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Received May 6, 2014
Accepted August 26, 2014
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Molecular dynamics simulation of carbon molecular sieve preparation for air separation
Department of Chemical Engineering, Faculty of Engineering, Ferdowsi University of Mashhad, Mashhad, Iran 1Department of Chemical Engineering, School of Engineering, University of Tehran, Tehran, Iran
n.farhadian@um.ac.ir, na.farhadian@gmail.com
Korean Journal of Chemical Engineering, March 2015, 32(3), 494-500(7), 10.1007/s11814-014-0250-9
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Abstract
Carbon deposition process on activated carbon (AC) in order to produce carbon molecular sieve (CMS) was simulated using molecular dynamics simulation. The proposed activated carbon for simulation includes micropores with different characteristic diameters and lengths. Three different temperatures of 773 K, 973 K, and 1,273 K were selected to investigate the optimum deposition temperature. Simulation results show that the carbon deposition process at 973 K creates the best adsorbent structure. While at lower temperature some micropore openings are blocked with carbon atoms, at higher temperature the number of deposited carbons on the micropores does not change significantly. Also, carbon deposition process confirms the pseudo-second-order kinetic model with an endothermic behavior. To evaluate the sieving property of adsorbent products, nitrogen and oxygen adsorption on the initial and final adsorbent products are examined. Results show that there is not any considerable difference between the equilibrium_x000D_
adsorption amounts of nitrogen and oxygen on the initial and final adsorbents especially at low pressure (P<10 atm). Although, adsorption kinetics curves of these gases change significantly after the carbon deposition process in comparison with the initial sample. These observations indicate that the final adsorbent has high selectivity towards oxygen compared with the nitrogen, so it can be called a carbon molecular sieve. All simulated results are in good agreement_x000D_
with experiments.
Keywords
References
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Liu YY, Wilcox J, Int. J. Coal Geol., 104, 83 (2012)
Fan C, Do DD, Nicholson D, Jagiello J, Kenvin J, Puzan M, Carbon, 52, 158 (2013)
Nasrabadi AT, Foroutan M, Comp. Mater. Sci., 61, 134 (2012)
Shi Y, J. Chem. Phys., 128 (2008)
Palmer JC, Llobet A, Yeon SH, Fischer JE, Shi Y, Gogotsi Y, Gubbins KE, Carbon, 48, 1116 (2010)
Palmer JC, Brennan JK, Hurley MM, Balboa A, Gubbins KE, Carbon, 47, 2904 (2009)
Fan LT, Argoti A, Walawender WP, Chou ST, Ind. Eng. Chem. Res., 44(7), 2343 (2005)
Ahmadpour A, Mahdyarfar M, Rashidi A, Abedinzadegan Abdi M, Eng. Fac. J-FUM, 18 (2007)
MacElroy JMD, Boyle MJ, Chem. Eng. J., 74(1-2), 85 (1999)
Wu ZQ, Liu ZP, Wang WC, Fan YQ, Xu NP, Chin. J. Chem. Eng., 16(5), 709 (2008)
Gauden PA, Terzyk AP, furmaniak S, Wloch J, Kowalczyk P, Zielinski W, J. Phys. Condens Matter, 26, 1 (2014)
Vela S, Larranaga FH, Carbon, 49, 4544 (2011)
Foroutann M, Nasrabadi AT, Physica E, 43, 261 (2010)
Hunenberger PH, Adv. Polym. Sci., 173, 105 (2005)
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Humphrey W, Dalke A, Schulten K, J. Mol. Graphics, 14, 33 (1996)
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Cai Q, Biggs MJ, Seaton NA, Phys. Chem. Chem. Phys., 10, 2519 (2008)
Xu L, Sedigh G, Sahimi M, Tsotsis TT, Phys. Rev. Lett., 80, 3511 (1998)
Lagergren S, Kung Seven Veten Hand, 24, 1 (1898)
Ho YS, McKay G, Process Biochem., 34(5), 451 (1999)
Vinodh R, Padmavathi R, Sangeetha D, Desalination, 267(2-3), 267 (2011)
Freundlich HMF, J. Phys. Chem., 57, 385 (1906)
Yang RT, Adsorbents fundamentals and application, Wiley, New Jersey (2003)