Equations of State (EoS)
Estimate phase equilibrium through accurate cubic EoS.
- Peng-Robinson 78
- Soave-Redlich-Kwong
Heavier Components Characterization
Characterize your fluid with accurate models, extending C7+ fractions up to C80 or C200. Later, lump it into pseudo fractions in a way that optimizes your results.
Regression Module with PVT Experimental Data
To better represent your fluid, match the simulation model with your experimental data from the following typical PVT experiments:
- Constant composition expansion
- Differential liberation
- Multi-stage separator tests
Phase Envelope
P-T phase diagrams based on the saturation points of the fluid.
Phase Properties
Estimate the following volumetric, thermodynamic, and transport properties of each phase present in your system:
- Molar and mass fractions
- Molar volume
- Relative volume
- Compressibility factor
- Density and its derivatives
- Heat capacities
- Enthalpy
- Entropy
- Internal energy
- Joule-Thomson coefficient
- Sound speed
- Viscosity
- Thermal conductivity
PVT Experiments Simulations
Simulate typical experiments that represent a reservoir process or a separation process carried out in PVT laboratories:
- Constant composition expansion
- Differential liberation
- Multi-stage separator tests