Paper Titles

Computer Simulation of High Temperature Corrosion Hazard of Anode Steel Stubs in Aluminium Electrolysis Cell
p.2969

Influence of Polymer on Resistance Method Measuring Saturation
p.2975

Phase Equilibria for CO₂-Ethanol Mixtures by Perturbed-Chain Statistical Associating Fluid Theory
p.2979

Research on the Differences in the Properties of the Crude Oil between H₂O Flooding and Polymer Flooding
p.2983

Experiments on the Kinetics and Solubility of CO₂ in AMP-PZ Aqueous Solutions
p.2989

Effects of Polyvinylamine and Polyvinyl Alcohol on DOP Migration of PVC Film
p.2993

Structural Optimization of Double Swirler Based on Experimental Design
p.2997

Performance Analysis of Heat Pump Cycle with an Expander
p.3006

The Experiment Research of High-Pressure Air Blowing Ballast Tanks
p.3010

HomeApplied Mechanics and MaterialsApplied Mechanics and Materials Vols. 411-414Experiments on the Kinetics and Solubility of CO2...

Experiments on the Kinetics and Solubility of CO₂ in AMP-PZ Aqueous Solutions

Article Preview

Abstract:

The solubility and saturated loading of CO₂ in piperazine (PZ) promoted 2-amino-2-methyl-1-propanol (AMP) aqueous solution were measured at normal pressure with temperatures ranging from 293.15K to 323.15K. The temperature and the mass fraction dependences of the solubility and saturated loading of CO₂were determined. The influence of the mass fraction of PZ on the absorption rate of CO₂ was illustrated.

You might also be interested in these eBooks

Information Technology Applications in Industry II

Info:

Periodical:

Applied Mechanics and Materials (Volumes 411-414)

Pages:

2989-2992

DOI:

https://doi.org/10.4028/www.scientific.net/AMM.411-414.2989

Citation:

Cite this paper

Online since:

September 2013

Authors:

Dong Fu, Hong Mei Wang, Lei Xia Du

Keywords:

AMP, CO₂ Loading, PZ, Solubility

Export:

RIS, BibTeX

Price:

Permissions CCC:

Request Permissions

Permissions PLS:

Request Permissions

Сopyright:

© 2013 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

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

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

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

[4] Y. Maham, A.E. Mather, Fluid Phase Equilibr. 182(2001)325-336.

[5] Y. Maham, A.E. Mather, C. Mathonat, J. Chem. Thermodyn. 32 (2000) 229-236.

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

[7] E. Alvarez strella, F. Cerdeira, D. Gomez-Diaz, J. Chem. Eng. Data 55(2)(2010), 994-999.

[8] F. H. Al-Masabi, M. Castier, Int. J. Greenh. Gas Con. 5 (2011) 1478-1488.

[9] S. Xu, Y. W. Wang, F. D. Otto, A. E. Mather, Chem. Eng. Sci. 51(1996) 841-850.

[10] Z. Pei, S. Yao, W. Jianwen, Z. Wei, Y. Qing, J. Environ. Sci. 20(2008) 39-44.

[11] J. Xiao, C.W. Li, M.H. Li, Chem. Eng. Sci. 55(2000) 161-175.

[12] G. Sartori, D. W. Savage, Ind. Eng. Chem. Fund. 22(1983) 239-249.

[13] B. P. Mandal, A. K. Biswas, S. S. Bandyopadhyay, Chem. Eng. Sci. 58 (2003) 4137- 4144.

[14] B.P. Mandal, S.S. Bandyopadhyay, Chem. Eng. Sci. 61 (2006) 5440-5447.

[15] A.K. Saha, S.S. Bandyopadhyay, A.K. Biswas, Chem. Eng. Sci. 50(1995) 3587-3598.

[16] B. P. Mandal, M. Guha, A.K. Biswas, Chem. Eng. Sci. 56(2001) 6217-6224.

[17] B. P. Mandal, S.S. Bandyopadhyay, Chem. Eng. Sci. 60(2005) 6438-6445.

[18] B. P. Mandal, M. Kundu, S.S. Bandyopadhyay, J. Chem. Eng. Data 50(2005) 252-258.

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

[20] G. Astarita, D. W. Savage, J. M. Longo, Chem. Eng. Sci., 36 (3) (1981) 581-588.