摘要
A spherical γ-Al 2O 3 catalyst was employed for the heterogeneous synthesis of ethylene glycol (EG) through ethylene carbonate (EC) hydrolysis in a fixed-bed reactor. The effects of reaction temperature, LHSV, mole ratio of H 2O to EC and reaction pressure on the hydrolysis were investigated. The conversion of EC and the selectivity to EG can reach 98.4% and 100% respectively under the optimal conditions of reaction temperature 170-180°C, LHSV 0.8-1.5 h -1, mole ratio of H 2O to EC 1.7-3.0 and reaction pressure 1.0~1.8 MPa. In addition, the catalytic activity and pore structure of the catalyst can be maintained well during a run for 500 hours.
源语言 | 英语 |
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页(从-至) | 1005-1010 |
页数 | 6 |
期刊 | Petrochemical Technology |
卷 | 41 |
期 | 9 |
出版状态 | 已出版 - 9月 2012 |