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1.
A series of the Ce 1−xCu xO 2−x/Al 2O 3/FeCrAl catalysts ( x = 0–1) were prepared. The structure of the catalysts was characterized using XRD, SEM and H 2-TPR. The catalytic activity of the catalysts for the combustion of methane was evaluated. The results indicated that in the Ce 1−xCu xO 2−x/Al 2O 3/FeCrAl catalysts the surface phase structure were the Ce 1−xCu xO 2−x solid solution, -Al 2O 3 and γ-Al 2O 3. The surface particle shape and size were different with the variety of the molar ratio of Ce to Cu in the Ce 1−xCu xO 2−x solid solution. The Cu component of the Ce 1−xCu xO 2−x/Al 2O 3/FeCrAl catalysts played an important role to the catalytic activity for the methane combustion. There were the stronger interaction among the Ce 1−xCu xO 2−x solid solution and the Al 2O 3 washcoats and the FeCrAl support. 相似文献
2.
Catalytic methane combustion and CO oxidation were investigated over AFeO 3 (A=La, Nd, Sm) and LaFe 1−xMg xO 3 ( x=0.1, 0.2, 0.3, 0.4, 0.5) perovskites prepared by citrate method and calcined at 1073 K. The catalysts were characterized by X-ray diffraction (XRD). Redox properties and the content of Fe 4+ were derived from temperature programmed reduction (TPR). Specific surface areas (SA) of perovskites were in 2.3–9.7 m 2 g −1 range. XRD analysis showed that LaFeO 3, NdFeO 3, SmFeO 3 and LaFe 1−xMg xO 3 ( x·0.3) are single phase perovskite-type oxides. Traces of La 2O 3, in addition to the perovskite phase, were detected in the LaFe 1−xMg xO 3 catalysts with x=0.4 and 0.5. TPR gave evidence of the presence in AFeO 3 of a very small fraction of Fe 4+ which reduces to Fe 3+. The fraction of Fe 4+ in the LaFe 1−xMg xO 3 samples increased with increasing magnesium content up to x=0.2, then it remained nearly constant. Catalytic activity tests showed that all samples gave methane and CO complete conversion with 100% selectivity to CO 2 below 973 and 773 K, respectively. For the AFeO 3 materials the order of activity towards methane combustion is La>Nd>Sm, whereas the activity, per unit SA, of the LaFe 1−xMg xO 3 catalysts decreases with the amount of Mg at least for the catalysts showing a single perovskite phase ( x=0.3). Concerning the CO oxidation, the order of activity for the AFeO 3 materials is Nd>La>Sm, while the activity (per unit SA) of the LaFe 1−xMg xO 3 catalysts decreases at high magnesium content. 相似文献
3.
Hydrodechlorination of chlorobenzenes on platinum (Pt)-supported γ-alumina and alumina Lewis superacid (AmLSA) catalysts was carried out at room temperature and ambient pressure using a fixed bed flow reactor and a semi-batch reactor. Both the catalysts indicated good activity for the hydrodechlorination, but the former was superior to the latter. The hydrodechlorinations of reactants C 6H 6−xCl x ( x=1, 2, 3) proceeded step-wisely to benzene and then cyclohexane via C 6H 6−yCl y ( y= x−1). The reactions seem to be promoted by the contribution of spillover hydrogen formed on the Pt-supported catalysts. The catalysts deactivated with reaction time and the amount of chlorine that accumulated on the Pt-supported γ-alumina catalyst in the hydrodechlorination of 1,4-dichlorobenzene for 3 h was near to that estimated from the converted reactant molecules. When the deactivated catalysts were treated in a stream of hydrogen above 503 K, the original activity was completely restored, but the deactivation phenomenon with reaction time was observed again. 相似文献
4.
The structural and electronic properties of selected compositions of Sn xTi 1−xO 2 solid solutions ( x=0, 1/24, 1/16, 1/12, 1/8, 1/6, 1/4, 1/2, 3/4, 5/6, 7/8, 11/12, 15/16, 23/24 and 1) were investigated by means of periodic density functional theory (DFT) calculations at B3LYP level. The calculations show that the corresponding lattice parameters vary non-linearly with composition, supporting positive deviations from Vegard’s law in the Sn xTi 1−xO 2 system. Our results also account for the fact that chemical decomposition in Sn xTi 1−xO 2 system is dominated by composition fluctuations along [0 0 1] direction. A nearly continuous evolution of the direct band gap and the Fermi level with the growing value of x is predicted. Ti 3d states dominate the lower portion of the conduction band of Sn xTi 1−xO 2 solid solutions. Sn substitution for Ti in TiO 2 increases the oxidation–reduction potential of the oxide as well as it renders the lowest energy transition to be indirect. These two effects can be the key factors controlling the rate for the photogenerated electron–hole recombination. These theoretical results are capable to explain the enhancement of photoactivity in Sn xTi 1−xO 2 solid solutions. 相似文献
5.
LaMn 1−xMg xO 3 perovskite catalysts ( x=0–0.5) were synthesised by the so-called “citrates method”, characterised (chemical analysis, TEM, BET, XRD, temperature-programmed desorption of oxygen) and tested for their activity towards the catalytic combustion of methane. The role of MgO as a textural promoter, which hinders the sintering of the catalyst crystals by geometrical interposition, has also been assessed. Finally, a kinetics study was performed on the most promising catalysts prepared (LaMnO 3 and LaMn 0.8Mg 0.2O 3). The major results obtained are: (i) Mg substitution in the basic LaMnO 3 perovskite has a positive effect on the catalytic activity only at low x values ( x≤0.2); (ii) as opposed to the results of previous studies on the LaCr 1−xMg xO 3 system, the role of MgO as a textural promoter is not always significant and depends strongly on the calcination temperature of the samples (800–1200°C) and on the value of x; (iii) an Eley–Rideal mechanism could satisfactorily fit the experimental kinetics results for both catalysts, even though, as opposed to LaMnO 3, the catalytic combustion over LaMn 0.8Mg 0.2O 3 seems to involve two different types of adsorbed oxygen species, depending on the operating temperature. 相似文献
6.
Catalytic combustion of methane has been investigated over AMnO 3 (A = La, Nd, Sm) and Sm 1−xSr xMnO 3 ( x = 0.1, 0.3, 0.5) perovskites prepared by citrate method. The catalysts were characterized by chemical analysis, XRD and TPR techniques. Catalytic activity measurements were carried out with a fixed bed reactor at T = 623–1023 K, space velocity = 40 000 N cm 3 g −1 h −1, CH 4 concentration = 0.4% v/v, O 2 concentration = 10% v/v. Specific surface areas of perovskites were in the range 13–20 m2 g−1. XRD analysis showed that LaMnO3, NdMnO3, SmMnO3 and Sm1−xSrxMnO3 (x = 0.1) are single phase perovskite type oxides. Traces of Sm2O3 besides the perovskite phase were detected in the Sm1−xSrxMnO3 catalysts for x = 0.3, 0.5. Chemical analysis gave evidence of the presence of a significant fraction of Mn(IV) in AMnO3. The fraction of Mn(IV) in the Sm1−xSrxMnO3 samples increased with x. TPR measurements on AMnO3 showed that the perovskites were reduced in two steps at low and high temperature, related to Mn(IV) → Mn(III) and Mn(III) → Mn(II) reductions, respectively. The onset temperatures were in the order LaMnO3 > NdMnO3 > SmMnO3. In Sm1−xSrxMnO3 the Sr substitution for Sm caused the formation of Mn(IV) easily reducible to Mn(II) even at low temperature. Catalytic activity tests showed that all samples gave methane complete conversion with 100% selectivity to CO2 below 1023 K. The activation energies of the AMnO3 perovskites varied in the same order as the onset temperatures in TPR experiments suggesting that the catalytic activity is affected by the reducibility of manganese. Sr substitution for Sm in SmMnO3 perovskites resulted in a reduction of activity with respect to the unsubstituted perovskite. This behaviour was related to the reduction of Mn(IV) to Mn(II), occurring under reaction conditions, hindering the redox mechanism. 相似文献
7.
A new methodology that combines the sol–gel method and a template approach is used to synthesize porous LiNi 1−xCo xO 2 films. Conventional films are obtained through the sol–gel method. The films are used to evaluate the influence of this new methodology on the electrochemical performance. It was observed, from X-ray diffraction analysis on the conventional film that a further increase in the annealing temperature to 450 °C leads to a more ordered system indicated by the presence of characteristics LiNi 1−xCo xO 2 diffraction patterns. Above this temperature no significant modification in the X-ray patterns is observed in the porous film. We concluded, using other experimental techniques including cyclic voltammetry, electrochemical impedance and charge/discharge tests) that electrochemical properties, such as, oxidation and reduction charges and charge/discharge capacity of LiNi 1−xCo xO 2 are significantly improved in the porous film, which demonstrates the feasibility of the proposed methodology. 相似文献
8.
La xSr 2−xMnO 4 (0 ≤ x ≤ 0.8) oxides were synthesized and single-phase K 2NiF 4-type oxides were obtained in the range of 0.1 ≤ x < 0.5. The catalytic activity of La xSr 2−xMnO 4 for NO–CO reaction increased with increasing x in the range of solubility limit of La. La 0.5Sr 1.5MnO 4 showed the highest activity among La xSr 2−xMnO 4 prepared in this study, but its activity was inferior to perovskite-type La 0.5Sr 0.5MnO 3. Among the Pd-loaded catalysts, however, Pd/La 0.8Sr 1.2MnO 4 showed the higher activity and the selectivity to N 2 than Pd/La 0.5Sr 0.5MnO 3 and Pd/γ-Al 2O 3. The excellent catalytic performance of Pd/La 0.2Sr 1.2MnO 4 could be ascribable to the formation of SrPd 3O 4 which was detected by XRD in the catalyst but not in the other two catalysts. 相似文献
9.
Catalytic decomposition of nitrous oxide has been carried out over calcined cobalt aluminum hydrotalcites of general formula [Co 1−xAl x(OH) 2[CO 3] x/2 H 2O where x = 0.25–0.33 at 50 Torr (1 Torr = 133 Pa) initial pressure of N 2O in a static glass recirculatory reactor (130 cc) in the temperature range 150–280°C. All catalysts showed a first order dependence in N 2O without significant oxygen inhibition. The activity increased with an increase in cobalt concentration present in the sample. The catalyst precursor synthesized under low supersaturation (LS) exhibited a higher activity than the precursor synthesized by sequential precipitation (SP) method. The observed trend in the activity is explained based on the surface concentration of cobalt, determined by XPS and matrix effects. Prior to catalytic studies, the fresh and calcined samples were characterized by various physicochemical techniques such as XRD, FT–IR, TG–DSC, TEM (with EDAX) and BET surface area measurements. 相似文献
10.
The binary systems ReS 2–TaS 2 and OsS 2-TaS 2 are studied. Mixed layer structure (MLS) phases are found in Re xTa 1−xS 2 with a composition range of 0.25 x0.5, as well as in the Os xTa 1−xS 2 with a composition range of 0.26 x0.33. The MLSs of both phases are constructed by a random and mixed stacking of the 2Hb-layers and 3R-layers. The magnetic susceptibilities of samples from both phases show a weak Pauli-paramagnetism. The paramagnetic moment and the electrical conductivity of both phases decrease as the composition x increases. The behaviour of the paramagnetic moment and the electrical conductivity of those phases offer us a good example of the number of conduction electrons and their effect. 相似文献
11.
The microstructural and electrochemical properties of La 2.3−xCa xMg 0.7Ni 9 hydrogen storage alloys have been studied systematically. The microstructure examined by XRD, SEM and EDX shows that the alloys consist of multi-phases, which are (La, Mg) 2Ni 7 phase, LaMgNi 4 phase, (La, Mg)Ni 3 phase and LaNi 5 phase. It is can be found that Ca does not appear to segregate. This phenomenon is different from Mg. With increasing Ca content, the main phase varies from (La, Mg) 2Ni 7 phase ( x = 0) to (La, Mg)Ni 3 phase ( x = 0.3), LaNi 5 phase ( x = 0.6, 0.8) and (La, Mg)Ni 3 phase ( x = 1.0, 1.3). The maximum discharge capacities of the alloy electrodes increase from 244.6 mAh/g ( x = 0) to 380 mAh/g ( x = 1.0), and then decrease to 353.6 mAh/g ( x = 1.3). The discharge capacities of the alloys are related to phase content. Cell volumes of LaNi 5 phase, (La, Mg) 2Ni 7 phase and (La, Mg)Ni 3 phase all decrease and the high rate dischargeability (HRD) is improved by adding Ca. The alloy electrodes also show relative good cycling stability up to 100 cycles. 相似文献
12.
Effect of substitution of CuO and WO 3 on the microwave dielectric properties of BiNbO 4 ceramics and the co-firing between ceramics and copper electrode were investigated. The (Bi 1−xCu x)(Nb 1−xW x)O 4 ( x = 0.005, 0.01, 0.015, 0.02) composition can be densified between 900 and 990 °C. The microwave dielectric constants lie between 36 and 45 and the pores in ceramics were found to be the main influence. The Q values changes between 1400 and 2900 with different x values and sintering temperatures while Qf values lie between 6000 and 16,000 GHz. The microwave dielectric losses, mainly affected by the grain size, pores, and the secondary phase, are discussed. The (Bi 1−xCu x)(Nb 1−xW x)O 4 ceramics and copper electrode was co-fired under N 2 atmosphere at 850 °C and the EDS analysis showed no reaction between the dielectrics and copper electrodes. This result presented the (Bi 1−xCu x)(Nb 1−xW x)O 4 dielectric materials to be good candidates for LTCC applications with copper electrode. 相似文献
13.
Water–gas shift reaction was studied over two nanostructured Cu xCe 1−xO 2−y catalysts: a Cu 0.1Ce 0.9O 2−y catalyst prepared by a sol–gel method and a Cu 0.2Ce 0.8O 2−y catalyst prepared by co-precipitation method. A commercial low temperature water–gas shift CuO–ZnO–Al 2O 3 catalyst was used as reference. The kinetics was studied in a plug flow micro reactor at an atmospheric pressure in the temperature interval between 298 and 673 K at two different space velocities: 5.000 and 30.000 h −1, respectively. Experimentally estimated activation energy, Eaf, of the forward water–gas shift reaction at CO/H 2O = 1/3 was 51 kJ/mol over the Cu 0.1Ce 0.9O 2−y, 34 kJ/mol over the Cu 0.2Ce 0.8O 2−y and 47 kJ/mol over the CuO–ZnO–Al 2O 3 catalyst. A simple rate expression approximating the water–gas shift process as a single reversible surface reaction was used to fit the experimental data in order to evaluate the rate constants of the forward and backward reactions and of the activation energy for the backward reaction. 相似文献
14.
Electrical resistivity and Seebeck ( S) measurements were performed on (La 1−xSr x)MnO 3 (0.02 x0.50) and (La 1−xSr x)CoO 3 (0 x0.15) in air up to 1073 K. (La 1−xSr x)MnO 3 ( x0.35) showed a metal-to-semiconductor transition; the transition temperature almost linearly increased from 250 to 390 K with increasing Sr content. The semiconductor phase above the transition temperature showed negative values of S. (La 1−xSr x)CoO 3 (0 x0.10) showed a semiconductor-to-metal transition at 500 K. Dominant carriers were holes for the samples of x0.02 above room temperature. LaCoO 3 showed large negative values of S below ca. 400 K, indicative of the electron conduction in the semiconductor phase. 相似文献
15.
Novel Ir-substituted hexaaluminate catalysts were developed for the first time and used for catalytic decomposition of high concentration of N 2O. The catalysts were prepared by one-pot precipitation and characterized by X-ray diffraction (XRD), N 2-adsorption, scanning electronic microscopy (SEM) and temperature-programmed reduction (H 2-TPR). The XRD results showed that only a limited amount of iridium was incorporated into the hexaaluminate lattice by substituting Al 3+ to form BaIr xFe 1−xAl 11O 19 after being calcined at 1200 °C, while the other part of iridium existed as IrO 2 phase. The activity tests for high concentration (30%, v/v) of N 2O decomposition demonstrated that the BaIr xFe 1−xAl 11O 19 hexaaluminates exhibited much higher activities and stabilities than the Ir/Al 2O 3-1200, and the pre-reduction with H 2 was essential for activating the catalysts. By comparing BaIr xFe 1−xAl 11O 19 with BaIr xAl 12−xO 19 ( x = 0–0.8), it was found that iridium was the active component in the N 2O decomposition and the framework iridium was more active than the large IrO 2 particles. On the other hand, Fe facilitated the formation of hexaaluminate as well as the incorporation of iridium into the framework. 相似文献
16.
The aim of the present work is to obtain ceramic materials with a hexagonal structure and high density, hardness and mechanical strength at lower synthesis temperature. Ceramic samples with nominal composition La 1−xCa xAl 11−y−zMg yTi zO 18 ( x=0–1; y=0–3; z=0–3,5) are prepared. The samples are sintered at temperature 1500 °C by one-stage and two-stage ceramic technology. By X-ray diffraction and scanning electron microscopy, predominant phase LaAl 11O 18 and second phases LaAlO 3 and -Al 2O 3 are identified. Ceramic materials are characterized with high physico-mechanical properties and may be find application for production of mill bodies and materials for immobilization of nuclear waste. 相似文献
17.
Layered Li[Ni (1−x)/3Mn (1−x)/3Co (1−x)/3Cr x]O 2 materials with x = 0, 0.01, 0.02, 0.03, 0.05 are prepared by a solid-state pyrolysis method. The oxide compounds were calcined with various Cr-doped contents, which result in greater difference in morphological (shape, particle size and specific surface area) and the electrochemical (first charge profile, reversible capacity and rate capability) differences. The Li[Ni (1−x)/3Mn (1−x)/3Co (1−x)/3Cr x]O 2 powders were characterized by means of X-ray diffraction (XRD), charge/discharge cycling, cyclic voltammetry, and SEM. XRD experiment revealed that the Li[Ni (1−x)/3Mn (1−x)/3Co (1−x)/3Cr x]O 2 ( x = 0, 0.01, 0.02, 0.03, 0.05) were crystallized to well layered -NaFeO 2 structure. The first specific discharge capacity and coulombic efficiency of the electrode of Cr-doped materials were higher than that of pristine material. When x = 0.02, the sample showed the highest first discharge capacity of 241.9 mAh g −1 at a current density of 30 mA g −1 in the voltage range 2.3–4.6 V, and the Cr-doped samples exhibited higher discharge capacity and better cycleability under medium and high current densities at room temperature. 相似文献
18.
A series of palladium-substituted La 2CuO 4, corresponding to the formula La 2Cu 1 −xPd xO 4 ( x = 0−0.2) were prepared by metal nitrate decomposition in a polyacrylamide gel. This method allows an easy incorporation of palladium in the mixed-oxides, which are formed at moderate temperature with rather high specific areas (13–17 m 2/g). The partial substitution of copper for palladium allows a strong improvement of the three-way catalytic activity, in particular for NO reduction. The light-off temperatures for the conversions of CO, NO and C 3H 6 decreased markedly when increasing the palladium content, the activity of catalysts La 2Cu 0.9Pd 0.1O 4 and La 2Cu 0.8Pd 0.2O 4 being comparable to that of a Pt-Rh/CeO 2–Al 2O 3 catalyst for NO reduction, and higher for CO and C 3H 6 oxidation. All the La2Cu1 − x PdxO4 catalysts are activated under reacting conditions. This activation corresponds to the destruction of the mixed-oxide structure, with formation of reduced Pd0 ions atomically dispersed, surrounded by Cu+ and Cu2+ species on a lanthanum oxycarbonate matrix. This high dispersion state of the two transition metals in various oxidation states is supposed to originate from the initial La2Cu1 −xPdxO4 structure. 相似文献
19.
Perovskite type La 1 − xSr xMnO 3 ( x = 0–0.5) oxides were prepared by the amorphous citrate process, characterised by X-ray diffraction, oxygen desorption, temperature-programmed reduction, infrared and X-ray photoelectron spectroscopic techniques, and tested for methane combustion within the 473–1073 K temperature range. Since catalyst activity was found to depend strongly on BET areas and to a lesser extent, on the degree of substitution ( x), intrinsic activities were computed for La 1 − xSr xMnO 3 catalyst series. Among the compositions investigated, the degree of substitution x = 0.2 showed the highest intrinsic activity within the temperatures explored. Characterisation techniques made possible to correlate catalytic performance with the structural characteristics of the oxides. The stability of Mn 4+ is probably the most important parameter, but excess of oxygen and atomic surface composition should also be taken into account. 相似文献
20.
The catalytic oxidation of unsymmetrical dimethylhydrazine (UDMH) by air has been studied in a vibro-fluidized catalyst bed laboratory kinetic setup over catalysts Cu xMg 1−xCr 2O 4/γ-Al 2O 3, 32.9%Ir/γ-Al 2O 3 and β-Si 3N 4 in a temperature range 150–400 °C. The catalyst Cu xMg 1−xCr 2O 4/γ-Al 2O 3 was found to be optimal regarding high yields of CO 2 and low yields of NO x. A probable mechanism of UDMH heterogeneous catalytic oxidation is proposed. Catalyst Cu xMg 1−xCr 2O 4/γ-Al 2O 3 has been further used in the pilot plant specially designed for the destruction of UDMH. Results of testing the main fluidized bed catalytic reactor for UDMH oxidation and the reactor for selective catalytic reduction of NO x with NH 3 are presented. These results prove that the developed UDMH destruction technology is highly efficient and environmentally safe. 相似文献
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