Catalytic dehydration of glycerol to acrolein over sulfuric acid-activated montmorillonite catalysts

Catalytic dehydration of glycerol to acrolein over sulfuric acid-activated montmorillonite catalysts
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DOI:
10.1016/j.clay.2012.09.011
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发表时间:
2013-04
影响因子:
5.6
通讯作者:
Heng-yu Zhao;C. Zhou;L. Wu;Jianqiu Lou;Na Li;Huimin Yang;D. Tong;W. Yu
Heng-yu Zhao;C. Zhou;L. Wu;Jianqiu Lou;Na Li;Huimin Yang;D. Tong;W. Yu
中科院分区:
地球科学2区
文献类型:
--
作者:
Heng-yu Zhao;C. Zhou;L. Wu;Jianqiu Lou;Na Li;Huimin Yang;D. Tong;W. Yu

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For the development of efficient solid acid catalysts for the catalytic dehydration of glycerol to acrolein, catalysts made from montmorillonitic clay activated by sulfuric acid were investigated. Montmorillonite was activated in diluted sulfuric acid in the concentration range of 5–40wt.%. The effects of sulfuric acid treatment on the structure of the montmorillonite were characterized by X-ray diffraction, measurements of acidity, N2adsorption–desorption isotherms, and Fourier transform infrared spectroscopy. The catalytic behavior of sulfuric acid-activated montmorillonite catalysts in the gas-phase dehydration of glycerol were investigated under varying conditions, including the reaction temperature, the feed rate, and the concentration of glycerol. After montmorillonitic clay was activated by sulfuric acid, the layered structural features of montmorillonite remained nearly intact. Ca2+-montmorillonite was changed to H+-montmorillonite by ion exchange reaction during activation. The optimal catalytic glycerol dehydration reaction conditions were found to be: temperature at 320°C, liquid hourly space velocity (LHSV)=18.5h−1, concentration of glycerol solution=10wt.%, and the flow rate of N2carrier gas=10mL/min. A conversion of 54.2% of glycerol and a yield of 44.9wt.% acrolein were achieved over the montmorillonite catalyst activated by an aqueous 10wt.% sulfuric acid solution. The H+in the interlayer space of acid-activated montmorillonite catalysts played a critical role in the catalytic dehydration of glycerol. The temperature, the LHSV, and the concentration of glycerol affected the performance of the catalysts through their influence on the reaction mechanism, the contact time, and the reaction equilibrium.