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Kinetic study of double-walled carbon nanotube synthesis by catalytic chemical vapour deposition over an Fe-Mo/MgO catalyst using methane as the carbon source

机译:以甲烷为碳源,在Fe-Mo / MgO催化剂上催化化学气相沉积合成双壁碳纳米管的动力学研究

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摘要

A kinetic study was performed to describe experimental reaction rates of double-walled carbon nanotube (DWNT) synthesis by catalytic chemical vapour deposition (CCVD) over an Fe-Mo/MgO catalyst using methane as the carbon source. Initial reaction rates were determined by mass spectrometry for methane partial pressures ranging from 0.01 atm to 0.9 atm and for three temperatures: 900°C, 950 C and 1000°C. Mass transfers from the bulk of the fluid to the external surface of the catalytic bed and through the catalytic bed were negligible as determined experimentally and confirmed by the methane mass balance. A detailed kinetic study was carried out to discriminate between phenomenological kinetic models and to validate the good agreement between the chosen model and the experimental data. The best model was found to involve the irreversible dissociative adsorption of methane followed by the irreversible decomposition of the adsorbed methyl group, which is the rate-determining centre. Activation energy of adsorbed methyl decomposition was found to be equal to 58 kJ mol~(-1). The catalytic deactivation by coking was expressed by a decreasing function of coke content, which leads to a sigmoid equation.
机译:进行了动力学研究,以描述以甲烷为碳源,在Fe-Mo / MgO催化剂上通过催化化学气相沉积(CCVD)合成双壁碳纳米管(DWNT)的实验反应速率。初始反应速率是通过质谱法测定的,其中甲烷分压范围为0.01 atm至0.9 atm,并且三个温度分别为900°C,950°C和1000°C。通过实验确定并通过甲烷质量平衡证实,从大量流体到催化床外表面并通过催化床的质量转移可以忽略不计。进行了详细的动力学研究,以区别现象动力学模型,并验证所选模型与实验数据之间的良好一致性。发现最好的模型涉及甲烷的不可逆解离吸附,然后是吸附的甲基的不可逆分解,这是决定速率的中心。发现吸附的甲基分解的活化能等于58 kJ mol〜(-1)。焦炭的催化失活由焦炭含量的递减函数表示,这导致了S形方程。

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