Adsorption of Chlorobenzene on V2O5/γ-Al2O3 Catalyst

Isotherms of chlorobenzene adsorption on V₂O₅/-Al₂O₃ catalyst within the 0.07-18 Pa range of adsorbate partial pressure were measured, and certain thermodynamic characteristics of adsorption were found.     

Conversion of Rapeseed Oil to Biodiesel on KF/γ-Al2O3 CATALYST

Theoretical and Experimental Chemistry - It is shown that the KF/γ-Al2O3 catalyst obtained by the sol–gel method has a greater activity in the process of transesterification of methanol...     

High Activity SnO2／Al2O3 Catalyst for NO Reduction in the Presence of Oxygen

The novel sol-gel SnO2/Al2O3 catalysts for selective catalytic reduction NO by propene under lean burn condition were investigated. The results showed thatthe maximum NO conversion was 82% on the SnO2/Al2O3 (5%Sn) catalyst, and the presence of H20 and SO2 improved the catalytic activity at low temperature. The catalytic activity of NO2 reduction by propene is much higher than that of NO at the entire temperature range, and the maximum NO2 conversion reached nearly 100% around the temperature 425℃.     

Adsorption of benzene on the V2O5/γ-Al2O3 catalyst

Adsorption of benzene on the V₂O₅/-Al₂O₃ catalysts was studied in the temperature interval from 443 to 493 K and at partial pressures of the adsorbate ranging from 1 to 400 Pa. The adsorption isotherms were plotted. The isosteric heats and various entropy characteristics of adsorption were determined. Mobility of benzene in the adsorption layer is restricted compared to the model of ideal dimeric gas. The adsorbed amounts of benzene and chlorobenzene are compared.     

A Plasma-Activated Ni/α-Al2O3 Catalyst for the Conversion of CH4 to Syngas

Nickel-based catalysts supported on -Al₂O₃ for the partial oxidationof methane were activated by a glow discharge plasma technique. Theactivating process was simple, quick, audio-visual, and easy to control. Theactivity and stability of the activated catalyst were higher than those ofconventional catalysts. The methane conversion of 98.2% and selectivity of97.3% to hydrogen and 96.5% to carbon monoxide were obtained at850°C. The catalyst could maintain its activity over 15 hr. According tothe results of X-ray diffraction (XRD) and temperature-programmed reduction(TPR), the component of crystal phase and the reducibility of the activatedcatalyst were significantly different from those of conventionalcatalysts.     

Catalytic Conversion of Glycerol in the Presence of Ni/F–Al2O3 Catalyst

Russian Journal of Physical Chemistry A - It is shown that glycerol hydrogenation in the presence of Ni/F–Al2O3 catalyst leads to the formation of simple alcohols ethanol and propanol-1. The...     

Study of CO2 Hydrogenation to Methanol over Cu-V/γ-Al2O3 Catalyst

The effect of vanadium addition to CU/γ-Al2O3 catalyst used in the hydrogenation of CO2 to produce methanol was studied. It was found that the catalytic performance of the Cu-based catalyst improved after V addition. The influence of reaction temperature, space velocity and the molar ratio of H2 to CO2 on the performance of 12%Cu-6%V/γ-Al2O3 catalyst were also studied. The results indicated that the best conditions for reaction were as follows: 240℃, 3600 h-1 and a molar ratio of H2 to CO2 of 3:1. The results of XRD and TPR characterization demonstrated that the addition of V enhanced the dispersion of the supported CuO species, which resulted in the enhanced catalytic performance of CU-V/γ-Al2O3 binary catalyst.     

Structural Aspect of a Thermal Activation Effect in the MnO x /γ-Al2O3 System

Solid-phase reactions in the aluminum–manganese oxide system, including the structural mechanism of the thermal activation of catalysts, were studied at temperatures up to 1100°C. It was found that the solid-phase reaction at 900–1000°C occurred via two pathways because of the diffusion of manganese ions to aluminum oxide and aluminum ions to manganese oxide. Nanoheterogeneous state of the active component, which was observed in the range 25–600°C, is the product of incomplete decomposition of the high-temperature aluminum–manganese phase Mn_{2.1 – x} Al_{0.9 + x} O₄ (0 x 0.6) with a cubic spinel structure; this phase was equilibrium at the synthesis temperature but metastable below 650°C.     

Stereoselective hydrogenation of 2-hexyne on Cu/γ-Al2O3 catalysts

The stereoselective hydrogenation of 2-hexyne in ethanol on Cu/-Al₂O₃ catalysts (1–40 % Cu) at 4–10 atm and 80–120 °C has been studied. The reaction affordscis-2-hexene as the only reaction product in 100 % yield at [Cu] 30 %. For samples with 20 % Cu, hydrogenation proceeds in parallel with absorption of H₂ by the catalyst.Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 7, pp. 1314–1315, July, 1993.     

CuCl/γ-Al2O3上NO脱除过程研究

设计了一系列的对比实验,利用ＸＲＤ,ＸＰＳ,ＴＰＲ,ＥＸＡＦＳ等技术,系统研究了ＣｕＣｌ／γ－Ａｌ２Ｏ３上的ＮＯ脱除反应过程。结果发现,ＣｕＣｌ／γ－Ａｌ２Ｏ３样品暴露在空气中,表面被部分氧化生成ＣｕＣｌ２及ＣｕＯ等,在高温处理和反应过程中,造成样品表面氯的损失,同时生成更多的ＣｕＯ,因而得新还原处理后测活性时,得到高分散的金属铜,使样品的ＮＯ分解活性提高,但由于ＮＯ对低价铜有很强的氧化作用,ＮＯ     

焙烧温度对CuO/γ-Al2O3和CeO2-CuO/γ-Al2O3催化剂NO还原活性的影响

用浸渍法制备了CuO/γ-Al2O3催化剂和CeO2改性的CeO2-CuO/γ-Al2O3催化剂,考察了焙烧温度对CuO/γ-Al2O3和CeO2-CuO/γ-Al2O3催化剂C3H6还原NO反应活性的影响,以及CeO2的添加量对CeO2-CuO/γ-Al2O3催化剂C3H6还原NO反应活性的影响。结果表明,在200 ℃～500 ℃的焙烧温度范围内,焙烧温度对CuO/γ-Al2O3催化剂的活性影响很小；在500 ℃～800 ℃的焙烧温度范围内,随着焙烧温度的升高CuO/γ-Al2O3催化剂的活性急剧下降,由XRD物相测定结果可知,归因于对反应表现惰性的尖晶石CuAl2O4相的生成。当焙烧温度为500 ℃时,CeO2的添加对CuO/γ-Al2O3催化剂的活性影响很小；当焙烧温度为800 ℃时,CeO2的添加对CuO/γ-Al2O3催化剂有明显的助催化作用,当Ce和Cu的摩尔比为1∶10时,NO转化率较为理想。     

Comparison of the Activities of Pd(0) and Pd(I) in Low-Temperature Oxidation of Carbon Monoxide on the Pd/γ-Al2O3 Catalyst

Kinetics and Catalysis - Low-temperature oxidation of carbon monoxide on the Pd/γ-Al2O3 catalyst has been studied at room temperature and atmospheric pressure of air containing 100 mg/m3 CO....     

γ-Al2O3改性对AlCl3/γ-Al2O3催化剂性能的影响

采用HCl和NaOH改性γ-Al2O3载体制备AlCl3/γ-Al2O3固载催化剂,用吡啶-FTIR和吡啶-TPD技术分析了催化剂的表面酸性(酸中心类型、酸强度和酸量),并以1-癸烯齐聚作为探针反应,研究了催化剂的稳定性以及催化剂对聚合反应的影响.结果表明,催化剂含有两种酸类型,即Lewis酸和Br(o)nsted酸,与未改性的催化剂相比,氢氧化钠改性载体制备的催化剂,酸量增大了47％,催化剂催化1-癸烯的齐聚反应活性增加了11.4％;而经盐酸改性制备的催化剂酸量增大112％,催化剂的活性增加了33.6％.酸强度依AlCl3/γ-Al2O3,AlCl3/γ-Al2O3(NaOH),AlCl3/γ-Al2O3 (HCl)的顺序增强.     

Kinetics of Oxidative Cracking of n-Hexane to Light Olefins using Lattice Oxygen of a VOx/SrO-γAl2O3 Catalyst

The kinetics of oxidative cracking of n-hexane to light olefins using the lattice oxygen of VO_x/SrO-γAl₂O₃ catalysts has been investigated. Kinetic experiments were conducted in a CREC Riser Simulator (CERC: Chemical Reactor Engineering Center), which mimics fluidized bed reactors. The catalyst's performance is partly attributed to the moderate interaction between active VO_x species and the SrO-γAl₂O₃ support. This moderate interaction serves to control the release of lattice oxygen to curtail deep oxidation. The incorporation of basic SrO component in the support also helped to moderate the catalyst's acidity to checkmate excessive cracking. Langmuir-Hinshelwood model was applied to formulate the rate equations. The intrinsic kinetic parameters were obtained by fitting the experimental data to the kinetic model using a nonlinear regression algorithm at a 95% confidence interval, implemented in MATLAB. n-Hexane transforms to olefins at a specific reaction rate of 1.33 mol/gcat.s and activation energy of 119.2 kJ/mol. These values when compared with other duplets (i. e., ki° and E_A) for paraffins to olefins, show that indeed olefins are stable products of the oxidative conversion of n-hexane over VO_x/SrO-γAl₂O₃ under a fluidized bed condition. Values of activation energy for all CO_x formation routes indicate that intermediate paraffins are likely to be cracked to form CH₄ than to be converted directly to CO_x. On the other hand, olefins may transform partly, and directly to CO_x (E₉=9.65 kJ/mol) than to form CH₄ (E₈=89.1 kJ/mol) in the presence of excess lattice oxygen. Overall, olefins appear to be stable to deep oxidation due to the role of SrO in controlling the amount of lattice oxygen of the catalyst at the reaction temperature.     

Study of The Pd-B/ γ-Al2O3 Amorphous Alloy Catalyst

The Pd-B/γ-Al2O3 amorphous alloy catalyst and Pd/γ-Al2O3 crystalline metal catalyst were prepared by KBH4 reduction and routine impregnation,respectively.Pd-B/γ-Al2O3 and Pd/γ-Al2O3 catalysts were characterized by XRD and SEM.It was found that the catalytic activity of the Pd-B/γ-Al2O3 amorphous alloy catalyst was higher than that of the Pd/γ-Al2O3 crystalline metal catalyst in the anthraquinone hydrogenation.     

Effect of Temperature on the Deactivation of a Pd-Fe／α-Al2O3 Catalyst for CO Coupling to Diethyl Oxalate

Destructive tests of the catalyst was carried out to study the effect of temperature on the catalytic activity of CO coupling to diethyl oxalate (DEO) over a Pd-Fe/Al2O3 catalyst. It was found that a temperature jump could cause the deactivation of the Pd-Fe/α-Al2O3 catalyst. The catalyst deactivated at different temperatures has different characteristics. After deactivation the crystal structure of α-Al2O3 did not change, but the Pd particle size was enlarged. Most of the Pd^0 were oxidized to Pd^2 . and Fe^2 was oxidized to Fe^3 on the surface of the deactivated catalyst. The catalyst could be regenerated, but its original activity could not be recovered completely.