Kinetic laws for dehydrogenation of cyclohexane over Pd/C catalysts

A kinetic equation for cyclohexane dehydrogenation at P_O=1.0 MPa has been obtained.

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甲醛还原Pt/TiO2催化剂用于温和条件下高效催化氧化甲醛

通过浸渍法(IM)和沉积-沉淀(DP)法制备了一系列Pt/TiO2(P25)催化剂,并分别用甲醛溶液和氢气还原处理催化剂.利用原位红外监测催化剂表面吸附物种在反应过程中的变化,探究了催化剂制备和还原条件及Pt负载量对催化剂结构和催化氧化甲醛活性的影响.结果显示,用DP法制备并用甲醛还原的Pt/P25催化剂中Pt颗粒分散均匀,并具有合适的粒径和高浓度的表面活性氧,显示出良好的甲醛氧化活性.在空速30000 ml/(g·h)、反应温度30°C和甲醛初始浓度50 mg/m3的条件下,0.4%Pt/P25(DP-HCHO)上的甲醛转化率达到98%,并能稳定运行100 h以上.相比之下, Pt/P25(DP-H2)由于表面活性氧较少,不利于甲酸盐氧化,活性较低. Pt/P25(IM-H2)虽然具有高浓度的表面活性氧,却同时具有最大的Pt颗粒粒径,在甲醛转化为甲酸盐和甲酸盐氧化两步反应中的活性均较差,因而甲醛氧化活性最差.     

Importance of surface morphology in n-pentane reactions over Pt/alumina catalysts

The hydrocracking activity of a Pt/alumina catalyst has been determined and found to depend on surface morphology. Observed differences in thermal stability depend on whether the Pt is initially in a reduced or oxidized form. Various models proposed to account for the loss of hydroracking activity are re-examined in the light of the new data.

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Dehydrogenation of cyclohexane over Pt/SiO2?AlPO4 catalysts, I. Influence of the catalyst particle size

The influence of Pt loading on the metal dispersity and catalytic activity of Pt catalysts on SiO₂−AlPO₄ in the dehydrogenation of cyclohexane to benzene has been analyzed. Kinetic parameters and apparent reaction rate constants were determined by the Bassett-Habgood equation. Thermodynamic parameters for the reaction were determined.     

Selective oxidation of CO under conditions of catalyst surface ignition

The oxidation of CO in the presence of an excess of hydrogen and to 20% CO₂ and H₂O in the starting mixture was studied in flow reactors with high and low rates of heat removal. The ignition of the catalyst surface was observed in the reactor with a low rate of heat removal; catalyst surface ignition initially occurred at a “hot” spot (section) of the catalyst bed and gradually propagated along the bed. Experimental data on the relaxation dynamics of residual CO concentration and temperature in a catalyst bed under conditions of small heater temperature disturbances near and at the critical temperature of ignition and the effect of oxygen concentration in the starting mixture on this process are reported. It was found exprimentally that the ignition regime in the tested cases was more favorable for the selective oxidation of CO in an excess of hydrogen than the reaction in an isothermal reactor; this was likely due to the more favorable temperature distribution over the length of the catalyst bed.     

Study of cyclohexane conversion on A Pt/Al2O3 catalyst under reforming conditions by a gradientless method

A common type of rate equations for hydrocarbon conversions under reforming conditions has been shown, resulting from the features of the hydrocarbons and hydrogen adsorption on the Pt/Al₂O₃ catalyst. This has been confirmed by variations in the rate of cyclohexane conversion observed upon the introduction of methane into the reaction mixture. Methane does not react but is strongly adsorbed on the catalyst surface.

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Liquid-phase catalytic hydrogenation of 3,4-dichloronitrobenzene over Pt/C catalyst under gradient-free flow conditions in the presence of pyridine

Experimental data on nitro compound uptake, the intermediate product accumulation, and the corresponding amine compound generation were obtained on hydrogenating 3,4-dichloronitrobenzene over Pt/C catalyst in the gradient-free flow regime in the presence and absence of pyridine. In addition, a side reaction of dehalogenation was investigated. The role of pyridine admixture on every step of the process was analyzed and the rate of hydrogenation of the nitro compound was determined both in the presence and in the absence of inhibitor.

     

Investigation of n-heptane conversion over Pt?Al2O3 catalysts under gradientless reforming conditions

The rates of the total and individual directions of n-heptane conversion in reforming over platinum-on-alumina catalysts were shown to be independent of dilution with hydrogen. They can be described by simple equations following from kinetic concepts in ideal adsorbed layers.

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Transformation of the phase structure of an iron oxide catalyst for dehydrogenation of methyl butenes under industrial exploitation conditions

X-ray phase, differential-thermal, and elemental analyses were used to study the transformation of the phase structure of an iron oxide catalyst for dehydrogenation of methyl butenes after exploitation.     

Highly efficient iridium catalyst for asymmetric transfer hydrogenation of aromatic ketones under base-free conditions

[reaction: see text] Catalytic systems generated in situ from the chiral PNNP ligands with iridium or rhodium hydride complexes exhibited excellent catalytic activity and good enantioselectivity in the asymmetric transfer hydrogenation of aromatic ketones without added base. The best result was obtained in the IrH(CO)(PPh(3))(3)-ligand 2 catalytic system with up to 99% yield and 97% ee.     

A desorption thermographic study of the nature of surface heterogeneity of catalysts and sorbents

Conclusions The type of surface heterogeneity of catalysts and sorbents may be determined by desorption thermography from the shift in position of an extreme desorption rate value relative to the extreme point on the differential thermal analysis curve.Translated from Izvestiya Akademii Nauk SSSR, Seriya Khimicheskaya, No. 6, pp. 1377–1379.     

Selective deposition of Sn on the Pt surface of Pt/ZnAl2O4 catalyst and addition effect on isobutane dehydrogenation

Pt−Sn bimetallic catalysts were prepared by a CVD technique in which Sn was added by passing volatile organometallic compounds over Pt/ZnAl₂O₄ in a H₂ flow. Mixed Pt−Sn sites improve the activity of isobutane dehydrogenation, while Sn on the support improves the selectivity.     

Pt/SAPO-11临氢异构化催化剂反应特性的研究

以正庚烷为模型化合物，在10 mL连续流动固定床反应装置上，考察了温度、压力、空速与氢烃摩尔比对0.4%Pt/SAPO-11催化剂临氢异构化反应性能的影响。结果表明，催化反应以烷烃异构化为主，正庚烷转化率达70%时异构产物选择性保持在90%以上，压力和氢烃摩尔比较小时，产物的选择性较高；压力太高裂解产物生成量增多对异构化选择性不利。获得了正庚烷在Pt/SAPO-11催化剂上临氢异构化的优化反应条件为，360 ℃～380 ℃，0.5 MPa～1.0 MPa，2.1 h-1～4.1 h-1，H2/CH(摩尔比)2～6；烷烃临氢异构化反应的一个条件变化，需要其他条件的改变来达到最佳的匹配。     

A facile and convenient method for synthesis of alkyl thiocyanates under homogeneous phase transfer catalyst conditions

A simple and environmentally friendly method is described for the efficient conversion of alkyl halide to alkyl thiocyanate using tetrabutylammonium bromide （TBAB） as a phase transfer catalyst. The reactions occur in water and furnish the corresponding alkyl thiocyanate in high yields. No evidence for the formation of isothiocyanates as by-product of the reaction was observed and the products were obtained in pure form without further purification.     

Formation of the surface of Pt-Ni-Cr/C catalysts under reducing conditions

Russian Chemical Bulletin - The mutual influence of metals in processes of reduction of mono-, bi-, and trimetallic Pt-Ni-Cr catalysts on the Sibunite (C) carbon support during the...