Abstract

It is known that the use of natural gas as a vehicular fuel is advantageous; however, the drawback of this application is the storage limitations of natural gas. One method for storing natural gas at moderate temperatures and pressures is to dissolve it in organic mixtures. In this paper, an apparatus for measuring gas solubility in liquids under high pressures was used. The solubilities of methane in methanol + n-hexane, methanol + n-heptane, and methanol + cyclohexane at 303.15 K and in methanol + benzene and methanol + methylbenzene at 288.15 K and 303.15 K were measured. The experimental pressures are up to 12.0 MPa. The new solubility measurements are believed to have uncertainties of 0.002 (mole fraction). Meanwhile, the molar volumes of liquid-phase mixtures at high pressures were determined and well-estimated by the Aalto−Keskinen model. Because of the polarity of methanol, the PRSV equation of state with the Huron−Vidal mixing rule was used to estimate the equilibrium data for methane + methanol + hexane, methane + methanol + heptane, and methane + methanol + cyclohexane systems as well as to correlate the data for methane + methanol + benzene and methane + methanol + methylbenzene systems. The average absolute deviations (AAD) of the correlation were 3.0 % and 1.9 %, respectively.

Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.