Simultaneous removal of ethanol, acetaldehyde and nitrogen oxides over V-Pd/γ-Al_2O_3-TiO_2 catalyst

V-Pd/γ-Al2O3-TiO2 catalysts with different vanadium contents were prepared by a combined sol-gel and impregnation method. X-ray diffraction (XRD), N2 adsorption-desorption (BET), X-ray photoelectron spectroscopy (XPS) and catalytic removal of ethanol, acetaldehyde and nitrogen oxides at low temperature (<300 ?C) were used to assess the properties of the catalysts. The results showed that the sample with 1wt% vanadium exhibited an excellent catalytic performance for simultaneous removal of ethanol, acetaldehyde and nitrogen oxides. The conversions of ethanol, acetaldehyde and nitrogen oxides at 250 ?C were 100%, 74.4% and 98.7%, respectively. V-Pd/γ-Al2O3-TiO2 catalyst with 1 wt% vanadium showed the largest surface area and higher dispersion of vanadium oxide on the catalyst surface, and possessed a larger mole fraction of V4+ species and unique PdO species on the surface, which can be attributed to the strong synergistic effect among palladium, vanadium and the carriers. The higher activity of V-Pd/γ-Al2O3-TiO2 catalyst is related to the V4+ and Pd2+ species on the surface, which might be favorable for the formation of active sites.     

The role of bismuth as promoter in Pd–Bi catalysts for the selective oxidation of glucose to gluconate

Bismuth is a well-established promoter of noble metal-based catalysts for the selective liquid phase oxidation of alcohols, aldehydes and carbohydrates with molecular oxygen. Experiments were carried out to improve the understanding of the promoting role of bismuth in bimetallic Pd–Bi catalysts used for the selective oxidation of glucose to gluconate. In relationship with the fact that these catalysts undergo substantial bismuth leaching under the reaction conditions, particular attention was paid to the possible role played by the soluble fraction of bismuth in the oxidative process. Carbon-supported Pd–Bi/C catalysts characterized by various Bi–Pd compositions (0.33≤Bi/Pd≤3.0,10 wt.%Pd+Bi) were prepared from acetate-type precursors, tested under various experimental conditions and analyzed by X-ray diffractometry and X-ray photoelectron spectroscopy (XPS). Whatever the initial catalyst composition, the surface intensity ratio measured by XPS in used catalysts lies in the range 0.4–0.6, suggesting that the dynamic state of the catalyst involves the association of one Bi and two to three Pd atoms. The leaching process and the promoting effect itself are discussed in line with the formation of Bi–glucose and Bi–gluconate complexes present in solution but also as adsorbed species at the catalyst surface. The performances of a monometallic Pd/C catalyst are significantly improved in the presence of adequate amounts of soluble Bi. The involvement of the soluble fraction of bismuth in the overall mechanistic scheme of glucose oxidative dehydrogenation is suggested. The detrimental effect of large amounts of soluble bismuth is attributed to a too extensive adsorption of Bi–glucose complexes on the surface Pd atoms.     

Catalytic methanol decomposition to carbon monoxide and hydrogen over Pd/CeO2-ZrO2-La2O3 with different Ce/Zr molar ratios

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     

Oxidative carbonylation of phenol to diphenyl carbonate catalyzed by palladium complexes bridged with N,N‐ligands over functionalized silica

Heterogeneous palladium catalysts anchored on functionalized silica were prepared by sol–gel methods and their catalytic properties for the oxidative carbonylation of phenol to diphenyl carbonate (DPC) were investigated. The catalysts were characterized by means of IR, XPS, EA and BET. The Pd loading in the heterogeneous catalysts and leaching in solution were detected by atomic absorption. The effects of different reaction parameters such as temperature, solvent and inorganic cocatalyst on the yield of DPC and Pd leaching were also studied. It was found that Cu₂O and tetrahydrofuran (THF) were the best partners with these heterogeneous catalysts. In the presence of 3 Å molecular sieves as dehydrating agent, the heterogeneous palladium catalyst prepared from 2‐acylpyridine revealed excellent catalytic performance and stability at 110 °C for 5 h, giving 13.7% yield of DPC based on phenol and 4.0% Pd loss in solution. The heterogeneous catalyst was more active and stable compared with traditional supported Pd? C catalyst under the same reaction conditions. Copyright © 2005 John Wiley & Sons, Ltd.     

不同温度焙烧的Au-Pd/SiO2催化剂上甲醇选择性氧化制备甲酸甲酯

以溶胶固定法制备了Au-Pd/SiO₂催化剂,考察了催化剂焙烧温度对甲醇选择氧化制甲酸甲酯反应性能的影响。在200~500℃,400℃焙烧的Au-Pd/SiO₂具有最好的低温催化性能,在室温下就有活性,反应温度为100℃时甲醇转化率为25.3%,甲酸甲酯的选择性为100%。采用BET、XRD、UV-vis DRS、XPS、TEM和DRIFTS技术对催化剂进行表征,结果表明,催化剂中活性组分Au和Pd的高分散性,合适的Au和Pd粒径,Au-Pd合金的形成以及Au和Pd之间的强相互作用力,有利于甲醇氧化为甲酸甲酯反应的进行。初步推测出了甲醇在Au-Pd/SiO₂上氧化为甲酸甲酯的反应机理,甲醇在Au-Pd/SiO₂催化剂上是通过甲氧基中间体得到甲酸甲酯的。     

改性三氧化二铬催化1,1,3,3-四氯丙烯氟化高选择性合成反式-1-氯-3,3,3-三氟丙烯研究

反式-1-氯-3, 3, 3-三氟丙烯 (HCFO-1233zd (E))是近年来正在研发的第四代发泡剂,其大气臭氧消耗潜能值为0.00024,温室效应潜能值为7.0,毒性低,常态下不燃,使用安全;它也是合成含氟精细化工品的中间体,以及合成氟树脂和氟弹性体的单体。本论文制备了Al,Zn,Co改性的Cr2O3催化剂,将其成功应用于1, 1, 3, 3-四氯丙烯（HCC-1230za）与氟化氢反应中,高选择性地合成HCFO-1233zd (E),复合催化剂Zn / Cr2O3显示高稳定性,其中HCC-1230za转化率高达99.4％,HCFO-1233zd（E）的选择性高达98.2％。反应条件诸如反应物HF / HCC-1230za 的摩尔比和反应温度等对产物分布有显着影响。在相对较低的温度（200?C）和较大的HF / HCC-1230za 摩尔比（10：1）下,对HCFO-1233zd（E）的选择性有利。通过XRD,XPS,BET和V70吡啶吸附红外光谱技术对复合催化剂Zn / Cr2O3进行了表征。 XRD结果表明,催化剂中大多数无定形Cr2O3和高度分散微晶相Cr2O3共同导致催化剂的高活性和高稳定性。HCC-1230za的转化率与预氟化处理催化剂Zn / Cr2O3的比表面积有关,催化剂的比表面积越高,催化活性越高。XPS光谱表明,在预氟化过程中,表面铬氧化物可能与F原子强烈相互作用,从而导致Cr原子的化学环境发生广泛变化。V70吡啶吸附红外光谱和氨-程序升温脱附技术结果证明尚未失活的催化剂Lewis 酸和Br?nsted酸中心的数目和强度与新制备的催化剂相比明显提高。     

一步液滴法合成酸性和孔道属性可调的硅铝酸盐载体及其Pd基催化剂的性能研究

通过一步液滴法在不同的反应溶剂体系下制备了一系列无定形硅铝酸盐载体, 并进一步制备出Pd基负载型多孔催化材料, 探究了反应溶剂极性和反应物Si/Al比对载体材料和催化剂的影响, 实现了通过一步液滴法调控硅铝酸盐酸性和孔道属性. 结果表明, 在极性较小的反应溶剂体系中制得了富含介孔的无定形硅铝酸盐载体材料, 并且通过改变Si/Al比可实现载体材料的酸性、 比表面积及孔道尺寸的调控, 比表面积和总酸量分别达到349.6 m²/g和1.389 mmol/g. 由于该载体材料高的比表面积及丰富的介孔孔道, 所制得的Pd基负载型多孔催化材料的Pd金属分散性达到了63.17%, 在硝基苯加氢反应中实现了99.75%的转化率和94.62%的选择性, 在苯甲醇氧化反应中表现出40.61%的转化率及38.09%的选择性, 远远优于利用商用载体合成的 Pd/Al₂O₃催化材料. 这种简单有效的合成方法使得按照目标催化反应的类型来设计高效催化剂成为可能.     

Cu改性ZIF-67衍生的Co3O4/C催化剂的CO-SCR脱硝特性

采用CO气体对NO进行选择性催化还原(CO-SCR)是一种有前景的脱硝技术.目前已报道的CO-SCR催化剂的脱硝特性主要是在无氧条件下开展的研究,考虑到实际应用情况,探究一种在有氧环境中具有较高脱硝效率的催化剂是很有必要的.作为一种新型功能性材料的金属有机骨架是脱硝催化剂的优良载体,其中ZIFs系列具有优良的性能.引入Cu对ZIF-67衍生的Co₃O₄/C进行改性,通过浸渍法在载体上负载铜后,热解氧化获得一系列CuO_x/Co₃O₄/C催化剂.利用ICP、 SEM、 XRD、 TEM、 TGA、 XPS、 BET和H₂-TPR等技术对催化剂的物理化学性质进行表征,结果表明,由于Cu的引入增加了表面的氧空位,改善了氧化还原能力,进而提高了催化剂脱硝活性.在制备的一系列催化剂中, 8.0 CuO_x/Co₃O₄/C在300℃时即可达到约95%NO转化率,并且其N₂选择性也达到9...     

Pd-Cu/ZrO2催化CO2加氢制甲醇的性能

采用溶胶-凝胶法制备了n(Cu):n(Zr)=1:1、1:2、1:4和1:8的Cu/ZrO₂催化剂。 实验结果表明,当n(Cu):n(Zr)=1:4时,催化剂表现出较高的CO₂转化率(8.0%)和甲醇选择性(59.5%),为了增加CO₂的转化率,提高甲醇选择性,在n(Cu):n(Zr)=1:4的催化剂中添加质量分数1%的Pd,采用浸渍法制备了Pd-Cu/ZrO₂催化剂。 在250 ℃、2 MPa、12000 mL/(g·h)和V(H₂):V(CO₂)=3:1的反应条件下,CO₂转化率和CH₃OH收率相比Cu/ZrO₂催化剂(n(Cu):n(Zr)=1:4)分别提高了40.0%和80.9%。 通过X射线衍射仪(XRD)、傅里叶变换红外光谱仪(FT-IR)、N₂吸附-脱附(BET)、X射线光电子能谱仪(XPS)和程序升温还原化学吸附仪(H₂-TPR)等仪器表征证明Pd的添加提高了催化剂的分散性和比表面积。 催化剂中Pd和Cu之间强相互作用,使Cu2p轨道结合能向低处偏移,还原温度的降低,说明Pd-Cu/ZrO₂催化剂还原能力增强,使得CO₂加氢活性提高。     

Catalytic methanol decomposition to carbon monoxide and hydrogen over Pd/CeO2-ZrO2-La2O3 with different Ce/Zr molar ratios

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/Ce_0.76Zr_0.18 La_0.06O_1.97 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/Ce_0.76Zr_0.18La_0.06O_1.97 catalyst exhibited the best activity. A 100% conversion of methanol was achieved at around 260 °C, which was about 20-40 °C lower than other catalysts