Aspen Plus Thermodynamic Method Selection Guide v3.2
The Aspen Plus Thermodynamic Method Selection Guide v3.2 is an official AspenTech technical reference document that provides systematic, application-driven recommendations for selecting appropriate thermodynamic models (e.g., activity coefficient, equation of state, and hybrid models) in Aspen Plus simulations. It bridges theoretical thermodynamics with practical process engineering requirements by mapping chemical system characteristics—such as polarity, non-ideality, phase behavior, and temperature/pressure ranges—to validated model choices. The guide supports rigorous simulation accuracy, convergence reliability, and regulatory-compliant process design.
📖 Overview
📑 Key Components
🎯 Applications
- ✓ Design and optimization of separation processes (distillation, extraction, absorption)
- ✓ Safety and operability analysis (e.g., dew/bubble point calculations, hydrate formation)
- ✓ Regulatory submission support (e.g., EPA, FDA process modeling documentation)
📐 Key Formulas
NRTL Activity Coefficient
lnγ_i = ∑_j (x_j τ_ji G_ji) / ∑_k x_k G_ki + ∑_j x_j [ (G_ij / ∑_k x_k G_kj) (τ_ij − ∑_k x_k τ_kj G_kj / ∑_m x_m G_mj) ]
Calculates activity coefficients for non-ideal liquid-phase mixtures using local composition concepts; essential for VLE/LLE in polar and moderately non-ideal systems.
Peng–Robinson Equation of State
P = RT/(v−b) − a(T)/(v(v+b)+b(v−b))
Cubic equation of state used for vapor-phase and supercritical-phase equilibria; widely applied for hydrocarbon and non-polar mixtures at high pressure.
Electrolyte NRTL (eNRTL) Margules Term
lnγ_i^L = lnγ_i^{LN} + ν_i lnγ_i^E
Decomposes total activity coefficient into long-range (electrostatic, Debye–Hückel) and short-range (local composition) contributions for aqueous electrolyte solutions.