Maleic anhydride (MA) is a kind of important organic chemical raw materials and fine chemical products, has a wide application and strong market demand, while vanadium phosphorus oxide (VPO) catalyst is the most effective catalyst for n-butane selective oxidation to maleic anhydride. However, the catalysts suffer from the shorts of low activity, selectivity. Many efforts had been devoted to improve their catalytic performance. Among them, modification with metal promoters was considered as an effective method. In the present work, Ti/Zr promoter was selected as additive to modify VPO during its preparation with organic medium method. Their catalytic performance for selective oxidation of n-butane to produce maleic anhydride were tested in fixed-bed reactor at 420℃ with gas hourly space velocity of 2000 h?1. The effects of metal element, precursor and additive amount of promoters on the catalytic performance were investigated in details. The change of phase structure, the morphology as well as electronic properties of catalysts were characterized by X-ray diffraction, Raman, SEM, XPS. Compared with VPO catalyst without promoter, the VPO catalysts modified with Ti/Zr promoter effectively improved the catalytic performance for n-butane conversion rate and maleic anhydride selectivity. Especially, for the VPO catalyst promoted by Zr(NO3)4 doping with molar ratio of Zr to V of 1.5%, the conversion rate of n-butane can reached 99.1% and the yield to maleic anhydride was 54.4%. The promoters did not change the phase structure of the catalyst, but promoted the formation of the active phase (VO)2P2O7 and change the morphology of the catalyst, forming smaller size of VPO sheet and correspondingly exposing more active sites, furthermore, the interaction between the promoters and V has great effects on the concentration of P and the valence of V on the surface of VPO catalyst. In addition, the chemical compound formation of promoter elements had an important influence on the performance of VPO catalyst. When Zr(NO3)4 was used as the promoter, the conversion of n-butane was much higher than that with the promoter of ZrO2. Further, the promoter elements also had important influence on the performance of VPO catalyst. Compared with ZrO2, the catalysts modified by TiO2 showed better catalytic performance because Ti can better enter the lattice of catalyst instead of V.
[1] 周凌,李剑锋,李然家,等.超临界流体干燥方法在丁烷选择性氧化制顺酐VPO催化剂制备中的应用 [J][J].催化学报, 2001, (05):427-431 [2]Zhou L, Li J F, Li R J, et al.Application of Supercritical Fluid Desiccation to Preparation of VPO Catalysts for n-Butane Selective Oxidation to Maleic Anhydride[J]. Chinese Journal of Catalysis, 2001(05):427-431. [3] Ellison, I J, et al., Control of the Composition and Morphology of Vanadium Phosphate Catalyst Precursors from Alcohol Treatment of Vopo4.2h2o[J]. J Chem Soc Chem Comm 1994, (9):1093-1094. [4] Hutchings, G J, Characterisation of Variations in Vanadium Phosphate Catalyst Microstructure with Preparation Route[J].J Catal 1996, 162 31-47. [5] Hutchings, G J, Vanadium phosphate: a new look at the active components of catalysts for the oxidation of butane to maleic anhydride[J].J Mater Chem 2004, 14 (23):3385-3395. [6] Kamiya, Y, et al., Selective Oxidation of n-Butane over Highly Crystalline Vanadyl Pyrophosphate Catalyst Synthesized by Intercalation-exfoliation-reduction of Layered Vanadyl Phosphate Dihydrate[J]. J Jpn Petrol Inst 2009, 52 (3):81-89. [7] Rownaghi, A A, et al., High Surface Area Vanadium Phosphate Catalysts for n-Butane Oxidation[J]. Ind Eng Chem Res 2009, 48 (16):7517-7528. [8] Lin, Z J, et al., The synthesis of highly crystalline vanadium phosphate catalysts using a diblock copolymer as a structure directing agent[J]. Catal Today 2010, 157 (1-4):211-216. [9] Wu-Hsun Cheng, W W, Effect of calcination environment on the selective oxidation of n-butane to maleic anhydride over promoted and unpromoted VPO catalysts[J].Applied Catalysis A: General 1997, 156 57-69. [10] Patience, G S, Pressure Calcination of VPO Catalyst[J].Ind. Eng. Chem. Res. 2007, 46 4374-4381. [11] Taufiq-Yap, Y H; Saw, C S, Effect of different calcination environments on the vanadium phosphate catalysts for selective oxidation of propane and n-butane[J].Catal Today 2008, 131 (1-4):285-291. [12] LEE, Y H T-Y H V, Effect of Different Calcination Duration on Physicochemical Properties of Vanadium Phosphate Catalysts[J].E-Journal of Chemistry 2012, 9 1440-1448. [13] Sadiq, M, et al., Effect of calcination temperature on the structure of vanadium phosphorus oxide materials and their catalytic activity in the decomposition of 2-propanol[J]. Journal of Saudi Chemical Society 2012, 16 (4):445-449. [14] Rasmussen, S B, et al., Structural characteristics of an amorphous VPO monolayer on alumina for propane ammoxidation[J]. Catal Today 2012, 192 (1):96-103. [15] Mahdavi, V, et al., Liquid-Phase Selective Oxidation of Alcohols over Vanadium Phosphorus Oxide Catalysts Supported on Nanoporous SBA-15[J]. Chemical Engineering Communications 2014, 202 (9):1200-1210. [16] Zazhigalov, V A, et al., Development of VPO catalysts supported on mesoporous modified material based on an aerosil gel[J]. Kinetics and Catalysis 2014, 55 (3):380-389. [17] Jian, J, et al., Supported Ni–Al–VPO/MCM-41 As Efficient and Stable Catalysts for Highly Selective Preparation of Adipic Acid from Cyclohexane with NO2[J]. Ind Eng Chem Res 2016, 55 (13):3729-3735. [18] Santra, C, et al., Synthesis, characterization of VPO catalyst dispersed on mesoporous silica surface and catalytic activity for cyclohexane oxidation reaction[J]. Microporous and Mesoporous Materials 2016, 223 121-128. [19] Cavani, F, et al., The effect of cobalt and iron dopants on the catalytic behavior of V/P/O catalysts in the selective oxidation of n-pentane to maleic and phthalic anhydrides[J]. Catal Lett 1997, 43 (3-4):241-247. [20] de Farias, A M D, et al., Vanadium phosphorus oxide catalyst modified by niobium doping for mild oxidation of n-butane to maleic anhydride[J]. J Catal 2002, 208 (1):238-246. [21] Shen, S K, et al., Effect of Ce-Fe oxides additives on performance of VPO catalyst for n-butane oxidation to maleic anhydride in the absence of gas-phase oxygen[J]. Catal Today 2002, 74 (1-2):37-43. [22] Hutchings, G J, Effect of promoters and reactant concentration on the selective oxidation of n-butane to maleic anhydride using vanadium phosphorus oxide catalysts[J].Applied Catalysis A: General 1991, 72 (1):1-32. [23] Zazhigalov, V A, et al., n-Butane oxidation on V-P-O catalysts. Influence of alkali and alkaline-earth metal ions as additions[J]. Appl Catal a-Gen 1996, 134 (2):225-237. [24] Taufiq-Yap, Y H, et al., Influence of Milling Media on the Physicochemicals and Catalytic Properties of Mechanochemical Treated Vanadium Phosphate Catalysts[J]. Catal Lett 2010, 141 (3):400-407. [25] Hutchings, G J, et al., Improved method of preparation of vanadium phosphate catalysts[J]. Catal Today 1997, 33 (1-3):161-171. [26] Albonetti, S, et al., A comparison of the reactivity of ' ' nonequilibrated' ' and ' ' equilibrated' ' V-P-O catalysts: Structural evolution, surface characterization, and reactivity in the selective oxidation of n-butane and n-pentane[J]. J Catal 1996, 160 (1):52-64. [27] Haber, J, et al., Mechanochemistry: The activation method of VPO catalysts for n-butane partial oxidation[J]. Catal Today 1997, 33 (1-3):39-47. [28] Centi, G, et al., Nature of Active Species of (Vo)2p2o7 for Selective Oxidation of N-Butane to Maleic-Anhydride[J]. Faraday Discuss 1989, 87 215-225. [29] Hodnett, B K, Vanadium-Phosphorus Oxide Catalysts for the Selective Oxidation of C-4 Hydrocarbons to Maleic-Anhydride[J].Catal Rev 1985, 27 (3):373-424. [30] Cornaglia, L, et al., The beneficial effect of cobalt on VPO catalysts[J]. Catal Today 2003, 78 (1-4):291-301.