Parametric Study for Nitrogen Separation from Air by Pressure Swing Adsorption Using Carbon Molecular Sieve
Main Article Content
Abstract
The separation of air by carbon molecular sieve (CMS) adsorption was studied in this work over a range of adsorption pressure of (2–8) bar. Breakthrough curves showed no significant effect of the pressure on product nitrogen purity and adsorbent capacity above 4 bar. Maximum purity of about 98% is observed for time up to 60 s. Adsorbent capacity obtained is in agreement with multicomponent Langmuir isotherm up to 4 bar. Maximum constant adsorbent capacity of about 0.1 mol O2/kg CMS is obtained for pressure above 4 bar.
For PSA two columns 6-steps process, no significant effect of the pressure on the product purity above 4 bar. The purity increases with decreasing the productivity. Maximum purity of 97.6% is obtained at productivity of 156 lit/kg CMS.hr, cycle time of 100 s, and purge flowrate of 1 lit/min. The productivity of 606 lit/kg CMS.hr is obtained at purity of 94%, cycle time of 60s, and purge flowrate of 4 lit/min.
Metrics
Article Details

This work is licensed under a Creative Commons Attribution 4.0 International License.
THIS IS AN OPEN ACCESS ARTICLE UNDER THE CC BY LICENSE http://creativecommons.org/licenses/by/4.0/
Plaudit
References
- Mendes, A. M. M., Costa, C. A. V.,
Rodrigues, A. E., “Oxygen Separation from
Air by PSA: Modeling and Experimental
Results”, Separation and Purification
Technology, 24, 173-188, 2001. DOI: https://doi.org/10.1016/S1383-5866(00)00227-6
- Rege, S. U. and Yang, R. T., “Kinetic
Separation of Oxygen and Argon Using
Molecular Sieve Carbon”, Adsorption 6, 15–
, 2000.
- Lemcoff, N. O., and LaCava A. I., “Effect of
Regeneration Pressure Level in Kinetically
Controlled Pressure Swing Adsorption”, Gas
Separation & Purification Vol 6, No 1, 1992.
- Mostamand, A., Mofarahi, M., “Simulation
of a Single Bed Pressure Swing Adsorption
for Producing Nitrogen”, International
Conference on Chemical, Biological and
Environment Sciences (ICCEBS'2011)
Bangkok Dec., 2011.
- Ruthven, D. M., “Principles of Adsorption
and Desorption Processes”, John-Wiley and
Sons, 1984.
- Bae, Y.S., Lee, C. H., “Sorption Kinetics of Eight Gases on a Carbon Molecular Sieve at Elevated Pressure, Science Direct”, Carbon 43 95–107, 2005. DOI: https://doi.org/10.1016/j.carbon.2004.08.026
- Lizzio, A. A. and Rostam-Abadi, M., Production of Carbon Molecular Sieves from Illinois COAL”, Fuel Processing Technology, 34, P 97-122, 1993. DOI: https://doi.org/10.1016/0378-3820(93)90094-K
- Anson, R. S., Fletcher, A. J. and Thomas, K. M., “Adsorption Characteristics of Carbon Molecular Sieve: Deconvolution Competing Adsorption Processes”, Conference Proceeding, Carbon 2004, providence, USA, 2004.
- Vaduva, M., Stanciu, V., “Separation of Nitrogen From Air by Selective Adsorption of Carbon Molecular Sieves”, U.P.B. Sci. Bull., Series A, Vol. 68, No. 2, 2006.
- hiI-Rley, A. I. and Lemcoff, N. O., “Air Separation by Carbon Molecular Sieves”, Adsorption 8: 147–155, 2002. 11- Crittenden, B., and Thomas, W. J., “Adsorption Technology and Design”, Reed Ed., and Prof. Publishing Ltd 1998.
- Nabais, J. M. V., Carrott, P. J. M., Carrott, M. M. L. R., Padre-Eterno, A. M., Mene´ndez, J. A., Dominguez, A., and Ortiz, A. L., “New Acrylic Monolithic Carbon Molecular Sieves for O2/N2 and CO2/CH4 Separations”, Carbon 44 1158–1165, (2006). DOI: https://doi.org/10.1016/j.carbon.2005.11.005
- Gleuckauf, E. and Coates, J. I., “The Influence of Incomplete Equilibrium on the Front Boundary of Chromatograms and the Effectiveness of Separation”, J. Chem. Soc. 1947, cited in Ref.14. DOI: https://doi.org/10.1039/jr9470001315
- Sircar Sand Hufton J. R., “Why Does the Linear Driving Force Model for Adsorption Kinetics Work?”, Adsorption 6, 137–147, 2000. DOI: https://doi.org/10.1023/A:1008965317983
- Campo, M. C., Magalhães, F. D., Mendes, A., “Separation of Nitrogen from Air by Carbon Molecular Sieve Membranes”, Journal of Membrane Science 350, 139–147, (2010). DOI: https://doi.org/10.1016/j.memsci.2009.12.021