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In relation to this article, we declare that there is no conflict of interest.
Publication history
Received September 23, 2010
Accepted April 11, 2011
articles 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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Hydrodynamic characters of co-current operation for SO2 absorption in a laboratory packed column

Chemical Engineering Research Center, School of Chemical Engineering and Technology, Tianjin University, Tianjin, China
sjsh_tju@sina.cn
Korean Journal of Chemical Engineering, November 2011, 28(11), 2190-2195(6), 10.1007/s11814-011-0100-y
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Abstract

A co-current operation for SO2 absorption by water was performed in a laboratory-scale packed column. The effects of L/V (liquid-gas ratio) and F (gas phase loading factor) on the SO2 absorptivity were both investigated. The absorptivity for co-current increased with the increase of L/V and the percentage of absorptivity increase at higher L/V is larger. At lower F, in regular packing there is fluctuation of absorptivity with F increased, but in random packing there is not. With the increase of F, the absorption curve slowed down. It is proposed that in order to obtain a steady desulfurization efficiency, F factor in both kinds of packings should be higher than 4 kg0.5/m0.5s. For absorptivity, which could be reached by both co-current and counter-current, it is suggested that co-current is better because of the higher gas velocity.

References

Billet R, Towers P, VCH, Weinheim, Gernamy (1995)
Sun CG, Yin FH, Afacan A, Nandakumar K, KT, Trans IChemE, Part A., 78 (2000)
Hoffmann A, Maokowiak JF, Gorak A, Haas M, Loning JM, Runowski T, Hallenberger K, Trans IChemE, Part A, Chem.Eng. Res. Des., 85 (2007)
Billet R, Schultes M, Chem. Eng. Res. Des., 77 (1999)
Philip L, Environ. Sci. Technol., 37 (2003)
Sevilla JR, Alvarez M, Diaz MC, Marrero MC, J. Chem. Eng. Data., 49 (2004)
Shilkin A, Kenig EY, Chem. Eng. J., 110 (2005)
Iliuta I, Petre CF, Larachi F, Chem. Eng. Sci., 59 (2004)
Raynal L, Ballaguet JP, Tricca CB, Chem. Eng. Sci., 59 (2004)
Zidar M, Ind. Eng. Chem. Res., 39 (2000)
Boumedine RS, Raynal L, Catal. Today., 105 (2005)
Attou A, Ferschneider G, Chem. Eng. Sci., 55 (2000)
Liao Q, Tian X, Chen R, Zhu X, Int. J. Heat Mass Transfer., 51 (2008)
Akbarnejad MM, Safekordi AA, Zarrinpashne S, Ind. Eng. Chem. Res., 39 (2000)
Guo Y, Yuan X, Zeng AW, Yu GC, CJChE., 35 (2007)

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