ZHENG Hong-yan, ZHU Yu-lei, HUANG Long, XIANG Hong-wei, LI Yong-wang. Study on Cu-Mn-Si catalysts for the coupling process of cyclohexanol dehydrogenation and furfural hydrogenation:Effect of pH value and calcination temperature[J]. Journal of Fuel Chemistry and Technology, 2008, 36(05): 631-636.
Citation:
ZHENG Hong-yan, ZHU Yu-lei, HUANG Long, XIANG Hong-wei, LI Yong-wang. Study on Cu-Mn-Si catalysts for the coupling process of cyclohexanol dehydrogenation and furfural hydrogenation:Effect of pH value and calcination temperature[J]. Journal of Fuel Chemistry and Technology, 2008, 36(05): 631-636.
ZHENG Hong-yan, ZHU Yu-lei, HUANG Long, XIANG Hong-wei, LI Yong-wang. Study on Cu-Mn-Si catalysts for the coupling process of cyclohexanol dehydrogenation and furfural hydrogenation:Effect of pH value and calcination temperature[J]. Journal of Fuel Chemistry and Technology, 2008, 36(05): 631-636.
Citation:
ZHENG Hong-yan, ZHU Yu-lei, HUANG Long, XIANG Hong-wei, LI Yong-wang. Study on Cu-Mn-Si catalysts for the coupling process of cyclohexanol dehydrogenation and furfural hydrogenation:Effect of pH value and calcination temperature[J]. Journal of Fuel Chemistry and Technology, 2008, 36(05): 631-636.
Study on Cu-Mn-Si catalysts for the coupling process of cyclohexanol dehydrogenation and furfural hydrogenation:Effect of pH value and calcination temperature
State Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, China;2.Graduate School of the Chinese Academy of Sciences, Beijing 10039, China
The coupling process of the cyclohexanol dehydrogenation and the furfural hydrogenation on precipitated Cu-Mn-Si catalysts was carried out at atmospheric pressure in gas phase. The effects of pH value and calcination temperature on the performance of catalysts were studied in detail. There was no observable difference in furfural hydrogenation reaction over the catalysts precipitated at different values of pH. However, pH value had significant influence on the selectivity of cyclohexanone. The catalysts precipitated at the pH values range of 7.5 to 10.0 showed good performance for the coupling process. The increase of calcination temperature decreased the surface area and copper surface area and increased the average pore size, leading to a difficult reduction of the active phase. The calcination temperature had no significant effect on the cyclohexanol dehydrogenation to cyclohexanone, whereas the conversion of furfural and the selectivity of 2methylfuran declined with the increase of calcination temperature.