JOURNAL OF CHEMICAL ENGINEERING OF JAPAN | |
Continuous Toluene Hydrogenation System Using Compressed Carbon Dioxide | |
Yoshio Masuda1  Norihito Hiyoshi1  Osamu Sato1  Chandrashekhar V. Rode1  Masayuki Shirai1  Mitsumasa Osada1  | |
[1] Research Center for Compact Chemical Process, National Institute of Advanced Industrial Science and Technology (AIST) | |
关键词: Carbon Dioxide Solvent; Continuous Hydrogenation; Toluene; Methylcyclohexane; Process Simulation; | |
DOI : 10.1252/jcej.09we054 | |
来源: Maruzen Company Ltd | |
【 摘 要 】
References(17)The effect of the addition of compressed carbon dioxide in continuous hydrogenation of toluene has been evaluated with process simulation software and tested with a fixed-bed reactor. The simulation results show that the temperature rise is significantly suppressed in the presence of compressed carbon dioxide and that the equilibrium conversion of toluene (toluene/hydrogen = 1/3) reaches 99.9%, whereas around 60% in the absence of carbon dioxide. Experimental results show that the continuous hydrogenation of toluene (toluene/hydrogen/carbon dioxide = 1/3.1/31, inlet temperature: 20 °C, outlet temperature: <70 °C, and total pressure: 11 MPa) over activated carbon-supported rhodium catalysts proceeds without deactivation. The conversion of toluene reaches 99% and methylcyclohexane is the only product detected.
【 授权许可】
Unknown
【 预 览 】
Files | Size | Format | View |
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RO201912080696444ZK.pdf | 19KB | download |