Commenced in January 2007
Frequency: Monthly
Edition: International
Paper Count: 33122
Dehydroxylation of Glycerol to Propylene Glycol over Cu-ZnO/Al2O3 Catalyst: Effect of Feed Purity
Authors: Thitipong Auttanat, Siriporn Jongpatiwut, Thirasak Rirksomboon
Abstract:
The catalytic dehydroxylation of glycerol to propylene glycol was investigated over Cu-ZnO/Al2O3 prepared by incipient wetness impregnation (IWI) method with different purity feedstocks - refined glycerol and technical grade glycerol. The main purpose is to investigate the effects of feed impurities that cause the catalyst deactivation. The prepared catalyst were tested for its catalytic activity and selectivity in a continuous flow fixed bed reactor at 523 K, 500 psig, H2/feed molar ratio of 4 and WHSV of 3 h-1. The results showed that conversion of refined glycerol and technical grade glycerol at time on stream 6 hour are 99% and 71% and selectivity to propylene glycol are 87% and 56% respectively. The ICP-EOS and TPO results indicated that the cause of catalyst deactivation was the amount of impurities in the feedstock. The higher amount of impurities (especially Na and K) the lower catalytic activity.Keywords: Cu-ZnO/Al2O3, dehydroxylation, glycerol, propylene glycol,
Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1334455
Procedia APA BibTeX Chicago EndNote Harvard JSON MLA RIS XML ISO 690 PDF Downloads 1989References:
[1] M. Pagliaro, M. Rossi, The future of glycerol: new usages for a versatile raw material, RSC Publishing, Cambridge, 2008.
[2] Dasari, M.A., Kiatsimkul, P., Sutterlin, W.R., and Suppes, G.J. (2005). Low-pressuse hydrogenolysis of glycerol to propylene glycol. Applied Catalysis A: Genaral, 281(1-2), 225-231.
[3] Z. Chi, D. Pyle, Z. Wen, C. Frear, S. Chen, A laboratory study of producing docosahexaenoic acid from biodiesel-waste glycerol by microalgal fermentation, Process Biochem. 42 (2007) 1537-1545.
[4] T. Miyazawa, Y. Kusunoki, K. Kunimori, K. Tomishige, J. Catal. 240 (2006) 213.
[5] M. Hájek, F. Skopal, Treatment of glycerol phase formed by biodiesel production, Bioresource Technol 101 (2010) 3242-3245.
[6] I. Gandarias, P.L. Arias, J. Requies, M. El Doukkali, M.B. G├╝emez, (2011) .Liquid-phase glycerol hydrogenolysis to 1,2-propanediol under nitrogen pressure using 2-propanol as hydrogen source, J.Cat. 282. 237- 247.
[7] E.P. Maris, W.C. Ketchie, M. Murayama, R.J. Davis, J. Catal. 251 (2007) 281.
[9] L. Ma, D. He, Z. Li, Catal. Commun. 9 (2008) 2489.
[8] D.G. Lahr, B.H. Shanks, J. Catal. 232 (2005) 386.
[9] Sitthisa, S. (2007). Dehydroxylation of glycerol for propanediols production. M.S. Thesis, The Petroleum and Petrochemaical College, Chulalongkorn University.
[10] Swangkotchakorn, C. (2008). Dehydroxylation of glycerol for propanediols production: Catalytic activity and stability Testing. M.S. Thesis, The Petroleum and Petrochemical College, Chulalongkorn University.
[11] Chirddilok, I. (2009). Dehydroxylation of glycerol to propylene glycol over copper/zinc oxide-based catalysts: Effect of catalyst preparation. M.S. Thesis, The Petroleum and Petrochemical College, Chulalongkorn University.
[12] S. Panyad, S. Jongpatiwut, T. Sreethawong, T.Rirksomboon, S. Osuwan, (2011). Catalytic dehydroxylation of glycerol to propylene glycol over Cu-ZnO/Al2O3 catalysts: Effects of catalyst preparation and deactivation, Catalysis Today. 174. 59-64.
[13] L. Zhang, X. Wang, B. Tan, U.S. Ozkan, J.Mol. Catal. A: Chem. 297 (2009) 26-34.
[14] P. Kurr, I. Kasatkin, F. Girgsdies, A. Trunschk, R. Schlögl, T. Ressle, Appl. Catal.A: Gen. 348 (2008) 153-164.
[15] J.-P. Shen, C. Song, Catal. Today 77 (2002) 89-98.