Density of the Liquid (on the Liquid/Gas phase boundary): d_sat

• VDNS Expansion: (Output details)

  d_sat = d_c + a₁ × t^0.35 + åa_i+1 × tⁱ , where the summation is from i = 1 to nTerms -1.

  d_c = the critical density and t = 1 - T/T_c, where T_c is the critical temperature.

• Alternative 1: Rackett (Output details)

  d_sat = d_c ×B^{- (1-T/T_c)N}; where T_c and d_c are the critical temperature and critical density, respectively.

• Alternative 2: Rackett2/7 (Output details)

  d_sat = M / {R × T_c / P_c ×Z_c^(1-T/T_c)2/7}; where M is the molar mass, T_c, P_c, and Z_c are the critical temperature, critical temperature, and critical compressibility factor, respectively.

• Alternative 3: PPDS 10 (Output details)

  d_sat = d_c + a₁ × t^0.35 + a₂ × t^2/3 + a₃ × t + a₄ × t^4/3;

  d_c = the critical density and t = 1 - T/T_c, where T_c is the critical temperature.

• Alternative 4: PPDS 17 (Output details)

  d_sat = (a₁ + a₂ × t) ^{-1 - t2/7}/a₀ ; where t = 1 - T/T_c, and T_c is the critical temperature.

• Alternative 5: COSTALD (Output details)

  d_sat = M / [V₀(1 - 1.52816×τ^1/3 + 1.43907×τ^2/3 - 0.81446×τ + 0.190454×τ^4/3)
  {1 - Ω (-0.296123 + 0.386914 ×t_r - 0.0427258×t_r² - 0.0480645×t_r³)/(t_r - 1.00001)}],
  where M is the molar mass, t_r = T/T_c, τ = 1 - t_r, and T_c is the critical temperature.

• Alternative 6: PolynomialDensity (Output details)

  d_sat = å a_i × T ⁱ, where the summation is from i = 0 to nTerms - 1.