A new method to combine high-pressure vapor-liquid equilibrium and thermophysical property measurements for low-volatility liquids and a gas

被引:1
|
作者
Al-Barghouti, Karim S. [1 ,2 ]
Schmidt, Hannes [1 ,2 ]
Eichberger, Ethan [1 ,2 ]
Shiflett, Mark B. [1 ,2 ]
Scurto, Aaron M. [1 ,2 ]
机构
[1] Univ Kansas, Dept Chem & Petr Engn, Lawrence, KS 66045 USA
[2] Univ Kansas, Inst Sustainable Engn, Lawrence, KS 66045 USA
来源
关键词
Vapor-liquid equilibrium; Nonvolatile solvents; Gas solubility; Density; Viscosity; FLUID-PHASE EQUILIBRIA; IONIC LIQUIDS; CARBON-DIOXIDE; THERMODYNAMIC PROPERTIES; BINARY-MIXTURES; CONDENSATION BEHAVIOR; HYDROCARBON MIXTURES; NATURAL-GAS; VISCOSITY; SYSTEM;
D O I
10.1016/j.jct.2023.107246
中图分类号
O414.1 [热力学];
学科分类号
摘要
Vapor-liquid equilibria measurements involving liquids with low volatility, such as many types of lubricants, ionic liquids, and various solvents are essential for process research and development in a wide variety of fields. State-of-the-art methods to measure these phase equilibria, e.g. thermogravimetric analysis or equilibrium cells, generally cannot be combined with instruments measuring thermophysical properties, e.g. density, transport properties, spectroscopic properties, etc. A novel approach was developed to measure simultaneously vapor-liquid equilibrium and thermophysical properties involving a single gas dissolved in one or more low-volatility liquids. The method is based upon a mass balance measuring liquid phase density, total masses in the system, and volumes. The governing equations of the novel approach are derived, and a detailed uncertainty analysis is presented. As an example, the solubility, density, and viscosity are measured with the new apparatus for a system of a non-volatile ionic liquid solvent saturated with the compressed hydrofluorocarbon gas, pentafluoroethane (R-125), at 25 degrees C and 75 degrees C and pressures to similar to 3.1 MPa. The solubility data are validated by comparison to previously published literature data using a high precision gravimetric microbalance. The combination of vapor-liquid equilibria and thermophysical properties in a single experiment can significantly accelerate scientific and engineering studies.
引用
收藏
页数:13
相关论文
共 50 条
  • [21] High-pressure vapor-liquid equilibrium measurement for the binary mixtures of carbon dioxide+n-butanol
    Jong Sung Lim
    Cheol Hun Yoon
    Ki-Pung Yoo
    Korean Journal of Chemical Engineering, 2009, 26 : 1754 - 1758
  • [22] High-Pressure Vapor-Liquid Equilibrium Data for (Carbon Dioxide plus Cyclopentanol) and (Propane plus Cyclopentanol)
    Naidoo, Paramesperi
    Raal, J. David
    Ramjugernath, Deresh
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55 (01): : 196 - 200
  • [23] High-pressure vapor-liquid equilibrium - For the systems propylene-isobutane and propane-hydrogen sulfide
    Gilliland, ER
    Scheeline, HW
    INDUSTRIAL AND ENGINEERING CHEMISTRY, 1940, 32 : 48 - 54
  • [24] High-pressure vapor-liquid and solid-gas equilibria using a Peng-Robinson group contribution method
    Tochigi, K
    Iizumi, T
    Sekikawa, H
    Kurihara, K
    Kojima, K
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (09) : 3731 - 3740
  • [25] TERNARY SYSTEMS - A NUMERICAL METHOD FOR CALCULATION OF VAPOR-LIQUID EQUILIBRIUM DATA FROM TOTAL PRESSURE MEASUREMENTS
    RAMALHO, RS
    BUI, VT
    CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1970, 48 (04): : 446 - &
  • [26] New Design of the High-Pressure Optical Cell for Vapor-Liquid Equilibrium Measurements. Supercritical Binary Mixture (Propane/n-Butane) plus Acetophenone
    Khairutdinov, Vener F.
    Gumerov, Farid M.
    Gabitov, Farizan R.
    Zaripov, Zufar, I
    Khabriev, Ilnar Sh
    Akhmetzyanov, Talgat R.
    Abdulagatov, Ilmutdin M.
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2020, 65 (07): : 3306 - 3317
  • [27] Modelling of the Isothermal Vapor-Liquid Equilibrium of Alternative Refrigerants: Determination of Phase Diagrams (High-pressure/Low-pressure) and Optimized Binary Interaction Parameters
    Zerfa, A.
    Maalem, Y.
    Madani, H.
    Beicha, A.
    JOURNAL OF THE PAKISTAN INSTITUTE OF CHEMICAL ENGINEERS, 2023, 51 (01): : 39 - +
  • [28] High-pressure vapor-liquid equilibrium data for ternary systems co2 + organic solvent + curcumin
    Giufrida, Willyan M.
    Favareto, Rogério
    Cabral, Vladimir F.
    Meireles, M. Angela A.
    Cardozo-Filho, Lucio
    Corazza, Marcos L.
    Open Chemical Engineering Journal, 2010, 4 (01): : 3 - 10
  • [29] High-pressure vapor-liquid equilibrium measurement for the binary mixtures of carbon dioxide plus n-butanol
    Lim, Jong Sung
    Yoon, Cheol Hun
    Yoo, Ki-Pung
    KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2009, 26 (06) : 1754 - 1758
  • [30] High-pressure vapor-liquid equilibrium data and modeling of propane plus methanol and propane plus ethanol systems
    Joung, SN
    Shin, HY
    Kim, HS
    Yoo, KP
    JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2004, 49 (03): : 426 - 429