Chemical, Structural, and Morphological Changes of a MoVTeNb Catalyst during Oxidative Dehydrogenation of Ethane

脱氢 催化作用 碲 氧化物 拉曼光谱 化学 材料科学 高分辨率透射电子显微镜 化学工程 无机化学 透射电子显微镜 纳米技术 有机化学 光学 物理 工程类
作者
Jaime S. Valente,H. Armendáriz,Roberto Quintana,Paz del Ángel,Noel Nava,Amada Massó,Josè Manuel López Nieto
出处
期刊:ACS Catalysis [American Chemical Society]
卷期号:4 (5): 1292-1301 被引量:131
标识
DOI:10.1021/cs500143j
摘要

MoVTeNb mixed oxide, a highly active and selective catalyst for the oxidative dehydrogenation of ethane to produce ethylene, exhibits the so-called M1 and M2 crystalline phases. The thermal stability of the MoVTeNb catalytic system was assessed under varying reaction conditions; to this end, the catalyst was exposed to several reaction temperatures spanning from 440 to 550 °C. Both the pristine and spent materials were analyzed by several characterization techniques. The catalyst was stable below 500 °C; a reaction temperature of ≥500 °C brings about the removal of tellurium from the intercalated framework channels of the M1 crystalline phase. Rietveld refinement of X-ray diffraction patterns and microscopy results showed that the tellurium loss causes the progressive partial destruction of the M1 phase, thus decreasing the number of active sites and forming a MoO 2 crystalline phase, which is inactive for this reaction. Raman spectroscopy confirmed the MoO 2 phase development as a function of reaction temperature. From high-resolution transmission electron microscopy and energy-dispersive X-ray spectroscopy analyses it was noticed that tellurium departure occurs preferentially from the end sides of the needlelike M1 crystals, across the [001] plane. Detailed analysis of a solid deposited at the reactor outlet showrf that it consisted mainly of metallic tellurium, suggesting that the tellurium detachment occurs via reduction of Te 4+ to Te 0 due to a combination of reaction temperature and feed composition. Thus, in order to sustain the catalytic performance exhibited by MoVTeNb mixed oxide, hot spots along the reactor bed should be avoided or controlled, maintaining the catalytic bed temperature below 500 °C.
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