A steady state model for CO2- reactive absorption system was developed based on principle of mass transfer and chemical reaction. The pseudo-first order model is assumed and reversibility of chemical reaction was also neglected. The continuity model equation in term of material balance with chemical reaction across an elemental stage K on CO2 was developed. The model consists of system of linear simultaneous equations, and the equations representing the composition of CO2 in both liquid and gas phases were solved. The simulation studies were performed to investigate the effect of changing various process variables such as number of plate, gas flow rate, and CO2 composition in the feed vapor.
| Published in | American Journal of Chemical Engineering (Volume 2, Issue 2) |
| DOI | 10.11648/j.ajche.20140202.11 |
| Page(s) | 8-13 |
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This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited. |
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Copyright © The Author(s), 2014. Published by Science Publishing Group |
Carbon dioxide, Reactive Absorption Column, Process Variables, Modeling
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APA Style
Adeyinka Sikiru Yusuff, Charles Uliukhifo Omohimoria, Kayode Augustine Idowu. (2014). Determination Effects of Process Parameters on CO2 Reactive absorption System by Mathematical Modeling. American Journal of Chemical Engineering, 2(2), 8-13. https://doi.org/10.11648/j.ajche.20140202.11
ACS Style
Adeyinka Sikiru Yusuff; Charles Uliukhifo Omohimoria; Kayode Augustine Idowu. Determination Effects of Process Parameters on CO2 Reactive absorption System by Mathematical Modeling. Am. J. Chem. Eng. 2014, 2(2), 8-13. doi: 10.11648/j.ajche.20140202.11
AMA Style
Adeyinka Sikiru Yusuff, Charles Uliukhifo Omohimoria, Kayode Augustine Idowu. Determination Effects of Process Parameters on CO2 Reactive absorption System by Mathematical Modeling. Am J Chem Eng. 2014;2(2):8-13. doi: 10.11648/j.ajche.20140202.11
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Download@article{10.11648/j.ajche.20140202.11,
author = {Adeyinka Sikiru Yusuff and Charles Uliukhifo Omohimoria and Kayode Augustine Idowu},
title = {Determination Effects of Process Parameters on CO2 Reactive absorption System by Mathematical Modeling},
journal = {American Journal of Chemical Engineering},
volume = {2},
number = {2},
pages = {8-13},
doi = {10.11648/j.ajche.20140202.11},
url = {https://doi.org/10.11648/j.ajche.20140202.11},
eprint = {https://article.sciencepublishinggroup.com/pdf/10.11648.j.ajche.20140202.11},
abstract = {A steady state model for CO2- reactive absorption system was developed based on principle of mass transfer and chemical reaction. The pseudo-first order model is assumed and reversibility of chemical reaction was also neglected. The continuity model equation in term of material balance with chemical reaction across an elemental stage K on CO2 was developed. The model consists of system of linear simultaneous equations, and the equations representing the composition of CO2 in both liquid and gas phases were solved. The simulation studies were performed to investigate the effect of changing various process variables such as number of plate, gas flow rate, and CO2 composition in the feed vapor.},
year = {2014}
}
TY - JOUR T1 - Determination Effects of Process Parameters on CO2 Reactive absorption System by Mathematical Modeling AU - Adeyinka Sikiru Yusuff AU - Charles Uliukhifo Omohimoria AU - Kayode Augustine Idowu Y1 - 2014/05/30 PY - 2014 N1 - https://doi.org/10.11648/j.ajche.20140202.11 DO - 10.11648/j.ajche.20140202.11 T2 - American Journal of Chemical Engineering JF - American Journal of Chemical Engineering JO - American Journal of Chemical Engineering SP - 8 EP - 13 PB - Science Publishing Group SN - 2330-8613 UR - https://doi.org/10.11648/j.ajche.20140202.11 AB - A steady state model for CO2- reactive absorption system was developed based on principle of mass transfer and chemical reaction. The pseudo-first order model is assumed and reversibility of chemical reaction was also neglected. The continuity model equation in term of material balance with chemical reaction across an elemental stage K on CO2 was developed. The model consists of system of linear simultaneous equations, and the equations representing the composition of CO2 in both liquid and gas phases were solved. The simulation studies were performed to investigate the effect of changing various process variables such as number of plate, gas flow rate, and CO2 composition in the feed vapor. VL - 2 IS - 2 ER -
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