Metathesis of ethylene and butylene-2 to propylene with Mo on Hβ-Al2O3 catalysts
Metathesis of ethylene and butylene-2 to propylene with Mo on Hβ-Al2O3 catalysts
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DOI:
10.1016/j.cattod.2004.06.062
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发表时间:
2004-09
期刊:
影响因子:
5.3
通讯作者:
Shenglin Liu;Shengjun Huang;Wenjie Xin;Bai Jie;Sujuan Xie;Longya Xu
中科院分区:
文献类型:
--
作者:
Shenglin Liu;Shengjun Huang;Wenjie Xin;Bai Jie;Sujuan Xie;Longya Xu
Reaction performance, acidic and basic properties, as well as reduction properties of various supported molybdenum catalysts for the metathesis of ethylene and butylene-2 to propylene were investigated by TPR and NH3-TPD techniques in a flow-reactor. Besides temperature, space velocity and pressure, the stability of a Mo/(Hβ-Al2O3) catalyst is strongly affected by the Mo loading, the calcination temperature and the hydrothermal treatment conditions. A suitable molybdenum loading on Hβ-Al2O3is favorable to the stability of the catalyst that possesses suitable amount of acidity, which was determined by NH3-TPD measurements. The optimum preparation conditions of the Mo/(Hβ-Al2O3) catalyst are as follows: molybdenum content 3wt.%, hydrothermal treatment and calcination at 550°C for 2h and 700°C for 2h, respectively. Thus, the optimal catalyst of 3Mo/(Hβ-Al2O3), designated as 3Mo/Hβ5502700, could keep a conversion of C4H8-2 at about 82% during 22h of reaction time-on-stream under the following conditions: N2/C2H4=1.5, C2H4/C4H8-2=3/1, WHSV(C2H4+C4H8-2)=1h−1, T=120°C, and P=1.0MPa. In addition, a suitable pressure, such as 0.5–1.0MPa, and a low temperature, such as 35°C, are beneficial for keeping the stability of the 3Mo/Hβ5502700 catalyst.