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ISRN Chemical Engineering 7 currently working on CO2 capture from flue gases. It has been potentially demonstrated that CO2 can be captured using PSA [224–227] but more fundamental and long-term pilot plant studies are required to properly benchmark this technique against amines. Also, olefin-paraffin separation by adsorption was quite studied, but the energetic consumption of the separation by adsorption is still comparable to dis- tillation [228]. Utilization of PSA for natural gas upgrading (CH4-CO2 separation basically) still also remains a challenge [229, 230]. PSA technology and even RPSA can be used to upgrade biogas, but the flowrate and pressure levels of natural gas require alternative solutions. Furthermore, new stringent legislation related to reducing the emission of greenhouse gases is changing the design of processes in energy and fuel industries. New processes intend to include or integrate the CO2 capture, thus introducing specifications in the most adsorbed compound. A solution that is already in use and should be more explored is the dual PSA concept [231–235]. In all these emergent applications of PSA technology, faster and better solutions can happen by having a good interaction between materials science and process engineer- ing. References [1] I. Langmuir, “The adsorption of gases on plane surfaces of glass, mica and platinum,” The Journal of the American Chemical Society, vol. 40, no. 9, pp. 1361–1403, 1918. [2] M.Polanyi,“SectionIII.—theoriesoftheadsorptionofgases: a general survey and some additional remarks. Introductory paper to section III,” Transactions of the Faraday Society, vol. 28, pp. 316–333, 1932. [3] A.L.MyersandJ.M.Prausnitz,“Thermodynamicsofmixed- gas adsorption,” AIChE Journal, vol. 11, pp. 121–127, 1965. [4] D. M. Ruthven, Priciples of Adsorption and Adsorption Processes, John Wiley & Sons, New York, NY, USA, 1984. [5] R. T. Yang, Adsorbents. Fundamentals and Applications, John Wiley & Sons, New Jersey, NJ, USA, 2003. [6] P. C. Wankat, Large-Scale Adsorption and Chromatography, CRC Press, Boca Raton, Fla, USA, 1986. [7] A. E. Rodrigues, M. D. LeVan, and D. Tondeur, Adsorption, Science and Technology, Kluwer Academic Publishers, Boston, Mass, USA, 1989. [8] M. Suzuki, Adsorption Engineering, Chemical Engineering Monographs, Elsevier, Tokyo, Japan, 1990. [9] J. Ka ̈rger and D. M. Ruthven, Diffusion in Zeolites and Other Microporous Solids, John Wiley & Sons, London, UK, 1992. [10] C. Tien, Adsorption Calculations and Modeling, Butterworth- Heinemann, Boston, Mass, USA, 1994. [11] D. Basmadjian, The Little Adsorption Book: A Practical Guide for Engineers and Scientists, CRC Press, Boca Raton, Fla, USA, 1997. [12] J. L. Humphrey and G. E. Keller, Separation Process Technol- ogy, McGraw-Hill, New York, NY, USA, 1997. [13] D. D. Do, Adsorption Analysis: Equilibria and Kinetics, Imperial College Press, London, UK, 1998. [14] J. W. Thomas and B. D. Crittenden, Adsorption Technology and Design, Elsevier, Boston, Mass, USA, 1998. [15] O. Talu, “Needs, status, techniques and problems with binary gas adsorption experiments,” Advances in Colloid and Interface Science, vol. 76-77, pp. 227–269, 1998. [16] F. Rouquerol, J. Rouquerol, and K. Song, Adsorption by Powders and Porous Solids, Academic Press, London, UK, 1999. [17] J. Keller and R. Staudt, Gas Adsorption Equilibria: Experi- mental Methods and Adsorption Isotherms, Springer, Boston, Mass, USA, 2005. [18] P. C. Wankat, Separation Process Engineering, Prentice Hall, London, UK, 2nd edition, 2007. [19] K. S. Knaebel and F. B. Hill, “Pressure swing adsorption: development of an equilibrium theory for gas separations,” Chemical Engineering Science, vol. 40, no. 12, pp. 2351–2360, 1985. [20] M.D.LeVan,“Pressureswingadsorption:equilibriumtheory for purification and enrichment,” Industrial and Engineering Chemistry Research, vol. 34, no. 8, pp. 2655–2660, 1995. [21] G. Pigorini and M. D. LeVan, “Equilibrium theory for pressure swing adsorption. 2: purification and enrichment in layered beds,” Industrial and Engineering Chemistry Research, vol. 36, no. 6, pp. 2296–2305, 1997. [22] G. Pigorini and M. D. LeVan, “Equilibrium theory for pressure swing adsorption. 3: separation and purification in two-component adsorption,” Industrial and Engineering Chemistry Research, vol. 36, no. 6, pp. 2306–2319, 1997. [23] G. Pigorini and M. D. LeVan, “Equilibrium theory for pressure-swing adsorption. 4: optimizations for trace sep- aration and purification in two-component adsorption,” Industrial and Engineering Chemistry Research, vol. 37, no. 6, pp. 2516–2528, 1998. [24] A. Serbezov and S. V. Sotirchos, “Semianalytical solution for multicomponent pressure swing adsorption,” Chemical Engineering Science, vol. 53, no. 20, pp. 3521–3536, 1998. [25] A. Serbezov, “Effect of the process parameters on the lenght of the mass transfer zone during product withdrawal in pressure swing adsorption cycles,” Chemical Engineering Science, vol. 56, no. 15, pp. 4673–4684, 2001. [26] A. D. Ebner and J. A. Ritter, “Equilibrium theory analysis of rectifying PSA for heavy component production,” AIChE Journal, vol. 48, no. 8, pp. 1679–1691, 2002. [27] A. D. Ebner and J. A. Ritter, “Equilibrium theory analysis of dual reflux PSA for separation of a binary mixture,” AIChE Journal, vol. 50, no. 10, pp. 2418–2429, 2004. [28] H. W. Habgood, “The kinetics of molecular sieve action: sorption of nitrogen-methane mixtures by Linde Molecular Sieve 4A,” Canadian Journal of Chemistry, vol. 36, pp. 1384– 1397, 1958. [29] K. Chihara, M. Suzuki, and K. Kawazoe, “Adsorption rate on molecular sieving carbon by chromatography,” AIChE Journal, vol. 24, no. 2, pp. 237–246, 1978. [30] H. Ju ̈ntgen, K. Knoblauch, and K. Harder, “Carbon molec- ular sieves: production from coal and application in gas separation,” Fuel, vol. 60, no. 9, pp. 817–822, 1981. [31] A. Kapoor and R. T. Yang, “Kinetic separation of methane- carbon dioxide mixture by adsorption on molecular sieve carbon,” Chemical Engineering Science, vol. 44, no. 8, pp. 1723–1733, 1989. [32] R. Ramachandran, L. H. Dao, and B. Brooks, “Method of producing unsaturated hydrocarbons and separating the same from saturated hydrocarbons,” U.S. patent 5, 365, 011, 1994. [33] A. I. Fatehi, K. F. Loughlin, and M. M. Hassan, “Separation of methane-nitrogen mixtures by pressure swing adsorption using a carbon molecular sieve,” Gas Separation and Purifica- tion, vol. 9, no. 3, pp. 199–204, 1995.PDF Image | Advances in Pressure Swing Adsorption for Gas Separation
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