Catalytic Hydrogenation Performance of Methyl Isobutyl Ketone over Ni/γ-Al2O3 Catalysts

被引:0
|
作者
Liu Lixia [1 ]
Liao Tao [1 ]
Jin Haibo [1 ]
He Guangxiang [1 ]
Yang Suohe [1 ]
Guo Xiaoyan [1 ]
Luo Guohua [1 ]
机构
[1] Beijing Key Laboratory of Fuels Cleaning and Advanced Catalytic Emission Reduction Technology,School of Chemical Engineering, Beijing Institute of Petrochemical Technology
基金
中国国家自然科学基金;
关键词
Ni/γ-Al2O3 catalysts; hydrogenation; methyl isobutyl ketone(BIBK); methyl isobutyl carbinol(MIBC);
D O I
暂无
中图分类号
O643.36 [催化剂]; TQ223.121 [];
学科分类号
0817 ; 081705 ;
摘要
Supported nickel-based catalysts were prepared by the incipient wetness impregnation method for the selective hydrogenation of methyl isobutyl ketone to methyl isobutyl carbinol in a fixed-bed reactor. The effects of the nickel source,Ni loading, calcination time, and calcination temperature on the hydrogenation performance were studied. The experimental results showed that the Ni/γ-AlOcatalyst demonstrated the highest catalytic performance under the preparation conditions by using nickel nitrate as the nickel source with a NiO loading of 20%, followed by calcination at 440°C for 5h. In addition,this catalyst showed the largest specific surface area, best crystal structure, highest active component content, smallest particle size, and uniform distribution of NiO on the surface of the carrier. The nickel-based catalyst prepared using the optimized conditions exhibited a 96.1% conversion of methyl isobutyl ketone, with a methyl isobutyl carbinol selectivity of 99.6%. The described procedure is very effective for the preparation of methyl isobutyl carbinol using methyl isobutyl ketone as the feedstock.
引用
收藏
页码:29 / 36
页数:8
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