助剂P对Ni-Al-O催化剂乙烷氧化脱氢性能的影响

通过一锅水热法制备了一系列磷改性Ni-Al-O催化剂(Px-Ni-Al-O)，以O₂为氧化剂，评价了系列催化剂的乙烷氧化脱氢制乙烯性能。结果表明，助剂P的掺入不仅可以减小NiO晶粒的尺寸，还影响了Ni和Al之间的相互作用。在350~475℃的温度范围内，P改性Ni-Al-O催化剂上乙烯选择性均高于未改性的催化剂，且适量P的引入还可以提高乙烷转化率。当反应温度为475℃时，P_0.15-Ni-Al-O催化剂上乙烯选择性和收率分别为61.4%和31.9%。此外，P改性后的催化剂表现出较强的抗积碳性能，连续反应22 h不失活。     

掺杂钛酸盐对乙烷氧化脱氢催化性能的研究

在７００￣８５０℃范围内研究了掺杂ＣａＴｉＯ３、ＳｒＴｉＯ３催化剂用于乙烷氧化脱氢（ＯＤＨＥ）的催化行为，发现这类催化剂对ＯＤＨＥ均有一定的催化活性。适量的Ｌｉ＾＋取代Ｔｉ＾４＋后不仅提高了催化活性，而且改善了催化剂对乙烯的选择性。催化剂ＣａＴｉ０．９Ｌｉ０．１Ｏ３－δ在８５０℃时乙烷转化率和乙烯选择性分别为８７．８％和７１．７％。Ｓｒ对Ｃａ部分取代后制得的催化剂可在极宽的温度范围内（７００￣８５     

不同助剂掺杂的铬基催化剂的制备及其对乙烷氧化脱氢的催化性能

以硝酸盐作为前驱体,Al₂O₃为载体,采用等体积浸渍法制备了系列不同助剂（Mn, Co, Ce）及不同助剂含量（1%, 3%, 5%, 7%, 10%）掺杂的铬基催化剂,其结构经X-射线粉末衍射(XRD)、 H₂程序升温还原(H₂-TPR)和CO₂程序升温脱附（CO₂-TPD）表征。并考察了催化剂对乙烷氧化脱氢反应的催化性能。结果表明：添加Co助剂有利于活性组分铬的分散,10Cr₃Co/γ-Al₂O₃催化剂表现出最佳催化性能,在反应温度为650 ℃, V(CO₂) ：V(C₂H₆)=3 ：1,空速(GHSV)为3 600 mL·（g·h）^-1条件下,在该催化剂上乙烯产率为36.5%。     

乙烷在钛酸盐复合氧化物上的氧化脱氢Ⅰ.锂掺杂对催化性能的影响

研究了掺杂钛酸盐催化剂用于乙烷氧化脱氢的催化行为，发现适量的Ｌｉ＾＋取代Ｔｉ＾４＋后可明显改善催化剂对乙烯的选择性。催化剂ＣａＴｉ０．９Ｌｉ０．１Ｏ３－δ在８５０℃时乙烷转化率和乙烯选择性分别为８７．８％和７１．７％，乙类的单程收经为６３．０％．催化剂Ｓｒ０．９Ｃａ０．１Ｔｉ０．９Ｌｉ０．１Ｏ３－δ可在极宽的温度范围内保持很高的乙烯选择性。     

阶跃过渡应答技术研究Mo-V/Al2O3催化剂上乙烷氧化脱氧制乙烯反应的暂态动力学Ⅱ.乙烷氧化脱氢反应的机理和动力学参数的求取

通过一系列应答实验，证实了氧在ＭｏＯ３－Ｖ２Ｏ５／Ａｌ２Ｏ３催化剂上的吸附和吸附态氧转变为晶格氧的过程是慢过程，是乙烷氧化脱氢反应的速度控制步骤；乙烯的深度氧化是乙烯与催化剂表面上吸附态氧作用的结果，而不是与催化剂上晶格氧作用的结果。结合第Ⅰ部分的实验结果，提出了乙烷氧化脱氢制乙烯反应的机理，并用Ｔｒｅａｎｏｒ法和ＤＦＰ法求取了各基元步骤的速率常数、活化能和指前因子等动力学参数。用计算所得的结果进     

可动氧与载体对钴基催化剂的乙烷氧化脱氢性能的影响

 报道了未担载的氧化钴与担载在SiO2和Al2O3上的氧化钴的乙烷氧化脱氢行为,发现未担载的氧化钴在150℃的低温下就有活性．XRD研究表明,Co3O4为活性晶相组分,其含量与催化剂的焙烧温度密切相关,经500℃和1000℃焙烧的未担载的氧化钴中Co3O4晶相分别占100％和66％．对于担载型氧化钴催化剂,载体与氧化钴间的相互作用以及不同的氧化钴担载量导致催化性能发生明显改变．氧化钴与载体间的作用越强,催化活性越低．Co3O4也是担载型氧化钴催化剂的活性晶相．催化剂的O2－TPD－MS和H2－TPR研究结果表明,反应的活性氧物种为在低温下易脱除和易还原并具有较高流动性的可动氧．     

乙烷氧化脱氢制乙烯反应中制备方法及助剂对镍基催化剂性能的影响

采用不同方法制备了镍基催化剂,并考察了乙烷氧化脱氢制乙烯(ODE)的反应活性,结果表明,在3种不同制备方法的催化剂上,ODE反应的活性及产物选择性存在明显差异,浸渍法制备的催化剂性能最佳.在相同的条件下,以共浸渍法引入CeO2助剂后,N iO/-γA l2O3催化剂上的低温选择氧化活性显著提高,而目的产物C2H4的选择性变化不大.XRD,还原TG和XPS对催化剂进行表征的结果显示:反应的活性物相可能是易于还原的高度分散于催化剂表面的微晶N iO和表面尖晶石N iA l2O4物相;高分散的微晶N iO,类似于纯N iO,有利于ODE反应低温选择氧化生成目的产物C2H4,而易还原的表面尖晶石N iA l2O4物相的存在则可能是在高温下获得高选择氧化活性和选择性的主要原因之一.     

Li^＋／MgO上乙烷氧化脱氢制乙烯的研究（Ⅱ）：催化作用机理

借助ＸＲＤ、ＩＲ、ＴＧ等技术对Ｌｉ＾＋／ＭｇＯ进行了表征，结果表明，酸、碱中心的数目，强度、催化性与Ｌｉ＾＋的添加量相关 ，起酸碱作用的表面金属离子、表面低配位氧集团、Ｏ（Ｌ ｉ＾＋Ｏ＾－）是其反应的活性物种，反应机理可能由离子基、游离基协同完成。     

负载型SBA-15铬基催化剂的制备及其 催化CO2氧化乙烷脱氢性能

采用水热法制得具有不同孔径的SBA 15材料;采用浸渍法制备了负载型铬基SBA 15催化剂,其结构和性能经XRD、低温氮气吸附脱附、氢气程序升温还原和X 射线光电子能谱表征。并研究了催化剂的CO2氧化乙烷催化脱氢性能。结果表明：孔径对活性组分在SBA 15孔道内外的分布有影响,进而影响其催化性能。孔径为8.14 nm时,乙烷转化率25.8%,乙烯选择性81.0%。     

水蒸汽对Mn-Na2WO4/SiO2催化剂上乙烷氧化脱氢的影响

在Ｍｎ－Ｎａ２ＷＯ４／ＳｉＯ２催化剂上,考察了水蒸汽对惭烷氧化掊氢制乙烯反应伯影响。结果表明加入适量水蒸汽对提高乙烯选择性有利。在催化剂装量１０ｍＬ,Ｖ（Ｃ２Ｈ６）：Ｖ（Ｏ２）：Ｖ（Ｈ２Ｏ）＝１：０．６５：３．８,ＧＨＳＶ＝１６００ｈ＾－１,７４０℃时,乙烯收率仍可以稳定在５２％以上,过多加入水蒸汽将使催化剂活性很快下降,反应后的催化剂经ＸＲＤ及ＸＰＳ表征表明,不仅单层Ｎａ２ＷＯ４有流失,而且载体     

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.     

Oxidative dehydrogenation of ethane over movmnw oxide catalysts

Catalysts based on mixed oxide of MoVMn are active at relatively low temperature for oxidative dehydrogenation of ethane. Incorporation of tungsten into MoVMn oxides enhances the catalytic activity. Enhancement of the activity is explained in the light of acid-base interaction accompanied with a redox mechanism of surface reoxidation. This revised version was published online in June 2006 with corrections to the Cover Date.     

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.     

Electric heating of the Mo–V–Fe–Nb–Ox catalyst bed in oxidative dehydrogenation of ethane

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Catalytic activity in the oxidative dehydrogenation of ethane over Ni and/or Co molybdate catalysts: Synthesis and characterization

Ni and/or Co molybdate based catalysts were synthetized by co-precipitation for the oxidative dehydrogenation of ethane reaction. The catalysts were characterized by several techniques such TGA-DTA, HT-XRD, XRD, LRS, N₂ adsorption, XPS and TPR. The results showed that the addition of Ni or Co to MMoO₄matrices (M=Ni or Co) led to a high dispersion of additives into the molybdenum matrix without the formation of a significant amount of other bulk metal oxides. Compared to the pure MMoO₄, the modified molybdenum (Ni_0.5Co_0.5MoO₄) presents a higher thermal stability (up to 1000 °C). It has a lower BET surface area and higher reduction temperature compared to those of the NiMoO₄ sample. In the ODH of ethane, Ni_0.5Co_0.5MoO₄ shows a lower catalytic activity compared to that of MMoO₄ samples; however, the ethylene selectivity is enhanced (exceeding 90%). As a result, these series of catalysts show improved efficiency for ethylene production in the ethane ODH reaction.     

Effect of group VIII elements on the behavior of Li/CaO catalyst in the oxidative dehydrogenation of ethane

The effect of addition of group VIII elements to Li/CaO on the oxidative dehydrogenation of ethane has been investigated in the range of 550–650°c. Iron, cobalt and nickel promote the reaction. The experiments show that iron and cobalt additives in Li/CaO catalysts mainly increase the catalytic activity. Li/Ni/CaO catalyst gives a high ethane conversion and excellent ethylene selectivity. The results on the catalyst are probably due to coordinative interaction between lithium and nickel. The characteristics of the catalysts revealed by XRD also give evidence that the promotion for both catalytic activity and ethylene selectivity is directly related to the formation of favorable crystal phases.     

Preparation of MoVTe(Sb)Nb mixed oxide catalysts using a slurry method for selective oxidative dehydrogenation of ethane

The preparation of bulk MoVTe(Sb)Nb mixed oxide catalysts using a traditional slurry method, results in highly active catalysts for oxidative dehydrogenation of ethane to ethene. Several major phases including orthorhombic M1, hexagonal M2 or Mo_xM_1−xO_2.8 (M = V or Nb) have been detected in the catalysts from characterization results such as X-ray diffraction (XRD), SEM and EDX analyses. Ethane conversion and yield to ethene increase with increasing content of the M1 phase in the catalysts. The maximum yield of ethene (ca. 87% selectivity and ca. 90% conversion, STY_C2H4 of 176 g  h⁻¹) has been obtained with a MoV_0.31Te_0.2Nb_0.14 mixed oxide catalyst, calcined at 873 K under nitrogen, containing almost pure orthorhombic M1 phase and small amounts of unidentified impurity phases, operating at a relatively low reaction temperature of 673 K. The orthorhombic M1 phase has been shown to be the most active in ethane activation and the most selective for ethene formation. The hexagonal M2 phase is relatively inactive in ethane activation and less selective for ethene formation. The Te-free phases such as Sb₄Mo₁₀O₃₁ and Mo_xM_1−xO_2.8 (M = V or Nb) show the lowest selectivity to ethene.     

Oxidative dehydrogenation of propane over Ni-Mo-Mg-O catalysts

In this work, a series of Ni-Mo-Mg-O catalysts with mesoporous structure prepared by sol-gel method were investigated for the oxidative dehydrogenation of propane (ODHP). The techniques of temperature-programmed reduction with H2 (H2-TPR), N2 adsorption-desorption, Fourier transform infrared spectroscopy (FT-IR), X-ray diffraction (XRD) and X-ray photoelectron spectra (XPS) were employed for catalyst characterization. It is found that the activity of the catalysts for ODHP increases first and then decreases with the increase of Mo content. The catalyst with a Mo/Ni atomic ratio of 1/1 exhibits the best catalytic activity, which gives the propene selectivity of 81.4% at a propane conversion of 11.3% under 600°C and maintains the good catalytic performance for 22 h on stream. This is related not only to its high reducibility and dispersion as revealed by TPR and XRD, but also to the formation of more selective oxygen species on the MoOx-NiO interface as identified by XPS.     

In situ CO2 reactivation of FeCrOx/C catalyst in the oxidative dehydrogenation of ethane to ethylene

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