Steady-state simulation of wet phosphoric acid concentration process was carried out using process engineering simulator SCAPE (Software for Computer Aided Process Engineering), with the aim to study process performances. Industrial phosphoric acid was characterized by a mixture of phosphoric acid, water, and impurities in aqueous solution. The major phosphoric acid impurities were represented by a pseudocomponent. The Peng -Robinson equation of state was adapted to calculate phase equilibrium for industrial phosphoric acid using the pseudocomponent approach. The simulation of many points of cycle of phosphoric acid concentration process was carried out. The results obtained were compared to process data. The mean absolute relative error was within 0.4% for boiler temperature, 0.9% for heat exchanger outlet temperature, 0.3% for P 2 O 5 mass content of concentrated phosphoric acid, and 0.4% for concentrated phosphoric acid mass flow rate. The sensitivity of P 2 O 5 mass 2939 concentration of concentrated phosphoric acid vs. the main process parameters such as steam and weak phosphoric acid feeds, boiler pressure, and impurities mass content of weak phosphoric acid was studied.