GYLCEROL CONVERSION OVER NOVEL FLUORINE-DOPED TIN OXIDE SUPPORTED CATALYST : EFFECT OF METAL LOADINGS AND GLYCEROL CONCENTRATION ( Penukaran Gliserol

The catalytic activity of glycerol conversion to value-added chemicals was attempted using novel fluorine-doped tin oxide (FTO) as support material with ruthenium metal. The effect of metal loadings and glycerol concentration were investigated. Glycerol hydrogenolysis is generally done using a parr reactor with the presence of hydrogen gas. Furthermore, the reaction was carried out under a mild condition (150C, 8 hours, and 20 bar of hydrogen pressure). A series of metal loading of (1.5, 3.0, 4.5, 7.5, 9.0, and 11%) were prepared to observe the activity of glycerol conversion and selectivity of 1,2-propanediol as a major product. Meanwhile, glycerol concentrations at (20, 40, 60, and 80 wt%) were proceed to determine the capability of Ru/FTO catalyst to convert glycerol at lower and higher concentration. At the optimized results, metal loading of 7.5% give a better glycerol conversion (99%) and selectivity of 1,2-PDO at 94%. Meanwhile, Ru/FTO catalyst was observed to stabilize the highest glycerol conversion at average mean of 87% for every glycerol concentration.

[1]  A. Lemonidou,et al.  Kinetic study of liquid-phase glycerol hydrogenolysis over Cu/SiO2 catalyst , 2013 .

[2]  Minghui Zhang,et al.  Cu/boehmite: A highly active catalyst for hydrogenolysis of glycerol to 1,2-propanediol , 2013 .

[3]  Kangnian Fan,et al.  Reforming and Hydrogenolysis of Glycerol over Ni/ZnO Catalysts Prepared by Different Methods , 2012 .

[4]  Tao Zhang,et al.  Mesoporous WO3 Supported Pt Catalyst for Hydrogenolysis of Glycerol to 1,3-Propanediol , 2012 .

[5]  Jixiang Chen,et al.  Comparison of Ni2P/SiO2 and Ni/SiO2 for Hydrogenolysis of Glycerol: A Consideration of Factors Influencing Catalyst Activity and Product Selectivity , 2012 .

[6]  M. Yarmo,et al.  Enhanced activity of Ru/TiO2 catalyst using bisupport, bentonite-TiO2 for hydrogenolysis of glycerol in aqueous media , 2012 .

[7]  Yoshinao Nakagawa,et al.  Heterogeneous catalysis of the glycerol hydrogenolysis , 2011 .

[8]  Ashkan Shafiee,et al.  Structural, optical and electrical properties of fluorine doped tin oxide thin films deposited using inkjet printing technique , 2011 .

[9]  Dehua He,et al.  Promoting effect of rhenium on catalytic performance of Ru catalysts in hydrogenolysis of glycerol to propanediol , 2008 .

[10]  Haichao Liu,et al.  Selective hydrogenolysis of glycerol to propylene glycol on Cu–ZnO catalysts , 2007 .

[11]  Johnathan E. Holladay,et al.  Top Value Added Chemicals From Biomass. Volume 1 - Results of Screening for Potential Candidates From Sugars and Synthesis Gas , 2004 .

[12]  L. Hoang,et al.  Aqueous polyol conversions on ruthenium and on sulfur-modified ruthenium , 1991 .

[13]  R. Shanthi Hydrogenolysis of biomass - derived sorbitol to glycols and glycerol over Ni - MgO catalysts , 2013 .

[14]  R. K. Mewada,et al.  Development of rate expression for glycerol hydrogenation reaction , 2013 .