The demand for compositional simulation is growing in the petroleum industry. This is because this approach enables a detailed computer simulation of mass transfer processes in a reservoir fluid. On the other hand, compositional simulation requires high computational power for iterative calculation of multicomponent fluids' parameters in the thermodynamic equilibrium. The article presents an algorithm that allows for the determination of fluid parameters. This algorithm is based on direct Gibbs free energy minimization of a multicomponent system. The algorithm is compared with the standard iterative calculation algorithm by considering a set of multicomponent mixtures with known experimental parameters. The analysis has shown that the proposed algorithm does not concede the conventional one in accuracy and can demonstrate some calculation advantages in the critical region. Thus, the presented method is another independent way to verify the phase equilibrium parameters of multicomponent hydrocarbon mixtures.
Keywords: PHASE EQUILIBRIUM, MULTICOMPONENT SYSTEM, LINEAR PROGRAMMING, ENERGY MINIMIZATION, NUMERICAL SIMULATION.