Experiments on the Kinetics of CO2 Loaded MDEA-DEA Aqueous Solution

Shu Bin Zhao; Pan Zhang; Xiao Tong Cai; Dong Fu

doi:10.4028/www.scientific.net/AMR.955-959.2306

Paper Titles

Effects of Solid Organic Carbon on Nitrate Remove in Groundwater
p.2285

Electrochemical Removal Cyanide in Wastewater by Ti/RuO₂-Pt Electrodes
p.2290

Removal of Organic Pollutants from Reverse Osmosis Concentrate by Electro-Fenton Process
p.2294

Experimental Study on Removal of NO Using H₂O₂/UV System
p.2300

Experiments on the Kinetics of CO₂ Loaded MDEA-DEA Aqueous Solution
p.2306

Innovations in the Design and Construction of a Modified UNITANK Wastewater Treatment Plant
p.2310

Mechanism of Collection of Dust Particles by Charged Droplet
p.2313

Performance of Treatment of Domestic Wastewater by Sequencing Batch Biofilm Reactor
p.2318

Reason Analysis of ANAMMOX Occurred in a Landfill Leachate Treatment System
p.2322

HomeAdvanced Materials ResearchAdvanced Materials Research Vols. 955-959Experiments on the Kinetics of CO2 Loaded MDEA-DEA...

Experiments on the Kinetics of CO₂ Loaded MDEA-DEA Aqueous Solution

Abstract:

The absorption rates of CO₂ in diethanolamine (DEA) promoted N-methyldiethanolamine (MDEA) aqueous solution were measured at normal pressure with temperatures ranging from 303.15-323.15K. The influence of temperature and the mass fraction of DEA on the absorption rate of CO₂ was illustrated.

You might also be interested in these eBooks

Advances in Environmental Technologies III

View Preview

Info:

Periodical:

Advanced Materials Research (Volumes 955-959)

Pages:

2306-2309

DOI:

https://doi.org/10.4028/www.scientific.net/AMR.955-959.2306

Citation:

Cite this paper

Online since:

June 2014

Authors:

Shu Bin Zhao, Pan Zhang, Xiao Tong Cai, Dong Fu

Keywords:

Absorption Rate, CO₂ Loading, MDEA, MEA, Solubility

Export:

RIS, BibTeX

Price:

Permissions CCC:

Request Permissions

Permissions PLS:

Request Permissions

Сopyright:

Citation:

References

[1] N. Nahicenovic, A. John, Energy, 16 (1991) 1347-1377.

Google Scholar

[2] R. Steenevel, B. Berger, T. A. Torp, Chem. Eng. Res. Design, 84 (A9) (2006) 739-763.

Google Scholar

[3] J. Knudsen, J.N. Jensen, P. -J. Vilhelmsen, O. Biede, Energy Procedia, 1 (2009) 783-790.

Google Scholar

[4] L. Raynal, P. A. Bouillon, A. Gomez, P. Broutin, Chem. Eng. J., 171 (3) (2011) 742-752.

Google Scholar

[5] T. Chakravarty, U. K. Phukan, R. H. Weiland, Chem. Eng. Prog., 81 (1985) 32-36.

Google Scholar

[6] A. L. Kohl, R. Nielsen, Gas Purification, 5th Ed, Gulf Publishing: Houston, TX (1997).

Google Scholar

[7] Akanksha, K. K. Pant, V. K. Srivastava, Chem. Eng. J., 133 (1-3) (2007) 229-237.

Google Scholar

[8] M. Navaza, D. G. Diaz, M. D. L. Rubia, Chem. Eng. J., 146 (2009) 184-188.

Google Scholar

[9] M. Ghulam, M. S. Azmi, K. K. Lau, and A. B. Mohamad, J. Chem. Eng. Data, 56 (2011) 2660-2663.

Google Scholar

[10] G. Rochelle, E. Chen, S. Freeman, D. V. Wagener, Q. Xu, A. Voice, Chem. Eng. J., 171 (3) (2011) 725-733.

Google Scholar

[11] A. Samanta, S. S. Bandyopadhyay, J. Chem. Eng. Data, 51 (2006), 467-470.

Google Scholar

[12] S. Bishnoi, G. T. Rochelle, Chem. Eng. Sci., 55 (2000) 5531-5543.

Google Scholar

[13] R. Dugas, G. T. Rochelle, GHGT-9 Conference (2008).

Google Scholar

[14] S. Kadiwala, A. V. Rayer, A. Henni, Fluid Phase Equilibria, 292 (2010) 20-28.

DOI: 10.1016/j.fluid.2010.01.009

Google Scholar

[15] P. W. J. Derks, J. A. Hogendoorn, G. F. Versteeg, J. Chem. Thermodynamics, 42 (2010) 151-163.

Google Scholar