Influence of ammonia on propylene oxidation on tin-antimony and bismuth-antimony catalysts

The influence of ammonia on the direction of the oxidative transformations of propylene has been studied. Ammonia has been shown to block the surface oxygen of antimony catalysts. As a result, an increase in the selectivity with respect to the products of partial oxidation is observed.

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. , , .

     

Influence of calcination and lithium promotion on the surface properties of oxide supports

Thermal treatment and the addition of lithium influence the surface area of the oxides SiO₂, Al₂O₃ and MgO. A calcination temperature 1073 K causes a significant decrease of the surface area of SiO₂ and Al₂O₃; the same is not observed in case of MgO. Systems Li/MgO and Li/SiO₂ are characterized by a much smaller specific surface area than pure oxides thermally treated at the same temperature.     

Effect of calcination conditions on the catalytic behavior of Te-Mo mixed oxide catalysts in oxidation of isobutane and isobutene

A series of Te-Mo-O catalysts were prepared by decomposing (NH₄)₆TeMo₆O₂₄·nH₂O telluromolybdate under different conditions and tested for the selective oxidation of isobutane and isobutene. Characterization results showed that their structure and properties depend on the calcination conditions. Catalytic tests showed that molybdenum may be the key element for the activation of isobutane, whereas the selective oxidation of isobutene to methacrolein might proceed mainly on the surface of a TeMo-containing crystalline phase.     

Influence of sodium on the catalytic properties of bismuth-molybdenum oxide catalysts

In the ammoxidation of propylene, the presence of a normal NaBi(MoO₄)₂ phase in bismuth molybdenum oxide catalysts decreases the acrylonitrile yield due to its oxidation

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NaBi(MoO₄)₂ -- .

     

Influence of final calcination temperature and calcium addition on the properties of titania-based sulfur recovery catalysts

Compared to traditional alumina Claus catalysts, titania based sulfur recovery catalysts demonstrate improved initial activity for the recovery of elemental sulfur from both hydrogen sulfide and sulfur dioxide and are less prone to aging by sulfation. The influence of the preparation mode on the properties of titania catalysts is studied in detail: With increasing calcination temperature, surface area drastically decreases, whereas mechanical strength goes through a minimum, with only minor modifications of total pore volume and catalytic activity. Addition of calcium during catalyst preparation hinders the loss of mechanical properties while allowing a higher calcination temperature. Hydrothermal aging of such catalysts is therefore limited during operation in the plant.     

Physico-chemical properties of iron-tin mixed oxide catalysts in cyclohexane oxidation

The state of mixed iron-tin oxide catalysts with a variable ratio of their metallic components has been studied by Mössbauer and ESCA spectroscopy. The results are compared with the activity of these catalysts in cyclohexane oxidation.

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- . .

     

Surface and catalytic properties of Cu/Zn mixed oxide catalysts

Copper catalysts supported on zinc oxide, with different loading (1–20 wt.% CuO), were prepared by impregnation of the basic zinc carbonate with a water solution of copper nitrate. The impregnated samples were dried at 120°C and calcined at 400–700°C. The surface and catalytic properties of CuO loaded on ZnO were determined by N₂ adsorption measurements conducted at −196°C and CO oxidation by O₂ at 150–300°C, respectively. The results obtained revealed that the surface and catalytic properties of different solids were dependent upon CuO content and calcination temperature. The specific surface areas of various adsorbents decreased monotonically as a function of both calcination temperature and extent of loading. However, the activation energy of sintering, ΔE_S, was found to increase by increasing the amount of CuO present. On the other hand, the CO oxidation activity on various catalysts was found to increase progressively by increasing the calcination temperature from 400 to 500°C, then decreased by increasing the temperature from 500 to 700°C. The augmentation of CuO content from 1 to 5 wt.% resulted in an increase in the CO oxidation activity, which decreased by increasing the extent of loading above this limit.     

Influence of silica on the properties of evaporated V?Mo oxide catalysts

According to⁵¹V-NMR studies of the state of vanadium ions in parent solutions and in catalysts, evaporated V–Mo oxide catalysts are shown to be more active and selective in acrolein oxidation to acrylic acid than unsupported samples.

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- , , , . e₁V .

     

Effect of calcination temperature on the performance of nano-size iron oxide catalysts for ethylbenzene dehydrogenation

The effect of calcination temperature on the physicochemical properties and catalytic performance of nano-sized Fe-K oxides for ethylbenzene dehydrogenation was investigated. The catalyst calcined at 600°C showed the highest activity. The catalytic activity of the catalysts clearly depended on the structure of the nano-sized iron catalysts.     

Oxidative ammonolysis of 3-picoline on mixed oxide catalysts

The oxidative ammonolysis of 3-picoline has been studied on the following catalysts: V₂O₅ on corundum, V₂O₅ with the addition of 1% of H₂WO₄ on corundum, V₂O₅ + MoO₃ + P₂O₅ (10.350.35) on silica gel, V₂O₅ + Al₂O₃, and a melt of V₂O₅ + TiO₂ (10.22). Mixed catalysts of vanadium and titanium oxides exhibited the highest activity and selectivity. With the passage of 25–45 moles of oxygen (in the form of air), 5–10 moles of ammonia, and 50–70 moles of water per mole of 3-picoline at a temperature of 390–410° C, the amount of nicotinonitrile formed on these catalysts amounted to 85–90% of the theoretically possible amount.Part LXIII of the series Oxidation of organic compounds; for part LXII, see [1].     

Oxidative ammonolysis of 3-picoline on mixed oxide catalysts

The oxidative ammonolysis of 3-picoline has been studied on the following catalysts: V₂O₅ on corundum, V₂O₅ with the addition of 1% of H₂WO₄ on corundum, V₂O₅ + MoO₃ + P₂O₅ (1∶0.35∶0.35) on silica gel, V₂O₅ + Al₂O₃, and a melt of V₂O₅ + TiO₂ (1∶0.22). Mixed catalysts of vanadium and titanium oxides exhibited the highest activity and selectivity. With the passage of 25–45 moles of oxygen (in the form of air), 5–10 moles of ammonia, and 50–70 moles of water per mole of 3-picoline at a temperature of 390–410° C, the amount of nicotinonitrile formed on these catalysts amounted to 85–90% of the theoretically possible amount.     

Influence of phosphorus additives on the properties of Fe?Sb?O oxide catalysts

Modification of the surface of Fe–Sb–O oxide catalysts by phosphorus additives increases the yield of acrylonitrile in the oxidative ammonolysis of propylene, which can be attributed to the increase of the surface concentration of weakly acidic aprotic centers, viz. Sb³⁺ ions.

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, --Sb³⁺.

     

铈铁锆三元复合氧化物上碳烟的催化燃烧

采用水热法制备了纯CeO₂、Fe₂O₃和系列Ce₀.5Fe₀.5-xZr_{xO2复合氧化物催化剂,采用XRD、Raman、H2-TPR和BET等方法对其进行了表征,并利用程序升温氧化反应(TPO)技术研究了其碳烟燃烧催化性能。结果表明,Zr⁴+完全进入CeO2晶格中形成了固溶体,而Fe³+较难进入CeO2晶格中,部分Fe2O3分散在固溶体表面。固溶体形成产生的氧空位和表面高度分散的氧化铁协同作用是铈铁锆三元复合氧化物具有较高碳烟燃烧催化性能的关键。同时,与单纯的铈铁二元复合氧化物相比,Zr⁴+的掺杂明显提高了催化剂的抗老化能力,使Ce0.5Fe0.5-xZrxO2复合氧化物显示出更好的应用前景。在系列样品中,Ce0.5Fe0.30Zr0.20O2样品由于形成了最多的固溶体并具有良好分散性的表面Fe2O3,显示出最好的催化活性和稳定性。其催化碳烟的起燃温度(ti)和峰顶温度(tp)分别为251℃和310℃,长时间高温老化后其ti和tp仍较低,分别为273℃和361℃。}     

焙烧温度对非负载Ni-Mo-Al_2O_3催化剂加氢脱氧性能的影响

采用热分解硝酸镍和钼酸铵的方法制备了Ni-Mo-Al2O3非负载催化剂。分别以乙酸、苯酚为探针分子,在连续流动固定床反应器上评价了催化剂的加氢脱氧活性,并采用XRD、BET、XRD、EDS等技术对催化剂进行了表征,着重考察了焙烧温度对催化剂的晶态结构、表面元素相对含量及催化性能的影响。结果表明,随着焙烧温度的升高,催化剂的比表面积增大,晶化程度提高,焙烧温度550℃时,催化剂表面Ni、Mo、Al的比例达到最优,并具有最好的加氢脱氧活性。在250℃、0.4 MPa条件下,乙酸的脱氧率达到96.0%;在200℃、0.3 MPa条件下,苯酚的脱氧率达到96.8%。     

Cs-Fe-Co-Bi-Mn-Mo复合氧化物选择性催化氧化异丁烯

Mixed oxide catalyst Cs0.1 Fe2Co6BiMnMo12 Ox was prepared by the interprecipitation method, then the catalyst was calcined at different temperature. Selective oxidation of isobutene was carried out in a fixed-bed reactor. The results showed that the catalyst has high catalytic activity. Under the optimum reaction conditions ( n(-C4^= ) : n(O2) = 1:2-1:4, space velocity = 180h^-1, T = 360℃ ), the yield of methacmlein and methacrylic reached 80%, 8 %,respectively. The total yields of liquid products( methacrolein, methacrylic acid and acetic acid) reached about 90%.     

Influence of silica on the phase composition of vanadium-molybdenum oxide catalysts

The presence of silica inhibits the formation of V₂MoO₈ during thermal treatment of vanadium-molybdenum oxide catalysts in air. In its presence, vanadium-molybdenum compounds are formed under reductive conditions.

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- V₂MoO₈. - .

     

Electrocatalytic properties of oxide catalysts on a carbon carrier

Oxygen reduction of H₂O₂ decomposition have been investigated on carbon black and on carbon blacks promoted by cobaltates of different metals. Gas adsorption and electrochemical measurements reveal that the increase in rate on promoted catalysts is connected with the dispersity of cobaltates on the support surface.

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O₂ H₂O₂ , . , , .

     

Adsorption properties of Ni-Pd catalysts supported on aluminum oxide

The surface composition of Ni-Pd/Al₂O₃ catalysts has been studied using XPES and adsorption methods. The bimetallic catalysts differ from the single-metal Ni and Pd catalysts in the dispersivity of the metal phase which depends on the method of preparation and the presence of K⁺ promoter. A catalyst produced by the immersion method is strongly enriched in Pd compared with impregnated catalysts.Translated from Izvestiya Akademii Nauk SSSR, Seriya Khimicheskaya, No. 8, pp. 1746–1751, August, 1991.     

Hydrotalcite-derived Co-containing mixed metal oxide catalysts for methanol incineration

The Co–Mg–Al mixed metal oxides were prepared by calcination of co-precipitated hydrotalcite-like precursors at various temperatures (600–800 °C), characterised with respect to chemical (AAS) and phase (XRD) composition, textural parameters (BET), form and aggregation of cobalt species (UV–vis-DRS) and their redox properties (H₂-TPR, cyclic voltammetry). Moreover, the process of thermal decomposition of hydrotalcite-like materials to mixed metal oxide systems was studied by thermogravimetric method combined with the analysis of gaseous decomposition products by mass spectrometry. Calcined hydrotalcite-like materials were tested as catalysts for methanol incineration. Catalytic performance of the oxides depended on cobalt content, Mg/Al ratio and calcination temperature. The catalysts with lower cobalt content, higher Mg/Al ratio and calcined at lower temperatures (600 or 700 °C) were less effective in the process of methanol incineration. In a series of the studied catalysts, the best results, with respect to high catalytic activity and selectivity to CO₂, were obtained for the mixed oxide with Co:Mg:Al molar ratio of 10:57:33 calcined at 800 °C. High activity of this catalyst was likely connected with the presence of a Co–Mg–Al spinel-type phases, containing easy reducible Co³⁺ cations, formed during high-temperature treatment of the hydrotalcite-like precursor.     

Physico-chemical properties of silica-supported vanadium oxide catalysts

- . TiO₂ ZnO. - CO₂ H₂O. — .

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The effect of visible light on propane and n-butane oxidation has been sutied on a seires of metal oxides. TiO₂ and ZnO have been found to exert a photocatalytic effect. On TiO₂, propane and n-butane are oxidized to CO₂ and H₂O. On ZnO as catalyst, partial oxidation products, aldehydes and ketones, are formed.