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HERO ID
6039654
Reference Type
Journal Article
Title
Solubility of carbon dioxide, methane, and ethane in 1-butanol and saturated liquid densities and viscosities
Author(s)
Kariznovi, M; Nourozieh, H; Abedi, J
Year
2013
Is Peer Reviewed?
1
Journal
Journal of Chemical Thermodynamics
ISSN:
0021-9614
Volume
67
Page Numbers
227-233
DOI
10.1016/j.jct.2013.08.007
Web of Science Id
WOS:000325133600030
URL
http://www.sciencedirect.com/science/article/pii/S0021961413002875
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Abstract
A designed pressure–volume–temperature (PVT) apparatus has been used to measure the (vapor+liquid) equilibrium properties of three binary mixtures (methane +, ethane +, and carbon dioxide + 1-butanol) at two temperatures (303 and 323)K and at the pressures up to 6MPa. The solubility of the compressed gases in 1-butanol and the saturated liquid densities and viscosities were measured. In addition, the density and viscosity of pure 1-butanol were measured at two temperatures (303 and 323)K and at the pressures up to 10MPa. The experimental results show that the solubility of the gases in 1-butanol increases with pressure and decreases with temperature. The dissolution of gases in 1-butanol causes a decline in the viscosity of liquid phase. The saturated liquid density follows a decreasing trend with the solubility of methane and ethane. However, the dissolution of carbon dioxide in 1-butanol leads to an increase in the density of liquid phase. The experimental data are well correlated with Soave–Redlich–Kwong (SRK) and Peng–Robinson (PR) equations of state (EOSs). SRK EOS was slightly superior for correlating the saturated liquid densities.
Keywords
Solubility; Density; Viscosity; Gas; 1-Butanol; Mixture; Equation of state
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