Synthesis, characterization, and evaluation of high selectivity mixed molybdenum and vanadium oxide catalysts for oxidative dehydrogenation of propane

被引:5
|
作者
Alasiri, Hassan [1 ,2 ]
Ahmed, Shakeel [2 ]
Rahman, Faizur [2 ]
Al-Amer, Adnan [1 ]
Majeed, Uwais B. [2 ]
机构
[1] King Fahd Univ Petr & Minerals, Chem Engn Dept, Dhahran 31261, Saudi Arabia
[2] King Fahd Univ Petr & Minerals, Ctr Refining & Petrochem, Res Inst, Dhahran 31261, Saudi Arabia
来源
关键词
vanadium; molybdenum; citrate-nitrate auto-combustion; propylene; oxidative dehydrogenation of propane; PHYSICOCHEMICAL PROPERTIES; PROPYLENE PRODUCTION; NANOSTRUCTURED V2O5; ALUMINA; ETHANE; ALKANES;
D O I
10.1002/cjce.23472
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Molybdenum and vanadium oxide catalysts with varied compositions (Mo/V = 1/1, 7/3, 8/2, and 9/1) were prepared using a modified citrate-nitrate auto-combustion method for the oxidative dehydrogenation of propane to propylene. These catalysts were characterized by BET-technique, TPR, XRD, SEM, Raman, and UV spectroscopy. The effects of washing and supercritical CO2 drying on catalysts during the preparation steps were investigated. Results show an interaction between the molybdenum and vanadium metal ions in all of these catalysts due to the presence of a peak at 785 cm(-1) from the Raman study, which was assigned to a polymolybdovanadate species V-O-Mo vibration. This interaction could be efficient for alkane activation reaction. The catalysts were evaluated in a fixed bed micro-reactor at temperatures in the range of 350-600 degrees C and at atmospheric pressure. The activity of the catalyst increased by increasing the molybdenum content. All of the catalysts in this study showed 100 % selectivity for propylene in the temperature range of 350-450 degrees C; however, the propylene selectivity was found to decrease with an increase in the temperature. The highest yield of 4.8 % with 100 % propylene selectivity was obtained for a catalyst with Mo/V ratio of 9:1 at 500 degrees C.
引用
收藏
页码:2340 / 2346
页数:7
相关论文
共 50 条
  • [21] Isotopic tracer studies of reaction pathways for propane oxidative dehydrogenation on molybdenum oxide catalysts
    Chen, KD
    Iglesia, E
    Bell, AT
    JOURNAL OF PHYSICAL CHEMISTRY B, 2001, 105 (03): : 646 - 653
  • [22] The oxidative dehydrogenation of propane using gallium-molybdenum oxide-based catalysts
    Davies, T
    Taylor, SH
    JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2004, 220 (01) : 77 - 84
  • [23] Oxidative Dehydrogenation of Propane over Supported Nickel-Molybdenum-Oxide-Based Catalysts
    Putra, Meilana Dharma
    Al-Mesfer, Mohammed Khloofa
    Abasaeed, Ahmed Elhag
    Al-Zahrani, Saeed Mohammed
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2013, 46 (06) : 389 - 395
  • [24] The Oxidative Dehydrogenation of Propane Using Gallium–Molybdenum Based Catalysts
    Thomas Davies
    Stuart H. Taylor
    Catalysis Letters, 2004, 93 : 151 - 154
  • [25] Oxidative dehydrogenation of propane over molybdenum-containing catalysts
    Meunier, FC
    Yasmeen, A
    Ross, JRH
    CATALYSIS TODAY, 1997, 37 (01) : 33 - 42
  • [26] Kinetics and mechanism of oxidative dehydrogenation of propane on vanadium, molybdenum, and tungsten oxides
    Chen, KD
    Bell, AT
    Iglesia, E
    JOURNAL OF PHYSICAL CHEMISTRY B, 2000, 104 (06): : 1292 - 1299
  • [27] OXIDATIVE DEHYDROGENATION OF ETHANE AND PROPANE ON CUTH OXIDE CATALYSTS
    ABOUKAIS, A
    LOUKAH, M
    VEDRINE, JC
    REACTION KINETICS AND CATALYSIS LETTERS, 1994, 53 (01): : 107 - 114
  • [28] Oxidative dehydrogenation of propane over FeVal oxide catalysts
    Mamedov, EA
    Shaikh, SN
    ARABIAN JOURNAL FOR SCIENCE AND ENGINEERING, 1999, 24 (1C): : 27 - 40
  • [29] Propane oxidative dehydrogenation on silica based oxide catalysts
    Parmaliana, A
    Sokolovskii, V
    Arena, F
    Frusteri, F
    Miceli, D
    CATALYSIS LETTERS, 1996, 40 (1-2) : 105 - 108
  • [30] Oxidative dehydrogenation of propane over vanadium oxide based catalysts - Effect of support and alkali promoter
    Lemonidou, AA
    Nalbandian, L
    Vasalos, IA
    CATALYSIS TODAY, 2000, 61 (1-4) : 333 - 341