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1.
Systems V2O5–KHSO4 and V2O5–K2SO4 have been studied by the51V NMR method. The first system demonstrates the same states of vanadium as the previously studied V2O5–K2S2O7, in this system a compound with an equimolar ratio of components has been found. In V2O5–K2SO4 the state of vanadium differs from the above systems and the formation of a compound with V/K=4 is observed.
51V KHSO4–V2O5 K2SO4–V2O5. , K2S2O7–V2O5, . K2SO4–V2O5 V/K4.
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2.
The effects of doping of Co3O4with MgO (0.4–6 mol%) and V2O5 (0.20–0.75 mol%) on its surface and catalytic properties were investigated using nitrogen adsorption at −196°C and decomposition of H2O2 at 30–50°C. Pure and doped samples were prepared by thermal decomposition in air at 500–900°C, of pure basic cobalt carbonate and basic carbonate treated with different proportions of magnesium nitrate and ammonium vanadate. The results revealed that, V2O5 doping followed by precalcination at 500–900°C did not much modify the specific surface area of the treated Co3O4 solid. Treatment of Co3O4 with MgO at 500–900°C resulted in a significant increase in the specific surface area of cobaltic oxide. The catalytic activity in H2O2 decomposition, of Co3O4 was found to suffer a considerable increase by treatment with MgO. The maximum increase in the catalytic reaction rate constant (k) measured at 40°C on Co3O4 due to doping with 3 mol% MgO attained 218, 590 and 275% for the catalysts precalcined at 500, 700 and 900°C, respectively. V2O5-doping of Co3O4 brought about a significant progressive decrease in its catalytic activity. The maximum decrease in the reaction rate constant measured at 40°C over the 0.75 mol% V2O5-doped Co3O4 solid attained 68 and 93% for the catalyst samples precalcined at 500 and 900°C, respectively. The doping process did not modify the activation energy of the catalyzed reaction but much modified the concentration of catalytically active constituents without changing their energetic nature. MgO-doping increased the concentration of CO3+–CO2+ ion pairs and created Mg2+–CO3+ ion pairs increasing thus the number of active constituents involved in the catalytic decomposition of H2O2. V2O5-doping exerted an opposite effect via decreasing the number of CO3+–CO2+ ion pairs besides the possible formation of cobalt vanadate.  相似文献   

3.
合成了TiO_2-CeO_2柱撑黏土负载V_2O_5催化剂,通过XRD、氮气吸附脱附、TG、FT-IR、H_2-TPR、NH_3-TPD、XPS等方法对其物理化学性质进行了表征,研究了该催化剂在H2S选择性催化氧化反应中的活性。结果表明,负载5%V_2O_5的TiO_2-CeO_2柱撑黏土在180℃下催化效果最好,且尾气中不含SO_2。V_2O_5、TiO_2和CeO_2之间的相互作用提高了催化剂的活性,CeO_2提高了催化剂的热稳定性,同时提供大量晶格氧,加强了V_2O_5的氧化还原作用,降低了反应温度;TiO_2加强了VO_x和CeO_x的再氧化,降低了硫酸盐的覆盖率,从而降低了催化剂的失活速率。  相似文献   

4.
5.
The selectivity of the oxides under consideration to the oxidation of methanol to formaldehyde is shown to increase in the sequence V2O5–Nb2O5–Ta2O5. The same sequence corresponds to the decrease in specific activity. The activation energy of the reaction is 12 kcal/mol for V2O5, 14 kcal/mol for Nb2O5 and 22 kcal/mol for Ta2O5.
, V2O5–Nb2O5–Ta2O5. . : V2O5 12 /, Nb2O5 14 / Ta2O5 22 /.
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6.
The kinetics of Mn2O3 digestion in various H2SO4 solutions (0.5-2.0 M) and at various temperatures (ambient to 80 °C) to form solid γ-MnO2 and soluble Mn(II) have been examined using X-ray diffraction. Using a modified first-order Avrami expression to describe digestion kinetics, rate constants in the range 0.02-0.98 h−1 were found for Mn2O3 disappearance, and 0.03-0.42 h−1 for γ-MnO2 formation, with higher H2SO4 concentrations and temperatures leading to faster conversion rates. Also, for a particular set of experimental conditions, the rate of γ-MnO2 formation was always slower than Mn2O3 disappearance. This was interpreted in terms of the solubility and stability of the soluble Mn(III) intermediated formed during the digestion. Activation energies for Mn2O3 dissolution and γ-MnO2 formation were also determined.  相似文献   

7.
The thermodynamically unexpected reduction of V2O5 in the presence of the mixed oxides AlNbO4, GaNbO4, and TiNb2O7 under nitrogen at 630°C is reported and gives a supplementary example of the kind of interfacial reaction observed in the V2O5TiO2 system. It is shown that this phenomenon comes from the establishment of coherent interfaces between the cleavage planes of two crystals belonging to the same crystallo-chemical family. The reduction enables the system to diminish the elastic stress created by the slight interfacial misfit. A thermodynamic and kinetic explanation, based on structural factors, is given.  相似文献   

8.
A V2O5–Li2O–TiO2 (a) based catalyst for o-xylene oxidation to phthalic anhydride has been synthesized. The activity and selectivity of the specimen obtained are comparable with those of industrial catalysts.  相似文献   

9.
The texture properties (specific surface area and porosity) of V2O5/TiO2 catalysts obtained from VO(acetylacetonate)2 have been studied. The presence of sodium leads to a marked decrease in the SBET values, probably as a consequence of the formation of Na-V bronzes, which lead to a rutilization of the support.
( ) V2O5/TiO2, - VO()2. SBET, , Na-V, .
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10.
NH3, NO and CO2 were tested as adsorbates for selective determination of exposed surface area of V2O5 on a V2O5/Al2O3 catalyst. The most promising appears to be CO2 which interacts with the support Al2O3 only.
NH3, NO CO2 V2O5 V2O5/Al2O3. CO2, Al2O3.
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11.
Summary Three metalloporphyrin complexes are used as peroxidase mimics in the oxidation of phenol by hydrogen peroxide.A kinetic model for the titled reaction is constructed.  相似文献   

12.
A simple system is described, which oxidizes saturated hydrocarbons either in acetonitrile or (less efficiently) in water. The system consists of 50% aqueous hydrogen peroxide as an oxidant, sodium metavanadate, NaVO3, as a catalyst and sulfuric (or oxalic) acid as a co-catalyst. The reactions were carried out at 20-50 °C. In the oxidation of cyclohexane in acetonitrile, the highest yield (37% based on cyclohexane) and turnover number (TON=1700) were attained after 3 h at 50 °C. The corresponding parameters were 16% and 1090 for n-heptane oxidation under the same conditions. The oxidation of higher alkanes, RH, in acetonitrile gives almost exclusively the corresponding alkyl hydroperoxides, ROOH. Light alkanes (n-butane, propane, ethane, and methane) have been also oxygenated by the system under consideration. The highest TON (200) was attained for ethane and the highest yield (19%) was obtained in the case of n-butane. The selectivity parameters measured for the oxidation of linear and branched alkanes are low, the reaction with cis- and trans-1,2-dimethylcyclohexanes is not stereoselective. These facts lead us to conclude that the oxidation occurs with the formation of hydroxyl radicals in the crucial step.  相似文献   

13.
The performance of V2O5–TiO2 catalysts doped by WO3 and Nb2O5 in sulfur dioxide oxidation, and in selective catalytic reduction (SCR) of NO by ammonia has been studied. Addition of tungsten and niobium oxides was found to suppresses sulfur dioxide oxidation thus increasing the catalysts resistance to SO2 poisoning and their activity in SCR.  相似文献   

14.
以水热合成针铁矿为前驱体浸渍偏钒酸铵,分别于300,400和500℃空气中焙烧,制备了不同活性组分负载量的V2O5/赤铁矿(V/H)催化剂,用于氨选择性催化还原(SCR)脱硝。采用X射线衍射、透射电子显微镜、比表面积分析仪、程序升温还原及程序升温脱附等方法对催化剂结构进行了表征,并用标气配制模拟烟气进行了脱硝实验。结果表明,300℃煅烧3%V/H催化剂当烟气温度为250-300℃时NO转化率均可达95%以上;当配气中单独加入水蒸气或低浓度SO2(0.01%)时,V/H催化脱硝的活性不受影响;当系统加入高浓度的SO2(0.03%与0.05%)或同时添加H2O与SO2时,SCR脱硝效率下降,其机制可能是SO2在催化剂表面竞争吸附所致,停止添加后,催化活性迅速恢复。  相似文献   

15.
Infrared spectra of both fresh and reductively activated V2O5 and V2O5–MoO3 catalysts were recorded and compared with the results of catalytic measurements. The results indicate that the presence of V=O double bonds in the catalytically active mass is not essential for the selective oxidation of benzene to maleic anhydride.
, V2O5 V2O5–MoO3. . , V=O .
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16.
IR-spectroscopic studies indicate that on the oxidized surface of V2O5/Al2O3 catalysts propylene interacts mainly with Brönsted acid centers to form an alcoholate type complex transforming into acetone. On the reduced surface propylene is stabilized as a -complex of V3+ and V4+ ions.
- , V2O5/Al2O3 , . - V3+ V4+.
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17.
The V2O3-C dual-layer coated LiFePO4 cathode materials with excellent rate capability and cycling stability were prepared by carbothermic reduction of V2O5. X-ray powder diffraction, elemental analyzer, high resolution transmission electron microscopy and Raman spectra revealed that the V2O3 phase co-existed with carbon in the coating layer of LiFePO4 particles and the carbon content reduced without graphitization degree changing after the carbothermic reduction of V2O5. The electrochemical measurement results indicated that small amounts of V2O3 improved rate capability and cycling stability at elevated temperature of LiFePO4/C cathode materials. The V2O3-C dual-layer coated LiFePO4 composite with 1wt% vanadium oxide delivered an initial specific capacity of 167 mAh/g at 0.2 C and 129 mAh/g at 5 C as well as excellent cycling stability. Even at elevated temperature of 55 oC, the specific capacity of 151 mAh/g was achieved at 1 C without capacity fading after 100 cycles.  相似文献   

18.
This work uses ab initio calculations to obtain harmonic frequencies and anharmonic constants for the O–H symmetric and asymmetric stretches of H2SO4 in its C2, Cs, C1a, and C1b configurations. In addition, a high-resolution potential energy surface is calculated as a function of both O=S–O–H dihedral angles in order to accurately obtain minimum and saddle point energies. The resulting peak positions and Boltzmann populations are compared to experimental frequencies and intensities and provide evidence for the assignment of rotamers in H2SO4 as suggested in recent work.  相似文献   

19.
本文采用淬冷法制备了V2O5样品。采用FTIR、XRD对其进行了表征。结果表明所制样品为无定形V2O5。通过循环伏安法和恒电流充放电测试研究其电容特性,并探讨了电化学反应机理。电化学性能测试结果表明,水基电解液种类及浓度、电压范围、扫描速度、电流密度均对无定形V2O5 电容性能产生影响。在1 mol·L-1 NaNO3溶液中,电位窗口为-0.2~0.8 V(vs SCE)范围内,5 mV·s-1的扫描速度下,无定形V2O5具有良好的电容性能;在250 mA·g-1的电流密度下,比电容为185.1 F·g-1,循环性能良好。  相似文献   

20.
Studies of SO2 oxidation on a molten component of vanadium catalysts in non-steadystate conditions indicates that the kinetics agree fairly well with an oxidation-reduction mechanism. In the low temperature range (<790 K) tetravalent vanadium can be partially crystallized.
. , - . ( 790 ) .
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