Thermodynamics Research Center / ThermoML | Journal of Chemical Thermodynamics

Influence of nanofluid instability on thermodynamic properties near the critical point

Polikhronidi, Nikolai G., Batyrova, Rabiyat G., Magee, Joseph W., Abdulagatov, Ilmutdin M.
J. Chem. Thermodyn. 2019, 133, 46-59
ABSTRACT
Thermodynamic properties (isochoric heat capacity, critical and phase transition temperatures, pressure and thermal-pressure coefficient) of a nanofluid (2-propanol + TiO2) were experimentally studied near the critical point of the pure base fluid (2-propanol). Measurements were made using a high-temperature, high-pressure, nearly constant-volume adiabatic piezo-calorimeter that was designed for simultaneous measurements of caloric (CVVT) and density (PVT) properties of fluids along the near-critical isochores as a function of temperature in the two-phase and single-phase regions. The standard uncertainty of the density, temperature, pressure, thermal-pressure coefficient, and heat capacity measurements is estimated to be 0.1%, 0.02 K, 0.5%, 1.0%, and 1.5%, respectively. The measurements were made along a selected near-critical isochore of 282.68 kg*m-3 for a concentration of 0.132 mass fraction of TiO2 in the temperature range from (314 to 511) K. The measured CV and critical temperature data were interpreted in terms of finite-size scaling theory of critical phenomena for fluids confined in the finite-size media. The influence of finite size on the thermodynamic properties of the near- and supercritical fluid has been studied, along with thermal instability of the nanofluid (2-propanol + TiO2) at high temperatures (around 500 K).
Compounds
# Formula Name
1 C3H8O propan-2-ol
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 1
  • Molar heat capacity at constant volume, J/K/mol ; Liquid
  • Temperature, K; Liquid
  • Mass density, kg/m3; Liquid
  • Liquid
  • ADIACNV
  • 39
  • POMD
  • 1
  • Vapor or sublimation pressure, kPa ; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Closed cell (Static) method
  • 125
  • POMD
  • 1
  • Mass density, kg/m3 ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Pressure, kPa; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • ISOCHOR
  • 31
  • POMD
  • 1
  • Molar heat capacity at constant volume, J/K/mol ; Fluid (supercritical or subcritical phases)
  • Temperature, K; Fluid (supercritical or subcritical phases)
  • Mass density, kg/m3; Fluid (supercritical or subcritical phases)
  • Fluid (supercritical or subcritical phases)
  • ADIACNV
  • 110