非通孔多孔氧化铝基底上原位生成Pd纳米材料的制备及应用

以非双通的多孔氧化铝(AAO)(Al基底为支撑体)为模板,基底Al作为还原剂,在AAO孔道内原位合成了Pd单质(Pd/AAO)。本文详细研究了AAO阻挡层的去除以及Pd/AAO的酸腐蚀处理后的情况。采用扫描电子显微镜观察了不同条件下形成的形貌,提出了一个近似合理的生成Pd单质的机理。评价了其对苯硼酸和对溴苯甲醛Suzuki反应的活性。摩尔分数0.06%Pd催化剂在温和的实验条件下可以高效催化Suzuki反应,产率达到99.8%。Pd/AAO固体片状结构在液相反应中直接从溶液中取出即可进行下一次反应,易于分离和回收,可使用性强。此研究为有机反应异相催化剂的设计提供了一个有效的思路,在实际应用中具有一定的指导意义。     

ZrO2在Pd／Al2O3催化剂中的助剂作用

用流动反应法考察了富氧或贫氧气氛中添加ＺｒＯ２的Ｐｄ／Ａｌ２Ｏ３催化剂上ＣＯ的催化氧化反应，并用ＸＲＤ、ＴＰＲ和ＴＰＤ－ＭＳ等技术研究了助剂ＺｒＯ２与γ－Ａｌ２Ｏ３间的相互作用对催化剂上氧物种的还原和脱出－恢复行为的影响，结果表明，基质γ－Ａｌ２Ｏ３与ＺｒＯ２能发生相互作用，添加６％ＺｒＯ２的催化剂氧化活性最好，添加适量的ＺｒＯ２有利于催化剂上氧物种的脱出－恢复，从而促进ＣＯ氧化活性及表面活泼氧物     

Catalytic Performance of Carbon Materials Supported Pd Nanoparticles in Selective Hydrogenation of Acetylene

Pd/C catalysts were prepared by deposited Pd nanoparticles (NPs) on different carbon supports including activated carbon (AC), graphite oxide (GO), and reduced graphite oxide (rGO) using sol-immobilization method. Through transmission electron microscopy, powder X-ray di raction, and X-ray photoelectron spectroscopy, the role of the carbon supports for the catalytic performances of Pd/C catalysts was examined in selective hydrogenation of acetylene. The results indicate that Pd/AC exhibited higher activity and selectivity than Pd/GO and Pd/rGO in the gas phase selective hydrogenation of acetylene. Thermal and chemical treatment of AC supports also have some effect on the catalytic performance of Pd/AC catalysts. The differences in the activity and selectivity of various Pd/C catalysts were partly attributed to the metal-support interaction.     

Pd/Al2O3催化剂的高温热烧结研究

以汽车尾气净化催化剂为背景，用溶胶－凝胶法和浸渍法制备了低负载量贵金属单钯燃烧催化剂。通过ＸＲＤ宽化法检测了在１２７３Ｋ的模拟反应气流中烧结２４ｈ后催化剂上Ｐｄ晶粒大小的变化。     

Mizoroki-Heck coupling using immobilized molecular precatalysts: leaching active species from Pd pincers, entrapped Pd salts, and Pd NHC complexes

The Mizoroki-Heck reaction is a palladium-catalyzed reaction of both practical importance and scientific significance. Two challenges currently faced by practitioners of the Heck and other palladium-catalyzed coupling reactions are (i) minimizing the costs associated with this reaction by developing high TON catalysts or facilitating catalyst recovery and (ii) elucidating the nature of the active species when using various different precatalysts. These two challenges, one practical and one fundamental, served as our motivation in our studies of immobilized molecular palladium(II) complexes as precatalysts in Mizoroki-Heck reactions. This Forum Article describes our investigations in this area, highlighting our approach to the elucidation of the active catalyst by combining kinetic and poisoning studies of several different related precatalysts, our development of new, selective catalyst poisons, and our quest for stable, recyclable supported Heck, Suzuki, and Sonogashira coupling catalysts. Under high-temperature conditions (120 degrees C), all precatalysts studied are conclusively shown to decompose, liberating soluble, active palladium(0) species that are the true catalysts. Techniques for the elucidation of the nature of the truly active Pd species are enumerated.     

XPS analysis of the effect of Pt addition to Pd catalysts for complete benzene oxidation

Pt-Pd bimetallic catalysts were prepared in order to develop and investigate catalysts having excellent activity and stability for benzene destruction. The effect of Pt addition to Pd catalysts is studied by XPS analysis. This revised version was published online in August 2006 with corrections to the Cover Date.     

原子层沉积构筑Pd/TiO2限域催化剂及其在1,4-丁炔二醇加氢的应用

利用ALD制备了TiO₂限域的Pd催化剂, 研究了限域空间内Pd纳米颗粒与TiO₂的界面作用对1,4-丁炔二醇(BYD)加氢性能的影响. 相比于管外负载型催化剂, 限域催化剂在催化1,4-丁炔二醇选择性加氢反应中体现出非常高的催化活性和1,4-丁烯二醇的选择性. HR-TEM、 EDX-Mapping、 XRD、 XPS和H₂-TPR表征说明, 限域体系中Pd-TiO₂的界面相互作用强于传统TiO₂表面负载型Pd催化剂, 这种强界面作用不仅能够提高BYD的加氢活性, 也可抑制半加氢产物1,4-丁烯二醇的异构化和深度加氢, 提高1,4-丁烯二醇的选择性, 而且限域结构也可阻止管内壁Pd纳米颗粒的脱落, 提高催化剂的稳定性.     

Efficient Polymer-Supported Pd Catalysts for the Heck Reaction

Some efficient polymer‐supported palladium catalysts have been synthesized. Their catalytic effects were evaluated in the Heck reaction of iodobenzene with acrylates or styrene. High catalytic activities were achieved with turn over frequencies (TOF) up to 28000 and 6250, respectively. For the reaction of iodobenzene with styrene, high stereoselectivity was obtained. Additionally, the catalysts could be recovered by a simple filtration progress and can be reused for at least 5 times with a slow progressive decrease in activity.     

Structure of Pd/SiO2 sol-gel and impregnated catalysts

Palladium catalysts were prepared by sol-gel and impregnation techniques both in acid and basic media. The sol-gel catalysts resulted in larger PdO crystallites than the impregnated catalysts. In both preparation methods, an acid medium promoted the formation of small metal crystallites which provided catalytic activity. A stronger metal-support interaction was found in sol-gel catalysts synthesized from a square planar palladium complex. Deactivation results in phenylacetylene hydrogenation have been attributed to palladium hydrate formation or to deposition of carbonaceous compounds. The preparation mode determined the contribution of each deactivating reaction.     

载体性质对Pd催化剂加氢脱硫性能的影响

以Si O2、全硅MCM-41(Si-MCM-41)、通过机械混合Si-MCM-41与ZSM-5得到的Z-MCM-41-M以及通过在ZSM-5外部包覆MCM-41制备得到的Z-MCM-41四种材料为载体,制备了四种负载型Pd催化剂。采用XRD、HRTEM、N2吸附-脱附、NH3-TPD手段对Pd催化剂进行了表征;以二苯并噻吩(DBT)为模型化合物,在固定床反应器上对四种催化剂的加氢脱硫(HDS)活性、加氢路径选择性和加氢裂化活性进行了考察,研究了不同类型载体对Pd催化剂加氢脱硫性能的影响。结果表明,载体的性质会显著影响负载型Pd催化剂的加氢脱硫性能。载体的比表面积对负载型Pd催化剂加氢脱硫活性影响不大,但是HYD路径的选择性与载体的孔道结构有关;具有介孔孔道结构有利于加氢路径选择性的提高。酸性载体负载的Pd催化剂表现出较好加氢脱硫活性和加氢选择性,这与氢溢流有关。介孔材料的孔道结构与微孔沸石的酸性有机结合,所得到的Z-M CM-41复合材料是是潜在的贵金属Pd加氢脱硫催化剂优良载体,可有效提升其加氢脱硫活性。     

Revealing the true origin of size-dependent Pd/C catalytic behavior towards formic acid decomposition

Formic acid decomposition (FAD) is considered a promising hydrogen production route to facilitate the ambient storage and on demand release of hydrogen energy. To optimize the catalysts for FAD, efforts have been paid to explore the underlying reason for the varied catalytic activity among catalysts with similar composition but differed structure. However, such endeavors are highly challenging due to the deeply intermingled effects of electronic structure, particle size, and facets, etc. Herein, to separately evaluate the respective effects of these factors, a series of catalysts with the same surface electronic structure and different particle size was prepared by cation dipole adjustment method. The performance and characterization results showed that the catalysts with different sizes and facets exhibited similar intrinsic activity with deviation of less than 5%. However, they showed 252% deviation of site stability, indicating that only the optimized electronic structure could enhance the intrinsic activity and a smaller particle size could extend the catalyst's life.     

石墨烯负载高活性Pd催化剂对乙醇的电催化氧化

以石墨粉为原料, 采用Hummers法液相氧化合成了氧化石墨(GO), 然后用化学一步还原制得石墨烯负载钯催化剂. X射线衍射(XRD)、透射电镜(TEM)表征表明, Pd在石墨烯载体上有较好的分散度, 粒径为3-5 nm. 电化学活性面积(EASA)、循环伏安(CV)、计时电流(CA)和计时电位(CP)等电化学测试表明, 与传统Pd/Vulcan XC-72相比, Pd/石墨烯催化剂对碱性介质中乙醇电催化氧化的催化活性有了很大的提高.     

石墨烯负载高活性Pd催化剂对乙醇的电催化氧化

以石墨粉为原料, 采用Hummers法液相氧化合成了氧化石墨(GO), 然后用化学一步还原制得石墨烯负载钯催化剂. X射线衍射(XRD)、透射电镜(TEM)表征表明, Pd在石墨烯载体上有较好的分散度, 粒径为3-5 nm. 电化学活性面积(EASA)、循环伏安(CV)、计时电流(CA)和计时电位(CP)等电化学测试表明, 与传统Pd/Vulcan XC-72相比, Pd/石墨烯催化剂对碱性介质中乙醇电催化氧化的催化活性有了很大的提高.     

石墨烯负载高活性Pd催化剂对乙醇的电催化氧化

以石墨粉为原料, 采用Hummers法液相氧化合成了氧化石墨(GO), 然后用化学一步还原制得石墨烯负载钯催化剂. X射线衍射(XRD)、透射电镜(TEM)表征表明, Pd在石墨烯载体上有较好的分散度, 粒径为3-5 nm. 电化学活性面积(EASA)、循环伏安(CV)、计时电流(CA)和计时电位(CP)等电化学测试表明, 与传统Pd/Vulcan XC-72相比, Pd/石墨烯催化剂对碱性介质中乙醇电催化氧化的催化活性有了很大的提高.     

石墨烯负载高活性Pd催化剂对乙醇的电催化氧化

以石墨粉为原料, 采用Hummers法液相氧化合成了氧化石墨(GO), 然后用化学一步还原制得石墨烯负载钯催化剂. X射线衍射(XRD)、透射电镜(TEM)表征表明, Pd在石墨烯载体上有较好的分散度, 粒径为3-5 nm. 电化学活性面积(EASA)、循环伏安(CV)、计时电流(CA)和计时电位(CP)等电化学测试表明, 与传统Pd/Vulcan XC-72相比, Pd/石墨烯催化剂对碱性介质中乙醇电催化氧化的催化活性有了很大的提高.     

脂肪腈加氢胺化过程中Pd/C催化剂失活原因探讨

以活性炭为载体,负载氯化钯溶液,制备钯/炭催化剂,在循环使用于催化脂肪腈加氢制备单烷基二甲基叔胺时发现,催化剂活性持续下降。通过氮吸附、热重分析、X射线能谱和透射电子显微镜等手段,对催化剂失活前后的表面积、孔径分布变化、催化剂的失重状况、Pd的价态变化以及Pd晶粒的粒径变化研究表明,导致钯/炭催化剂失活的原因主要是反应过程中积炭的生成、Pd的价态变化和Pd晶粒粒径的增大。     

石墨烯负载高活性Pd催化剂对乙醇的电催化氧化

以石墨粉为原料, 采用Hummers法液相氧化合成了氧化石墨(GO), 然后用化学一步还原制得石墨烯负载钯催化剂. X射线衍射(XRD)、透射电镜(TEM)表征表明, Pd在石墨烯载体上有较好的分散度, 粒径为3-5 nm. 电化学活性面积(EASA)、循环伏安(CV)、计时电流(CA)和计时电位(CP)等电化学测试表明, 与传统Pd/Vulcan XC-72相比, Pd/石墨烯催化剂对碱性介质中乙醇电催化氧化的催化活性有了很大的提高.     

石墨烯负载高活性Pd催化剂对乙醇的电催化氧化

以石墨粉为原料, 采用Hummers法液相氧化合成了氧化石墨(GO), 然后用化学一步还原制得石墨烯负载钯催化剂. X射线衍射(XRD)、透射电镜(TEM)表征表明, Pd在石墨烯载体上有较好的分散度, 粒径为3-5 nm. 电化学活性面积(EASA)、循环伏安(CV)、计时电流(CA)和计时电位(CP)等电化学测试表明, 与传统Pd/Vulcan XC-72相比, Pd/石墨烯催化剂对碱性介质中乙醇电催化氧化的催化活性有了很大的提高.     

石墨烯负载高活性Pd催化剂对乙醇的电催化氧化

以石墨粉为原料, 采用Hummers法液相氧化合成了氧化石墨(GO), 然后用化学一步还原制得石墨烯负载钯催化剂. X射线衍射(XRD)、透射电镜(TEM)表征表明, Pd在石墨烯载体上有较好的分散度, 粒径为3-5 nm. 电化学活性面积(EASA)、循环伏安(CV)、计时电流(CA)和计时电位(CP)等电化学测试表明, 与传统Pd/Vulcan XC-72相比, Pd/石墨烯催化剂对碱性介质中乙醇电催化氧化的催化活性有了很大的提高.     

石墨烯负载高活性Pd催化剂对乙醇的电催化氧化

以石墨粉为原料, 采用Hummers法液相氧化合成了氧化石墨(GO), 然后用化学一步还原制得石墨烯负载钯催化剂. X射线衍射(XRD)、透射电镜(TEM)表征表明, Pd在石墨烯载体上有较好的分散度, 粒径为3-5 nm. 电化学活性面积(EASA)、循环伏安(CV)、计时电流(CA)和计时电位(CP)等电化学测试表明, 与传统Pd/Vulcan XC-72相比, Pd/石墨烯催化剂对碱性介质中乙醇电催化氧化的催化活性有了很大的提高.