Catalytic oxidation of isobutyraldehyde over a molybdenum-vanadium oxide catalyst

The effect of composition of reaction mixture on the gas-phase oxidation of isobutyraldehyde has been studied over a Mo–V oxide catalyst supported on Aerosil. It was found that oxygen, in contrast to water vapor, markedly changes the conversion of isobutyraldehyde and yields of acetone and methacrolein.     

Oxidation of ammonia on a bismuth-manganese oxide catalyst

The doping of MnO₂ with small quantities of Bi₂O₃ results in an increase of the surface oxygen bond energy. Accordingly, the values of the specific catalytic activity and selectivity to nitrous oxide are lower for the doped catalyst than for pure MnO₂. The mechanism of low temperature ammonia oxidation is the same on both catalysts.

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Bi₂O₃ MnO₂ . , , MnO₂. .

     

Selective oxidation of propane to acrylic acid over mixed metal oxide catalysts

The effects of metal atomic ratio, water content, oxygen content, and calcination temperature on the catalytic performances of MoVTeNbO mixed oxide catalyst system for the selective oxidation of propane to acrylic acid have been investigated and discussed. Among the catalysts studied, it was found that the MoVTeNbO catalyst calcined at a temperature of 600 ℃ showed the best performance in terms of propane conversion and selectivity for acrylic acid under an atmosphere of nitrogen. An effective MoVTeNbO oxide catalyst for propane selective oxidation to acrylic acid was obtained with a combination of a preferred metal atomic ratio （Mo1V0.31Te0.23Nb0.12）. The optimum reaction condition for the selective oxidation of propane was the molar ratio of C3H8 ：O2 ： H2O ： N2 = 4.4： 12.8 ： 15.3 ： 36.9. Under such conditions, the conversion of propane and the maximum yield of acrylic acid reached about 50% and 21%, respectively.     

Kinetics of the vapor-phase oxidation of o-xylene over a vanadium oxide catalyst

(Pt–Sn)/Al₂O₃. , , , , .

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The catalytic and adsorption properties of the (Pt–Sn)/Al₂O₃ system have been studied. The results of benzene hydrogenation, cyclohexane dehydrogenation and temperature-programmed hydrogen desorption show that the introduction of tin into the Pt/Al₂O₃ catalyst significantly changes the dispersity and electronic state of supported platinum.

     

Response studies of the mechanism of o-xylene oxidation over a vanadium-titanium oxide catalyst

A response method has been used to study the mechanism of o-xylene oxidation over a vanadium-titanium oxide catalyst. The products of partial and destructive oxidation are shown to be formed under the influence of molecular oxygen on the surface intermediates produced by the interaction between o-xylene and oxidized surface sites.

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- . , , - .

     

n-Butane oxidation over a vanadium-phosphorus catalyst

The activity of vanadium-phosphorus oxide catalysts with respect to maleic anhydride formation in n-butane oxidation has been found to correlate with the concentration of V⁴⁺ ions in the catalysts. The steady catalytic activitv of the samples examined is achieved more rapidly upon prereduction.

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杂多化合物催化丙烷的选择性氧化

杂多化合物由杂多阴离子和阳离子组成,杂多阴离子具有一定的空间结构,多种不同结合强度的晶格氧能够在氧化-还原反应中起传递电子和氧的作用。杂多化合物具有很强的酸性,可用作双功能催化剂。本文以磷、钼、钒杂多酸中掺杂过渡金属离子Cs^2 、Cu^2 、Fe^3 为催化剂,对丙烷氧化反应进行了研究。     

Effect of diluent and reaction parameter on selective oxidation of propane over MoVTeNb catalyst using nanoflow catalytic reactor

The selective oxidation of propane to acrylic acid over an MoVTeNb mixed oxide catalyst, dried and calcined before reaction has been studied using high-throughput instrumentation, which is called nanoflow catalytic reactor. The effects of catalyst dilution on the catalytic performance of the MoVTeNb mixed oxide catalyst in selective oxidation of propane to acrylic acid were also investigated. The effects of some reaction parameters, such as gas hourly space velocity （GHSV） and reaction temperature, for selective oxidation of propane to acrylic acid over diluted MoVTeNb catalyst have also been studied. The configuration of the nanoflow is shown to be suitable for screen catalytic performance, and its operating conditions were mimicked closely to conventional laboratory as well as to industrial conditions. The results obtained provided very good reproducibility and it showed that preparation methods as well as reaction parameters can play significant roles in catalytic performance of these catalysts.     

Kinetics of oxidation of acrolein on a vanadium-molybdenum oxide catalyst

A kinetic study has shown that, in the range of low conversions, the reaction rate depends only on the partial pressure of oxygen. Comparison of the oxidation of acrolein and I-deuteroacrolein suggests that the splitting of the H–CO bond is not rate-limiting.

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, , , . 1- , H–CO .

     

Reactions of o-aminobenzothiazole over a mixed oxide catalyst

A study is made of the reactions undergone by o-aminoethylbenzene over a mixed oxide catalyst at atmospheric pressure, temperature 580 °–620 ° C, either neat, or in the presence of H₂O, CO₂, or N₂ as diluent. It is shown that under those conditions the main reaction is dehydrocyclization of the o-aminoethylbenzene to indole. The maximum yield of indole (39%) is obtained at 620 ° C with dilution with CO₂ or N₂ at a weight ratio 11 or 12, respectively.     

Preparation of polypropylene over a chromium oxide catalyst

Summary The yield of highly crystalline polypropylene was considerably increased by polymerization of propylene on a chromium oxide catalyst in the presence of small amounts of i-(C₄H₉)₃Al.     

Investigation of propylene oxidation on multicomponent a Bi-and Mo-based oxide catalyst

It has been established that porpylene oxidation to acrolein on a multicomponent oxide catalyst containing Mo, Bi, Fe, Ni, Co, K, P and SiO₂ follows an alternating oxidation-reduction mechanism and involves the participation of lattice oxygen with the bond energy of about 280 kJ/mol.

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, Mo, Bi, Fe, Ni, Co, K, P SiO₂ 280 /.

     

Catalytic oxidation of propylene to acrolein on a multicomponent oxide catalyst

Rate equations have been found and reaction schemes for oxidation of propylene to acrolein and acrylic acid have been suggested.

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Oscillatory phenomena during ammonia oxidation in the presence of a PtRh catalyst

The paper describes oscillatory phenomena observed during ammonia oxidation on a PtRh catalyst in a single pellet reactor. The phenomena consist in periodical changes of the catalyst temperature and a periodical initiation of the reaction in the gas phase. They are interpreted via coupling of the catalytic dissociation and homogeneous oxidation of ammonia.

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, PtRh . . .

     

Effect of ammonia on toluene ammoxidation over oxide catalysts

The increased activity of the catalyst for ammoxidation of toluene observed in the presence of ammonia is ascribed to its binding with the acidic centers. which leads to the formation of new active basic sites on the catalyst surface.

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Bi-Pt催化剂在H-mordenite载体上的甘油选择性氧化

以Bi-Pt/H-mordenite为催化剂,对甘油(GLY, Glycerol)选择性氧化制备二羟基丙酮(DHA, Dihydroxyacetone)进行了研究。采用BET对催化剂进行表征,结果表明,催化剂的比表面积对催化剂的反应性能影响较小。甘油的裂解是主要的副反应,而H-mordenite可以抑制甘油的裂解,提高DHA的选择性。最佳反应条件为温度353 K,反应时间2~4 h,空气流量20 mL/min,甘油(水-乙醇1:1混合溶液的质量分数为10%),催化剂为1%Bi-5%Pt/H-mordenite时,甘油的转化率为70.6%,DHA的选择性为61.0%。     

Cr掺杂的丙烷选择氧化制丙烯酸高效催化剂

在丙烷选择氧化制丙烯酸催化剂MoVTeNbOx的活性相M1基础上掺杂一定量的Cr,当Cr/Nb摩尔比为0.002时,催化剂具有很高的丙烯酸选择性(78.3%)和收率(50.7%);并采用X射线衍射、X射线光电子能谱、程序升温还原、O2程序升温脱附、NH3程序升温脱附和异丙醇氧化等手段对催化剂的构效关系进行了探讨.结果表明,适量Cr的添加可调节催化剂表面Mo6+,V5+和Te4+等物种含量,提高催化剂的氧化能力,使丙烷转化率增加.同时,适量Cr的添加使得催化剂表面酸强度下降,酸性位点数量减少,从而抑制丙烯酸的深度氧化,提高了丙烯酸选择性.