Journal of Liaoning Petrochemical University
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Preparation and Property on Cyclohexane  Dehydrogenation Activity of Mo2C/CCA
LIU Zhao, MA Jun, WANG Hai-yan,BAI Ying-zhi, LIU Lu
Abstract296)      PDF (281KB)(347)      
The Mo3O/CCA was prepared by impregnation method using the (NH4)6Mo7O24·4H2O as the molybdenum source, carbon covered γ-Al2O3 (CCA) as support, and n-hexane as the carbon source. After carbonization of Mo3O/CCA obtained Mo2C/CCA. The catalysts prepared at different carbonization temperature were characterized by XRD. The effects of preparation and reaction conditions on dehydrogenation activity of the catalyst were studied in a fixed-bed down-flow reactor. The results show that the conversion of cyclohexane up to 91% was attained under the optimum condition as follows: CCA carbon covered 7.82%, final carbonization temperature 650 ℃, reaction temperature 475 ℃, reaction pressure 0.1 MPa, liquid hourly space velocity 2 h-1 and volume ratio of hydrogen to cyclohexane 200∶1.
2012, 32 (3): 13-16.
The Preparation of Hydrodenitrogenation Activity of the MoP/TiO 2-SiO 2-Al 2O 3
JIANG Xu,GU Yong-he,WANG Hai-yan*,WEI Min,BAI Ying-zhi,MA Jun
Abstract369)      PDF (260KB)(265)      
 
The TiO 2-SiO 2-Al 2O 3 composite support was prepared by sol-gel method, and then the MoP/TiO 2-SiO 2-Al 2O 3 catalyst was prepared in the way of co-impregnation. XRD results show that the diffraction peaks of TiO 2 crystalline phase is due to anatase and SiO 2 is mostly amorphous dispersed in γ-Al 2O 3 cystal surface. After in-situ reduction, the hydrodearomatization (HDA) activity of the catalyst was investigated in the fixed bed reactor. The results suggest that the mole ratio of Ti, Si and Al have a great influence on the activity of composite support catalyst. HDA activity of the MoP/TiO 2-SiO 2-Al 2O 3 catalyst shows the highest activity (65.6%) when the ratio of n(Ti)∶n(Si)∶n(Al) was 1∶1∶4, the Mo loading amount is 20%. In addition, the results also show that the HDA rate of the catalyst with the composite TiO 2-SiO 2-Al 2O 3 support was 19.6% and 13.6% higher than the traditional cataslysts of γ-Al 2O 3 and SiO 2-Al 2O 3, respectively.
2010, 30 (3): 24-27. DOI: 10.3696/j.issn.1672-6952.2010.03.007