Kinetic modeling of hydrogenolysis of glycerol to 1,2-propanediol using a chromium-free Ni-Cu-SiO2 nanocomposite catalyst

被引:2
作者
Woo, Yesol [1 ]
Lee, Maeum [2 ]
Cha, Seung Hyeok [2 ]
Hwang, Dong Won [2 ,3 ]
Park, Myung-June [1 ,4 ]
机构
[1] Ajou Univ, Dept Energy Syst Res, Suwon 16499, South Korea
[2] Korea Res Inst Chem Technol KRICT, Green Carbon Res Ctr, Daejeon 34114, South Korea
[3] Univ Sci & Technol UST, Dept Adv Mat & Chem Engn, Daejeon 34114, South Korea
[4] Ajou Univ, Dept Chem Engn, Suwon 16499, South Korea
关键词
Hydrogenolysis; Glycerol; 1; 2-propanediol; Kinetic modeling; Parameter estimation; PROPYLENE-GLYCOL; SELECTIVE HYDROGENOLYSIS; VAPOR-PHASE; GEL METHOD; PRESSURE; LIQUID; ACID;
D O I
10.1007/s11144-023-02390-3
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Kinetic modeling of the hydrogenolysis of glycerol was performed; a chromium-free Ni-Cu-SiO2 nanocomposite catalyst was used to produce 1,2-propanediol (1,2-PDO) at a low hydrogen-to-glycerol ratio. Kinetic data were produced in a fixed-bed reactor under a variety of temperatures, hydrogen-to-glycerol ratios, and space velocities. The reaction rates were developed based on the two-step reaction mechanism (the production of 1,2-PDO via acetol) and the reaction pathways for the byproducts observed in the experimental study. The kinetic parameters were estimated by fitting kinetic data, and the validity of the developed model was corroborated. Further analysis using the model showed that the reaction at a high temperature and a low space velocity could accomplish 95% conversion of glycerol; However, the low temperature was preferred to minimize the production of unwanted species (intermediate and byproducts) at the slight expense of conversion.
引用
收藏
页码:867 / 879
页数:13
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