激光溅射法制备Pt/CNTs催化剂用于邻氯硝基苯的液相加氢反应

采用激光溅射法制备了碳纳米管负载铂(Pt/CNTs)催化剂, 并利用透射电子显微镜(TEM)、X射线能量散射谱(EDS)、X射线衍射(XRD)、X射线光电子能谱(XPS)等表征手段研究了Pt粒子在碳纳米管表面存在的状态、组成、结构等性质. 讨论了Pt/CNTs催化剂的不同制备条件对催化剂结构的影响, 并考察了催化剂对邻氯硝基苯液相加氢合成邻氯苯胺反应的加氢性能. 研究结果表明, 在激光电压为250 V, 绝对压力为300 Pa, 载体温度为25 ℃条件下制备的Pt/CNTs催化剂, 在不加脱卤抑制剂, 反应温度为60 ℃和氢气压力为1.0 MPa的条件下, 邻氯硝基苯转化率可以达到99.7%以上, 邻氯苯胺选择性可达到98.2%以上, 表现出较高的加氢性能和抑制脱卤性能.     

碳纳米管负载铂催化剂的制备、结构及电化学加氢特性

采用浸渍沉淀法制备Pt/CNTs和Pt/C催化剂,并对其结构及电催化性能进行比较,表征.实验表明,以碳纳米管作催化剂载体可使催化剂的负载量,载体上铂的分散度以及其活性中心大大提高.与Pt/C(JohnsonMatthey)催化剂相比,Pt/CNTs的电化学性能表现出更大的活性.碳纳米管作为阴极材料在质子交换膜燃料电池加氢反应器合成化学品中的作用十分明显.     

肉桂醛催化选择加氢反应中双金属的协同效应

对既含有ＣＣ键又含有ＣＯ键的分子,ＣＣ键的选择加氢意义重大［１］．α,β不饱和醛选择加氢成饱和醛就属于此类．钯是已知的可在温和条件下将α,β不饱和醛选择加氢生成饱和醛最有效的催化剂之一．人们曾研究了不同钯化合物催化剂对α,β不饱和醛中ＣＣ的双键选择加...     

多壁碳纳米管负载铂的甲苯加氢脱芳催化剂

以多壁碳纳米管(CNTs)为载体制备了负载型Pt催化剂Pt/CNTs并将其用于催化甲苯加氢脱芳(HDA)反应.结果表明,在1.0%Pt/CNTs催化剂上,在0.4MPa,373K,PhCH3/H2摩尔比=6/94和GHSV=120L/(h.g)的反应条件下,甲苯转化率可达100%,比反应速率为0.0523mmol/(s.m2),分别是γ-Al2O3和AC负载各自最佳Pt负载量催化剂1.4%Pt/γ-Al2O3和2.4%Pt/AC上相应值的1.17和1.18倍.甲苯加氢产物全部为甲基环己烷,其他可能的加氢产物均在气相色谱检测限以下.催化剂的表征研究揭示,用CNTs代替γ-Al2O3或AC作为载体并不会引起所负载Pt催化剂上甲苯HDA反应的表观活化能发生明显变化.与γ-Al2O3或AC负载的相应催化剂相比,一方面,CNTs负载的Pt催化剂易于在较低温度下还原活化,并且其工作态催化剂表面催化活性Pt物种(Pt0)所占表面Pt摩尔分率有所提高;另一方面,CNTs负载的Pt催化剂对H2具有较高的吸附/活化和储存能力.这些促进效应对催化剂HDA活性的提高都有重要贡献.     

碳纳米管结构对碳纳米管载Pt催化剂电催化性能的影响

在制备单、双壁及不同管径的多壁碳纳米管(CNTs)的基础上, 用液相还原法把Pt沉积到单、双壁和管径不同的多壁CNTs上. 发现制得的CNTs载Pt(Pt/CNTs)催化剂对甲醇氧化的电催化活性随CNTs管径减小而增加. 这归结于管径小的CNTs的比表面积较大, 含氧基团多, 有利于提高Pt粒子分散度, 加上管径小的单壁CNTs具有更高的导电性, 这些因素都有利于提高Pt/CNTs催化剂对甲醇氧化的电催化活性.     

铂/酞菁/碳纳米管复合纳米催化剂的构建及其甲醇氧化性能

本文报道了一种方便地构建铂/酞菁/碳纳米管(Pt/Pc/CNTs)复合纳米催化剂的新方法：先通过简单的超声处理将酞菁分子(Pc)修饰至碳纳米管表面,随后采用乙二醇还原法将铂纳米粒子固载到酞菁修饰的碳纳米管表面,形成Pt/Pc/CNTs复合纳米催化剂。X射线衍射(XRD)和透射电镜(TEM)结果表明金属铂纳米颗粒均匀地分散在碳纳米管表面,尺寸约5 nm。采用UV-Vis、FTIR和Raman等手段研究了这种复合纳米催化剂的构建过程,结果表明酞菁分子与碳纳米管之间存在较强的π-π相互作用,使其能牢固地吸附于碳     

具有优异甲醇催化氧化性能的Pt/MoO3-WO3/CNTs催化剂

以聚二烯丙基二甲基胺盐酸盐(PDDA)为连接剂,采用原位自组装方式将MoO3和WO3负载到碳纳米管(CNTs)上,然后通过乙二醇还原法负载Pt纳米颗粒,得到Pt纳米颗粒均匀分布的Pt/MoO3-WO3/CNTs催化剂.当氧化物总量控制在10 wt%,MoO3与WO3摩尔比为1:0.5时,Pt/MoO3-WO3/CNTs催化剂催化甲醇氧化活性最高,甲醇氧化峰电流If高达835 A/gPt.WO3和MoO3的加入提高了催化剂的甲醇氧化活性、抗CO中毒能力和稳定性,使得Pt/MoO3-WO3/CNTs催化剂表现出优异的甲醇电催化氧化性能.     

Pt/CNTs催化剂的制备及其催化臭氧化活性研究

以碳纳米管(CNTs)为催化剂载体, 以H₂PtCl₆•6H₂O为贵金属活性组分前驱物, 采用等体积浸渍法制备了Pt/CNTs催化剂. 以草酸为目标污染物, 考察了所制备催化剂的催化活性, 并采用SEM, XRD和XPS等分析方法对催化剂进行表征. 对活性组分Pt的负载量、氢还原温度和热处理方式进行了研究, 确定了适宜的制备条件为Pt负载量1.0%、氢还原温度350 ℃. 研究表明, 在本实验条件下, 单独臭氧氧化、碳纳米管载体催化臭氧化和Pt/CNTs催化臭氧化分别能去除溶液中3.0%, 72.9%和97.9%的草酸. Pt的负载明显地提高碳纳米管催化臭氧化的效果. XRD分析显示催化剂的活性组分Pt以单质Pt⁰的形式存在; 与氢还原过程相比, 在空气气氛中焙烧制备的Pt/CNTs催化剂表面Pt的结晶度过高, 而且XPS结果表明此催化剂表面的Pt有化学吸附氧存在, 导致催化活性降低.     

Pt-CeO_2/聚苯乙烯磺酸盐功能化碳纳米管复合物的制备及对甲醇的电催化氧化性能

通过阴离子聚合物聚苯乙烯磺酸钠(PSS)对碳纳米管(CNTs)进行非共价功能化修饰得到PSS功能化的碳纳米管(PSS-CNTs),利用带负电的PSS和Ce3+之间的静电作用将Ce3+组装到CNTs表面,再利用Ce3+与Pt Cl2-4之间存在的静电作用和氧化还原反应实现CeO_2和Pt纳米粒子在CNTs表面的原位沉积,得到复合催化剂Pt-CeO_2/PSS-CNTs.采用透射电子显微镜(TEM)、X射线衍射仪(XRD)、能谱仪(EDS)及拉曼光谱仪(Raman)等对催化剂进行了表征.电化学性能测试结果表明,由于PSS-CNTs表面原位沉积的Pt纳米粒子相对于在原始CNTs上沉积的Pt纳米粒子具有更小的粒径、更好的分散均匀性和稳定性,同时Pt与CeO_2之间存在良好的协同效应,Pt-CeO_2/PSS-CNTs催化剂对甲醇电催化氧化具有较好的催化活性和化学稳定性,当nPt/nCe=2/3时催化性能最优.     

Pt/RuO2/CNTs纳米催化剂中RuO2含量对甲醇电催化氧化性能的影响

制备了一种新的甲醇直接燃料电池Pt/RuO2/CNTs阳极催化剂,在相同Pt负载量下,其甲醇电催化氧化活性是Pt/CNTs的3倍.采用循环伏安法研究发现Pt/RuO2/CNTs纳米催化剂中RuO2含量对甲醇电催化氧化活性有明显影响,当Pt和RuO2在碳纳米管上含量分别为15%和9.5%时,Pt/RuO2/CNTs催化剂具有最佳的甲醇电催化氧化活性.RuO2负载在碳纳米管上比电容的变化,反映了水合RuO2结构中质子与电子传输平衡的能力,分析表明,催化剂中RuO2含量不同导致电容的变化是影响甲醇电催化氧化活性的主要原因.当催化剂结构中质子与电子传输达到平衡时,催化剂比电容最大,电催化氧化活性最高.这种基于电容关联电催化剂的观点对甲醇直接燃料电池阳极催化剂的设计非常有意义.     

Studies of the roles of Sn or Fe on γ-Al2O3-supported Pt catalysts by CO adsorption microcalorimetry and dehydrogenation reaction of C4 alkanes

CO adsorption microcalorimetry was employed in the study of γ-Al₂O₃-supported Pt, Pt-Sn and Pt-Fe catalysts. The results indicated that the initial differential heat of CO adsorption of the Pt/γ-Al₂O₃ catalyst was 125 kJ/mol. As CO coverage increased, the differential heat of adsorption decreased. At higher coverages, the differential heat of adsorption decreased significantly. 60% of the differential heat of CO adsorption on the Pt/γ-N₂O₃ catalyst was higher than 100 kJ/mol. No significant effect on the initial differential heat was found after adding Sn and Fe to the Pt/γ-Al₂O₃ catalyst. The amount of strong CO adsorption sites decreased, while the portion of CO adsorption sites with differential heat of 60–110 kJ/mol increased after increasing the Sn or Fe content. This indicates that the surface adsorption energy was changed by adding Sn or Fe to Pt/γ-N₂O₃. The distribution of differential heat of CO adsorption on the Pt-Sn(C)/γ-Al₂O₃ catalyst was broad and homogeneous. Comparison of the dehydrogenation performance of C₄ alkanes with the number of CO adsorption sites with differential heat of 60–110 kJ/mol showed a good correlation. These results indicate that the surface Pt centers with differential heats of 60–110 kJ/mol for CO adsorption possess superior activity for the dehydrogenation of alkanes. Project supported by FORD and the National Natural Science Foundation of China (Grant No. 09412302) and the Transcentury Training Program Foundation for the Talents by The State Education Commission of China.     

The influence of the potassium promoter on the kinetics and thermodynamics of CO adsorption on a bulk iron catalyst applied in Fischer-Tropsch synthesis: a quantitative adsorption calorimetry, temperature-programmed desorption, and surface hydrogenation study

The adsorption of carbon monoxide on an either unpromoted or potassium-promoted bulk iron catalyst was investigated at 303 K and 613 K by means of pulse chemisorption, adsorption calorimetry, temperature-programmed desorption and temperature-programmed surface reaction in hydrogen. CO was found to adsorb mainly molecularly in the absence of H(2) at 303 K, whereas the presence of H(2) induced CO dissociation at higher temperatures leading to the formation of CH(4) and H(2)O. The hydrogenation of atomic oxygen chemisorbed on metallic iron was found to occur faster than the hydrogenation of atomically adsorbed carbon. At 613 K CO adsorption occurred only dissociatively followed by recombinative CO(2) formation according to C(ads) + 2O(ads)→ CO(2(g)). The presence of the potassium promoter on the catalyst surface led to an increasing strength of the Fe-C bond both at 303 K and 613 K: the initial differential heat of molecular CO adsorption on the pure iron catalyst at 303 K amounted to 102 kJ mol(-1), whereas it increased to 110 kJ mol(-1) on the potassium-promoted sample, and the initial differential heat of dissociative CO adsorption on the unpromoted iron catalyst at 613 K amounted to 165 kJ mol(-1), which increased to 225 kJ mol(-1) in the presence of potassium. The calorimetric CO adsorption experiments also reveal a change of the energetic distribution of the CO adsorption sites present on the catalyst surface induced by the potassium promoter, which was found to block a fraction of the CO adsorption sites.     

NiO增强Pt/C催化剂催化氧化甲醇活性的研究

本文基于NiO作为Pt催化甲醇助催化剂的思路,通过Pt纳米颗粒担载在NiO修饰的碳材料载体上制备了Pt/NiO-C催化剂,系统地研究了不同的NiO/C热处理温度对Pt粒径的影响,并重点探讨了Pt对NiO的质量比对催化氧化甲醇的影响。X射线衍射分析结果显示NiO和Pt均为立方晶系,且NiO的加入有利于主催化剂Pt形成较小的粒径,且经400℃热处理NiO修饰的C材料作为载体有利于Pt的有效分散。所获得的Pt/NiO-C催化剂的电化学活性在甲醇酸性溶液中通过循环伏安法(CV)和计时电流法(CA)进行性能测试。CV测试结果显示以Pt/NiO重量比为4∶1的催化剂其电氧化甲醇活性最大,其峰值氧化电流密度达806 mA/mgPt,是Pt/C催化剂的1.64倍。CA测试结果显示Pt/NiO-C比Pt/C具有更好的抗CO中毒性能和稳定性。     

石墨纳米纤维用作质子交换膜燃料电池催化剂载体

利用质子交换膜燃料电池用过的废旧碳纸,采用球磨法制备了石墨纳米纤维(GNF,BET比表面积为229·3m2/g),并以GNF作为载体制备了Pt/GNF催化剂(电化学比表面积为98m2/g).与传统的以VulcanXC-72碳黑为载体的Pt/XC-72催化剂相比,其电化学比表面积及Pt粒径大小相近.采用恒电位氧化法考察了GNF,XC-72,Pt/GNF和Pt/XC-72的电化学稳定性.结果表明,在相同条件下,XC-72的峰电流增加了60%,而GNF增加了2%;Pt/XC-72的腐蚀电流比Pt/GNF的大40%;恒电位氧化60h后,Pt/XC-72约有84·7%的电化学比表面积损失,Pt/GNF仅损失37·2%.这表明GNF的抗腐蚀性优于XC-72,有希望成为质子交换膜燃料电池抗腐蚀的催化剂载体.     

Ir/CNTs催化剂的制备及对氨的电催化氧化

分别以碳纳米管(CNTs)和XC-72活性碳为载体制备了Ir/CNTs和Ir/C催化剂. X射线衍射(XRD)结果显示, CNTs拥有更高的石墨化程度. 电化学研究结果表明, 与Ir/C催化剂相比, Ir/CNTs对氨氧化具有更高的电流密度、更低的起始氧化电位和更好的稳定性. 同时, Ir/CNTs催化剂对氨检测的线性范围更宽, 灵敏度更高, 检出限更低.     

Thermodynamics of carbon monoxide adsorption on polycrystalline titania studied by static adsorption microcalorimetry

The adsorption of CO on polycrystalline TiO2 was investigated by static adsorption microcalorimetry. The initial differential heat of adsorption (qdiff,0) of CO on polycrystalline titania is 40 kJ/mol, and the standard adsorption entropy (Deltas0) is -104 J mol(-1) K(-1). These results are consistent with those derived from temperature-programmed desorption and FTIR results in the literature. The good reproducibility of the isotherms and the stable qdiff indicate that the lattice oxygen and hydroxyl groups on titania surface are basically not reactive to adsorbed CO.     

Heat of adsorption of naphthalene on Pt(111) measured by adsorption calorimetry

The heat of adsorption of naphthalene on Pt(111) at 300 K was measured with single-crystal adsorption calorimetry. The heat of adsorption on the ideal, defect-free surface is estimated to be (300 - 34 - 199(2)) kJ/mol. From this, a C-Pt bond energy for aromatic hydrocarbons on Pt(111) of approximately 30 kJ/mol is estimated, consistent with earlier results for benzene on Pt(111). There is higher heat of adsorption at very low coverage, attributed to step sites where the adsorption heat is >/=330 kJ/mol. Saturation coverage, = 1 ML, corresponds to 1.55 x 10(14) molecules/cm(2). Sticking probability measurements of naphthalene on Pt(111) give a high initial value of 1.0 and a Kisliuk-type coverage dependence that implies precursor-mediated sticking. The ratio of the hopping rate to the desorption rate of this precursor is approximately 51. Naphthalene adsorbs transiently on top of chemisorbed naphthalene molecules with a heat of adsorption of 83-87 kJ/mol.     

酸处理石墨化碳载体对燃料电池催化剂性能的影响

通过1700 ℃高温处理XC-72CB得到石墨化碳黑(GCB), 并采用酸处理对GCB碳载体进行官能团修饰. 透射电子显微镜(TEM)、 X射线粉末衍射(XRD)和拉曼光谱的结果显示, 酸处理后GCB的石墨化程度增加; N₂吸附-脱附结果证明GCB比表面积减小, 微孔数量减少; 热重分析结果表明, GCB热稳定性增强; 红外光谱和拉曼光谱结果显示, GCB表面引入了含氧官能团, 并同时保持了GCB的有序化结构. 采用循环伏安(CV)法和线性扫描伏安(LSV)法测试了不同预处理后催化剂的电化学性能, 表明其电化学活性表面积(ECSA, 75.25 m²/g)和质量比活性(MA, 0.093 A/mg)均高于商业Pt/C(JM)催化剂. TEM结果表明, 使用经过浓硫酸和浓硝酸混合酸处理的GCB(简称OGCB)作为载体得到的Pt/OGCB平均粒径为2.28 nm, 略小于商业Pt/C(JM)催化剂(约2.5 nm); 经5000周电化学循环伏安测试后, Pt/OGCB的电化学活性表面积衰减17.3%, 质量比活性衰减29.5%, 而Pt/C(JM)的ECSA衰减达到25.1%, MA衰减达到42.5%.     

Effect of rare earths on selective hydrogenation of p-chloronitrobenzene over PtMOx/CNTs catalysts

The effect of rare earths(Sm,Pr,Ce,Nd and La)on the hydrogenation properties of p-chloronitrobenzene(CNB)over Pt/CNTs catalyst was studied in ethanol at 303 K and normal pressure.The results exhibited that the hydrogenation of p-CNB could be carded out over PtMOx/CNTs catalysts.Both catalytic activities and yields of p-chloroaniline(CAN)were all improved.PtCeOx/ CNTs catalyst exhibited the best catalytic activity(TOF was 0.47 s~(-1))and the highest yield of p-CAN(97.5 mol%).PtCeOx/CNTs (1.0 wt%)catalyst ...     

新型阳极材料Pt-Ru/CMK-3的制备与性能研究

通过在多元金属体系中加入络合剂四氢呋喃(THF), 改变其热力学参数进而改变其动力学还原速率, 在低温下同时还原金属Pt和Ru, 制备了高分散、高合金化的Pt-Ru固溶体并均匀担载在有序介孔碳CMK-3上, 以形成二元复合金属催化剂. XRD图谱表明, f.c.c结构中Pt原子部分被h.c.p结构中Ru原子取代形成置换固溶体, 且几乎没有未合金的Ru存在. TEM, XRD和N₂吸附-脱附研究显示, Pt-Ru/CMK-3催化剂中Pt-Ru合金粒子的平均粒径为3.2 nm, 且具有良好的均一度. 还研究了催化剂对甲醇的电催化氧化性能, 并与E-TEK公司同类催化剂进行了对比. 结果显示, Pt-Ru/CMK-3催化剂拥有较大的电化学活性面积, 对甲醇的电催化氧化性能和抗CO中毒能力明显优于其他同类催化剂.