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Catalytic Performance of Ultrastable Y Type Zeolite and Mg-Modified Ultrastable Y Type Zeolite on the Pyrolysis of Neosinocalamus affinis
Corresponding Author(s) : C.W. Hu
Asian Journal of Chemistry,
Vol. 25 No. 7 (2013): Vol 25 Issue 7
Abstract
Commercially available ultrastable Y type (USY) and Mg-modified USY (Mg-USY) zeolites have been used in the catalytic pyrolysis of Neosinocalamus affinis respectively, in a fixed bed reactor under nitrogen atmosphere at 773 K. The activity tests showed that the liquid yield increased to 56.4 % and 60.1 % with USY and Mg-USY zeolites respectively, in comparison with that of 25.3 % without catalyst. In particular, Mg-USY catalyst exhibited higher liquefaction activity and resulted in low solid residue of 3.5 % comparing to 28.7 % in non-catalytic experiment. In the presence of USY catalyst, acetic acid was observed as the major component and its content reached 72 % from 37.6 % without catalyst. In the presence of Mg-USY catalyst, the content of acetic acid reduced markedly (to just 25.9 %), whereas those of 1-hydroxy-2-propanone, 2-furanmethanol and other moderate-molecular weight compounds increased.
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References
K. Gadgil and K. Sharma, Asian J. Chem., 17, 2710 (2005).
W.Y. Qi, C.W. Hu, G.Y. Li, L.H. Guo, Y. Yang, J. Luo, X. Miao and Y. Du, Green Chem., 8, 183 (2006).
P. Wang, S.H. Zhan, H.B. Yu, X.F. Xue and N. Hong, Bioresour. Technol., 101, 3236 (2010).
E. Pütün, Energy, 35, 2761 (2010).
H.L. Chum and R.P. Overend, Fuel Process. Technol., 71, 187 (2001).
J.A. Caballero, A. Marcilla and J.A. Conesa, J. Anal. Appl. Pyrol., 44, 75 (1997).
F. Suarez-Garcia,A.M. Alonso and J.M.D. Tascon, J. Anal. Appl. Pyrol., 62, 93 (2002).
P.T. Williams and S. Besler, Fuel, 72, 151 (1993).
D. Meier and O. Faix, Biosour. Technol., 68, 71 (1999).
S. Czernik and A.V. Bridgwater, Energy Fuels, 18, 590 (2004).
I.N. Slam and F.N. Ani, Bioresour. Technol., 73, 67 (2000).
D.J. Mihalcik, C.A. Mullen and A.A. Boateng, J. Anal. Appl. Pyrol., 92, 224 (2011).
D. Sutton, B. Kelleher and J.R.H. Ross, Fuel Process. Technol., 73, 155 (2001).
E.G. KhamLich and L. Belkbir, Asian J. Chem., 12, 941 (2000).
D. Mohan, C.U. Pittman and P.H. Steele, Energy Fuels, 20, 848 (2006).
Y.D. Wang, A.M. Zhang, Q.H. Xu and R.Z. Chen, Appl. Catal. A, 214, 167 (2001).
D. Li, A. Nishijima and D.E. Morris, J. Catal., 182, 339 (1999).
D.Y.C. Leung, X.L. Yin, Z.L. Zhao, B.Y. Xu and Y. Chen, Fuel Process. Technol., 79, 141 (2002).
M.C. Samolada,A. Papafotica and I.A. Vasalos, Energy Fuels, 14, 1161 (2000).
A.E. Borgund and T. Barth, Org. Geochem., 30, 1517 (1999).
F. Ates, A.E. Putun and E. Putun, Energy Convers. Manage., 46, 421 (2005).
J. Rath and G. Staudinger, Fuel, 80, 1379 (2001).
J.Y. Miao, L.F. Yang and J.X. Cai, Surf. Interf. Anal., 28, 123 (1999).
S. Vitolo, M. Seggiani, P. Frediani, G. Ambrosini and L. Politi, Fuel, 78, 1147 (1999).
J.D. Adjaye and N.N. Bakhshi, Fuel Process. Technol., 45, 161 (1995).