High pressure phase behavior for carbon dioxide-1-butanol and carbon dioxide-1-octanol systems |
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Authors: | Hun-Soo Byun Chul Kwak |
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Affiliation: | (1) Department of Chemical Engineering, Yosu National University, Yosu, 550-749 Chonnam, South Korea;(2) School of Chemical Engineering, Kyungnam University, Masan, 550-701 Kyungnam, South Korea |
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Abstract: | Pressure-composition isotherms are obtained for binary mixtures of carbon dioxide-1-butanol and carbon dioxide-1-octanol systems
at 40, 60, 80, 100, and 120 °C and pressures up to 220 bar. The accuracy of the experimental apparatus was tested by comparing
the measured phase equilibria data of the carbon dioxide-1-butanol system at 40 °C with those of Ishihara et al. 1996]. The
solubility of 1-butanol and 1-octanol for the carbon dioxide-1-butanol and carbon dioxide-1-octanol systems increases as the
temperature increases at constant pressure. The carbon dioxide-1-butanol and carbon dioxide-1-octanol systems have continuous
critical mixture curves that exhibit maximums in pressure at temperatures between the critical temperatures of carbon dioxideand
1-butanol or 1-octanol. The carbon dioxide-1-butanol system exhibits type-I phase behavior, characterized by a continuous
critical line from pure carbon dioxide, to the second component with a maximum in pressure. Also, the carbon dioxide-1-octanol
system exhibits type-I curve at 60–120 °C, and shows liquid-liquid-vapor phase behavior at 40 oC. The experimental results
for the carbon dioxide-1-butanol and carbon dioxide-1-octanol systems have been modeled by the Peng-Robinson equation of state.
A good fit of the data is obtained with the Peng-Robinson equation by using two adjustable interaction parameters for the
carbon dioxide-1-butanol system and a poor fit using two adjustable parameters for the carbon dioxide-1-octanol mixture. |
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Keywords: | Phase Behavior Carbon Dioxide-1-Butanol System Carbon Dioxide-1-Octanol System Peng-Robinson Equation of State |
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