较小,钯与载体间作用较弱,存在的CeOCl抑制了氧空穴的生成,因此对各种反应物的催化活性都较低.但Pd/CZ(Cl)催化剂表现出了较好的热稳定性,这是由于老化处理消除了残余的氯物种并且促进了钯与载体间的作用.  相似文献   

2.
Pd/TiO(2) catalysts have been prepared using TiO(2) supports consisting of various rutile/anatase crystalline phase compositions. Increasing percentages of rutile phase in the TiO(2) resulted in a decrease in Brunauer-Emmett-Teller surface areas, fewer Ti(3+) sites, and lower Pd dispersion. While acetylene conversions were found to be merely dependent on Pd dispersion, ethylene selectivity appeared to be strongly affected by the presence of Ti(3+) in the TiO(2) samples. When TiO(2) samples with 0-44% rutile were used, high ethylene selectivities (58-93%) were obtained whereas ethylene losses occurred for those supported on TiO(2) with 85% or 100% rutile phase. X-ray photoelectron spectroscopy and electron spin resonance experiments revealed that a significant amount of Ti(3+) existed in the TiO(2) samples composed of 0-44% rutile. The presence of Ti(3+) in contact with Pd can probably lower the adsorption strength of ethylene resulting in an ethylene gain. Among the five catalysts used in this study, the results for Pd/TiO(2)-R44 suggest an optimum anatase/rutile composition of the TiO(2) used to obtain high selectivity of ethylene in selective acetylene hydrogenation.  相似文献   

3.
Anatase TiO2 nanospindles containing 89% exposed {101} facets (TiO2-101) and nanosheets with 77% exposed {001} facets (TiO2-001) were hydrothermally synthesized and used as supports for Pd catalysts. The effects of the TiO2 materials on the catalytic performance of Pd/TiO2-101 and Pd/TiO2-001 catalysts were investigated in the selective hydrogenation of acetylene to polymer-grade ethylene. The Pd/TiO2-101 catalyst exhibited enhanced performance in terms of acetylene conversion and ethylene yield. To understand these effects, the catalysts were characterized by H2 temperature-programmed desorption (H2-TPD), H2 temperatureprogrammed reduction (H2-TPR), transmission electron microscopy (TEM), pulse CO chemisorption, X-ray photoelectron spectroscopy (XPS), and thermogravimetric analysis (TGA). The TEM and CO chemisorption results confirmed that Pd nanoparticles (NPs) on the TiO2-101 support had a smaller average particle size (1.53 nm) and a higher dispersion (15.95%) than those on the TiO2-001 support (average particle size of 4.36 nm and dispersion of 9.06%). The smaller particle size and higher dispersion of Pd on the Pd/TiO2-101 catalyst provided more reaction active sites, which contributed to the improved catalytic activity of this supported catalyst.  相似文献   

4.
 通过有机物分解碳化处理TiO2 纳米管制得了TiO2C, 并以其为载体制备了Pd/TiO2C电催化剂,考察了该催化剂对碱性介质中乙醇电催化氧化的活性. 结果表明,碳化导电处理的TiO2C纳米管载体能有效改善催化剂中贵金属的分散度和电极结构,从而提高催化剂的电催化活性. 对催化剂活性组分的优化实验表明, Pd/TiO2C质量比为1/1时催化剂的活性最高. 在1 mol/L KOH溶液中Pd载量均为0.3 mg/cm2的条件下, Pd/TiO2C催化剂对乙醇氧化的催化活性是Pd/C催化剂的3.8倍.  相似文献   

5.
在Pd/TiO2上CO的光催化增强效应   总被引:4,自引:0,他引:4  
在Pd(2%)/TiO2上CO催化氧化的研究中发现:室温下, 以黑光灯(λ=365 nm)照时, CO的氧化活性比暗态显著提高,产生了明显的光催化增强效应(两者速率常数比约为15).但在TiO2上,无论暗态还是黑光灯(λ=365 nm)照,均无CO氧化反应发生.这可能是由于氧分子解离吸附时的键能减弱,使Pd表面氧原子(或O-)浓度增加和氧原子的溢流(oxygen spillover)两种效应结合产生的.  相似文献   

6.
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.  相似文献   

7.
To obtain noble metal catalysts with high efficiency, long‐term stability, and poison resistance, Pt and Pd are assembled in highly ordered and vertically aligned TiO2 nanotubes (NTs) by means of the pulsed‐current deposition (PCD) method with assistance of ultrasonication (UC). Here, Pd serves as a dispersant which prevents agglomeration of Pt. Thus Pt–Pd binary catalysts are embed into TiO2 NTs array under UC in sunken patterns of composite spherocrystals (Sps). Owing to this synthesis method and restriction by the NTs, the these catalysts show improved dispersion, more catalytically active sites, and higher surface area. This nanotubular metallic support material with good physical and chemical stability prevents catalyst loss and poisoning. Compared with monometallic Pt and Pd, the sunken‐structured Pt–Pd spherocrystal catalyst exhibits better catalytic activity and poison resistance in electrocatalytic methanol oxidation because of its excellent dispersion. The catalytic current density is enhanced by about 15 and 310 times relative to monometallic Pt and Pd, respectively. The poison resistance of the Pt–Pd catalyst was 1.5 times higher than that of Pt and Pd, and they show high electrochemical stability with a stable current enduring for more than 2100 s. Thus, the TiO2 NTs on a Ti substrate serve as an excellent support material for the loading and dispersion of noble metal catalysts.  相似文献   

8.
采用密度泛函理论(DFT)计算模拟Pd平板和Pd_(38)团簇上的CO催化氧化过程,分析了CO在Pd催化剂表面上的氧化反应机理。结果表明,在Pd_(38)团簇模型上CO催化氧化的决速步骤是O_2的解离,反应能垒为0.65 eV,而在Pd平板模型上的决速步骤是CO的氧化,其反应能垒为0.87 eV。对比决速步骤的活化能发现,CO在Pd_(38)团簇上的氧化反应更易进行,说明CO氧化更易在小颗粒催化剂表面上进行,即Pd催化剂的活性与活性组分颗粒大小相关,活性组分颗粒越小,暴露的活性位点越多,其催化活性也越高。  相似文献   

9.
The catalytic behaviors of Pd (1.4 wt%) catalysts supported on CeO2-ZrO2-La2O3 mixed oxides with different Ce/Zr molar ratios were investigated for methanol decomposition. Nitrogen adsorption-desorption (BET), X-ray photoelectron spectroscopy (XPS), H2 temperature-programmed reduction (H2-TPR), X-ray diffraction (XRD) and Pd dispersion analysis were used for their characterization. Pd/Ce0.76Zr0.18 La0.06 O1.97 catalyst showed the highest BET surface area, best Pd dispersion capability and strongest metal-support interaction. Moreover, XPS showed that there was lattice defect oxygen or mobile oxygen. According to the result of O 1s measurements the lattice defect oxygen or mobile oxygen helped to maintain Pd in a partly oxidized state and increased the activity for methanol decomposition. The Pd/Ce0.76Zr0.18La0.06O1.97 catalyst exhibited the best activity. A 100% conversion of methanol was achieved at around 260℃, which was about 20-40 ℃ lower than other catalysts  相似文献   

10.
The Pd/fibroin (Fib) was easily prepared by the auto-reduction of the silk-fibroin conjugated Pd(OAc)2 using MeOH as a solvent and a reductant and exhibited good chemoselectivity in the hydrogenation of olefins and azides in the presence of aromatic carbonyls and/or halogens or an O-benzyl protective group.  相似文献   

11.
铈和镧改性γ-Al2O3担载Pd催化剂的结构效应   总被引:1,自引:0,他引:1  
分别以镧-铈、铈-镧顺序浸渍和镧铈共浸渍的方式在γ-Al2O3载体上引入助剂La2O3和CeO2,然后担载Pd制备了一系列催化剂.以甲醇分解为探针反应,采用XRD、EXAFS和XPS对催化剂的体相和表面结构进行表征,用BET法测定比表面积,并进行了吸附态CO的FTIR研究.结果表明,La2O3容易进入CeO2的晶格中,促进了CeO2在γ-Al2O3上的分散.但不同的La2O3、CeO2加入方式对活性组分Pd在改性载体上的分散度、优势暴露面及其与CeO2之间的相互作用产生不同的影响.关联甲醇分解性能测试结果说明,Pd在载体上的高度分散以及Pd和CeO2之间通过界面产生的强相互作用是催化剂具有高活性的关键.  相似文献   

12.
本文通过化学修饰的方法改变了γ-Al_2O_3载体等电点(IEPS),并用具有不同等电点的Al_2O_3作载体,以(NH_4)_2PdCl4为活性组分前身制备了一系列Pd/Al_2O_3催化剂,在固定床微反色谱装置上考察了其对CO氧化的催化活性,用Hi—O_2滴定、紫外漫反射光谱(DRS)、透射电子显微镜(TEM)中的能量色散谱(EDXS)等方法对上述催化剂进行了表征,结果表明:Al_2O_3的等电点(IEPS)对所得催化剂中金属分散度和浓度分布都有明显影响,IEPS越高。活性组分越靠近外表面,在相同担载量下,其分散度也越高。这主要是由于载体IEPS的改变,导致了(NH_4)_2PdCl_4在γ-Al_2O_3上吸附机理的变化,并使所得催化剂对CO氧化的催化活性发生了规律性的变化。  相似文献   

13.
以MWCNTs为载体,用HNO_3做氧化剂对MWCNTs进行处理,通过XPS研究了处理前后MWCNTs表面官能团的变化,并采用超声浸渍法制得Pd/MWCNTs催化剂,借助TEM,揭示了Pd粒子在催化剂表面分散度和粒径与MWCNTs表面含氧量、羟基和羰基间的关系。并考察了Pd/MWCNTs催化剂预处理方法对低浓甲烷催化燃烧活性和稳定性的影响,研究表明,Pd的价态以及Pd粒子的粒径,都与催化剂的甲烷燃烧活性直接关联。单质Pd的氧化和Pd粒径的长大是导致催化剂性能衰减的原因。通过原位FT-IR技术对反应气氛下中间物种的监测,提出了Pd/MWCNTs催化剂上的低浓度甲烷催化氧化反应机理。  相似文献   

14.
董春燕  周燕  塔娜  刘雯璐  李名润  申文杰 《催化学报》2021,42(12):2234-2241
氧化铈由于在氧化和还原气氛下具有快速Ce4+/Ce3+氧化还原循环作用,使其具有优异的储放氧能力,不仅可以分散和稳定金属粒子,还可在界面处与金属物种发生化学键合,并形成活性位点,因此已被广泛应用于多个催化反应体系,且表现出显著的形貌效应.通过对氧化铈形貌进行调控,使其暴露特定(111)、(110)和(100)晶面,已成为调节金属-氧化铈相互作用强度及金属物种电子、几何结构,提高催化性能的有效策略,但对其机制及活性位结构还没有清晰的认识.我们以氧化铈纳米粒子和纳米立方体为载体,其中氧化铈立方体平均尺寸为23 nm,主要暴露6个{100}晶面,边缘和截角暴露少量{110}及{111}晶面;球形氧化铈纳米粒子平均尺寸为11 nm,主要暴露{111}晶面;并进一步将2.0 wt%Pd物种分散在氧化铈立方体和球形纳米粒子上,通过扫描透射电子显微镜(STEM)和X射线光电子能谱(XPS)等研究了钯物种在氧化铈球形粒子和立方体上的原子结构和化学环境,进而分析了纳米结构氧化铈形貌对钯物种分散的影响.在球形氧化铈纳米粒子上主要形成了平均尺寸为2.0 nm的非晶态Pd纳米粒子以及极小的Pd物种,这主要是因为球形氧化铈纳米粒子上丰富的表面氧空位可通过Pd-CeO2强相互作用和Pd物种紧密键合.氧化铈立方体上的晶态Pd粒子尺寸为2.9 nm,金属与载体之间具有明显的界面,且Pd原子嵌入到氧化铈晶格中.同时,CO化学吸附测试也证明了氧化铈球形粒子上的钯分散度(70%)高于氧化铈立方体(52%).对于甲烷燃烧反应,主要涉及发生在金属粒子表面的PdO/Pd氧化还原循环,即Pd被O2氧化,PdO被CH4还原,富氧条件下决速步骤是PdO对CH4中C?H的活化,因此氧化铈立方体表面大尺寸的晶态Pd粒子被氧化后更容易被CH4还原,有利于PdO/Pd氧化还原循环,从而具有更高的活性和稳定性;然而在CO氧化反应中Pd/CeO2却呈现了相反的形貌效应,这是由于该反应遵循Mars-van Krevelen机理:CO吸附在金属Pd上,化学吸附的CO移动到钯-氧化铈界面,被氧化铈晶格氧氧化成CO2,产生的氧空位被表面氧补充,最后表面氧空位被气相氧补充;由于氧化铈球形粒子上的较小尺寸Pd具有更大的钯-氧化铈界面周长和更强的氧物种移动性,更易完成界面处的氧化还原循环,因此具有更高的CO氧化活性.  相似文献   

15.
 采用湿浸法制备了用于蒽醌氢化制H2O2的La2O3促进的Pd/Al2O3催化剂,并考察了不同La2O3含量对催化性能的影响. 采用XRD,N2物理吸附,CO2-TPD,H2-O2滴定和电子探针等技术对催化剂进行了表征. 结果表明,加入适量的La2O3能够抑制高温焙烧时Al2O3晶粒的长大,增大催化剂的比表面积,提高金属Pd的分散度,增强载体表面碱性,提高催化剂表面的Pd浓度,减小Pd层厚度,从而提高催化剂的氢化活性. 加入La2O3可使催化剂的Pd负载量由0.281%降至0.188%,而催化剂活性提高了44%.  相似文献   

16.
We present a Molecular Dynamics (MD) study based on Density Functional Theory (DFT) calculations for H(2) interacting with a Pd-Cu(111) surface alloy for low Pd coverages, Θ(Pd). Our results show, in line with recent experimental data, that single isolated Pd atoms evaporated on Cu(111) significantly increase the reactivity of the otherwise inert pure Cu surface. On top of substitutional Pd atoms in the Pd-Cu(111) surface alloy, the activation energy barrier for H(2) dissociation is smaller than the lowest one found on Cu(111) by a factor of two: 0.25 eV vs. 0.46 eV. Also in agreement with experiments, our DFT-MD calculations show that a large fraction of the dissociating H atoms efficiently spillover from Pd (i.e. the active sites), thanks to their extra kinetic energy due to the ~0.50 eV chemisorption exothermicity. Still, our DFT-MD calculations predict a dissociative sticking probability for low energy H(2) molecules that is much smaller than the estimated value from scanning tunneling microscopy experiments. Thus, further theoretical and experimental investigations are required for a complete understanding of H(2) dissociation on low-Θ(Pd) Pd-Cu(111) surface alloys.  相似文献   

17.
The reaction between bromomethane CH(3)Br and Pd(0) phosphine complexes Pd(PR(3)) and Pd(PR(3))(2) resulting in the corresponding Pd(II) species Pd(PR(3))(CH(3))Br and Pd(PR(3))(2)(CH(3))Br was studied computationally with DFT methods. The oxidative addition can take place through two different mechanisms: concerted or S(N)2 transition state. The effect of a number of variables on the height of the barrier associated to each of these two mechanisms is systematically analyzed. The variables considered include the number of ligands on the metal (mono- or bis-phosphine), the nature of the phosphine (PF(3), PH(3), PMe(3) or PPh(3)), and the nature of the solvent (gas phase, tetrahydrofuran or dimethylformamide). A number of trends can be identified, resulting in a complex picture where the nature of the phosphine and the solvent can be tuned to favor one of the two possible mechanisms, with the corresponding stereochemical implications that can be extrapolated to the behaviour of more sophisticated substrates.  相似文献   

18.
[Structure: see text] A Pd/C-catalyzed chemoselective hydrogenation using diphenylsulfide as a catalyst poison has been developed. This methodology selectively hydrogenates olefin and acetylene functionalities without hydrogenolysis of aromatic carbonyls and halogens, benzyl esters, and N-Cbz protective groups.  相似文献   

19.
潘喜强  杨向光 《应用化学》2014,31(2):177-181
Pd/ZrO2是甲烷低温燃烧研究较为广泛的催化剂,其中载体ZrO2对稳定PdO起到了重要作用。 采用水热法合成了纯相的M-ZrO2和T-ZrO2,然后采用浸渍法制备了Pd/M-ZrO2和Pd/T-ZrO2催化剂,并考察了不同晶型ZrO2对催化剂的活性和稳定性的影响。 结果表明,Pd/M-ZrO2催化剂的活性和稳定性明显优于Pd/T-ZrO2。 结合XRD、TEM和TPO表征结果,发现Pd/M-ZrO2活性高的原因是PdO分散性更好,Pd/M-ZrO2较好的稳定性与PdO和ZrO2的作用方式有关。  相似文献   

20.
Akinori Mori 《Tetrahedron》2006,62(51):11925-11932
While Pd/C is one of the most useful catalysts for hydrogenation, the high catalyst activity of Pd/C causes difficulty in its application to chemoselective hydrogenation between different types of reducible functionalities. In order to achieve chemoselective hydrogenation using Pd/C, we investigated catalyst poison as a controller of the catalyst activity. We found that the addition of Ph2S (diphenylsulfide) to the Pd/C-catalyzed hydrogenation reaction mixture led to reasonable deactivation of Pd/C. By the use of the Pd/C-Ph2S catalytic system, olefins, acetylenes, and azides can be selectively reduced in the coexistence of aromatic carbonyls, aromatic halides, cyano groups, benzyl esters, and N-Cbz (benzyloxycarbonyl) protecting groups. The present method is promising as a general and practical chemoselective hydrogenation process in synthetic organic chemistry.  相似文献   

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