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Measurement of Vapor Pressures and Saturated Liquid Densities of Pure Fluids with a New Apparatus

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Institut für Verfahrens- und Energietechnik, Universität für Bodenkultur, Muthgasse 107, A-1190 Wien, Austria
Cite this: J. Chem. Eng. Data 2005, 50, 2, 429–437
Publication Date (Web):February 22, 2005
https://doi.org/10.1021/je0497496
Copyright © 2005 American Chemical Society

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    Abstract

    A new apparatus has been constructed to measure vapor−liquid equilibria and saturated liquid densities of pure and mixed fluids. The density measurement is based on the buoyancy method using a single sinker and a magnetic suspension balance. The permanent magnet of the magnetic suspension balance carries the sinker with a load-coupling device. Both are completely submerged in the liquid phase. The electromagnet is placed outside the magnetically neutral cell walls. Both magnets transfer the buoyancy force of the sinker through the walls to a microbalance. The apparatus is limited to the temperature range from (−60 to 250) °C, pressures up to 200 bar, and densities in the range from (10 to 2000) kg·m-3. Here, the first tests have been done with pure fluids at temperatures from (−40 to 90) °C and pressures up to 60 bar. Measurements of the compressed liquid density of water and gas density of nitrogen, carbon dioxide, and R134a confirm the accuracy of the density measurement. Also, measurements of the vapor pressure and the saturated liquid density were made for carbon dioxide and R134a. The estimated uncertainties of the experimental data are ±0.02 K for the temperature, ±5.0 mbar for the pressure, and ±0.013% + 0.01 kg·m-3 for the density.

    *

     Corresponding author. E-mail:  martin.wendla[email protected]. Tel:  +43-1-3709726-212. Fax:  +43-1-3709726-210.

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    2. Tao Yang, J. Ilja Siepmann, Jiangtao Wu. Phase Equilibria of Difluoromethane (R32), 1,1,1,2-Tetrafluoroethane (R134a), and trans-1,3,3,3-Tetrafluoro-1-propene (R1234ze(E)) Probed by Experimental Measurements and Monte Carlo Simulations. Industrial & Engineering Chemistry Research 2021, 60 (1) , 739-752. https://doi.org/10.1021/acs.iecr.0c05442
    3. Charithea Charalambous, Giulio Santori, Enrique Vilarrasa-Garcia, Moises Bastos-Neto, Célio L. Cavalcante, Jr., Stefano Brandani. Pure and Binary Adsorption of Carbon Dioxide and Nitrogen on AQSOA FAM Z02. Journal of Chemical & Engineering Data 2018, 63 (3) , 661-670. https://doi.org/10.1021/acs.jced.7b00864
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    10. Michela Mazzoccoli, Barbara Bosio, Elisabetta Arato. Analysis and Comparison of Equations-of-State with p-ρ-T Experimental Data for CO2 and CO2-Mixture Pipeline Transport. Energy Procedia 2012, 23 , 274-283. https://doi.org/10.1016/j.egypro.2012.06.052
    11. José M.S. Fonseca, Ralf Dohrn, Stephanie Peper. High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2005–2008). Fluid Phase Equilibria 2011, 300 (1-2) , 1-69. https://doi.org/10.1016/j.fluid.2010.09.017

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