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High pressure phase equilibrium measurements for binary systems CO sub(2) + 1-pentanol and CO sub(2) + 1-hexanol
This work reports phase equilibrium measurements for the systems CO sub(2)(1) + 1-pentanol(2) and CO sub(2)(1) + 1-hexanol(2). Experiments were carried out using a high pressure variable-volume view cell with operating temperatures ranged from 303.15 K to 373.15 K and pressures up to 17.05 MPa for t...
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Published in: | The Journal of supercritical fluids 2014-04, Vol.88, p.38-45 |
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Main Authors: | , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Online Access: | Get full text |
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Summary: | This work reports phase equilibrium measurements for the systems CO sub(2)(1) + 1-pentanol(2) and CO sub(2)(1) + 1-hexanol(2). Experiments were carried out using a high pressure variable-volume view cell with operating temperatures ranged from 303.15 K to 373.15 K and pressures up to 17.05 MPa for the system CO sub(2) + 1-pentanol, and 303.15 K to 353.15 K with pressures up to 16.2 MPa for the system CO sub(2) + 1-hexanol. The CO sub(2) molar fractions were ranged from 0.3987 to 0.9192 for the system CO sub(2)(1) + 1-pentanol(2) and from 0.3926 to 0.9800 for the system CO sub(2)(1) + 1-hexanol(2), respectively. Only vapor-liquid (VL) phase transitions were observed for the system CO sub(2)(1) + 1-pentanol(2), while for the system with 1-hexanol(2) vapor-liquid (VL), liquid-liquid (LL) and vapor-liquid-liquid (VLL) phase transition were observed. The experimental data sets were modeled using the Peng-Robinson equation of state with a classical van der Waals quadratic mixing rule (PR-vdW2) and with Wong-Sandler (PR-WS) mixing rule, and they were compared with predicted values using the Predictive Soave-Redlich-Kwong (PSRK) equation of state. PR-WS model provided a better fitting to experimental data for both systems modeled. |
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ISSN: | 0896-8446 |
DOI: | 10.1016/j.supflu.2014.01.005 |