丙烷氧化脱氢催化剂V2O5/MPO4(M=Al,Zr,Ca)的研究

制备了3种磷酸盐(MPO₄,M=Al,Zr,Ca)载体,并在其上负载0.6%～6.0%的V₂O_5.活性评价结果表明,负载型V₂O₅/MPO₄催化剂在丙烷氧化脱氢反应中具有良好的催化性能.丙烯选择性按V₂O₅/Ca₃(PO₄)₂>V₂O₅/Zr₃(PO₄)₄>V₂O₅/AlPO₄顺序降低,这与载体的碱性强弱顺序变化一致.载体的性质和钒的负载量影响催化剂的氧化还原性能.ESR结果表明,V⁴⁺离子能可逆存在于催化剂中,暗示V⁵⁺/V⁴⁺氧化还原偶参与了氧化还原反应.     

钒基催化剂在双氧水存在下对甲、乙苯液相选择氧化的研究

研究了若干钒基催化剂在双氧水存在下对甲、乙苯的液相选择性氧化催化性能.结果表明:在乙腈为溶剂的反应体系中,所研究的钒基催化剂包括VPO,VOPO₄,V₂O₅,VO(acac)₂和NH₄VO₃等均表现出以苯甲醛为甲苯选择性氧化主产物和以苯乙酮为乙苯选择氧化主产物的反应结果;从反应活性和主产物选择性来看,按以下顺序递减:VPO＞V₂O₅＞VOPO₄＞VO(acac)₂＞NH₄VO₃.对于具有(VO)₂P₂O₇晶相的VPO催化剂,在双氧水存在下对甲苯选择性氧化主产物苯甲醛的最高选择性为58.8%,乙苯选择性氧化主产物苯乙酮的最高选择性为67.8%;其催化性能与P/V比、焙烧条件、双氧水的使用量、反应溶剂等有关.从已有的实验结果推测,钒基催化剂在双氧水存在下的甲、乙苯选择氧化反应与V⁵⁺/V⁴⁺的"氧化-还原"作用密切相关.     

氧化钼对氧化钒催化剂的影响

本文运用集团结构适应理论,结合测定磁化率和不可逆吸附量,以及连续流动法和脉冲法等实验手段,研究MoO₃对V₂O₅/SiO₂催化剂的影响。结果表明MoO₃增加V₂O₅表面V⁴⁺浓度,提高双V⁴⁺集团形成概率。从而提高催化剂恢复氧的能力,促进供氧活性。还讨论了MoO₃和P₃O₅对V₃O₅催化剂影响的差异。     

Cr负载V2O5-WO3/TiO2催化剂的低温NH3-SCR脱硝活性

采用浸渍法制备了一系列不同Cr负载量的CrO_x-V₂O₅-WO₃/TiO₂催化剂, 研究了Cr改性对该催化剂脱硝活性及抗硫性能的影响. 结果表明, Cr的引入使V₂O₅-WO₃/TiO₂催化剂的低温NO_x去除效果和抗硫性能显著提升. Cr的负载量为3%(以Cr₂O₃计算质量分数)时, 催化剂具有最佳的低温脱硝活性和N₂选择性. 结构表征结果表明, 改性催化剂中Cr元素主要以Cr³⁺形式存在, Cr的引入使催化剂的氧化性能明显提升, 并使表面弱酸位点、 强酸位点和催化剂表面吸附氧数量增多. XPS分析结果表明, Cr能使催化剂中V⁵⁺/V⁴⁺比例降低, 促进催化剂中自由电子的迁移. In situ DRIFTs表征结果显示, Cr的引入能促进NO与吸附在Brönsted酸位点上的NH₃在低温条件下反应, 从而使催化剂具有更好的低温脱硝活性. UV-Vis光谱分析结果表明, CrO_x负载量提高会显著增加高价态Cr的烧结聚集. 同时, 提出了一种选择性催化还原(SCR)反应中Cr-V协同催化的机理.     

SCR脱硝过程中SO2催化氧化的原位红外研究

采用工业用V₂O₅-WO₃/TiO₂催化剂,基于傅里叶原位红外光谱(FT-IR)技术考察SO₂的氧化过程及烟气组分对SO₂氧化行为的影响;结果表明,SO₂在催化剂表面氧化主要是首先吸附在催化剂表面V₂O₅活性位上,占据其O原子,以SO^2-₃形式存在,后与催化剂表面V⁵⁺-OH发生反应,生成金属硫酸盐(VOSO₄)中间产物,O₂重新氧化催化氧化过程中由于被SO₂夺取O原子而被还原的V₂O₅物种,使V⁴⁺转化为V⁵⁺,促进金属硫酸盐(VOSO₄)向SO₃转化;SO₂与NO、NH₃的竞争吸附阻碍SO₂在V₂O₅活性点位上的氧化;在SCR中,NO的脱除与SO₂的氧化是相互抑制的关系。     

Keggin型杂多酸铯盐催化苯羟基化反应

采用室温固相法制备了具有Keggin结构的杂多酸铯盐催化剂(Cs_xH_3+n-xPMo_12-nV_nO₄₀, n＝0, 1, 2, x＝0.5～3.0). 红外、X射线粉末衍射及循环伏安技术研究显示, 钒取代钼原子可提高催化剂的氧化还原性, 铯取代数的增加可提高催化剂的疏水性但降低氧化还原性. 在H₂O₂为氧化剂的苯羟基化反应中, 随着铯取代数目的增加, 催化剂的溶脱情况得到明显改善. 在氧化还原性和疏水性协同作用下, Cs₂H₃PMo₁₀V₂O₄₀在Cs_xH_3+n-xPMo_12-nV_nO₄₀系列催化剂中显示出相对最佳的苯羟基化催化活性(苯酚收率19.2%)和重复使用性能.     

Cu、Mn、Ce改性V2O5-WO3/TiO2/堇青石催化剂Urea-SCR脱除NO

采用硅胶为黏结剂,在堇青石蜂窝陶瓷上以涂覆法依次负载Cu、Mn、Ce改性的纳米TiO₂粉末、W改性的V₂O₅粉末得到复合催化剂,在120～550 ℃用尿素选择性催化还原(Urea-SCR)氮氧化物时显示良好活性。与商业催化剂V₂O₅-WO₃/TiO₂相比,添加Cu、Mn、Ce后,催化剂脱硝活性显著提高,活性温度窗口明显拓宽。结果表明,催化剂的高活性与催化剂表面适度的酸碱性、高比值的V⁴⁺/V⁵⁺以及良好的氧化还原性能和锐钛矿相的TiO₂、丰富的表面裂纹的存在等因素有关。     

前驱体溶液pH值对V2O5-WO3/TiO2催化剂的低温NH3-SCR性能的影响

采用调节前驱体溶液pH值的方法制备了用于低温NH₃-SCR的V₂O₅-WO₃/TiO₂催化剂。通过XPS、Raman光谱、H₂-TPR、NH₃-TPD、NH₃-DRIFT、XRD及物理吸附等手段对催化剂进行了表征分析,并对其脱硝催化活性进行了测试。结果表明,前驱体溶液酸性的增强能够提高催化剂表面聚合态钒物种和V⁴⁺⁽³⁺⁾/V⁵⁺的比值以及表面酸性,增加活性位数量、降低反应的活化能、提高其脱硝催化性能。因此,通过提高前驱体溶液的酸性,有助于制备出脱硝活性较好的NH₃-SCR催化剂。     

五氧化二钒/铈改性二氧化钛催化甲醇高选择性氧化制备二甲氧基甲烷

通过溶剂热法制备Ce掺杂的TiO₂,利用等体积浸渍法制得一系列V₂O₅/Ce-TiO₂催化剂,并用于甲醇选择性氧化制二甲氧基甲烷(DMM)。 采用XRD、UV-Vis、 H₂-TPR、NH₃-TPD等技术手段对催化剂进行了表征。 结果表明,Ce掺杂改性后的TiO₂负载V₂O₅更有利于催化剂表面钒氧物种的分散,且钒氧物种主要以孤立的和聚合态的形式存在,没有形成V₂O₅晶相结构。 Ce掺杂改性后,改变了TiO₂载体与钒氧物种间的作用力,Ce掺杂量越大,钒氧物种的还原温度逐渐向高温移动,使得催化剂的氧化还原能力减弱。 Ce改性的TiO₂负载V₂O₅,Ce的改性量对催化剂的酸性质几乎没有影响,但是催化剂的酸性却随着V₂O₅负载量的增大而逐渐减弱。 当Ce和Ti的摩尔比为0.01,V₂O₅的负载量为10%所得催化剂10V/1Ce-TiO₂具有较为适宜的氧化还原性和酸性,在反应温度160 ℃时,甲醇的转化率为39.6%,DMM的选择性高达99.9%。     

SBA-15负载钒氧化物催化剂上甲烷选择氧化反应

对SBA-15负载的钒、钼、钨氧化物催化的甲烷选择氧化反应性能进行了比较,发现VO_x/SBA-15催化剂优于MoOx/SBA-15和WOx/SBA-15催化剂.针对钒氧化物催化剂,考察了不同钒源、不同载体以及少量P元素的添加对催化性能的影响,结果表明以SBA-15为载体的催化剂的性能好于MCM-41和Cab-O-Sil为载体的催化剂;与V₂O₅,VO(C₂O₄)相比,NH₄VO₃是制备性能良好的VO_x/SBA-15的钒源;在VO_x/SBA-15中,添加少量P元素后,HCHO的选择性有一定程度的提高.XRD,N₂物理吸附、UN-Raman和H₂-TPR表征结果表明,负载量低于3 wt%时,钒组分可能主要以高分散的单核的VO_x物种存在,我们推测该物种对甲烷选择氧化制甲醛起关键作用.     

Correlation between reduction potential of vanadium-containing heteropolyacid (HPA) catalysts and their oxidation activity for cyclohexanol dehydrogenation

Vanadium-containing H_6+xP₂Mo_18−xV_xO₆₂ (x = 0, 1, 2 and 3) Wells-Dawson heteropolyacid (HPA) and H_3+xPMo_12−xV_xO₄₀ (x = 0, 1, 2 and 3) Keggin HPA catalysts were applied to the vapor-phase dehydrogenation of cyclohexanol. The catalytic oxidation activity showed a volcano-shaped curve with respect to vanadium substitution for both families of HPA catalysts. The Wells-Dawson HPA showed a better catalytic oxidation performance than the Keggin HPA at the same level of vanadium substitution.     

Effect of direct ultrasound synthesis via a sesquihydrate route on bismuth-promoted vanadyl pyrophosphate catalysts

A series of 1, 3, and 5% Bi-doped vanadium phosphate catalyst catalysts were prepared via sesquihydrate route using direct ultrasound method and were denoted as VPSB1, VPSB3, and VPSB5, respectively. These catalysts were synthesized solely using a direct ultrasound technique and calcined in a n-butane/air mixture. This study showed that catalyst synthesis time can be drastically reduced to only 2 hr compared to conventional 32–48 hr. All Bi-doped catalysts exhibited a well-crystallized (VO)₂P₂O₇ phase. In addition, two V⁵⁺ phases, that is, β-VOPO₄ and α_II-VOPO₄, were observed leading to an increase in the average oxidation state of vanadium. All catalysts showed V2p_3/2 at approx. 517 eV, giving the vanadium oxidation state at approx. 4.3–4.6. Field-emission scanning electron microscopy micrographs showed the secondary structure consisting of thin and small plate-like crystal clusters due to the cavitation effect of ultrasound waves. VPSB5 showed the highest amount of oxygen species removed associated with the V⁵⁺ and V⁴⁺ species in temperature-programmed reduction in H₂ analyses. TheX-ray absorption near edge structure (XANES) measurement showed the occurrence of vanadium oxide reductions in hydrogen gas flow, indicating the presence of V⁴⁺ and V⁵⁺ species. Higher average valence states of V⁵⁺, indicating more V⁵⁺ phases, were present. The addition of bismuth has increased the activity and selectivity to maleic anhydride.     

Synthesis, structure and catalytic activity of an oxo-bridged dinuclear oxovanadium complex of an isonicotinohydrazide ligand

A mononuclear dioxo vanadium(V) complex of a hydrazone ONO donor ligand, [V^VO₂(L¹)] (1), was synthesized by the reaction of V₂O₅ and terephthalic acid with H₂L¹ in 1:1:1 mol ratio, while an oxo-bridged bis(vanadium(IV)oxo) complex, [μ ₂–O–{V^IVO(L²)}₂] (2), was synthesized by the treatment of isonicotinic acid hydrazide, salicylaldehyde and CoSO₄·7H₂O with bis(acetylacetonato)oxovanadium(IV) (H₂L¹ = isonicotinic acid(2-hydroxy-benzylidene)-hydrazide, H₂L² = isonicotinic acid (1-methyl-3-oxo-butylidene)-hydrazide). The complexes were characterized by elemental analyses and spectroscopic methods. The crystal structure of complex 2 was determined by X-ray analysis. The complexes were tested as catalysts for the oxidation of cycloalkenes and benzyl alcohol using H₂O₂ as terminal oxidant. Excellent selectivity was achieved in the oxidation of cyclohexene.     

The selective catalytic oxidation of toluene

It was found for the first time that the selectivity of toluene transformations into benzaldehyde and benzoic acid decreased and into maleic anhydride and deep oxidation products increased as the ability of vanadium-containing catalysts of toluene oxidation to generate the singlet form of molecular oxygen grew. A scheme of the formation of the products of toluene oxidation with oxygen was suggested. Quinones were shown to be final rather than intermediate oxidation products. The selectivity of the reaction with respect to mild oxidation products in the presence of V₂O₅, MoO₃, and V₂O₅ · MoO₃ could be increased by changing the temperature of catalyst preparation from 400 to 500°C.     

Vapor-phase oxidation of β-picoline to nicotinic acid on V2O5 and modified vanadium oxide catalysts

Modification of V₂O₅ with Ti, Sn, Zr, Nb, and Al oxides improves the activity and selectivity of the vanadium oxide catalyst in vapor-phase oxidation of β-picoline to give nicotinic acid. It is shown that the conversion of β-picoline and the yield of nicotinic acid on two-component V₂O₅-TiO₂, V₂O₅-SnO₂, V₂O₅-ZtrO₂, V₂O₅-Nb₂O₅, and V₂O₅-Al₂O₃ catalysts may be several times those on the V₂O₅ catalyst. It was found that, on passing from V₂O₅ to double-component vanadium-containing catalysts, the proton affinity of active oxygen bonded to vanadium, calculated by the quantum-chemical method, grows simultaneously with the increase in the activity of the catalysts in the oxidation reaction.     

掺Ni钒磷氧化物催化剂的合成和表征

以VOPO4.2H2O为原料制备了钒磷氧化物催化剂,考察了镍掺杂(1%,2%和5%)对该催化剂的影响.低掺杂量的Ni明显提高了活性晶格氧物种O-的数量,降低了V5 和V4 相的还原峰温.粉末X射线衍射、程序升温还原和化学分析结果表明,高掺杂量的Ni促使V5 物相生成并抑制V4 物相出现.高含量与V5 相关的氧物种会降低正丁烷的转化率,但会提高马来酸酐的选择性.     

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.     

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.     

Synthesis,characterization, and catalytic oxidation of styrene,cyclohexene, allylbenzene,and cis-cyclooctene by recyclable polymer-grafted Schiff base complexes of vanadium(IV)

Schiff base-functionalized chloromethylated polystyrenes, PS-[Ae-Eol] (I), PS-[Hy-Eda] (II) and PS-[HyP-Eda] (III), were synthesized by reacting 2-(2-aminoethoxy)ethanol (Ae-Eol), N-(2-hydroxyethyl)ethylenediamine (Hy-Eda), and N-(2-hydroxpropyl)ethylenediamine (HyP-Eda) with oxidized chloromethylated polystyrene. Oxidized chloromethylated polystyrene (PS-CHO) was prepared by oxidation of chloromethylated polystyrene (PS) with sodium bicarbonate in DMSO. By reacting DMSO solution of [VO(acac)₂] with polymer-anchored Schiff base ligands I, II, and III, vanadium(IV) complexes PS-[V^IVO(Ae-Eol)] (1), PS-[V^IVO(Hy-Eda)] (2), and PS-[V^IVO(HyP-Eda)] (3) were prepared. Structure and bonding of I, II, and III as well as corresponding vanadium complexes 1, 2, and 3 were confirmed by FT-IR, UV–vis spectroscopy, SEM, EDX, AAS, TGA, EPR, etc. Polymer-anchored vanadium(IV) complexes 1, 2, and 3 show, efficient catalysis toward oxidation of styrene, cyclohexene, allylbenzene, and cis-cyclooctene in the presence of hydrogen peroxide. Optimized reaction conditions for the oxidation of these alkenes was achieved by changing various reaction parameters (like amount of catalyst, amount of oxidizing agent, volume of solvent, etc.). Polymer-grafted 1, 2, and 3 can be reused multiple times without depletion of their activity.     

酸性助剂对V2O5/TiO2催化剂甲醇选择氧化为甲缩醛的影响

研究了酸性助剂对TiO₂纳米管(TNT)负载的V₂O₅催化剂(V₂O₅/TNT)性能的影响, 发现经硫酸、磷酸或磷钨酸处理后, TNT的结构稳定, 但表面酸性和氧化-还原性发生了变化, 从而改变了甲醇选择氧化为甲缩醛的催化性能. 实验结果表明, V₂O₅/TNT催化剂经硫酸修饰和673 K焙烧, 其甲缩醛选择性显著提高, 且维持了较高的甲醇转化率. 催化剂表征表明, 高温焙烧促进了硫酸根与钒物种之间的强相互作用, 从而提高了催化剂的表面酸性而没有降低钒的氧化-还原性. 磷酸和磷钨酸修饰虽然也提高了V₂O₅/TNT催化剂的表面酸性, 但降低了其中钒氧化物的氧化-还原能力, 反而降低了催化剂的活性.