Catalytic oxidation of methane at low temperature over Pd-containing perovskite type oxides

Two types of catalysts with the same palladium loading, palladium-substituted perovskite La_0.95Ce_0.05Co_0.95Pd_0.05O₃ and perovskite-supported palladium catalyst Pd/La_0.95Ce_0.05CoO₃ were prepared by the combustion and impregnation method, respectively. The catalyst structure was characterized by X-ray diffraction (XRD), BET measurements, temperature-programmed reduction (TPR) and the methane oxidation activity of the catalysts were investigated in detail. It was found that the activity performance of Pd/La_0.95Ce_0.05CoO₃ was higher than that of La_0.95Ce_0.05Co_0.95Pd_0.05O₃, and this was owing to the ease of reduction of palladium in the former.     

Catalytic properties of La0.8Sr0.2Co0.5M0.5O3 (M Co, Ni, Cu) in methane combustion1

A set of perovskite-type catalysts of general formula La_0.8Sr_0.2Co_0.5M_0.5O₃ (M = Co, Ni, Cu) were prepared by alanine solution combustion method and used successfully for the methane combustion. The property of these materials were characterized by XRD, and TPR measurements. The effects of transition-metal ions on site B on structure and performance of the catalysts were studied. The result indicated that the structure and catalytic activities of the catalysts can remarkably affect by transition-metal ions on site B, the decrease of the electrons filled in d orbitals in the atom on site B is propitious to increase the catalytic activity for methane combustion, and the sequences of catalysts activities are La_0.8Sr_0.2CoO₃ τ; Ce_0.8Sr_0.2CoO₃ τ; Nd_0.8Sr_0.2CoO₃.     

Distinctive features of supported catalysts prepared from platinum carbonyl clusters

The formation of Pt/γ-Al₂O₃ and Pt/C catalysts from platinum carbonyl clusters H₂[Pt₃(CO)₆]_n (n = 2, 5) is studied. The strength of interaction between clusters (strong Lewis bases) and the support and the state of platinum in catalysts are governed by the acceptor strength of the support. The formation of a stable platinum compound with a surface of γ-Al₂O₃ (strong Lewis acid) is shown for a Pt/γ-Al₂O₃ catalyst by the method of radial distribution functions. In a Pt/C catalyst containing the same amount of Pt supported on a carbon material known to be a weaker acceptor, metallic platinum is formed along with surface-bonded platinum. Proceeding from the existence of the active phase of catalysts in the form of a surface platinum complex and platinum crystallites, the properties of catalysts are discussed in the complete oxidation of methane and the dehydrogenation of cyclohexane, as well as the high dispersity of platinum and its thermal stability     

Electrocatalysis and redox behavior of Pt2+ ion in CeO2 and Ce0.85Ti0.15O2: XPS evidence of participation of lattice oxygen for high activity

Electronic states of CeO₂, Ce_1????em>x Pt _x O_2????em>δ , and Ce_{1????em>x????em>y} Ti _y Pt _x O_2????em>δ electrodes have been investigated by X-ray photoelectron spectroscopy as a function of applied potential for oxygen evolution and formic acid and methanol oxidation. Ionically dispersed platinum in Ce_1????em>x Pt _x O_2????em>δ and Ce_{1????em>x????em>y} Ti _y Pt _x O_2????em>δ is active toward these reactions compared with CeO₂ alone. Higher electrocatalytic activity of Pt²⁺ ions in CeO₂ and Ce_1????em>x Ti _x O₂ compared with the same amount of Pt⁰ in Pt/C is attributed to Pt²⁺ ion interaction with CeO₂ and Ce_1????em>x Ti _x O₂ to activate the lattice oxygen of the support oxide. Utilization of this activated lattice oxygen has been demonstrated in terms of high oxygen evolution in acid medium with these catalysts. Further, ionic platinum in CeO₂ and Ce_1????em>x Ti _x O₂ does not suffer from CO poisoning effect unlike Pt⁰ in Pt/C due to participation of activated lattice oxygen which oxidizes the intermediate CO to CO₂. Hence, higher activity is observed toward formic acid and methanol oxidation compared with same amount of Pt metal in Pt/C.     

Bimetallic Pd—Pt/γ-Al<Subscript>2</Subscript>O<Subscript>3</Subscript> catalysts for complete methane oxidation: the effect of the Pt: Pd ratio

Alumina-supported bimetallic Pt—Pd catalysts proved to be more active in the complete oxidation of methane than monometallic systems (Pt/Al₂O₃, Pd/Al₂O₃). The maximum activity of the bimetallic catalysts was achieved at ~40 at.% Pt in Pd on the catalyst surface. After the oxidation reaction, redistribution of platinum and palladium was observed in the active component of the catalysts with the degree of redistribution depending on the initial Pt: Pd ratio.     

La<Subscript>0.1</Subscript>Ca<Subscript>0.9</Subscript>MnO<Subscript>3</Subscript>/Co<Subscript>3</Subscript>O<Subscript>4</Subscript> for oxygen reduction and evolution reactions (ORER) in alkaline electrolyte

Non-precious metal bifunctional catalysts are of great interest for metal–air batteries, electrolysis, and regenerative fuel cell systems due to their performance and cost benefits compared to the Pt group metals (PGM). In this work, metal oxides of La_0.1Ca_0.9MnO₃ and nano Co₃O₄₇ catalyst as bifunctional catalysts were used in oxygen reduction and evolution reactions (ORER). The catalysts were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), transmission electron microscopy (TEM), and N₂ adsorption isotherms. The electrocatalytic activity of the perovskite-type La_0.1Ca_0.9MnO₃ and Co₃O₄ catalysts both as single and mixtures of both were assessed in alkaline solutions at room temperature. Electrocatalyst activity, stability, and electrode kinetics were studied using cyclic voltammetry (CV) and rotating disk electrode (RDE). This study shows that the bifunctional performance of the mixed La_0.1Ca_0.9MnO₃ and nano Co₃O₄ was superior in comparison to either La_0.1Ca_0.9MnO₃ or nano Co₃O₄ alone for ORER_. The improved activity is due to the synergistic effect between the La_0.1Ca_0.9MnO₃ and nano Co₃O₄ structural and surface properties. This work illustrates that hybridization between these two metal oxides results in the excellent bifunctional oxygen redox activity, stability, and cyclability, leading to a cost-effective application in energy conversion and storage, albeit to the cost of higher catalyst loadings.     

Standard enthalpies of formation of LaxCe1−x CoO3 compounds

An isothermal-jacket calorimeter was used to measure the enthalpies of the reactions of CeCl₃(cr) and La_xCe_1?x CoO₃(cr) (x = 0.80, 0.85, 0.90, and 0.95) with a 2m hydrochloric acid solution. Based on these values and published data, the standard enthalpy of formation of La_xCe_1?x CoO₃(cr) was calculated for the above x values at 298.15 K.     

SO2对La0.8K0.2Cu0.05Mn0.95O3钙钛矿催化剂氧化碳烟的影响

采用柠檬酸配位法制备K、Cu掺杂的Lu0.8K0.2Cu0.05Mn0.95O3钙钛矿催化剂,运用程序升温氧化(TPO)考察在不同浓度SO2气氛下La0.8K0.2Cu0.05Mn0.95O3催化剂催化氧化模拟碳黑的性能,并用XRD、FFIR和XPS等进行表征.结果表明,催化剂在0～0.1%的SO2气氛中呈现出不同活性,φSO2≤0.05%的气氛可促进催化剂催化氧化碳黑的活性,当φSO2=0303%,催化剂活性最高;引入φSO2≥0.06%时催化剂活性明显下降.XPS说明表面活性氧的增加是低浓度的SO2促进催化活性的原因,同时XRD、FTIR结果表明高浓度的SO2所产生的大量SO42-是抑制催化剂活性的原因.     

Synthesis, hydrothermal stability and thermal reaction behavior of nepheline hydrate i (NH I)

Summary The activity of Pt/Ce_1-xGd_xO_2-y samples in steam and dry reforming of methane at short contact times correlates with the lattice oxygen mobility. For the partial oxidation of methane (POM), the oxygen mobility should be optimized to prevent methane combustion.     

Preparation of mesoporous CexCoO as highly effective catalysts for toluene combustion: The synergetic effects of structural template and Ce doping

Cobalt‐based catalyst, as a typical catalyst for volatile organic compounds (VOCs) combustion, has attracted extensive attention. However, the catalytic activity of pure Co₃O₄ is difficult to meet the requirements of practical application especially at low temperatures. Therefore, it is key to find an effective way to improve the catalytic performance of Co₃O₄. In this paper, Co₃O₄ is modified by engineering a combination of structural template and Ce dopant. The various characterization results verify that the template agent and the doping of appropriate Ce lead to great changes in the texture property and low temperature reducibility of Co₃O₄, thus resulting in superior catalytic performances of obtained mesoporous Ce_xCoO catalysts. In particular, the best catalyst, Ce_0.05CoO, achieves a toluene conversion of T_90% at 238°C, which is significantly lower than many of the Co‐based catalysts reported in previous literatures. Furthermore, the toluene conversion rate maintains above 90% during 100 h at 238°C. The excellent catalytic performance of Ce_0.05CoO can be attributed to its large specific surface area, uniform pore structure, good low temperature reducibility, and abundant surface oxygen species.     

Effect of Substitution of Cobalt for Iron in Sr4Fe6O13-δon the Catalytic Activity for Methane Combustion

A series of mixed oxides Sr₄Fe_6?xCo_xO_13?δ (x=0, 1, 2, 3, or 4) were prepared by sol‐gel method and used for catalytic combustion of methane. The structural properties of oxides were characterized by XRD, TGA, and XPS. The layered intergrowth perovskite‐like oxide Sr₄Fe₅CoO_13?δ exhibits the highest catalytic activity for methane combustion under the experimental conditions. The enhanced catalytic activity of Sr₄Fe₅CoO_13?δ for methane combustion could be attributed to the increased amount of oxygen vacancy caused by the partial substitution of cobalt for iron in the Sr₄Fe₆O₁₃, which was confirmed by TGA and XPS.     

Design of coke-free methane dry reforming catalysts by molecular tuning of nitrogen-rich combustion precursors

The valorization of methane and carbon dioxide is a promising solution for mitigating global warming. The dry reforming of methane (DRM) is capable of concomitant conversion of these greenhouse gases into starting materials for production of synthetic fuels, promoting a carbon neutral avenue for fuel production. The development of efficient, stable, and economic catalysts presents a challenge owing to the comparatively rapid deactivation of DRM catalysts under reaction conditions. Here, Ni/La₂O₃ DRM catalysts are prepared by combustion synthesis of Ni and La complexes of nitrogen-rich precursors. We expound the relationship between structures of the combustion precursors, the thermochemistry of their combustion, the structures of the resultant Ni/La₂O₃ catalysts, and their performance under DRM conditions. We show that the best catalyst is derived from energetic precursor which has the sharpest exotherm and rapidly releases the largest amounts of nitrogen gas. These properties give rise to the crystallization of the Ni/La₂O₃ catalyst with high Ni dispersion and strong metal-support interactions. This work can act as starting point to expand the link between the chemistry of combustion precursors and the resulting catalyst properties, eventually realizing the rational design of high-performance catalysts prepared by combustion synthesis through tailoring the chemistry and structure of the nitrogen-rich precursors.     

Synthesis of Pt3Ni-based functionalized MWCNTs to enhance electrocatalysis for PEM fuel cells

Nanoscale Pt₃Ni/functionalized multiwalled carbon nanotubes (FMWCNTs) catalysts, successfully synthesized by anchoring nickel–platinum alloy nanoparticles on FMWCNTs, are presented in this paper. Compared with conventional commercial Pt/C catalysts, the preliminary results revealed that the Pt₃Ni/FMWCNTs catalysts demonstrated not only higher specific activity for oxygen reduction reaction (ORR) but also outstanding stability. The enhancement in the stability of the Pt₃Ni/FMWCNTs catalysts is believed to be due to the anchor effects in Pt₃Ni alloy structure, the stronger interaction between Pt₃Ni alloy nanoparticles and FMWCNTs, and the “π sites” anchoring centers for metal nanoparticles from CNTs with high graphite.     

Effect of Ru Substitution in La0.85Sr0.15CoO3 towards Oxygen Evolution Reaction: Activity of Ionic Ru

Nano crystalline La_0.85Sr_0.15CoO₃ and ruthenium doped compounds (La_0.85Sr_0.15Co_0.9975Ru_0.0025O_3, La₀.₈₅Sr_0.15Co_0.995Ru_0.005O_3, La_0.85Sr_0.15Co_0.99Ru_0.01O₃) are synthesized using solution combustion method. Completely characterized samples are studied for electrochemical OER in neutral and basic medium. Significant enhancement in catalytic activity is noticed once Ru is substituted in the cobalt site. With higher doping level of Ru, capacitance also increases as depicted in the CV behavior. Tafel slope measurements indicate that Ru substitution has profound effect as enhancement in the exchange current density is observed in neutral K₂SO₄ medium. Enhancement is anticipated due to substitution of Ru, as the RuO₂ mixed catalyst does not give similar activity.     

Ce0.5Zr0.5O2修饰的Ni/SiC、Fe/SiC和Co/SiC催化燃烧甲烷性能

以铈锆固溶体（Ce_0.5Zr_0.5O₂）修饰的高比表面积SiC为载体,采用两步浸渍法制备了Ni、Fe和Co基催化剂,研究了其在煤层气催化燃烧脱氧中的催化活性和稳定性. 利用X射线衍射（XRD）、X射线光电子能谱（XPS）、电感耦合等离子体质谱（ICP-MS）、高分辨透射电子显微镜（HRTEM）、比表面积（BET）、热重分析（TGA）和H₂程序升温还原（H₂-TPR）对催化剂进行了表征. 分析结果表明,Ni、Fe和Co部分进入Ce_0.5Zr_0.5O₂固溶体晶格内部,导致催化剂体相形成更多的缺陷;同时Ce_0.5Zr_0.5O₂固溶体有助于加速金属氧化物和金属之间氧化还原过程的进行,促进了氧吸附、传输和对甲烷的活化. 另外,SiC和Ce_0.5Zr_0.5O₂固熔体良好的抗积碳性能,有效避免了催化剂在富甲烷反应气氛中因积碳而失活,从而使三种催化剂均具有优良的催化燃烧脱氧活性和稳定性. 其中,Co/Ce_0.5Zr_0.5O₂/SiC活性最高,可在320 ℃活化催化甲烷,并在410 ℃实现完全脱氧.     

Improvement of electrochemical properties of LiNi1/3Mn1/3Co1/3O2 by coating with La0.4Ca0.6CoO3

In this paper, La_0.4Ca_0.6CoO₃-coated LiNi_1/3Mn_1/3Co_1/3O₂ is successfully prepared by the sol–gel method associated with microwave pyrolysis method. The structure and electrochemical properties of the La_0.4Ca_0.6CoO₃-coated LiNi_1/3Co_1/3Mn_1/3O₂ are investigated by using X-ray diffraction (XRD), electrochemical impedance spectroscopy (EIS), and charge/discharge tests. XRD analyses show that the La_0.4Ca_0.6CoO₃ coating does not change the structure of LiNi_1/3Co_1/3Mn_1/3O₂. The electrochemical performance studies demonstrate that 2 wt.% La_0.4Ca_0.6CoO₃-coated LiNi_1/3Co_1/3Mn_1/3O₂ powders exhibit the best electrochemical properties, with an initial discharge capacity of 156.9 mAh g^–1 and capacity retention of 98.9 % after 50 cycles when cycled at a current density of 0.2 C between 2.75 and 4.3 V. La_0.4Ca_0.6CoO₃ coating can improve the rate performance because of the enhancement of the surface electronic/ionic transportation by the coating layer. EIS results suggest that the coating La_0.4Ca_0.6CoO₃ plays an important role in suppressing the increase of cell impedance with cycling especially for the increase of charge-transfer resistance.     

Study of the local structure of supported nanostructural platinum catalysts

The possibility of controlling the state of platinum deposited on the support surface via minor changes in the catalyst preparation procedure is demonstrated using a series of highly dispersed Pt/γ-Al₂O₃ catalysts with different particle size of the active component. Dispersity, local structure and electronic state of supported platinum were examined by a combination of high resolution transmission electron microscopy and X-ray absorption spectroscopy (EXAFS/XANES). It was shown that various platinum species can be obtained on the surface of the support: bulk or surface Pt(II) or Pt(IV) oxides, mixed metal-oxide structures, bulk particles of metallic platinum, and two-dimensional surface Pt⁰ particles strongly interacting with the support.     

Effect of stoichiometric ratio of organic fuel to oxidizer on performance of La0.8Sr0.2CoO3 catalysts for CH4 combustion

Perovskite-type La_0.8Sr_0.2CoO₃ mixed oxides were prepared by d,l-alanine solution combustion synthesis and used successfully in CH₄ combustion as catalysts. These samples were characterized by means of XRD, FTIR, BET, and H₂-TPR methods. The effects of stoichiometric ratio (φ) of organic fuel to oxidizer on the structure and catalytic activities of the catalysts were studied. The results indicate that all La_0.8Sr_0.2CoO₃ mixed oxides with different φ have perovskite structures. Their structures and catalytic activities vary along with the change of φ. The catalytic activity of La_0.8Sr_0.2CoO₃ mixed oxide with φ = 1.52 is the best among all the samples, whose T ₅₀ and T ₁₀₀ (the temperatures of methane conversions reaching 50 and 100%, respectively) are respectively 470 °C and 550 °C, which can be explained in terms of the smaller of average crystal size, higher specific surface area, bigger lattice distortion, lower activation energy, and higher mobility of chemically adsorbed oxygen on the surface and vacancy of the catalysts.     

Promotional effect of cobalt addition on catalytic performance of Ce<Subscript>0.5</Subscript>Zr<Subscript>0.5</Subscript>O<Subscript>2</Subscript> mixed oxide for diesel soot combustion

A series of Co-modified Ce_0.5Zr_0.5O₂ catalysts with different concentrations of Co (mass %: 0, 2, 4, 6, 8, 10) was investigated for diesel soot combustion. Ce_0.5Zr_0.5O₂ was prepared using the coprecipitation method and Co was loaded onto the oxide using the incipient wetness impregnation method. The activities of the catalysts were evaluated by thermogravimetric (TG) analysis and temperature-programmed oxidation (TPO) experiments. The results showed the soot combustion activities of the catalysts to be effectively improved by the addition of Co, 6 % Co/Ce_0.5Zr_0.5O₂ and that the 8 % Co/Ce_0.5Zr_0.5O₂ catalysts exhibited the best catalytic performance in terms of lower soot ignition temperature (T_i at 349°C) and maximal soot oxidation rate temperature (T_m at 358°C). The reasons for the improved activity were investigated by X-ray diffraction (XRD), Brunauer–Emmett–Teller (BET), H₂ temperature-programmed reduction (H₂-TPR), X-ray photoelectron spectroscopy (XPS) and transmission electron microscopy (TEM). These results revealed that the presence of Co could lower the reduction temperature due to the synergistic effect between Co and Ce, thereby improving the activity of the catalysts in soot combustion. The 6 % Co catalyst exhibited the best catalytic performance, which could be attributed to the greater amounts of Co³⁺ and surface oxygen species on the catalyst.     

Effects of Ethanol Impregnation on the Catalytic Properties of Silica-Supported Cobalt Catalysts

Silca-supported Co₃O₄ (6 wt% as Co) catalysts were prepared by pore volume impregnation of ethanol or aqueous cobalt nitrate solutions, and calcined in vacuo to 300 °C. The catalytic performances of these catalysts for oxidation and hydrogenation of CO were examined. All Co₃O₄/SiO₂ catalysts were found to be very active in catalyzing oxidation of CO to CO₂ as compared to a commercial 1 wt% Pt/Al₂O₃. The ethanol-prepared catalysts exhibited higher activity than those of the aqua-prepared catalysts. Pre-calcination of the ethanol-prepared catalysts in oxygen at 600 °C resulted in a dramatic decrease in the activity. Temperature programmed oxidation indicated the presence of carbon deposits on the surface of used catalysts. Infrared spectra showed the continuous generation of CO₂ when these catalysts were exposed to CO. These indicate the primary role of CO disproportionation in catalytic oxidation of CO on Co₃O₄ at low temperature and explain the sharp decrease in activity in the initial period. After reduction at 400 °C, the ethanol-prepared catalysts were also found to be more active in catalyzing hydrogenation of CO, and produced less methane and olefin (C2-C4) fraction. Higher turnover frequencies were observed after high temperature reduction (600 °C) as well, at which ethoxyl groups were removed from silica surface. In both reactions, the enhanced activity for the ethanol-prepared catalysts can not be fully accounted for by the increase in the dispersion of Co₃O₄ or CO metal. This suggests that the surface structures of Co₃O₄ or CO were further modified by the carbonaceous species derived from ethanol.