Kinetic study of glycerol hydrodeoxygenation on Al2O3 and NiMo2C/Al2O3 catalysts

被引:1
作者
Duarte, Rafael Belo [1 ,3 ]
Corazza, Marcos Lucio [2 ]
Pimenta, Joao Lourenco Castagnari Willimann [1 ]
Jorge, Luiz Mario de Matos [1 ]
机构
[1] Univ Estadual Maringa, Dept Chem Engn, Ave Colombo, 5790, BR-87020900 Maringa, PR, Brazil
[2] Univ Fed Parana, Dept Chem Engn, R Francisco H dos Santos, BR-81531990 Curitiba, PR, Brazil
[3] Univ Estadual Maringa, Dept Chem Engn, UEM, Ave Colombo, 5790-Zona 7, BR-87020900 Maringa, PR, Brazil
关键词
Glycerol; Hydrodeoxygenation; Alumina; Nickel; Molybdenum; Kinetic model; PHASE HYDROGENOLYSIS; SUPPORTED COPPER; 1,2-PROPANEDIOL; 1,3-PROPANEDIOL; PROPYLENE; NICKEL; CARBON; OXIDE; RE;
D O I
10.1016/j.fuel.2023.129257
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A kinetic study of glycerol hydrodeoxygenation (HDO) on NiMo2C/Al2O3 and Al2O3, prepared by sol-gel technique, was carried out in a batch reactor, from 250 degrees C to 285 degrees C, at high glycerol concentration (95wt%). Structural and surface properties of the catalysts were determined by XRD, nitrogen physisorption, TEM and NH3-TPD. Impregnation of alumina with Ni and Mo and subsequent carburization at 730 degrees C increased crystallite sizes and reduced total acidity of the catalyst to 1/3 that of pure alumina. All reactions were well fitted to a zeroth order model. Estimation of reagents mass transport rates suggests no diffusion limitation. Main products were propanediols, ethylene glycol and long-chain molecules from oligomerization reactions, as well as methane, ethane and propane. At this temperature range, long-chain compounds have the highest yields, mainly on alumina.
引用
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页数:15
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