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Reaction kinetics of ethane partial oxidation to acetic acid
Applied Petrochemical Research Pub Date : 2018-03-07 , DOI: 10.1007/s13203-018-0195-8
Sulaiman I. Al-Mayman , Moustafa A. Soliman , Abdulrahman S. Al-Awadi , Yousef S. Al-Zeghayer

The partial oxidation of ethane to ethylene and acetic acid on supported MoVNbPd/TiO2 (P25 of Degussa) has been investigated. Pd was added in a nano-metallic form. The catalyst composition was also different from similar studied catalysts. This results in a better selectivity towards acetic acid formation. The reaction was carried out in a tubular reactor at temperature range 225–275 °C, total pressure range 0–200 psig and oxygen percentage in the feed gas of 10–40%. The feed gas contains ethane and oxygen. In this work, we develop a kinetic model for the reaction for the developed catalyst. In this model, we assume that oxidation reactions take place on different sites; ethane oxidation takes place on one site, ethylene oxidation on another site, and CO is oxidized to CO2 on a third site. The model exhibits good agreement with the experimental data.

中文翻译:

乙烷部分氧化为乙酸的反应动力学

已经研究了在负载的MoVNbPd / TiO 2(Degussa的P25)上乙烷部分氧化为乙烯和乙酸。以纳米金属形式添加Pd。催化剂组成也不同于类似的研究催化剂。这导致对乙酸形成的更好的选择性。反应在管式反应器中于225–275°C的温度,总压力范围0–200 psig的条件下进行,进料气中的氧气百分比为10–40%。进料气体包含乙烷和氧气。在这项工作中,我们为开发的催化剂开发了动力学模型。在这个模型中,我们假设氧化反应发生在不同的位置。在一个位置发生乙烷氧化,在另一个位置发生乙烯氧化,CO被氧化为CO 2在第三个网站上。该模型与实验数据吻合良好。
更新日期:2018-03-07
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