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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

Postal Subscription Code 80-969

2018 Impact Factor: 2.809

Front. Chem. Sci. Eng.    2008, Vol. 2 Issue (4) : 368-372    https://doi.org/10.1007/s11705-008-0067-3
Effect of fine solid particles on absorption rate of gaseous CO
LU Sumin1, MA Youguang2, SHEN Shuhua2, ZHU Chunying2
1.Department of Material and Chemical, Tianjin Polytechnic University; 2.School of Chemical Engineering and Technology, State Key Laboratory of Chemical Engineering, Tianjin University
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Abstract The influence of the properties of solid particles in slurry on the absorption of CO2 in the slurry was investigated in a stirred thermostatic reactor. The absorption experiments were carried out in three different slurries consisting of water, cyclohexane and soybean oil, respectively, and three kinds of solid particles (active carbon, active alumina and silica gel) were incorporated into each of the above mentioned slurries separately. The experimental results show that the active carbon particles could enhance the absorption rate of gaseous CO2 in the aqueous slurry, while in the cyclohexane slurry, active carbon particles indicated no the absorption enhancement effect. However, it was observed that the active alumina and silica gel particles could enhance the absorption rate of CO2 in the cyclohexane slurry. These phenomena indicate that the solid particles, which could enhance the gaseous CO2 absorption rate, should possess two properties simultaneously, i.e. they rejected the solvent and had higher adsorption capacity for the solute. The experimental results also show that, as for those solid particles which could enhance the gas absorption rate, the enhancement increased quickly with the increase of solid concentration in slurry at first, and then reached a constant value gradually. It was also found that the enhancement factor was related to the coverage fraction of solid particles on the gas-liquid interface, and due to the reduction of surface fraction with increasing stirred speed, the enhancement factor decreased.
Issue Date: 05 December 2008
 Cite this article:   
MA Youguang,LU Sumin,SHEN Shuhua, et al. Effect of fine solid particles on absorption rate of gaseous CO [J]. Front. Chem. Sci. Eng., 2008, 2(4): 368-372.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-008-0067-3
https://academic.hep.com.cn/fcse/EN/Y2008/V2/I4/368
1 Ruthiya K C, van der Schaaf J, Kuster B F M, Schouten J C . Mechanisms of physical and reaction enhancement of masstransfer in a gas inducing stirred slurry reactor. Chem Eng J, 2003, 96: 55–69.
doi:10.1016/j.cej.2003.08.005
2 Wei G T, Li Z M, Liao D K, Tong Z F . Adsorption and decolouration process of molasses alcohol wastewaterby using modified bentonite. J Chem Engof Chinese Univ, 2004, 18: 414–419 (in Chinese)
3 Kaya A, Schumpe A . Surfactantadsorption rather than “shuttle effect”?Chem Eng Sci, 2005, 60: 6504–6510.
doi:10.1016/j.ces.2005.03.002
4 Kluytmans J H J, van Wachem B G M, Kuster B F M, Schouten J C . Mass transfer in sparged and stirred reactors: influenceof carbon particles and electrolyte. ChemEng Sci, 2003, 58: 4719–4728.
doi:10.1016/j.ces.2003.05.004
5 Dagaonkar M V, Heeres H J, Beenackers A A C M, Pangarkar V G . The application of fine TiO2 particlesfor enhanced gas absorption. Chem Eng J, 2003, 92: 151–159.
doi:10.1016/S1385-8947(02)00188-2
6 Brilman D W F, van Swaaij W P M, Versteeg G F A . One-dimensional instationaryheterogeneous mass transfer model for gas absorption in multiphasesystems. Chem Eng Proc, 1998, 37: 471–488.
doi:10.1016/S0255-2701(98)00055-5
7 Demmink J F, Mehra A, Beenackers A A C M . Gas absorption in the presenceof particles showing interfacial affinity: case of fine sulfur precipitates. Chem Eng Sci, 1998, 53: 2885–2902.
doi:10.1016/S0009-2509(98)00104-3
8 Joosten G E H, Schilder J G M, Janssen J J . The influence of suspendedsolid material on the gas-liquid mass transfer in stirred gas-liquidcontactors. Chem Eng Sci, 1977, 32: 563–566.
doi:10.1016/0009-2509(77)87017-6
9 Miyauchi M, Iguchi A, Uchida S, Koide K . Effectof solid particles in liquid-phase on liquid-side mass transfer coefficient. Can J Chem Eng, 1981, 59: 640–641
10 Albal R S, Shah Y T, Schumpe A, Carr N L . Mass transfer in multiphase agitated contactors. Chem Eng J, 1983, 27: 61–80.
doi:10.1016/0300-9467(83)80053-7
11 Janakiraman B, Sharma M M, Fast liquid-liquidreactions: rate enhancement by fine carbon particles. Chem Eng Sci, 1983, 38: 817–818.
doi:10.1016/0009-2509(83)80190-0
12 Holstvoogd R D, van Swaaij W P M . The influence adsorption capacity on enhanced gas absorption in activatedcarbon slurries. Chem Eng Sci, 1990, 45: 151–162.
doi:10.1016/0009-2509(90)87089-B
13 Beenackers A A C M, van Swaaij W P M . Mass transfer in gas-liquid slurry reactors. Chem Eng Sci, 1993, 48: 3109–3139.
doi:10.1016/0009-2509(93)80199-Z
14 Quicker Q, Alper E, Deckwer W D . Effect of fine activated carbon particleson the rate of CO2 absorption. AIChE J, 1987, 33: 871–875.
doi:10.1002/aic.690330523
15 Kars R L, Best R J, Drinkenburg A A H, The sorption of propane inslurries of active carbon in water. ChemEng J, 1979, 17: 201–210
16 Alper E, Wichtendahl B, Deckwer W D . Gas absorption mechanismin catalytic slurry reactors. Chem EngSci, 1980, 35: 217–222.
doi:10.1016/0009-2509(80)80090-X
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