期刊文献+

Deoxygenation of methyl laurate to hydrocarbons on silica-supported Ni-Mo phosphides: Effect of calcination temperatures of precursor 被引量:2

Deoxygenation of methyl laurate to hydrocarbons on silica-supported Ni-Mo phosphides: Effect of calcination temperatures of precursor
下载PDF
导出
摘要 SiO2-supported Ni-Mo bimetallic phosphides were prepared by temperature-programmed reduction (TPR) method from the phosphate precur- sors calcined at different temperatures. Their properties were characterized by means of ultraviolet-visible diffuse reflectance spectroscopy (UV-Vis DRS), H2 temperature-programmed reduction (H2-TPR), X-ray diffraction (XRD), transmission electron microscopy (TEM), CO chemisorption, H2 and NH3 temperature-programmed desorptions (H2-TPD and NH3-TPD). Their catalytic performances for the deoxygena- tion of methyl laurate were tested in a fixed-bed reactor. When the precursors were calcined at 400 and 500 ℃, respectively, NiMoP2 phase could be formed apart from Ni2P and MoP phases in the prepared C400 and C500 catalysts. However, when the precursors were calcined at 600, 700 and 800 ℃, respectively, only Ni2P and MoP phases could be detected in the prepared C600, C700 and C800 catalysts. Also, in C400, C500 and C600 catalysts, Mo atoms were found to be entered in the lattice of Ni2P phase, but the entering extent became less with the increase of calcination temperature. As the calcination temperature of the precursor increased, the interaction between Ni and Mo in the prepared catalysts decreased, and the phosphide crystallite size tended to increase, subsequently leading to the decrease in the surface metal site density and the acid amount. C600 catalyst showed the highest activity among the tested ones for the deoxygenation of methyl laurate. As the calcination temperature of the precursor increased, the selectivity to C12 hydrocarbons decreased while the selectivity to C11 hydrocarbons tended to increase. This can be mainly attributed to the decreased Ni-Mo interaction and the increased phosphide particle size. In sum, the structure and performance of Ni-Mo bimetallic phosphide catalyst can be tuned by the calcination temperature of precursor. SiO2-supported Ni-Mo bimetallic phosphides were prepared by temperature-programmed reduction (TPR) method from the phosphate precur- sors calcined at different temperatures. Their properties were characterized by means of ultraviolet-visible diffuse reflectance spectroscopy (UV-Vis DRS), H2 temperature-programmed reduction (H2-TPR), X-ray diffraction (XRD), transmission electron microscopy (TEM), CO chemisorption, H2 and NH3 temperature-programmed desorptions (H2-TPD and NH3-TPD). Their catalytic performances for the deoxygena- tion of methyl laurate were tested in a fixed-bed reactor. When the precursors were calcined at 400 and 500 ℃, respectively, NiMoP2 phase could be formed apart from Ni2P and MoP phases in the prepared C400 and C500 catalysts. However, when the precursors were calcined at 600, 700 and 800 ℃, respectively, only Ni2P and MoP phases could be detected in the prepared C600, C700 and C800 catalysts. Also, in C400, C500 and C600 catalysts, Mo atoms were found to be entered in the lattice of Ni2P phase, but the entering extent became less with the increase of calcination temperature. As the calcination temperature of the precursor increased, the interaction between Ni and Mo in the prepared catalysts decreased, and the phosphide crystallite size tended to increase, subsequently leading to the decrease in the surface metal site density and the acid amount. C600 catalyst showed the highest activity among the tested ones for the deoxygenation of methyl laurate. As the calcination temperature of the precursor increased, the selectivity to C12 hydrocarbons decreased while the selectivity to C11 hydrocarbons tended to increase. This can be mainly attributed to the decreased Ni-Mo interaction and the increased phosphide particle size. In sum, the structure and performance of Ni-Mo bimetallic phosphide catalyst can be tuned by the calcination temperature of precursor.
出处 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2015年第1期77-86,共10页 能源化学(英文版)
基金 supported by the National Natural Science Foundation of China(No.21176177) the Natural Science Foundation of Tianjin(No.12JCYBJC13200) State Key Laboratory of Catalytic Materials and Reaction Engineering(RIPP,SINOPEC)
关键词 metal phosphide calcination temperature methyl laurate hydrodeoxygenation DECARBONYLATION metal phosphide calcination temperature methyl laurate hydrodeoxygenation decarbonylation
  • 相关文献

同被引文献31

  • 1Krivtcova N I,Tataurshikov A A,Ivanchina I D,et al.Calculation of the kinetic parameters of the hydrofining process of diesel fraction using mathematical modeling[J].Procedia Engineering,2015,113:73-78.
  • 2Cezary Debek,Jerzy Walendziewski.Hydrorefining of oil from pyrolysis of whole tyres for passenger cars and vans[J].Fuel,2015,159:659-665.
  • 3Bang Yongju,Seungwon Park,Seung Ju Han,et al.Hydrogen production by steam reforming of liquefied natural gas(LNG)over mesoporous Ni/Al2O3catalyst prepared by an EDTA-assisted impregnation method[J].Applied Catalysis B:Environmental,2015,339:179-188.
  • 4Han Yuiang,Gu Guangfeng,Sun Jingya,et al.Selective hydrodechlorination of 1,2-dichloroethane to ethylene over Pd-Ag/Al2O3catalysts prepared by surface reduction[J].Applied Surface Science,2015,355:183-190.
  • 5Aída Gutiérrez-Alejandre,Geovani Laurrabaquio-Rosas,Jorge Ramírez,et al.On the role of triethylene glycol in the preparation of highly active Ni-Mo/Al2O3hydrodesulfurization catalysts:A spectroscopic study[J].Applied Catalysis B:Environmental,2015,S166/167:560-567.
  • 6Popa Tiberiu,Zhang Yulong,Jin Erlei,et al.An environmentally benign and low-cost approach to synthesis of thermally stable industrial catalyst Cu/Si O2for the ehydrogenation of dimethyl oxalate to ethylene glycol[J].Applied Catalysis A:General,2015,505:52-61.
  • 7Kistamurthy D,Saib A M,Moodley D J,et al.Ostwald ripening on a planar Co/Si O2catalyst exposed to model Fischer-Tropsch synthesis conditions[J].Journal of Catalysis,2015,328:123-129.
  • 8Ali Alsalme,Nabil Alzaqri,Ahmad Alsaleh,et al.Efficient Ni-Mo hydrodesulfurization catalyst prepared through Keggin polyoxometalate[J].Applied Catalysis B:Environmental,2015,182:102-108.
  • 9Vishwanath G Deshmane,Sri Lanka Owen,Richard Y Abrokwah,et al.Mesoporous nanocrystalline Ti O2supported metal(Cu,Co,Ni,Pd,Zn,and Sn)catalysts:Effect of metal-support interactions on steam reforming of methanol[J].Journal of Molecular Catalysis A:Chemical,2015,408:202-213.
  • 10Ye Dong,Qu Ruiyang,Song Hao,et al.New insights into the various decomposition and reactivity behaviors of NH4HSO4with NO on V2O5/Ti O2catalyst surfaces[J].Chemical Engineering Journal,2015,283:846-854.

引证文献2

二级引证文献5

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部