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Mathematical modeling for the simultaneous absorption of CO2 and SO2 using MEA in hollow fiber membrane contactors
被引:41
|作者:
Hosseinzadeh, Abolhassan
[1
]
Hosseinzadeh, Mohammadtaghi
[2
]
Vatani, Ali
[1
]
Mohammadi, Toraj
[3
,4
]
机构:
[1] Univ Tehran, Coll Chem Engn, Tehran, Iran
[2] Univ Yasuj, Yasuj, Iran
[3] Iran Univ Sci & Technol, Tehran, Iran
[4] Sch Chem Engn Tahran, Tehran, Iran
关键词:
Membrane;
Hollow fibers;
Gas permeation;
Modeling;
FLUE-GAS;
SIMULTANEOUS REMOVAL;
AQUEOUS MEA;
NATURAL-GAS;
CAPTURE;
SEPARATION;
H2S;
POLYPROPYLENE;
MIXTURE;
ENERGY;
D O I:
10.1016/j.cep.2016.08.002
中图分类号:
TE [石油、天然气工业];
TK [能源与动力工程];
学科分类号:
0807 ;
0820 ;
摘要:
In this study, it is attempted to model and simulate simultaneous removal of CO2 and SO2 from gas streams using polypropylene hollow fiber membrane contactor (HFMC) with Monoethanolamine (MEA) as a liquid absorbent. A comprehensive two-dimensional mathematical model was developed for the transport of pollutant gases through HFMC with chemical reaction on the liquid side. The Equations that obtained for the three sections of membrane contactor with the appropriate boundary conditions were solved using the COMSOL Multiphysics software version 4.2. The effect of MEA concentration, feed gases concentration, gas and liquid velocity on absorption has been studied. The velocity profile and concentration distribution of gas and liquid are also investigated on HFMC. The modeling predictions indicated that the removal of acid gas increased with increasing the liquid velocity in the membrane contactor. Also increasing the gas velocity will decrease the acid gas removal efficiency. And increasing solvent concentration will increase removal efficiency. Finally, to validate the developed model, a comparison was made between the simulation predictions of the model and the experimental data which resulted into significant corroboration between them. (C) 2016 Published by Elsevier B.V.
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页码:35 / 45
页数:11
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