TY - JOUR
T1 - Significance of gas velocity change during the transport of CO2 through hollow fiber membrane contactors
AU - Faiz, Rami
AU - El-Naas, Muftah H.
AU - Al-Marzouqi, M.
N1 - Funding Information:
The authors would like to thank JCCP (Japan Corporation Center, Petroleum) and Research affairs at UAE University for their financial support. The authors would also like to thank Dr. Masaaki Teramoto, Kobe University, Emeritus Professor, Kyoto Institute of Technology, for the scientific and technical support.
PY - 2011/4/1
Y1 - 2011/4/1
N2 - A comprehensive 2D mathematical model was developed for the physical and chemical absorption of CO2 from natural gas containing high percentage of CO2. Unlike previous mathematical models, the model considers change in the axial gas velocity as CO2 is being absorbed from the gas mixture. The model was validated with the experimental data and compared with previous model results for a gas mixture containing 10% CO2, and then was expanded to account for higher percentages of CO2. For 10% CO2, the model predictions showed a slight difference between the previous model and the experimental data for the physical absorption of CO2. However, there was a much improved agreement between the model predictions and the experimental data for the case of chemical absorption using 0.005M MEA. Although this difference might be small for low content of CO2 in gas mixtures, the model results showed that the decrease in gas velocity becomes significant for higher content of CO2, particularly if high absorption rate of CO2 was achieved and thus, maintaining a high percent of removal of CO2 due to the increase in residence time. This is a major contrast with the previous model behavior where the percent removal of CO2 continuously decreased with the introduction of more CO2 in the gas mixture. Furthermore, the model results showed that the effect of bulk flow contribution for gas mixtures containing high content of CO2 is insignificant for systems where the gas phase mass transfer resistance is small when compared to that of the liquid phase.
AB - A comprehensive 2D mathematical model was developed for the physical and chemical absorption of CO2 from natural gas containing high percentage of CO2. Unlike previous mathematical models, the model considers change in the axial gas velocity as CO2 is being absorbed from the gas mixture. The model was validated with the experimental data and compared with previous model results for a gas mixture containing 10% CO2, and then was expanded to account for higher percentages of CO2. For 10% CO2, the model predictions showed a slight difference between the previous model and the experimental data for the physical absorption of CO2. However, there was a much improved agreement between the model predictions and the experimental data for the case of chemical absorption using 0.005M MEA. Although this difference might be small for low content of CO2 in gas mixtures, the model results showed that the decrease in gas velocity becomes significant for higher content of CO2, particularly if high absorption rate of CO2 was achieved and thus, maintaining a high percent of removal of CO2 due to the increase in residence time. This is a major contrast with the previous model behavior where the percent removal of CO2 continuously decreased with the introduction of more CO2 in the gas mixture. Furthermore, the model results showed that the effect of bulk flow contribution for gas mixtures containing high content of CO2 is insignificant for systems where the gas phase mass transfer resistance is small when compared to that of the liquid phase.
KW - Bulk flow
KW - CO absorption
KW - Change in gas velocity
KW - Mathematical modeling
KW - Membrane contactors
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U2 - 10.1016/j.cej.2011.01.029
DO - 10.1016/j.cej.2011.01.029
M3 - Article
AN - SCOPUS:79953310304
SN - 1385-8947
VL - 168
SP - 593
EP - 603
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
IS - 2
ER -