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Siani A Captain B Alexeev OS Stafyla E Hungria AB Midgley PA Thomas JM Adams RD Amiridis MD 《Langmuir : the ACS journal of surfaces and colloids》2006,22(11):5160-5167
The catalytic performance of cluster-derived PtFe/SiO(2) bimetallic catalysts for the oxidation of CO has been examined in the absence and presence of H(2) (PROX) and compared to that of Pt/SiO(2). PtFe(2)/SiO(2) and Pt(5)Fe(2)/SiO(2) samples were prepared from PtFe(2)(COD)(CO)(8) and Pt(5)Fe(2)(COD)(2)(CO)(12) organometallic cluster precursors, respectively. FTIR data indicate that both clusters can be deposited intact on the SiO(2) support. The clusters remained weakly bonded to the SiO(2) surface and could be extracted with CH(2)Cl(2) without any significant changes in their structure. Subsequent heating in H(2) led to complete decarbonylation of the supported clusters at approximately 350 degrees C and the formation of Pt-Fe nanoparticles with sizes in the 1-2 nm range, as indicated by HRTEM imaging. A few larger nanoparticles enriched in Pt were also observed, indicating that a small fraction of the deposited clusters were segregated to the individual components following the hydrogen treatment. A higher degree of metal dispersion and more homogeneous mixing of the two metals were observed during HRTEM/XEDS analysis with the cluster-derived samples, as compared to a PtFe/SiO(2) catalyst prepared through a conventional impregnation route. Furthermore, the cluster-derived PtFe(2)/SiO(2) and Pt(5)Fe(2)/SiO(2) samples were more active than Pt/SiO(2) and the conventionally prepared PtFe/SiO(2) sample for the oxidation of CO in air. However, substantial deactivation was also observed, indicating that the properties of the Pt-Fe bimetallic sites in the cluster-derived samples were altered by exposure to the reactants. The Pt(5)Fe(2)/SiO(2) sample was also more active than Pt/SiO(2) for PROX with a selectivity of approximately 92% at 50 degrees C. In this case, the deactivation with time on stream was substantially slower, indicating that the highly reducing environment under the PROX conditions helps maintain the properties of the active Pt-Fe bimetallic sites. 相似文献
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Fe对Pt-Fe/C催化剂电催化氧还原反应活性的影响 总被引:1,自引:1,他引:0
制备了用作直接甲醇燃料电池的碳载Pt-Fe(Pt-Fe/C)阴极催化剂, X射线能量色散谱(EDX)、X射线衍射谱和电化学测量的结果表明, 在Pt-Fe/C催化剂中, Fe以3种形式存在. 质量分数大约为20%的Fe进入Pt的晶格, 形成Pt-Fe合金, 质量分数大约为80%的Fe没有进入Pt的晶格而以Fe和Fe2O3的形式单独存在. 该催化剂经酸处理后, 非合金化Fe和Fe2O3被溶解, 而使Pt-Fe/C催化剂的电化学活性比表面积要比未经酸处理前的增加约30%左右, 导致Pt-Fe/C催化剂对氧还原的电催化活性优于未经酸处理前的Pt-Fe/C催化剂. 研究结果表明, Pt-Fe/C催化剂的电化学活性比表面积对氧还原的电催化活性起重要的作用, 另外, 只有与Pt形成合金的Fe能提高Pt对氧还原的电催化活性, 而非合金化的Fe对Pt催化剂对氧还原的电催化活性基本没有影响. 相似文献
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Cesium-exchanged zeolite X was impregnated with cesium acetate (Cs(Ac)/CsX) or cesium carbonate (Cs(2)CO(3)/CsX) and subsequently calcined to yield a basic catalyst. The Raman spectra of calcined Cs(Ac)/CsX and Cs(2)CO(3)/CsX exhibited a new peak at 1036 cm(-1) associated with the occluded species. No evidence for cesium peroxide or superoxide was observed. The occluded cesium species in both samples is proposed to be an oxycarbonate, which is a metastable intermediate between cesium carbonate and cesium oxide. The isomerization of 1-butene to cis- and trans-2-butene was catalyzed by cesium-loaded zeolite X. Although CO(2) readily poisoned the active base sites for catalysis, pretreatment of a basic zeolite with O(2) at 373 K did not. Co-feeding O(2) with 1-butene at 373 K, however, completely deactivated the base sites. Analysis of the reactor effluent at 473 K and the IR spectrum of the catalyst indicated the formation of carbon dioxide, which irreversibly adsorbed on the basic sites of the catalyst. Deactivation of basic catalysts by O(2) is proposed to occur through a low temperature oxidation of 1-butene to carbon dioxide, which strongly adsorbs on the active sites. 相似文献
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甲醇在Pt-Fe(111)/C表面吸附的理论研究 总被引:1,自引:0,他引:1
采用密度泛函理论和周期平板模型相结合的方法, 对CH3OH分子在Pt-Fe(111)/C表面top, fcc, hcp和bridge位的吸附模型进行了构型优化、能量计算, 结果表明bridge位是较有利的吸附位. 掺杂后费米能级的位置发生了右移, 价带和导带均增宽, 极利于电子-空穴的迁移, 这对提高催化活性是非常有利的. 考察抗中毒性发现: CO在Pt(111)/C面上的吸附能比甲醇吸附能要高, CO在Pt-Fe(111)/C的吸附能比甲醇吸附能要低, 可说明CO在Pt(111)/C面上有中毒效应, 而Pt-Fe(111)/C的抗CO中毒能力增强, 是催化氧化甲醇良好的催化剂. 相似文献
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Chunzheng Wang Weisong Xu Zhengxing Qin Hailing Guo Xinmei Liu Svetlana Mintova 《Journal of Energy Chemistry》2021,(1)
Palladium containing EMT zeolite catalyst(Pd/EMT) was prepared and used for the indirect oxidative carbonylation of methanol to dimethyl carbonate(DMC).The EMT zeolite was employed as a new catalyst support and compared with the conventional Pd containing FAU zeolite catalyst(Pd/FAU).The Pd/EMT in contrast to the Pd/FAU catalyst exhibited high intrinsic activity with the turnover frequency of 0.25 s-1 vs.0.11 s-1.The Pd/EMT catalyst showed high CO conversion of 82% and DMC selectivity of 79%,that maintained for at least 130 h,while the activity of the Pd/FAU catalyst rapidly deteriorated within 12 h.The enhanced interactions between Pd and EMT zeolite inhibited the sintering of palladium clusters and maintained the Pd2+ active sites in the Pd/EMT catalyst.The stabilization of the mono-dispersed Pd clusters within the EMT zeolite is paramount to the excellent performance of the catalyst for the indirect oxidative carbonylation of methanol to DMC. 相似文献
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High activity and high formation selectivity for aromatics in the dehydrocondensation reaction of methane were realized only on selected catalysts. The requisites of a metal and a zeolite support as the selected catalyst were described. However, the catalytic activity steadily declined even on the selected catalysts with time on stream because of coke accumulation. A stable catalytic activity was obtained when CO2 or CO was added into methane feed due to effective removal of coke from the catalyst surface by CO or CO2. The route from methane to aromatics and the formation process of active phase of catalyst were discussed. 相似文献
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High activity and high formation selectivity for aromatics in the dehydrocondensation reaction of methane were realized only on selected catalysts. The requisites of a metal and a zeolite support as the selected catalyst were described. However, the catalytic activity steadily declined even on the selected catalysts with time on stream because of coke accumulation. A stable catalytic activity was obtained when CO2 or CO was added into methane feed due to effective removal of coke from the catalyst surface by CO or CO2. The route from methane to aromatics and the formation process of active phase of catalyst were discussed. 相似文献
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分子筛硅/铝比对Cu-ZnO-Al2O3/HMCM-22催化合成二甲醚反应性能的影响 总被引:2,自引:0,他引:2
以六亚甲基亚胺为模板剂,采用动态水热晶化法合成了不同硅/铝比的HMCM-22分子筛,并以其为甲醇脱水活性组分与铜基甲醇合成活性组分(Cu-ZnO-Al2O3)组成双功能催化剂,在连续流动加压固定床微型反应器上考察了其对合成气直接制二甲醚反应的催化性能. 结果表明,随着HMCM-22分子筛硅/铝比的增大, CO转化率变化不大,但CO2和烃类副产物的生成量逐渐减少,从而导致目的产物二甲醚的选择性和收率均逐渐升高. 氨程序升温脱附和吡啶吸附红外光谱表征结果表明,随着分子筛硅/铝比的增大, HMCM-22分子筛的酸中心的数量逐渐减少. 相似文献
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Suppression of methane formation during Fisher-Tropsch synthesis using manganese-cobalt oxide supported on H-5A zeolite as a catalyst 下载免费PDF全文
In Fischer-Tropsch synthesis reaction, methane formation is one of the side reactions which must be suppressed in order to get better catalytic selectivity for light olefins. In the present study, we have modified cobalt based Fischer-Tropsch catalyst and developed a process to minimize methane production, consequently to produce maximum yield of light olefins. Manganese-cobalt oxide supported on H-5A zeolite catalyst was synthesized using modified H-5A zeolite, to increase its surface acid sites. Increased acidity of zeolite plays a major part in the suppression of methane formation during the Fischer-Tropsch reaction. The modified zeolite results in the electronic modification of catalyst surface by creating new active catalytic sites. The results are compared with other supported catalysts along with unmodified zeolite. Appreciable reduction in methane formation is achieved on modified zeolite supported catalyst in comparison with unsupported catalyst. 相似文献
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noxides(mainlyNO)aremajorairpollutantsthatcausephotochemicalsmogandacidrain.Therefore,thereisaworldwideefforttodiscoverimprovedsolutionsfortheeffectiveremovalofNO.emissionsl.UntilnoW,nosuitablecatalystthatcaneffectivelyconvertNOintoN,andO:althoughthe... 相似文献
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Precise synthesis and characterization of site-isolated rhodium complexes and extremely small rhodium clusters supported on zeolite HY allow control of the catalyst selectivity in the conversion of ethene to n-butene or ethane, respectively, as a result of tuning the structure of the active sites at a molecular level. 相似文献
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分子筛改性对一步法合成二甲醚的影响 总被引:5,自引:2,他引:3
采用浸渍法制备了MgO、CaO、ZnO改性的HZSM 5分子筛,并以改性HZSM 5为脱水剂与JC207甲醇合成催化剂组成双功能催化剂,在固定床反应器上考察了其对一步法合成二甲醚影响。结果表明,适量碱性氧化物的引入,引起分子筛表面的B酸中心(强酸中心)向L酸中心(弱酸中心)转变,而弱酸和中强酸中心是甲醇脱水生成二甲醚的活性中心,强酸中心会造成二甲醚进一步脱水生成烃类副产品,所以改性后产物中二氧化碳和烃类的选择性下降,二甲醚选择性升高。这种趋势在CaO/HZSM 5脱水剂上表现的更为明显。 相似文献
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In order to obtain highly active catalytic materials for oxidation of carbon monoxide and volatile organic compounds (VOCs), monometallic platinum, copper, and palladium catalysts were prepared by using of two types of ZSM-5 zeolite as supports—parent ZSM-5 and the same one treated by HF and NH4F buffer solution. The catalyst samples, obtained by loading of platinum, palladium, and copper on ZSM-5 zeolite treated using HF and NH4F buffer solution, were more active in the reaction of CO and benzene oxidation compared with catalyst samples containing untreated zeolite. The presence of secondary mesoporosity played a positive role in increasing the catalytic activity due to improved reactant diffusion. The only exception was the copper catalysts in the reaction of CO oxidation, in which case the catalyst, based on untreated ZSM-5 zeolite, was more active. In this specific case, the key role is played by the oxidative state of copper species loaded on the ZSM-5 zeolites. 相似文献
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The kinetics of formation of primary products from cumene cracking over a partially exchanged LaNaY catalyst have been studied at 400, 450, and 500°C. It has been found that in both the fully and the partially exchanged LaNaY zeolite catalysts the nature of active sites is the same. The higher activity of the fully exchanged catalyst is attributed to a higher concentration of the active sites. It has also been found that an increase in exchange level leads to an increase in the number of both Bronsted and Lewis active sites, but in somewhat different proportions. A comparatively slight increase in the decay rate constant is observed over the same increase in the level of exchange. 相似文献
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烯基芳香化合物是重要的精细化学品及中间体,在医药、染料、农药、香料、新型高分子材料和天然产品等化学工业领域得到广泛应用.传统工艺采用芳香化合物与烯基化合物的反应合成烯基芳香化合物.但是,传统过程存在许多不足:(1)芳环需预活化,如卤代等;(2)伴生氢卤酸等废物,污染环境;(3)原子经济性差.因此,研究烯基芳香化合物的清洁、高原子经济性合成备受关注.采用芳香化合物与炔基化合物的烯基化,可以100%原子经济性地合成烯基芳香化合物,且芳环无需预活化,不产生废弃物.因此,通过芳香化合物与炔的烯基化路线来合成烯基芳香化合物引起了人们的极大兴趣.尤其是固体酸催化烯基化,工艺成本低,清洁无污染,颇具工业前景.然而,固体酸催化烯基化不同于烷基化,烯基阳离子稳定性很差,比碳正离子易于聚合,进而导致催化剂积碳失活.微孔沸石分子筛用于烯基化存在底物适用范围窄、催化效率低、选择性差和炔聚合严重的问题.本研究组开展了硫酸化的镧锆氧化物介孔固体超强酸、担载磷钨酸介孔固体酸催化烯基化.采用前者,合成有序的介孔镧锆氧化物较为困难;而采用后者,催化剂的再生需要大量有机溶剂,会造成环境污染.硅铝分子筛固体酸易于制备,且可以通过简单的焙烧来再生.多级孔分子筛具有微孔分子筛和介孔分子筛的双重优势,用于烯基化反应可望获得良好效果.本文采用碱、酸对商业微孔β沸石分子筛进行处理,通过脱硅、脱铝过程来合成多级孔β分子筛,并进行稀土金属铈改性,从而制备了氧化铈改性的多级孔β分子筛,研究了其催化对二甲苯与苯乙炔的烯基化反应.通过改变碱浓度和酸浓度,对所制备的多级孔β分子筛的织构性质和酸性质进行调控,在优化的条件下获得了良好的烯基化催化性能,得到95.8%的苯乙炔转化率和95.1%的目标产物α-2,5-二甲苯基苯乙烯的选择性,总的烯基化产物(α-和β-烯基芳香化合物)的选择性达到98%.相对于微孔β分子筛,所制备的多级孔β分子筛展示了显著增强的催化活性和稳定性,目标产物选择性也有所提高.显著提高的催化性能归因于多级孔分子筛的传质强化和酸性位的增多.氧化铈的改性使得多级孔β分子筛的弱、中等和强酸中心的数目减少,可能源于减少了表面暴露的B酸位,从而导致了催化稳定性的显著提高.可见,本文所制备的氧化铈改性多级孔β分子筛用于烯基化反应具有一定前景. 相似文献
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Cu/Ni负载型Beta分子筛催化剂的乙醇水蒸气重整制氢催化性能研究 《燃料化学学报》2017,45(11):1392-1400
采用等体积浸渍的方式,在全硅Beta分子筛载体上担载Cu、Ni活性组分,制备出一系列xCuyNi-ABZ多功能乙醇水蒸气重整制氢催化剂。通过XRD、TEM、SEM-EDX以及XPS等多种表征手段,研究催化剂的结构特性、活性组分含量等因素对催化性能的影响,依据反应产物分布,揭示其作用机理。结果表明,以Beta分子筛为载体可促使活性组分以纳米颗粒的形式高度分散于载体表面,并且存在较强的载体-金属作用力。与传统SiO_2为载体催化剂相比,2.5Cu2.5Ni-ABZ催化剂具备良好的乙醇水蒸气重整催化性能,当反应温度为450℃,实现100%的乙醇转化率和67.23%的H_2选择性,且副产物CO(4.14%)、CH_4(5.65%)含量相对较低。这可归因于Cu和Ni活性组分间的高效协同作用,Cu具有良好的乙醇脱氢性能,生成反应中间体乙醛;在反应过程中,乙醛的重整和分解是两个受温度影响的竞争反应,Ni组分利用其较强的C-C键断裂能力,随温度的升高,乙醛重整反应占主导作用,生成目标产物H_2。通过对反应后样品分析表明,2.5Cu2.5Ni-ABZ催化剂具备良好的抗烧结和抗积炭催化性能。 相似文献