Study of catalytic hydrodeoxygenation performance of Ni catalysts: Effects of prepared method

被引:61
作者
Chen, Shuang [1 ]
Miao, Caixia [1 ]
Luo, Yan [2 ]
Zhou, Guilin [1 ,2 ]
Xiong, Kun [1 ]
Jiao, Zhaojie [1 ]
Zhang, Xianming [1 ]
机构
[1] Minist Educ, Engn Res Ctr Waste Oil Recovery Technol & Equipme, Chongqing 400067, Peoples R China
[2] Chongqing Technol & Business Univ, Coll Environm & Resources, Dept Mat Sci & Engn, Chongqing Key Lab Catalysis & Environm New Mat, Chongqing 400067, Peoples R China
基金
中国国家自然科学基金;
关键词
Ni catalyst; Mesoporous structure; Ethyl acetate; Hydrodeoxygenation; Catalytic activity; Ethane; WASTE COOKING OIL; CO2; METHANATION; OXIDE CATALYST; GREEN DIESEL; HYDROGENATION; SILICA; TEMPERATURE; KINETICS; SUPPORT; COPPER;
D O I
10.1016/j.renene.2017.09.028
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Ni-HT, Ni-ST, Ni-PC, and Ni-CA catalysts were synthesized using hard-template, soft-template, co precipitation, and complex methods, respectively, characterized by XRD, BET, H-2-TPR, and H-2-TPD technology. The catalytic hydrodeoxygenation performance of the prepared Ni catalysts was evaluated by using ethyl acetate as the model compound. The prepared Ni catalyst activities are in the following order: Ni-HT > Ni-ST > Ni-PC > Ni-CA. Ni-FIT and Ni-ST catalysts have developed pore structure; they show large specific surface area of 90.2 and 45.4 m(2)/g, respectively. The active phase of the catalyst is well dispersed, the active sites are widely distributed, thereby promoting the effective activation for reactant molecules. Ethyl acetate can be completely converted over Ni-HT and Ni-ST catalysts at 300 degrees C and 320 degrees C, respectively, and the ethane selectivity reaches 97.8% and 97.2%. Ni-PC and Ni-CA catalysts are mainly composed of dense particles, and have low specific surface areas of 11.2 and 2.4 m(2)/g, respectively. The crystallinity of the active phase is poor, the activation ability for the hydrogen molecule is obviously weaker than that of Ni-HT and Ni-ST catalysts. Ethyl acetate can be completely converted with the activity of Ni-PC and Ni-CA catalysts at 360 degrees C and 380 degrees C, and the ethane selectivity reached 96.7% and 93.5%, respectively. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1109 / 1117
页数:9
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