Studies on the oxidative dehydrogenation of propane to propene over Co-V-O catalysts

A series of Co-V-O catalysts were prepared and their catalytic performances for the oxidative dehydrogenation of propane to propene were investigated. It was found that the p-type catalysts showed higher catalytic behavior than the n-type catalyst.     

Oxidative dehydrogenation of propane by nitrous oxide and/or oxygen over Co beta zeolite

The oxidative dehydrogenation of propane has been studied with nitrous oxide (or mixture of nitrous oxide and oxygen) as oxidant. Nitrous oxide is a more selective but less active oxidant as compared with molecular oxygen. Upon increasing the concentration of N2O in the reaction mixture of propane and oxygen results in a substantial increase of propane conversion, while the selectivity to propene remains constant. The synergistic effect of O₂ and N₂O leads to a threefold higher yield of propene relative to than that of oxygen or nitrous alone. This revised version was published online in June 2006 with corrections to the Cover Date.     

Oxidative dehydrogenation of propane over chromium and nickel oxide modified V2O5/ZrO2 catalysts

The effect of addition of chromium and nickel oxides on the physicochemical properties and performance of V₂O₅/ZrO₂ catalysts was studied for the oxidative dehydrogenation of propane. Addition of chromium oxide increased, whereas addition of nickel oxide lowered the activity. Selectivity for propene was lower for the doped catalysts. The selectivity was lowered by higher total acidity as well as the higher concentration of stronger acid sites in doped catalysts.     

Oxidative dehydrogenation of propane on TiO2-supported chromium and zinc oxides

Oxidative dehydrogenation of propane has been studied on chromium, zinc and zinc-chromium mixed oxides supported on anatase titania. The order of activity and selectivity to propene was CrTi>ZnCrTi>ZnTi. The activity and selectivity to propene did not change markedly with increase in the reaction temperature.     

介孔氧化铝负载钒催化剂上丙烷氧化脱氢制丙烯

 采用浸渍法制备了介孔氧化铝 (m-Al2O3) 负载钒催化剂 (V/m-Al2O3), 并考察了其催化丙烷氧化脱氢制丙烯反应活性. 通过 N2 吸附-脱附、透射电镜、X 射线粉末衍射、紫外-可见漫反射光谱、氢-程序升温还原和氨-程序升温脱附对催化剂进行了表征. 结果表明, 介孔氧化铝具有大比表面积、窄孔径分布和两维六方相结构, 在其上负载适量的 V 可实现 V 活性物种的高分散及催化剂的弱酸性, 从而有利于提高丙烷转化率和丙烯选择性. 与共合成法制备的含 V 介孔氧化铝 V/m-Al2O3(C) 和浸渍法制备的 V/?-Al2O3 相比, V/m-Al2O3 表现出更高的催化活性. 这与载体较弱的酸性和较大的比表面积以及 V 物种的高分散有关.     

载体对负载型NiSn催化剂丙烷脱氢性能的影响

研究了载体对负载型Ni Sn催化剂丙烷脱氢性能的影响,主要对比考察了以Si O2、Mg O、Al2O3、Mg Al2O4为载体的Ni Sn催化剂的丙烷脱氢性能。采用X射线衍射技术(XRD)、氮气吸附-脱附技术、氨气程序升温脱附技术(NH3-TPD)以及氢气程序升温还原技术(H2-TPR)对催化剂样品进行表征。结果表明,Si O2因具有较大的比表面积、大孔径、酸性较弱等特点,以其为载体制备所得催化剂中Ni2.67Sn2组分含量高,催化剂性能较高。     

P改性V-MCM-41催化剂的合成及其在丙烷直接脱氢中的应用（英文）

钒基催化剂的脱氢性能与表面氧钒物种的形态密切相关。为了进一步增强传统原位合成的V-MCM-41催化剂上钒物种的分散性,本研究通过在制备过程中添加有机磷前驱物的方法对其进行改性。采用XRD、N₂吸附-脱附、TPR、TPD、XPS、拉曼光谱及O₂脉冲等方法对催化剂的结构、钒物种形态及分散度进行了系统的表征。表征结果表明,P改性后V-MCM-41催化剂的比表面积随着P含量的增加而缓慢下降,但整体仍能保持有序的六方介孔结构;P改性后表面钒物种的还原性和分散性均得到改善,聚合形态的钒物种比例明显下降。丙烷脱氢反应结果表明P改性后催化剂的丙烷脱氢性能和稳定性均有提高。在Si/P投料物质的量比为30时制备的催化剂能够获得最大表面钒氧位点和最佳丙烷脱氢性能。     

Oxidative dehydrogenation of propane under steady-state and transient regimes over alumina-supported catalysts prepared from mixed V_2W_4O_（19）~（4-） hexametalate precursors

An integrated approach combining the development of an innovative catalyst and the research of a set of adequate operating conditions for the propane oxidative dehydrogenation (ODH) is described. The experimental set-up, specially designed for steady-state and transient studies is presented. The preparation method, the characterization and the performances in steady-state and transient regimes of catalysts based on V_2W_4O_(19)~(4-) Lindqvist isopolyanion used as a precursor and supported on alumina are reported. The influence of the preparation method of the catalyst and the role of water in the feed gas are more particularly discussed.     

Oxidative dehydrogenation of ethane over sufated zirconia supported oxides catalysts

The oxidative dehydrogenation of ethane into ethylene has been investigated on metal oxide-based sulfated zirconia catalysts at temperatures of 400–600°C. It is found that the activity and selectivity toward ethylene depend on the nature of metal oxide and temperature and that Ni and V oxides supported on sulfated zirconia exhibited higher ethylene yields.     

Ni-V-O催化剂上丙烷氧化脱氢制丙烯的反应

考察了Ｎｉ－Ｖ－Ｏ系列催化剂对丙烷氧化脱氢反应的催化性能,结合ＸＲＤ和电导法等表征结果研究了催化剂的物相结构与仙化活性之间的关系。结果表明：同ｎ型半导体氧化物相比,ｐ型半导体具有优良的催化性能,并且丙烯的选择性与催化剂中ＮｉＯ及Ｎｉ３Ｖ２Ｏ８相的共存有关。适当控制反应条件,４５２℃时该系列催化剂可达到１８．６％的丙烷转化率和４９．９％的丙烯选择性。     

Oxidative dehydrogenation of propane

At temperatures near 650°C and residence times ofca. 3 s, the homogeneous oxidative dehydrogenation (OXD) of propane to propylene and ethylene approached oxygen limiting conditions, even when the reactor was filled with quartz chips. The addition of catalysts that are known to be effective in the OXD of ethane slightly increased the reaction rate, but the selectivities at a given conversion level were the same as those that were achieved in the homogeneous reaction.     

Deep oxidation in propane oxidative dehydrogenation to propene over V2O5/γ-Al2O3 studied by in-situ DRIFTS

In-situ DRIFTS was used to study the deep oxidation of propane, a side reaction during propane oxidative dehydrogenation to propene. Strong adsorption of propene was supposed to be the main reason for the deep oxidation. It was found that gaseous oxygen in the feed and the reaction temperature had great influence on the reaction. To obtain a relative high selectivity to propene, the reaction temperature should be maintained at 150250 °C with a proper content of gaseous oxygen in the feed for a certain catalyst and some modifiers which could weaken the adsorption of propene on the catalyst surface would be favorable.     

Nitrogen‐doped mesoporous carbon materials for oxidative dehydrogenation of propane

The CN‐15‐x series materials with different doses of SBA‐15 template and the CN‐y‐2.0 series materials with different hard templates were prepared by the hard template method with hexamethylenetetramine as the carbon and nitrogen source. The obtained mesoporous carbon materials were characterized by X‐ray diffraction (XRD), N₂ adsorption–desorption, transmission electron microscopy (TEM), Raman spectroscopy, and X‐ray photoelectron spectroscopy (XPS). The catalytic performance of propane oxidative dehydrogenation was determined. The characterization results indicate that the catalytic activity of CN‐15‐2.0 with a bipartite hexagonal ordered structure was higher than those of the other materials. The conversion of propane was 22.98%, and the selectivity toward propylene was 41.70%.     

铯添加对VOx/SBA-15催化剂丙烷氧化脱氢性能影响

我们考察了碱金属铯的添加对具有单一活性中心（分立的VOx四面体）的VOx／SBA-15催化剂上丙烷氧化脱氢反应性能的影响,发现铯的加入可以显著改善丙烯的选择性．在相同的丙烷转化率时,丙烯选择性提高了约10％．对催化剂的X射线衍射,拉曼光谱,程序升温还原,吡啶吸附IR光谱和程序升温脱附表征结果表明,少量碱金属的加入,并未改变活性中心的结构及其可还原性能,但明显降低了催化剂表面酸量,尤其是B酸量,从而有利于产物丙烯的脱附,抑制了深度氧化产物COx的产生,提高了丙烯的选择性．     

TiO2-ZrO2复合氧化物负载的氧化钒催化剂用于丙烷氧化脱氢反应

 丙烷氧化脱氢反应制备丙稀酸，丙烯醛，由于其巨大的工业价值而成为催化领域研究的热点。该反应也可分为两步实现。即先由丙烷到丙烯，再由丙烯到丙稀酸，丙烯醛。后一步已成功的实现工业化，在低温下( £350℃)，使用钒基催化剂，丙稀酸，丙烯醛的产率可高达80%以上。但是，对于前一步，使用迄今为止最有效的V-Mg-O催化剂，在550℃的高温下，丙烯的产率仅为20%。而在如此高的温度下，在紧接着的第二步反应中，大部分的丙烯会直接转化为深度氧化产物（CO2, H2O）。所以，制备一种能在低温下有效实现丙烷氧化脱氢反应制丙烯的催化剂是由丙烷制备高产率的丙稀酸，丙烯醛的另一种途径。\r\n 催化剂V2O5/TiO2最显著的特点是它具有较高的低温催化活性。但是，作为载体材料，TiO2有一些缺点，如比表面较小，热稳定性较差，机械性能较低，抗磨损性较差等。相比之下，载体ZrO2就具有许多TiO2所不具备的优点。第一，ZrO2具有很大的比表面积（＞300m2/g），并且在高温下它也能保持较高的比表面积。第二，ZrO2的热稳定性，机械性能和抗磨损性都较好。第三，金属氧化物在ZrO2表面能够得到很好的分散。第四，ZrO2非常稳定，在烷烃氧化脱氢反应的条件下是惰性的，不参加反应。所以，如果向TiO2中掺杂ZrO2进行改性，能极大的提高其载体的表面积，热稳定性，机械性能和抗磨损性。那么复合载体TiO2-ZrO2很可能成为在低温下丙烷氧化脱氢制丙烯的极有潜力的催化剂载体材料。在本文中，我们采用溶胶-凝胶法，用廉价的无机盐作为初始材料制备了一系列不同TiO2/ZrO2质量比的TiO2-ZrO2复合氧化物作为催化剂载体并研究了这些催化剂用于丙烷氧化脱氢反应的催化活性。     

Oxidative dehydrogenation of propane over Mo/g-Al2O3. effect of precursor

Alumina supported molybdenum oxide was prepared using ammonium heptamolybdate and molybdenum acetate as different precursors. The catalysts were characterized by BET, AAS, SEM-EDAX, XRD, TPR and surface acidity measurements. The characterization results and the catalytic behavior in oxydehydrogenation of propane were similar irrespective of precursor. This revised version was published online in August 2006 with corrections to the Cover Date.     

Influence of redox properties on the activity of iron oxide catalysts in dehydrogenation of propane with CO2

Different Fe-containing catalysts (pure Fe₂O₃, Fe₂O₃ supported on active carbon or g-Al₂O₃, and hydrotalcite derived Mg-Fe oxides) were examined in the dehydrogenation of propane performed in an Ar or CO₂ atmosphere at 873 K. A promoting effect of carbon dioxide was found for the Fe₂O₃ and Fe₂O₃/AC samples. The catalytic results are discussed in terms of redox properties of the catalysts determined by temperature-programmed reduction (TPR). This revised version was published online in August 2006 with corrections to the Cover Date.     

Effect of gallium, aluminium, and chromium on silica supported V-Mg-O catalysts during oxidative dehydrogenation of propane: Kinetic study

The oxidative dehydrogenation （ODH） of propane was conducted on gallium, aluminum, and chromium doped Si30VMgO catalysts. On doping, the concentrations of the phases responsible for the activity and selectivity increased in their concentrations. The reaction studies were conducted in a tubular steel reactor at temperatures of 753, 783, 813, and 843 K and atmospheric pressure. The total flow rates of the feed were chosen as 30, 40, 50, and 60 ml/min. The propane to oxygen ratios were chosen at 1 ： 1, 2 ： 1, and 3 ： 1, respectively. The effect of various dopants on the activity and selectivity of the catalysts was studied. Deactivation studies were conducted over all the catalysts. The kinetic data were analyzed in terms of power law models and Langmuir-Hinshelwood （LH） models. The kinetic data results were analyzed by comparing the effect of dopants. Statistical model discrimination was done for the proposed models. AIC and BIC criteria were used for discrimination of the models.     

Dehydrogenation of propane in the presence of carbon dioxide over oxide-based catalysts

In the present study, we show the advantages of CO₂ use for the dehydrogenation of propane to propene on the basis of thermodynamic considerations and some experimental results. Several metal oxides Ga₂O₃, Cr₂O₃, Fe₂O₃ unsupported and supported on g- Al₂O₃ and SiO₂ were tested. Ga₂O₃ catalyst was found to be an effective agent for dehydrogenation of propane to propene. The yield of propene at 873 K was 30.1 %. This revised version was published online in June 2006 with corrections to the Cover Date.