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Hydrogenolysis of Glycerol using Fe-Fe/Al2O3 Complex Catalyst
Corresponding Author(s) : Sunder Lal
Asian Journal of Chemistry,
Vol. 28 No. 12 (2016): Vol 28 Issue 12
Abstract
Macrocyclic complex catalyst Fe-FeL1 complex of L1 (L1 = C24H26O2N4.) was synthesized and studied in the hydrogenolysis reaction of glycerol reaction in a high pressure batch reactor. The catalyst was well characterized i.e. FTIR, XRD, TGA and BET surface area. The study of hydrogenolysis was found that the selectivity of 1,2-propane diol 80 % at 220 °C temperature and 0.35 MPa pressure in presence of hydrogen gas and Fe-Fe/Al2O3 and 30 % glycerol concentration in water gives 1,2-propane diol as the only product and conversion was 36 % at 220 °C. It is further seen that if the concentration of glycerol in water is increased beyond 40 % there is a decrease in the total conversion and carbon is produced as coke during the reaction.
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References
R. Connor and H. Adkins, J. Am. Chem. Soc., 54, 4678 (1932); doi:10.1021/ja01351a026.
W.E. Kaufmann and R. Adams, J. Am. Chem. Soc., 45, 3029 (1923); doi:10.1021/ja01665a033.
R.D. Cortright, R.M. Watwe and J.A. Dumesic, J. Mol. Catal. Chem., 163, 91 (2000); doi:10.1016/S1381-1169(00)00402-7.
S. Wang and H. Liu, Catal. Lett., 117, 62 (2007); doi:10.1007/s10562-007-9106-9.
J. Chaminand, L. Djakovitch, P. Gallezot, P. Marion, C. Pinel and C. Rosier, Green Chem., 6, 359 (2004); doi:10.1039/b407378a.
A. Perosa and P. Tundo, Ind. Eng. Chem. Res., 44, 8535 (2005); doi:10.1021/ie0489251.
X. Guo, Y. Li, R. Shi, Q. Liu, E. Zhan and W. Shen, Appl. Catal. A, 371, 108 (2009); doi:10.1016/j.apcata.2009.09.037.
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M.A. Dasari, P.-P. Kiatsimkul, W.R. Sutterlin and G.J. Suppes, Appl. Catal. A, 281, 225 (2005); doi:10.1016/j.apcata.2004.11.033.
Y. Kusunoki, T. Miyazawa, K. Kunimori and K. Tomishige, Catal. Commun., 6, 645 (2005); doi:10.1016/j.catcom.2005.06.006.
T. Miyazawa, S. Koso, K. Kunimori and K. Tomishige, Appl. Catal. A, 318, 244 (2007); doi:10.1016/j.apcata.2006.11.006.
T. Miyazawa, Y. Kusunoki, K. Kunimori and K. Tomishige, J. Catal., 240, 213 (2006); doi:10.1016/j.jcat.2006.03.023.
D. Roy, B. Subramaniam and R.V. Chaudhari, Catal. Today, 156, 31 (2010); doi:10.1016/j.cattod.2010.01.007.
K.A. Anand, K.S. Anisia, A.K. Agarwal and A. Kumar, Can. J. Chem. Eng., 88, 208 (2010); doi:10.1002/cjce.20273.
C.W. Chiu, M.A. Dasari, W.R. Sutterlin and G.J. Suppes, Ind. Eng. Chem. Res., 45, 791 (2006); doi:10.1021/ie050915s.
G. Zhou, T. Cheng, W. Li, Y. Bi and K. Zhen, React. Kinet. Catal. Lett., 79, 295 (2003); doi:10.1023/A:1024590203256.
P. Fouilloux, Appl. Catal., 8, 1 (1983); doi:10.1016/0166-9834(83)80051-7.
D.G. Lahr and B.H. Shanks, Ind. Eng. Chem. Res., 42, 5467 (2003); doi:10.1021/ie030468l.
L. Ma, D. He and Z. Li, Catal. Commun., 9, 2489 (2008); doi:10.1016/j.catcom.2008.07.009.
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