Mechanosynthesis and mechanochemical treatment of bismuthdoped vanadium phosphorus oxide catalysts for the partial oxidation of n-butane to maleic anhydride

Three Bi-doped vanadyl pyrophosphate catalysts were prepared via dihydrate route （VPD method）, which consisted of different preparation methods including mechanosynthesis, mechanochemical treatment, and the conventional reflux method. The catalysts produced by the above three methods were characterized by x-ray diffraction （XRD）, scanning electron microscopy （SEM）, and temperature programmed reduction （TPR）. Catalytic evaluation for the partial oxidation of n-butane to maleic anhydride （MA） was also carried out. The XRD patterns of all the Bi-doped catalysts showed the main peaks of pyrophosphate phase. Lower intensity peaks were observed for the mechanochemically treated Bi-doped catalyst （VPDBiMill） with two additional small peaks corresponding to the presence of a small amount of V5＋ phase. The TPR profiles showed that the highest amount of active oxygen species, i.e, V4＋–O- pair, responsible for n-butane activation, was removed from VPDBiMill. Furthermore, from the catalytic test results, the graph of selectivity to MA as a function of the conversion of n-butane demonstrated that VPDBiMill was the most selective catalyst. This suggests that the mechanochemical treatment of vanadium phosphate catalyst （VPDBiMill） is a potential method to improve the catalytic properties for the partial oxidation of n-butane to maleic anhydride.     

Effect of tellurium promoter on vanadium phosphate catalyst for partial oxidation of n-butane

Te-promoted (1%) vanadium phosphate catalyst (VPDTe) was prepared via VOPO4·2H2O by calcining its precursor VOHPO4·0.5H2O in a flow of n-butane/air.VPDTe catalyst has resulted a higher existence of V5+ phase with V5+/V4+ ratio of 0.23.SEM micrographs show that Te addition altered the arrangement of the platelets from "rose-like" clusters to layer with irregular shape.Te addition has also markedly lowered the reduction activation energies of the vanadium phosphate catalyst as revealed by TPR profile.The amount of active oxygen species associated with V4+ phase of the Te promoted catalyst was significantly higher than those of the unpromoted catalyst.These observations suggest that high mobility and availability of reactive oxygen species contributed to the enhancement of n-butane conversion up to 80% at 673 K,while only 47% over unpromoted catalyst (2400 h-1,1.7% n-butane in air).     

Promotional Effect of Bismuth as Dopant in Bi-Doped Vanadyl Pyrophosphate Catalysts for Selective Oxidation of n-Butane to Maleic Anhydride

Bismuth-promoted (1% and 3%) vanadyl pyrophosphate catalysts were prepared by refluxing Bi(NO3)3·5H2O and VOPO4·2H2O in isobutanol. The incorporation of Bi into the catalysts lattice increased the surface area and lowered the overall V oxidation state. Profiles of temperature programmed reduction (TPR) in H2 show a significant shift of the maxima of major reduction peaks to lower temperatures for the Bi-promoted catalysts. A new peak was also observed at the low temperature region for the catalyst with 3% of Bi dopant. The addition of Bi also increased the total amount of oxygen removed from the catalysts. The reduction pattern and reactivity information provide fundamental insight into the catalytic properties of the catalysts. Bi-promoted catalysts were found to be highly active (71% and 81% conversion for 1% and 3% Bi promoted catalysts, respectively, at 703 K), as compared to the unpromoted material (47% conversion). The higher activity of the Bi-promoted catalysts is due to that these catalysts possess highly active and labile lattice oxygen. The better catalytic performance can also be attributed to the larger surface area.     

铬掺杂对V2O5/TiO2催化氧化3-甲基吡啶合成烟酸性能的影响

为进一步提高V2O5/TiO2催化剂对气相一步催化合成烟酸反应的活性和选择性.通过浸渍法制备一系列掺杂过渡金属铬的V2O5/TiO2催化剂,并对催化剂进行了BET、XRD、H2-TPR、NH3-TPD表征.结果表明,掺杂Cr后催化剂产生了新晶相CrVO4,减小了V2O5晶粒尺寸,并提高了催化剂的酸性,可较大地提高催化剂...     

Physico-chemicals and catalytic properties of manganese-promoted vanadium phosphate (VPO) catalyst

The addition of 1% Mn promoter to vanadium phosphate catalyst led to doubling of the specific surface area from 20.3 (unpromoted) to 39.4 m² g⁻¹. The XRD pattern of the Mn-promoted catalyst gave only the characteristics of the (VO)₂P₂O₇ phase, indicating that the Mn was incorporated into the crystal lattice of the catalyst. The Mn-promoted catalyst was also twice as active in removing the total amount of oxygen. However, since the only oxygen species related to V⁴⁺ being removed and no oxygen species associated with V⁵⁺ was observed, the n-butane conversion was not much improved as compared to the unpromoted counterpart. A necessary amount and distribution of the V⁵⁺ phase in a well crystalline V⁴⁺ phase is essential in order to enhance the catalytic performance in the mild oxidation of n-butane to maleic anhydride.     

n-Butane Oxidation over γ-Al2O3 Supported Vanadium Phosphate Catalysts

Four vanadium phosphate catalysts supported onγ-Al_2O_3(20 wt%)were synthesized via wetness impregnation of VOHPO_4·0.5H_2O precursor and calcined for different durations(6,10,30 and 75 h)at 673 K in a reaction flow of n-butane/air mixture.The samples calcined for 6 and 10 h produced only a single phase of(VO)_2P_2O_7.However,the VOPO_4 phase(β-VOPO_4)was detected and became more prominent with only a minor pyrophosphate peaks were found after 30 h of calcination.All these pyrophosphate peaks disappeared after 75 h of calcination.The formation of V~(5 )phase was also observed in the SEM micrographs.The redox properties and the nature of oxidants of the catalysts employed in this study were investigated by H_2-TPR analysis.Selective oxidation of n-butane to maleic anhydride(MA) over these catalysts shows that the percentage of n-butane conversion decreases with the transformation of the catalysts from V~(4 )to V~(5 )phases.An appropriate ratio of V~(5 )/V~(4 )can enhance the performance of the VPO catalyst.However,a higher amount of V~(5 )and its associated oxygen species are responsible to promote the MA selectivity.     

Effects of mechanochemical treatment to the vanadium phosphate catalysts derived from VOPO4·2H2O

Modification by using mechanochemical treatment of vanadium phosphate catalysts on the microstructure, morphology, oxygen nature and catalytic performance for n-butane oxidation is described and discussed. In this work, the precursor, VOHPO₄·0.5H₂O prepared by reduction of VOPO₄·2H₂O by isobutyl alcohol was subjected to a high energy planetary ball mill for 30, 60 and 120 min in ethanol. The ball milling process reduced the crystallite size of the catalysts and consequently increased their surface area. The morphologies of the milled catalysts are dependent on milling time. The highest reactivity and mobility of the lattice oxygen species has been achieved by the catalyst milled for 60 min with lower reduction peak temperature and higher amount of oxygen atoms removed. The oxygen species removed from the active V⁴⁺ phase was shown to be correlated with the rate of reaction. A good relationship was also found between the oxygen species associated with V⁵⁺ and maleic anhydride selectivity. However, a larger amount of this oxygen species will give a deleterious effect on the conversion rate. The present study demonstrate that the mechanochemical method (with an appropriate duration) effectively enhanced the catalytic activity by increasing the surface area and controlling the reactivity, and that the amount of oxygen species contributed to the partial oxidation of n-butane to maleic anhydride.     

Synthesis and Characterization of Sol-Gel Cu-ZrO2 and Fe-ZrO2 Catalysts

Fe-ZrO₂ and Cu-ZrO₂ xerogels were prepared by a sol-gel method. The effect of the hydrolysis catalyst during the gelation step, namely H₂SO₄ or NH₄OH, on the properties of the resulting materials was investigated by XRD, BET, TGA/DTA, TPD of ammonia, FTIR, and TPR. Fe-ZrO₂ and Cu-ZrO₂ xerogels, with sulfuric acid introduced as the hydrolysis catalyst, mainly crystallyzed in the tetragonal phase and exhibited larger surface area and acid amount than those obtained with NH₄OH. Ammonia TPD shows that copper promoted sulfated zirconia is the most acidic material. TGA and FTIR reveal that under oxidizing conditions sulfated zirconia promoted with iron and copper retains more sulfate species than unpromoted sulfated zirconia. Regardless of the hydrolysis catalyst employed, copper promoted catalysts calcined at 600°C, contain a large fraction of copper oxide specieseasily reduced at low temperatures. These copper oxide species are believed to have different environment and interactions with the surface oxygen vacancies of the zirconia support. A FeO-like phase appears to be the most probable one after reduction of Fe-ZrO₂ catalysts prepared with NH₄OH as the hydrolysis catalyst. The formation of Fe° species may be hindered by the high dispersion and interaction of Fe²⁺ ions with the zirconia support. On the other hand, the reduction peaks of iron oxide and sulfate species exhibit a considerable overlap in the TPR profiles of sulfated Fe-ZrO₂ samples. Hence, the nature of the supported phase in the latter samples is rather uncertain.     

Photocatalytic oxidation of propylene with molecular oxygen over highly dispersed titanium, vanadium, and chromium oxides on silica

Photocatalytic oxidation of propylene with molecular oxygen at room temperature was investigated over various silica-supported metal oxides with low loading. The photocatalytic active site is assumed to be the isolated tetrahedrally coordinated metal oxides in the ligand-to-metal charge-transferred state, such as (Mdelta- -OLdelta+). Photocatalytic epoxidation of propylene into propylene oxide was promoted over silica-supported V and Ti oxides at steady state. Over silica-supported Cr oxide, the propylene oxide formation rate was remarkably decreased with the time course in the reaction. The oxidation state and the coordination environment of the supported Ti, V, and Cr oxide species were determined by diffuse reflectance UV-vis spectroscopy (DRS) and electron spin resonance (ESR). During the photocatalytic oxidation, the oxidation state of the Ti4+ species was not varied. On the other hand, the V5+ species was partially reduced to V4+ and the Cr6+ species was successively reduced to Cr5+ and Cr3+. An isotopic tracer study of the C3H6-18O2 reaction suggests the difference of the active oxygen species between TiO2/SiO2 and V2O5/SiO2. The active oxygen species on TiO2/SiO2 is derived from molecular oxygen. On the other hand, the photogenerated products on V2O5/SiO2 incorporate the lattice oxygen of the surface metal oxide species. It is suggested that the kinds of terminal ligand (hydroxyl or oxo) of the tetrahedrally coordinated metal oxides on silica decide the active oxygen species in the photocatalytic oxidation. A photoinduced hole center on the monohydroxyl (SiO)3Ti-OH species activates molecular oxygen that reacts with propylene. In the case of the monooxo (SiO)3V=O and dioxo (SiO)2Cr=O2 species, the photoactivated lattice oxygen (OL-) directly reacts with propylene.     

The Effect of Sulfate Ion on the Isomerization of n-Butane to iso-Butane

The effect of sulfate ion (SO42-) loading on the properties of Pt/SO42- -ZrO2 and on the catalytic isomerization of n-butane to iso-butane was studied. The catalyst was prepared by impregnation of Zr(OH)4 with H2SO4 and platinum solution followed by calcination at 600℃. Ammonia TPD and FT-IR were used to confirm the distribution of acid sites and the structure of the sulfate species. Nitrogen physisorption and X-ray diffraction were used to confirm the physical structures of Pt/SO42--ZrO2. XRD pattern showed that the presence of sulfate ion stabilized the metastable tetragonal phase of zirconia and hindered the transition of amorphous phase to monoclinic phase of zirconia. Ammonia TPD profiles indicated the distributions of weak and medium acid sites observed on 0.1 N and 1.0 N sulfate in the loaded catalysts. The addition of 2.0 N and 4.0 N sulfate ion generated strong acid site and decreased the weak and medium acid sites. However, the XRD results and the specific surface area of the catalysts indicated that the excessive amount of sulfate ion collapsed the structure of the catalyst. The catalysts showed high activity and stability for isomerization of n-butane to iso-butane at 200℃under hydrogen atmosphere. The conversion of n-butane to iso-butane per specific surface area of the catalyst increased with the increasing amount of sulfate ion owing to the existence of the bidentate sulfate and/or polynucleic sulfate species ((ZrO)2SO2), which acts as an active site for the isomerization.     

基于脉冲微反装置的Au/HZSM-5催化剂上正丁烷反应性能研究

以HZSM-5沸石分子筛为载体,尿素为沉淀剂,采用常压沉积-沉淀法和负压沉积-沉淀法制备了系列Au/HZSM-5沸石催化剂并采用常规催化剂表征方法对其进行了表征.用脉冲微反装置评价了纯正丁烷(99.9%)在氢型和金改性的纳米HZSM-5催化剂上的反应活性和烯烃选择性.结果表明,在550℃下,负压沉积-沉淀法制备的不同金负载量的纳米HZSM-5催化剂上的转化率和烯烃选择性都远高于常压沉积沉淀法制备的催化剂.改性量为2.0%的Au/HZSM-5-A(负压)催化剂正丁烷转化率达到了58.0%、烯烃选择性为57.2%.脱氢和脱甲基活化是正丁烷的重要活化方式,也是影响其烯烃选择性的主要因素.金改性在提高正丁烷转化率的同时,也促进了正丁烷的脱氢和脱甲基活化.纳米HZSM-5因晶粒度小,孔道短和微孔扩散阻力低而有利于正丁烷转化.负压有利于清除HZSM-5内部的无定型杂质和脱气净化处理,有利于金的负载量和分散度.     

Application of Sol-Gel Method to Preparation of Ultra-Uniform Co-Based Catalysts for Fischer-Tropsch Reaction

Uniformly dispersed Co/SiO₂ catalysts (10–60 wt% on metal basis) were prepared by the sol-gel method, and used for the Fischer-Tropsch (F-T) synthesis in slurry phase at 503 K and 1 MPa in a flow of synthesis gas (H₂/CO = 2/1, W/F = 10 g-catal·h/mol). The catalysts were characterized by temperature-programmed reduction (TPR), X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), transmission electron microscopy (TEM), and chemisorption. Although CO conversion over the unpromoted catalysts prepared by the sol-gel method was lower than the conventional catalysts prepared by impregnation, the catalytic activity of the former catalysts was more stable than the latter catalysts. The conversion was improved drastically, when 0.01–1 wt% of Ir or Ru (on metal basis) was added to the catalysts prepared by the sol-gel method. The TPR and XPS spectra and the H₂ chemisorption revealed that the noble metal addition was responsible for the reduction of Co particles in the catalysts. It is supposed that the durability of the promoted catalysts prepared by the sol-gel method was ascribed to the high dispersion of Co particles stabilized on the catalyst surface.     

Promotion of Mn Doped Co/CNTs Catalysts for CO Hydrogenation to Light Olefins

With various contents, Mn was introduced into carbon nanotubes (CNTs) supported cobalt catalysts and the obtained Mn‐Co/CNTs catalysts were investigated for CO hydrogenation to light alkenes and characterized by N₂ adsorption, X‐ray diffraction (XRD), X‐ray photoelectron spectra (XPS), H₂ temperature programmed reduction (TPR), CO temperature programmed desorption (TPD) and transmission electron microscope (TEM). The results indicate that the addition of a small amount of Mn (0.3 wt%) to CNTs‐supported Co catalyst significantly increased the selectivity of C₂–C₄ olefins and decreased the selectivity of CH₄. However, with further addition of Mn to the cobalt catalysts, the CH₄ selectivity decreased obviously along with the increase of the C₅₊ selectivity. Compared with the unpromoted catalysts, the Mn‐promoted cobalt catalysts increased the C₂^?–C₄^?/C₂⁰–C₄⁰ molar ratio.     

V5+物种对钒磷氧化物催化性能的影响

采用有机相法制备钒磷氧化物催化剂，通过空气或氧气气氛中不同时间的原位预处理以系统调变样品中V⁵⁺物种的含量及其状态，并考察对催化正丁烷选择氧化制马来酐的反应性能的影响。理化表征手段的结果表明，空气或氧气预处理改变了V物种的价态及V⁵⁺/V⁴⁺的相对含量，但对催化剂的比表面积和表面P/V比没有显著影响。表面V⁵⁺/V⁴⁺的合适比例及相应的结构状态可能在V⁵⁺-V⁴⁺物种之间产生较好的协同作用，从而获得较为理想的催化反应性能。     

Cr改性钒基催化剂对NH3低温选择性催化还原NOx的影响

火电厂和机动车辆等的NOx排放量与日俱增, NOx的治理已成为环境保护的重要组成部分.以NH3作为还原剂的选择性催化还原(SCR)技术是目前消除NOx最为高效的方法之一.该反应最为典型的催化剂是V2O5–WO3(MoO3)/TiO2,催化活性窗口为250–400 oC.国外通常将SCR系统置于省煤器之后,此时烟气温度在300 oC以上,催化剂能保持较高的活性,但易受到烟气中高浓度烟尘、SO2和碱金属等的影响,寿命相对较短.此外,高温工艺中副产物硫酸铵的堵塞也是一个不可忽视的问题.因此,将SCR脱硝装置设在脱硫除尘之后成为一种优选技术之一,但烟气温度会降至250 oC以下,而常规的钒基催化剂不能满足低温活性要求.通过添加助剂或改变载体可改善钒基催化剂的低温活性,同时保持其高效的抗硫能力.
　　本文以Cr和V为活性组分, TiO2为载体,采用浸渍法制备了铬钒钛(Cr–VOx/TiO2)系列催化剂,考察了它们的低温脱硝活性和抗水抗硫性,并通过N2吸附-脱附、X射线衍射、NH3程序升温脱附(NH3-TPD)、H2程序升温还原(H2-TPR)和X射线光电子能谱等手段对催化剂进行了表征,分析了Cr–V催化剂的作用机制.
　　结果显示,当n(Cr)：n(V)为0.2：0.8,活性组分负载量为10 wt%时, Cr–VOx/TiO2催化剂表现出最佳的低温催化活性;当反应温度为160°C时, NOx转化率达到90%以上,明显优于其他催化剂,同时活性窗口(160–300°C)得到拓宽. NH3-TPD结果表明, VOx/TiO2催化剂表面呈中弱酸性,随着Cr的添加,钒基催化剂的NH3脱附峰向高温拓宽,说明其表面强酸量有所增加, Cr0.2–V0.8/TiO2在160–300°C范围内均出现了NH3的脱附峰,此时催化剂表面弱酸量最大.当n(Cr)：n(V)大于0.2：0.8时,催化剂表面出现强酸位,这种强酸位不利于NH3脱附,从而不利于SCR反应的进行.因此适量Cr的添加有助于提高钒基催化剂表面弱酸及中性酸量. H2-TPR结果发现,助剂Cr的添加使得催化剂表面氧量增加,这可能是由于Cr的添加形成了较多的氧空穴和未饱和的化学键.催化剂表面化学吸附氧是氧化还原反应最活跃的氧物种,在SCR反应中,表面氧可作为NO的吸附介质参与到催化剂表面反应中,可有效提高SCR反应速率.通过考察活性组分负载量对催化剂活性的影响,发现不同负载量催化剂的催化活性依次为10 wt%>20 wt%>50 wt%>5 wt%. XPS分析发现,当负载量为10 wt%时,催化剂表面非计量的钒离子和化学性质活跃的自由电子最多,因此表现出最佳的SCR活性;当负载量过高时,大量氧化物堆积烧结形成V2O5和Cr2V4O13,覆盖了钒离子活性位点,降低了催化剂脱硝效率.
　　催化剂在220°C表现出良好的抗硫性,在通入100 ppm SO212 h后NOx的转化率仍可达99%以上,并未出现硫中毒现象.同时该催化剂也表现出较好的抗水性,在通入10 vol%水蒸气12 h后, NOx转化率仍能达85%以上.     

Studies on Kinetic Properties of Active Oxygen on the Surfaces of V_2O_5/SiO_2, V_2O_5-MoO_3/SiO_2 and V_2O5-P_2O5/SiO_2 Catalysts

Applying the TPD-MS with a high sensitivity of determination, the TPD spectrum of surface oxygen of V2O5/SiO2, V2O5-MoO3/SiO2 and V2O6-P2O5/SiO2 catalysts was obtained. The surface oxygen of these catalysts can be divided into three groups according to the desorption temperature. O2- desorbs mainly from 373K. to 423K, O- from 673K to 873K and O2- at above 873K. The activation energy and frequency factor of all the three kinds of oxygen species were calculated. Based on these results, the mechanism of oxygen desorption and the influence of P2O5 and MoO3 on the properties of oxygen supply of V2O5/SiO2 catalst were investigated. MoO3 and a small amount of P2Os increase the number of supplying oxygen and increase the activity of O- species. A large amount of P2O5 increases the number of supplying oxygen and restrains the activity of O- species.     

钙钛矿型La1+X/2Sr1-x/2Co1-xCuxO3催化CO氧化活性与表征

The catalytic activity and the reactive properties of perovskite-type oxides catalysts La(1+x/2)Sr(1-x/2)Co1-xCuxO3 for CO oxidation reaction were investigated. Results showed that the catalytic activity for CO oxidation reached to a maximum when x＝0.4. The temperature for complete CO oxidation under atmospheric and experimental conditions was 168℃. According to the stoicheometry of catalyst, all catalysts were oxygen defect compounds. The active oxygen species on this catalyst was the adsorbed oxygen which was adsorbed on the surface lattice oxygen defect. It was also found that Co4+ existed in the catalysts and the sufrace active oxygen species was caused by the Co4+. It was concluded that CO oxidation reaction on this catalyst was carried out by the valence change between Co3+ and Co4+ which was adjusted by the adsorbed oxygen.     

Co-Cr-O复合氧化物上丙烷低温完全氧化:结构效应、反应动力学和原位光谱研究（英文）

低碳烷烃是一类主要的挥发性有机污染物(VOCs),广泛生成于汽车尾气以及各种工业过程如煤处理、石油精炼以及天然气处理等.随着对环保要求的日益提高,对高效VOCs消除技术的需求愈加迫切.催化完全氧化(催化燃烧)技术具有起燃温度低、能耗低、净化效果好(无二次污染)等优点,因而极具应用潜力.对于低碳烷烃的催化燃烧,贵金属催化剂如Pt和Pd等具有很高的反应活性,但存在价格昂贵并易中毒等缺陷限制了其商业应用.另一方面,过渡金属氧化物由于其价格低廉、抗中毒性能优异及热稳定性好等特点受到广泛关注.Cu,Mn,Co,Fe等氧化物都具有良好的催化活性,其中Co氧化物由于其在丙烷催化燃烧中的高活性受到关注.而在Co氧化物中添加第二金属更能促进其反应性能.因此本文制备了一系列不同Co/Cr比例的复合氧化物用于丙烷催化燃烧,考察了催化剂结构和表面性质对其反应行为的影响,并通过反应动力学和原位光谱技术对反应机理进行了探索.实验结果表明,随着Co/Cr比例的变化,催化剂的晶相结构、颗粒尺寸、比表面积、表面酸性以及氧化还原性等特性均发生了明显变化,进而影响了其反应行为.当Co/Cr比例为1/2时(1Co2Cr),催化剂为尖晶石结构并具有最大的比表面积.该催化剂上具有最高的反应活性(250℃时反应速率为1.38μmol g^-1 s^-1),可归因于其最高的表面酸性和低温氧化还原性能的协同作用.反应动力学结果表明,1Co2Cr催化剂上丙烷和氧气的反应级数分别为0.58±0.03和0.34±0.05,低于2Co1Cr(分别为0.77±0.02和0.98±0.16)和1Co5Cr(分别为0.66±0.05和1.30±0.11),表明1122Cr催化剂相比后二者具有更高的丙烷和氧气表面覆盖度,得益于其更高的表面酸性和更好的低温氧化还原性能.此外,原位红外光谱表明,在反应过程中,1Co2Cr催化剂上的主要表面物种为多齿碳酸盐,该物种在低温时(<250℃)在表面积聚,但在高温时被分解.     

掺杂Pr对VPO催化剂性质的影响

在ＶＰＯ催化剂中添加Ｐｒ，用ＸＲＤ，ＬＲＳ，ＸＰＳ，ＥＳＲ和＾３１Ｐ固体核磁共振考察了催化剂的相组成和钒的氧化态，用ＮＨ３－ＴＰＤ和吡啶吸会原位红外光谱表征了催化剂表面的酸量。将催化剂应用于正丁烷选择氧化生成顺酐的反应中，实验结果表明，当Ｐｒ／Ｖ原子比＝０．０５时，活性相（ＶＯ）２Ｐ２Ｏ７的量增加，表面酸性增强，正丁烷转化率和生成顺酐的选择性都有所提高，而Ｐｒ／Ｖ≥０．１０时，（ＶＯ）２Ｐ２Ｏ７的     

Cr掺杂的丙烷选择氧化制丙烯酸高效催化剂

在丙烷选择氧化制丙烯酸催化剂MoVTeNbOx的活性相M1基础上掺杂一定量的Cr,当Cr/Nb摩尔比为0.002时,催化剂具有很高的丙烯酸选择性(78.3%)和收率(50.7%);并采用X射线衍射、X射线光电子能谱、程序升温还原、O2程序升温脱附、NH3程序升温脱附和异丙醇氧化等手段对催化剂的构效关系进行了探讨.结果表明,适量Cr的添加可调节催化剂表面Mo6+,V5+和Te4+等物种含量,提高催化剂的氧化能力,使丙烷转化率增加.同时,适量Cr的添加使得催化剂表面酸强度下降,酸性位点数量减少,从而抑制丙烯酸的深度氧化,提高了丙烯酸选择性.