Vol.3 , No. 1, Publication Date: Mar. 14, 2018, Page: 29-40
[1] | Dibyendu Bandyopadhyay, Heavy Water Division, Bhabha Atomic Research Centre, Mumbai, India. |
[2] | Rupsha Bhattacharyya, Heavy Water Division, Bhabha Atomic Research Centre, Mumbai, India. |
[3] | Sandeep Kannuparambil Chandrasejgaran, Heavy Water Division, Bhabha Atomic Research Centre, Mumbai, India. |
Separation of hydrogen and its isotopes from helium gas is a necessary operation in the context of fusion energy systems. One of the techniques available for this separation is selective cryogenic adsorption of hydrogen on microporous adsorbents like molecular sieves (MS). In this work, adsorption isotherm data at 77 K for hydrogen on four kinds of commercially available molecular sieves have been experimentally obtained and fitted to the Langmuir isotherm. The adsorption isotherms and the constant pattern breakthrough model has been used to determine the breakthrough time and length of the mass transfer zone, and hence the size of an adsorbent bed for a given breakthrough hydrogen concentration. The cost of hydrogen adsorbed has been obtained by considering the cost of adsorbent, adsorption vessel, nitrogen boil-off losses and gas pumping costs. The effect of variation of parameters like adsorbent particle type, size, gas velocity through the bed, feed hydrogen concentration on the normalized cost of the adsorption system per adsorption cycle per mole of hydrogen adsorbed was studied. These parametric studies allowed determination of preliminary design parameters of the most economical adsorption system for hydrogen-helium separation, based on the entire adsorption process and using minimal experimental data.
Keywords
Cryogenic Adsorption, Molecular Sieves, Cost Analysis, Hydrogen Helium Separation, Parametric Optimization
Reference
[01] | Fujimura K, Raffray AR, Abdou MA. Analysis of helium purge flow in a solid breeder blanket. Fus Eng Des 1989; 8: 109-114. |
[02] | Das NK, Kumar P, Mallick C, Bhandari RK. Development of a helium purification system using pressure swing adsorption. Curr Sci 2012; 103 (6): 632-634. |
[03] | Ruthven DM, Principles of adsorption and adsorption processes. 1st ed. New York: John Wiley and Sons; 1984. |
[04] | Qian X, Luo D, Huang G, Song X, Liu W. Experimental investigation on cryogenic hydrogen adsorption of molecular sieves. Int J Hydrogen Energy 2012; 87 (4): 359-362. |
[05] | Seader JD, Henley EJ, Roper DK, Separation Process Principles-Chemical and Biochemical Operations. 3rd ed. New Jersey: John Wiley & Sons; 2011. |
[06] | Kong W, Zhang Q, Xu X, Chen D. A Simple Expression for the Tortuosity of Gas Transport Paths in Solid Oxide Fuel Cells’ Porous Electrodes. Energies 2015; 8: 13953-13957. |
[07] | Pisani L. Simple Expression for the Tortuosity of Porous Media. Trans Porous Med 2011; 88: 193-203. |
[08] | Molecular Sieves - Technical Information Bulletin, available at http://www.sigmaaldrich.com/chemistry/chemical-synthesis/learning-center/technical-bulletins/al-1430/molecular-sieves.html, last accessed on 05.10.2017. |
[09] | Dutta BK, Principles of Mass Transfer and Separation Processes. 1st ed. New Delhi: Prentice Hall of India Pvt. Ltd.; 2007. |
[10] | Geankoplis CJ, Transport Processes and Unit Operations. 3rd ed. New Jersey: Prentice Hall International, Inc.; 1993. |
[11] | McCabe W, Smith J, Harriott P, Unit Operations of Chemical Engneering. 7th ed. Boston: McGraw Hill Companies, Inc.; 2005. |
[12] | Yang WC, Flow through Fixed Beds, in W. C. Yang, (Ed.); Handbook of Fluidization and Fluid-Particle Systems. 1st ed., New York: Marcel Dekker Inc.; 2003. |
[13] | Froment GF, Bischoff KB, Chemical Reactor Analysis and Design. 1st ed. New York: John Wiley and Sons; 1979. |
[14] | Molecular Sieves, available at http://www.sigmaaldrich.com/programs/research-essentials-products.html?TablePage=14577469, last accessed on 05.10.2017. |
[15] | Latest Price 316 304 316L Stainless Steel Pipe 2016-2017, available at http://www.ashtapadoverseas.com/blog/stainlesssteelpipe-sspipe/, last accessed on 17.10.2017. |
[16] | About Liquid Nitrogen, available at https://technifab.com/cryogenic-resource-library/cryogenic-fluids/liquid-nitrogen/, last accessed on 17.10.2017. |
[17] | Schmitz B, Müller Ulrich, Trukhan N, Schubert M, Ferey G, Hirscher M. Heat of Adsorption for Hydrogen in Microporous High-Surface-Area Materials. Chem Phys Chem 2008; 9: 2181-2184. |
[18] | Price of Liquid Nitrogen, available at https://hypertextbook.com/facts/2007/KarenFan.shtml, last accessed on 17.10.2017. |
[19] | Botshekan M, Degallaix S, Desplanques Y, Polak J. Tensile and LCF properties of AISI 316LN SS at 300 and 77 K. Fatigue Fract Engg Matl Struct 1998; 21: 651-660. |
[20] | What is ITER?, available at https://www.iter.org/proj/inafewlines#6, last accessed on 13.11.2017. |
[21] | Polevoi AR, Campbell DJ, Chuyanov VA, Houlberg W, Ivanov AA, Kukushkin AS, Lamalle P, Loarte A, Mukhovatov VS, Oikawa T. Assessment of plasma parameters for the low activation phase of ITER operation. Nucl. Fusion 2013; 53: 123026-123032. |
[22] | Moss D, Pressure Vessel Design Manual. 3rd ed. Oxford: Gulf Professional Publishing; 2004. |