Commenced in January 2007
Frequency: Monthly
Edition: International
Paper Count: 33122
Equilibrium Modeling of Carbon Dioxide Adsorption on Zeolites
Authors: Alireza Behvandi, Somayeh Tourani
Abstract:
High pressure adsorption of carbon dioxide on zeolite 13X was investigated in the pressure range (0 to 4) Mpa and temperatures 298, 308 and 323K. The data fitting is accomplished with the Toth, UNILAN, Dubinin-Astakhov and virial adsorption models which are generally used for micro porous adsorbents such as zeolites. Comparison with experimental data from the literature indicated that the virial model would best determine results. These results may be partly attributed to the flexibility of the virial model which can accommodate as many constants as the data warrants.Keywords: adsorption models, zeolite, carbon dioxide
Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1062434
Procedia APA BibTeX Chicago EndNote Harvard JSON MLA RIS XML ISO 690 PDF Downloads 2889References:
[1] I. Langmuir, J. Am. Chem. Soc. 40 (1918) 1361-1403
[2] R. Sips, J. Chem. Phys. 16 (1948) 490-495.
[3] J. Toth, Acta chim. Acad. Sci. Hung. 69 (1971) 311-328.
[4] R. Sips, J. Chem. Phys. 18 (1950) 1024-1026.
[5] J.M. Honig, L.H. Reyerson, J. Phys. Chem. 56 (1952) 140-144.
[6] M.M. Dubinin, V. A. Astakhov, Russ. Chem. Bull. 20 (1971) 8-12.
[7] V.A. Astakhov, M.M. Dubinin, Russ. Chem. Bull. 20 (1971) 13-16.
[8] M.M. Dubinin, V.A. Astakhov, Adv. Chem. Ser. 102 (1971) 69-85.
[9] R.M. Barrer, D.E.W. Vaughan, J. Phys. Chem. Solids. 32 (1971) 731- 734.
[10] D. M. Ruthven, B.K. Kaul, Lnd, Eng. Chem. Res. 32 (1993) 2047-2052.
[11] C.L. Cavalcante, D.M. Ruthven, Ind. Eng. Chem. Res. 34 (1995) 177- 184.
[12] G.W. Miller, K.S. Knaebel, K.G. Ikels, AIChE J. 33 (1987) 194-201.
[13] A. Khelifa, L. Benchehida, Z. Derriche, J. Colloid Interface Sci. 278 (2004) 9-17.
[14] D.P. Valenzuela, A.L. Mayers, Adsorption Equilibrium Data Handbook, Prentic¬e Hall, Englewood Cliffs, New Jersey, 1989 (Chapters 1 and 2).
[15] S.G. Chen, R.T. Yang, Langmuir 10 (1994) 4244-4249.
[16] S. Cavenati, C. A. Grande, and A.E. Rodrigues, J. Chem. Eng. Data ( 2004) 49, 1095-1101.