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1.
Open circuit dependence of potential on oxygen partial pressure as well as potentiostatic behavior in O 2- and He-saturated solution were determined. Stable hydrogen-oxygen species were formed, but potential-determining reversbility was found only in the potential range from 0·64–0·70 V ( nhe). This equilibrium could be reasonably explained by an O 2/H 2O 2 exchange. Oxygen, H 2O 2, or other hydrogen-oxygen species may affect open circuit potentials and potentiostatic behavior, but analysis of data assuming reversibility or quasi-equilibrium kinetic theory may be justified only between 0·64 and 0·70 V. 相似文献
2.
CeO 2 and CeReO x_ y catalysts are prepared by the calcination at different temperatures ( y = 500–1000 °C) and having a different composition (Re = La 3+ or Pr 3+/4+, 0–90 wt.%). The catalysts are characterised by XRD, H 2-TPR, Raman, and BET surface area. The soot oxidation is studied with O 2 and NO + O 2 in the tight and loose contact conditions, respectively. CeO 2 sinters between 800–900 °C due to a grain growth, leading to an increased crystallite size and a decreased BET surface area. La 3+ or Pr 3+/4+ hinders the grain growth of CeO 2 and, thereby, improving the surface catalytic properties. Using O 2 as an oxidant, an improved soot oxidation is observed over CeLaO x_ y and CePrO x_ y in the whole dopant weight loading and calcination temperature range studied, compared with CeO 2. Using NO + O 2, the soot conversion decreased over CeLaO x_ y catalysts calcined below 800 °C compared with the soot oxidation over CeO 2_ y. CePrO x_ y, on the other hand, showed a superior soot oxidation activity in the whole composition and calcination temperature range using NO + O 2. The improvement in the soot oxidation activity over the various catalysts with O 2 can be explained based on an improvement in the external surface area. The superior soot oxidation activity of CePrO x_ y with NO + O 2 is explained by the changes in the redox properties of the catalyst as well as surface area. CePrO x_ y, having 50 wt.% of dopant, is found to be the best catalyst due to synergism between cerium and praseodymium compared to pure components. NO into NO 2 oxidation activity, that determines soot oxidation activity, is improved over all CePrO x catalysts. 相似文献
3.
La 2O 3 films were deposited using O 3 and the structural and electrical properties were investigated and compared with those of La 2O 3 films deposited using O 2. The deposition temperature of the La 2O 3 films using O 3 was slightly reduced compared to that of the La 2O 3 films generated using O 2. After a post-annealing process at 600 and 900 °C, the crystallinity of the La 2O 3 films using O 3 were smaller than that using O 2. The leakage current density increased after annealing at 600 °C due to densification and then decreased after annealing at 900 °C due to interfacial layer growth. The effective dielectric constant of the La 2O 3 films deposited using O 3 decreased at 900 °C due to interfacial layer growth. The La 2O 3 films deposited using O 3 showed better structural and electrical properties in this study. 相似文献
4.
Pt supported on CeO 2 and 10 wt.% La 3+-doped CeO 2 catalysts have been prepared, characterised and tested for soot oxidation by O 2 in TGA. The reaction mechanism has been studied in a TAP reactor with labelled O 2. Isotopic oxygen exchange between molecular O 2 and ‘O’ on the support/catalyst was observed and soot oxidation is being carried out by lattice oxygen. TAP studies further show that Pt improves O 2 adsorption and, therefore, 5 wt.% Pt-containing catalysts are more active for soot oxidation than the counterpart supports. In addition, CeO 2 doping by La 3+ leads to an improved support, since La 3+ stabilises the structure of CeO 2 when calcined at high temperature (1000 °C) and minimises sintering. In addition, La 3+ improves the Ce 4+/Ce 3+ reduction as deduced from H 2-TPR experiments and favours oxygen mobility into the lattice. A synergetic effect of Pt and La 3+ is observed, Pt-containing La 3+-doped CeO 2 being the most active catalyst for soot oxidation by O 2 among the samples studied. 相似文献
5.
The effect of a commercial Pt/Al 2O 3 catalyst on the oxidation by NO 2 and O 2 of a model soot (carbon black) in conditions close to automotive exhaust gas aftertreatment is investigated. Isothermal oxidations of a physical mixture of carbon black and catalyst in a fixed bed reactor were performed in the temperature range 300–450 °C. The experimental results indicate that no significant effect of the Pt catalyst on the direct oxidation of carbon by O 2 and NO 2 is observed. However, in presence of NO 2–O 2 mixture, it is found that besides the well established catalytic reoxidation of NO into NO 2, Pt also exerts a catalytic effect on the cooperative carbon–NO 2–O 2 oxidation reaction. An overall mechanism involving the formation of atomic oxygen over Pt sites followed by its transfer to the carbon surface is established. Thus, the presence of Pt catalyst increases the surface concentration of –C(O) complexes which then react with NO 2 leading to an enhanced carbon consumption. The resulting kinetic equation allows to model more precisely the catalytic regeneration of soot traps for automotive applications. 相似文献
6.
Dispersing La 2O 3 on δ- or γ-Al 2O 3 significantly enhances the rate of NO reduction by CH 4 in 1% O 2, compared to unsupported La 2O 3. Typically, no bend-over in activity occurs between 500° and 700°C, and the rate at 700°C is 60% higher than that with a Co/ZSM-5 catalyst. The final activity was dependent upon the La 2O 3 precursor used, the pretreatment, and the La 2O 3 loading. The most active family of catalysts consisted of La 2O 3 on γ-Al 2O 3 prepared with lanthanum acetate and calcined at 750°C for 10 h. A maximum in rate (mol/s/g) and specific activity (mol/s/m 2) occurred between the addition of one and two theoretical monolayers of La 2O 3 on the γ-Al 2O 3 surface. The best catalyst, 40% La 2O 3/γ-Al 2O 3, had a turnover frequency at 700°C of 0.05 s −1, based on NO chemisorption at 25°C, which was 15 times higher than that for Co/ZSM-5. These La 2O 3/Al 2O 3 catalysts exhibited stable activity under high conversion conditions as well as high CH 4 selectivity (CH 4 + NO vs. CH 4 + O 2). The addition of Sr to a 20% La 2O 3/γ-Al 2O 3 sample increased activity, and a maximum rate enhancement of 45% was obtained at a SrO loading of 5%. In contrast, addition of SO =4 to the latter Sr-promoted La 2O 3/Al 2O 3 catalyst decreased activity although sulfate increased the activity of Sr-promoted La 2O 3. Dispersing La 2O 3 on SiO 2 produced catalysts with extremely low specific activities, and rates were even lower than with pure La 2O 3. This is presumably due to water sensitivity and silicate formation. The La 2O 3/Al 2O 3 catalysts are anticipated to show sufficient hydrothermal stability to allow their use in certain high-temperature applications. 相似文献
7.
The kinetics of CO and H 2 oxidation over a CuO-CeO 2 catalyst were simultaneously investigated under reaction conditions of preferential CO oxidation (PROX) in hydrogen-rich mixtures with CO 2 and H 2O. An integral packed-bed tubular reactor was used to produce kinetic data for power-law kinetics for both CO and H 2 oxidations. The experimental results showed that the CO oxidation rate was essentially independent of H 2 and O 2 concentrations, while the H 2 oxidation rate was practically independent of CO and O 2 concentrations. In the CO oxidation, the reaction orders were 0.91, −0.37 and −0.62 with respect to the partial pressure of CO, CO 2 and H 2O, respectively. In the H 2 oxidation, the orders were 1.0, −0.48 and −0.69 with respect to the partial pressure of H 2, CO 2 and H 2O, respectively. The activation energies of the CO oxidation and the H 2 oxidation were 94.4 and 142 kJ/mol, respectively. The rate expressions of both oxidations were able to predict the performance of the PROX reactor with accuracy. The independence between the CO and the H 2 oxidation suggested different sites for CO and H 2 adsorption on the CuO-CeO 2 catalyst. Based on the results, we proposed a new reaction model for the preferential CO oxidation. The model assumes that CO adsorbs selectively on the Cu + sites; H 2 dissociates and adsorbs on the Cu 0 sites; the adsorbed species migrates to the interface between the copper components and the ceria support, and reacts there with the oxygen supplied by the ceria support; and the oxygen deficiency on the support is replenished by the oxygen in the reaction mixture. 相似文献
8.
In this study, in order to develop low-temperature sintering ceramics for a multilayer piezoelectric transformer application, we explored CuO and Bi 2O 3 as sintering aids at low temperature (900 °C) sintering condition for Sb, Li and Mn-substituted 0.8Pb(Zr 0.48Ti 0.52)O 3–0.16Pb(Zn 1/3Nb 2/3)O 3–0.04Pb(Ni 1/3Nb 2/3)O 3 ceramics. These substituted ceramics have excellent piezoelectric and dielectric properties such as d33 347 pC/N, kp 0.57 and Qm 1469 when sintered at 1200 °C. The addition of CuO decreased the sintering temperature through the formation of a liquid phase. However, the piezoelectric properties of the CuO-added ceramics sintered below 900 °C were lower than the desired values. The additional Bi 2O 3 resulted in a significant improvement in the piezoelectric properties. The composition Sb, Li and Mn-substituted 0.8Pb(Zr 0.48Ti 0.52)O 3–0.16Pb(Zn 1/3Nb 2/3)O 3–0.04Pb(Ni 1/3Nb 2/3)O 3 + 0.5 wt% CuO + 0.5 wt% Bi 2O 3 showed the value of kp = 0.56, Qm = 1042 (planar mode), d33 = 350 pC/N, when it was sintered at 900 °C for 2 h. These values indicated that the newly developed composition might be suitable for multilayer piezoelectric transformer application. 相似文献
9.
Fine powders of submicron-sized crystallites of BaTiO 3 were prepared at 85–130°C by the hydrothermal method, starting from TiO 2.ξH 2O gel and Ba(OH) 2 solution. The products obtained below 110°C incorporated considerable amounts of H 2O and OH − in the lattice. As-prepared BaTiO 3 is cubic and converts to the tetragonal phase after heat treatment at 1200°C, accompanied by the loss of residual OH − ions. Hydrothermal reaction of SnO 2.ξH 2O gel with Ba(OH) 2 at 150–260°C gives rise to the hydrated phase, BaSn(OH) 6.3H 2O, due to the amphoteric nature of SnO 2.ξH 2O which stabilises Sn(OH) 62− anions in basic media. On heating in air or releasing the pressure in situ at 260°C, BaSn(OH) 6.3H 2O converts to BaSnO 3 through an intermediate, BaSnO(OH) 4. Solid solutions of Ba(Ti,Sn)O 3 are directly formed from (TiO 2 + SnO 2)..ξH 2O gel up to 35 mol% SnO 2. At higher Sn contents, the hydrothermal products are mixtures of BaSn(OH) 6.3H 2O and BaTiO 3, which on annealing at 1000°C result in monophasic Ba(Ti,Sn)O 3. The sintering characteristics and the dielectric properties of the ceramics prepared out of these fine powders are presented. The dielectric properties of fine-grained Ba(Ti,Sn)O 3 ceramics are explained on the basis of the prevailing diffuse phase transition behaviour. 相似文献
10.
The electrical and electromechanical properties of Pb(Mg 1/3Nb 2/3)O 3–Pb(Ni 1/3Nb 2/3)O 3–Pb(Zr,Ti)O 3 (PMN–PNN–PZT, PMN/PNN/PZT = 20/10/70) on Pt/Ti/SiO 2/Si substrates by chemical solution deposition was investigated. The PMN–PNN–PZT films annealed at 650 °C exhibited slim polarization hysteresis curves and a high dielectric constant of 2100 at room temperature. A broad dielectric maximum at approximately 140–170 °C was observed. The field-induced displacement was measured by scanning probe microscopy, the bipolar displacement was not hysteretic, and the effective piezoelectric coefficient ( d33) was 66 × 10 −12 m/V. The effective d33 decreased with temperature, but the value at 100 °C remained 45 × 10 −12 m/V. 相似文献
11.
This paper reports results of studies on structure and activity in soot combustion of nanocrystalline CeO 2 and CeLnOx mixed oxides (Ln = Pr, Tb, Lu, Ce/Ln atomic ratios 5/1). Nano-sized (4–5 nm) oxides with narrow size distribution were prepared by a microemulsion method W/O. Microstructure, morphology and reductivity of the oxides annealed up to 950 °C in O 2 and H 2 were analyzed by HRTEM, XRD, FT-IR, Raman spectroscopy and H 2-TPR. Obtained mixed oxides had fluorite structure of CeO 2 and all exhibited improved resistance against crystal growth in O 2, but only CeLuOx behaved better than CeO 2 in hydrogen. The catalytic activity of CeO2, CeLnOx and physical mixtures of CeO2 + Ln2O3 in a model soot oxidation by air was studied in “tight contact” mode by using thermogravimetry. Half oxidation temperature T1/2 for soot oxidation catalysed by nano-sized CeO2 and CeLnOx was similar and ca. 100 °C lower than non-catalysed oxidation. However, the mixed oxides were much more active during successive catalytic cycles, due to better resistance to sintering. Physical mixtures of nanooxides (CeO2 + Ln2O3) showed exceptionally high initial activity in soot oxidation (decrease in T1/2 by ca. 200 °C) but degraded strongly in successive oxidation cycles. The high initial activity was due to the synergetic effect of nitrate groups present in highly disordered surface of nanocrystalline Ln2O3 and enhanced reductivity of nanocrystalline CeO2. 相似文献
12.
Catalytic partial oxidation of methane to synthesis gas over ZrO 2 and yttrium-stabilized zirconia (YSZ) is studied using O 2 and N 2O as oxidants. ZrO 2 is much more active than YSZ in oxidation of methane with N 2O. In contrast, YSZ is significantly more active than ZrO 2 when O 2 is used as an oxidant. The presence of O 2 does not influence the rate of N 2O decomposition over ZrO 2 and YSZ, while the presence of H 2O in the system decreases N 2O conversion significantly. O 2 and N 2O are activated at different active sites. Y-induced oxygen vacancies are active for O 2 activation, whereas oxygen co-ordinatively unsaturated Zr cations (Zr-CUS) located at corners, edges, steps and kinks are responsible for N 2O activation. These sites are also capable of dissociating H 2O, resulting in competition between H 2O and N 2O. As compared with N 2O, molecular O 2 is easier to be activated over YSZ and ZrO 2. 相似文献
13.
Properties of the oxidized activated carbon KAU treated at different temperatures in inert atmosphere were studied by means of DTA, Boehm titration, XPS and AFM methods and their catalytic activity in H 2S oxidation by air was determined. XPS analysis has shown the existence of three types of oxygen species on carbon catalysts surface. The content of oxygen containing groups determined by Boehm titration is correlated with their amount obtained by XPS. Catalytic activity of the KAU catalysts in selective oxidation of hydrogen sulfide is connected with chemisorbed charged oxygen species (O 3.1 oxygen type with BE 536.8–537.7 eV) present on the carbons surface. Formation of dense sulfur layer (islands of sulfur) on the carbons surface and removal of active oxygen species are the reason of the catalysts deactivation in H2S selective oxidation. The treatment of deactivated catalyst in inert atmosphere at 300 °C gives full regeneration of the catalyst activity at low temperature reaction but only its partial reducing at high reaction temperature. The last case is connected with transformation of chemisorbed charged oxygen species into CO groups. The KAU samples treated in flow of inert gas at 900–1000 °C were very active in H2S oxidation to elemental sulfur transforming up to 51–57 mmol H2S/g catalyst at 180 °C with formation of 1.7–1.9 g Sx/g catalyst. 相似文献
14.
A new mixed-valent iron MOF, formulated as Fe 3O(F 4BDC) 3(H 2O) 3·(DMF) 3.5 (1), has been synthesized by using a perfluorinated linear dicarboxylate to link trigonal prismatic Fe 3(μ 3-O)(O 2C–) 6 clusters. The structure refinement based on single crystal X-ray diffraction data collected from 1 reveals the material exhibits the acs topology with large channels along the crystallographic c-axis. Due to the presence of fluorine atoms the organic link, 2,3,5,6-tetrafluorobenzene-1,4-dicarboxylate (F 4BDC), has a 63° torsion angle between the carboxylate and aromatic planes, resulting in larger channels compared to those in the isoreticular material MOF-235. While few iron-based MOFs have demonstrated porosity, nitrogen and hydrogen sorption experiments carried out at 77 K proved the porosity of outgassed 1, which has a Langmuir surface are of 635 m 2/g and a gravimetric capacity of 0.9 wt% of hydrogen at 1 bar. 相似文献
15.
Ceria (CeO 2) and rare-earth modified ceria (CeReO x with Re = La, Pr, Sm, Y) catalysts are prepared by nitrate precursor calcination and are characterised by BET surface area, XRD, H 2-TPR, and Raman spectroscopy. Potential of the catalysts in the soot oxidation is evaluated in TGA with a feed gas containing O 2. Seven hundred degree Celsius calcination leads to a decrease in the surface area of the rare-earth modified CeO 2 compared with CeO 2. However, an increase in the meso/macro pore volume, an important parameter for the soot oxidation with O 2, is observed. Rare-earth ion doping led to the stabilisation of the CeO 2 surface area when calcined at 1000 °C. XRD, H 2-TPR, and Raman characterisation show a solid solution formation in most of the mixed oxide catalysts. Surface segregation of dopant and even separate phases, in CeSmO x and CeYO x catalysts, are, however, observed. CePrO x and CeLaO x catalysts show superior soot oxidation activity (100% soot oxidation below 550 °C) compared with CeSmO x, CeYO x, and CeO 2. The improved soot oxidation activity of rare-earth doped CeO 2 catalysts with O 2 can be correlated with the increased meso/micro pore volume and stabilisation of external surface area. The segregation of the phases and the enrichment of the catalyst surface with unreducible dopant decrease the intrinsic soot oxidation activity of the potential CeO 2 catalytic sites. Doping CeO 2 with a reducible ion such as Pr 4+/3+ shows an increase in the soot oxidation. However, the ease of catalyst reduction and the bulk oxygen-storage capacity is not a critical parameter in the determination of the soot oxidation activity. During the soot oxidation with O 2, the function of the catalyst is to increase the ‘active oxygen’ transfer to the soot surface, but it does not change the rate-determining step, as evident from the unchanged apparent activation energy (around 150 kJ mol −1), for the catalysed and un-catalysed soot oxidation. Spill over of oxygen on the soot surface and its subsequent adsorption at the active carbon sites is an important intermediate step in the soot oxidation mechanism. 相似文献
16.
A series of CeO 2 promoted cobalt spinel catalysts were prepared by the co-precipitation method and tested for the decomposition of nitrous oxide (N 2O). Addition of CeO 2 to Co 3O 4 led to an improvement in the catalytic activity for N 2O decomposition. The catalyst was most active when the molar ratio of Ce/Co was around 0.05. Complete N 2O conversion could be attained over the CoCe0.05 catalyst below 400 °C even in the presence of O 2, H 2O or NO. Methods of XRD, FE-SEM, BET, XPS, H 2-TPR and O 2-TPD were used to characterize these catalysts. The analytical results indicated that the addition of CeO 2 could increase the surface area of Co 3O 4, and then improve the reduction of Co 3+ to Co 2+ by facilitating the desorption of adsorbed oxygen species, which is the rate-determining step of the N 2O decomposition over cobalt spinel catalyst. We conclude that these effects, caused by the addition of CeO 2, are responsible for the enhancement of catalytic activity of Co 3O 4. 相似文献
17.
Kinetics of N 2O decomposition over catalyst prepared by calcination of Co–Mn hydrotalcite was examined in integral fixed-bed reactor ( ) at various N 2O and O 2 initial partial pressure at temperature range of 330–450 °C. Kinetic data were evaluated by linear and non-linear regression method, 15 kinetic expressions were tested. Based on the obtained results a redox model of N 2O decomposition was proposed. At low pressures of O 2, adsorbed oxygen is formed by the N 2O decomposition; the N 2O chemisorption is considered as the rate-determining step. On the contrary, at high O 2 pressure it could be assumed that adsorbed oxygen species appear as a result of O 2 adsorption and the Eley–Rideal mechanism is the rate determining. N 2O decomposition is well described by the 1st rate law at N 2O and O 2 concentrations typical for waste gases. 相似文献
18.
The effect of additives on Pt-ZSM-5 catalysts was studied for the selective NO reduction by H 2 in the presence of excess O 2 (NO–H 2–O 2 reaction) at 100 °C. The reaction of NO in a stream of 0.08% NO, 0.28% H 2, 10% O 2, and He balance yielded N 2 with less than 10% selectivity, which could not be increased by changing Pt loading or H 2 concentration in the gas feed. Co-impregnation of NaHCO 3 and Pt onto ZSM-5 decreased the BET surface area and the Pt dispersion. Nevertheless, the Na-loaded catalyst (Na-Pt-ZSM-5) exhibited the higher NO x conversion (>90%) and the N 2 selectivity (ca. 50%). Such a high catalytic activity even at high Na loadings (≥10 wt.%) is completely contrast to other Na-added Pt catalyst systems reported so far. Further improvement of N 2 selectivity was attained by the post-impregnation of NaHCO 3 onto Pt-ZSM-5. In situ DRIFT measurements suggested that the addition of Na promotes the adsorption of NO as NO 2−-type species, which would play a role of an intermediate to yield N 2. The introduction of Lewis base to the acidic supports including ZSM-5 would be applied to the catalyst design for selective NO–H 2–O 2 reaction at low temperatures. 相似文献
19.
A multi-component NO x-trap catalyst consisting of Pt and K supported on γ-Al 2O 3 was studied at 250 °C to determine the roles of the individual catalyst components, to identify the adsorbing species during the lean capture cycle, and to assess the effects of H 2O and CO 2 on NO x storage. The Al 2O 3 support was shown to have NO x trapping capability with and without Pt present (at 250 °C Pt/Al 2O 3 adsorbs 2.3 μmols NO x/m 2). NO x is primarily trapped on Al 2O 3 in the form of nitrates with monodentate, chelating and bridged forms apparent in Diffuse Reflectance mid-Infrared Fourier Transform Spectroscopy (DRIFTS) analysis. The addition of K to the catalyst increases the adsorption capacity to 6.2 μmols NO x/m 2, and the primary storage form on K is a free nitrate ion. Quantitative DRIFTS analysis shows that 12% of the nitrates on a Pt/K/Al 2O 3 catalyst are coordinated on the Al 2O 3 support at saturation. When 5% CO2 was included in a feed stream with 300 ppm NO and 12% O2, the amount of K-based nitrate storage decreased by 45% after 1 h on stream due to the competition of adsorbed free nitrates with carboxylates for adsorption sites. When 5% H2O was included in a feed stream with 300 ppm NO and 12% O2, the amount of K-based nitrate storage decreased by only 16% after 1 h, but the Al2O3-based nitrates decreased by 92%. Interestingly, with both 5% CO2 and 5% H2O in the feed, the total storage only decreased by 11%, as the hydroxyl groups generated on Al2O3 destabilized the K–CO2 bond; specifically, H2O mitigates the NOx storage capacity losses associated with carboxylate competition. 相似文献
20.
The influence of sintering and poling conditions on dielectric properties and microstructures of the system 0·125Pb(Mg 1/3Nb 2/3)O 3−0·875Pb (Zr 0·5Ti 0·5)O 3 was investigated. Specimens were prepared by the conventional mixed-oxide technique. On account of eliminating the pyrochlore phase and lowering the sintering temperature, the calcined 0·125PZT−0·875PMN ceramic was doped with 4PbO.B 2O 3 glass powder. The 4PbO.B 2O 3 glass frit not only has a low flow temperature, but also a high polarizability. Additions of 4PbO.B 2O 3 to the perovskite 0·125PMN–0·875PZT solid solution will form a liquid phase, which served as a densification aid for the ceramics. With additions of 0·2 wt% glass frit, densities in excess of 98% of theoretical were obtained after sintering at 115°C. By variation of the fabrication processes, the influence of sintering and poling conditions on the properties of the ceramics was studied. 相似文献
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