Amine-Based Carbon Dioxide Capture: Densities of CO2-Loaded Monoethanolamine Aqueous Solution at 10 to 90 °C

Article Preview

Abstract:

The global warming phenomenon has led to world climate change caused by high concentrations of greenhouse gases (GHG) especially carbon dioxide (CO2) in the atmosphere. Carbon dioxide is produced in large quantities from fuel combustions, gas sweetening processes, etc. Since its emission rises annually, some efforts to reduce the emission are, therefore, required. Monoethanolamine (MEA), a primary amine, has been widely used for many years for acid gas removal. To get a better column performance, an accurate physical properties measurement, such as density, needs to be conducted. This study aims to measure the densities of 10 wt.% MEA aqueous solutions at temperatures from 10 to 90 °C and CO2 loadings up to 0.417 mol CO2/mol MEA. The results show that the higher the concentration of CO2 the higher the density at a constant temperature, while the densities decrease as temperatures increase due to volumetric expansion. Besides, an expression to correlate the densities of 10 wt.% MEA aqueous solutions was also developed based on the pure-component molar volumes together with the excess molar volumes. The average error of the measurement was found to be 0.18%.

You might also be interested in these eBooks

Info:

Periodical:

Solid State Phenomena (Volume 319)

Pages:

47-51

Citation:

Online since:

June 2021

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2021 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] S. Ma'mun, H.F. Svendsen, I M. Bendiyasa, Amine-based carbon dioxide absorption: Evaluation of kinetic and mass transfer parameters, J. Mech. Eng. Sci. 12 (2018) 4088-4097.

DOI: 10.15282/jmes.12.4.2018.08.0354

Google Scholar

[2] Van der Hoeven, World Energy Outlook 2012, International Energy Agency, Paris, (2012).

Google Scholar

[3] U. Desideri, R. Corbelli, CO2 capture in small size cogeneration plants: Technical and economical considerations, Energ. Convers. Manage. 39 (1998) 857-867.

DOI: 10.1016/s0196-8904(97)10050-4

Google Scholar

[4] R. Hiwale, R. Smith, S. Hwang, A novel methodology for the modeling of CO2 absorption in monoethanolamine (MEA) using discrimination of rival kinetics, J. Ind. Eng. Chem. 25 (2015) 78-88.

DOI: 10.1016/j.jiec.2014.10.016

Google Scholar

[5] W.H. Tay, K.K. Lau, A.M. Shariff, High frequency ultrasonic-assisted chemical absorption of CO2 using monoethanolamine (MEA), Sep. Purif. Technol. 183 (2017) 136-144.

DOI: 10.1016/j.seppur.2017.03.068

Google Scholar

[6] N.A. Ramli, N.A. Hashim, M.K. Aroua, Supported ionic liquid membranes (SILMs) as a contactor for selective absorption of CO2/O2 by aqueous monoethanolamine (MEA), Sep. Purif. Technol. 23 (2020) Article 115849.

DOI: 10.1016/j.seppur.2019.115849

Google Scholar

[7] J.S. Eckert, Selecting the proper distillation column packing, Chem. Eng. Prog. 66 (1970) 39-44.

Google Scholar

[8] G.Q. Wang, X.G. Yuan, K.T. Yu, Review of mass-transfer correlations for packed columns. Ind. Eng. Chem. Res., 44 (2005) 8715-8729.

DOI: 10.1021/ie050017w

Google Scholar

[9] R.H. Weiland, J.C. Dingman, D.B. Cronin, G.J. Browning, Density and viscosity of some partially carbonated aqueous alkanolamine solutions and their blends, J. Chem. Eng. Data 43 (1998) 378-382.

DOI: 10.1021/je9702044

Google Scholar

[10] T.G. Amundsen, L.E. Øi, D.A. Eimer, Density and viscosity of monoethanolamine + water + carbon dioxide from (25 to 80) °C, J. Chem. Eng. Data 54 (2009) 3096-3100.

DOI: 10.1021/je900188m

Google Scholar

[11] S. Ma'mun, Selection and characterization of new absorbents for carbon dioxide capture, doctoral thesis, Norwegian University of Science and Technology, Trondheim, Norway (2005).

Google Scholar

[12] S. Ma'mun, H.F. Svendsen, K. A. Hoff, O. Juliussen, Selection of new absorbents for carbon dioxide capture, Energy Convers. Manag. 48 (2007) 251–258.

DOI: 10.1016/j.enconman.2006.04.007

Google Scholar