(341e) Molecular Distillation Modeling and Simulation to Split Heavy Petroleum Fractions Conference: AIChE Annual MeetingYear: 2008Proceeding: 2008 AIChE Annual MeetingGroup: Separations DivisionSession: Distillation: Equipment and Processes Time: Tuesday, November 18, 2008 - 4:15pm-4:30pm Authors: Zuñiga Liñan, L., University of Campinas, UNICAMP Lima, N. M. N., University of Campinas, UNICAMP Wolf Maciel, M. R., University of Campinas, UNICAMP Manenti, F., Politecnico di Milano Manca, D., Politecnico di Milano Medina, L. C., PETROBRAS - Research Center Batistella, C. B., University of Campinas, UNICAMP Maciel Filho, R., University of Campinas, UNICAMP Modeling and simulation of molecular distillation to split of heavy petroleum residues (400°C + AET) are proposed. A theoretical study of this problem is illustrated for a heavy petroleum cut (372°C-811°C AET) divided into six pseudo-components. In the process simulation, a falling film, a heater and an extremely low pressure evaporator are considered. The mathematical model comprises equations for the evaluation of the physico-chemical properties, in order to characterize the distilled mixture. Physico-chemical properties are formulated through the adjustment of experimental parameters such as molecular mass, specific heat, viscosity, and density. Heat and material balances on the liquid film are numerically solved by using a central finite-difference method. Specifically, the Crank-Nicolson method is adopted. The simulation is carried out at the steady-state conditions, where the relevant process variables, such as film thickness, surface evaporation rate, liquid interface temperature, concentration profiles, and amount of distillate flow rate are computed. In molecular distillation, the concentration of the most volatile components shrinks in both axial and radial directions, especially due to the fast increase of the temperature in the falling film. As a consequence, the less volatile component of the liquid mixture undergoes a fast increase on the liquid interface, by clearly showing the potentialities of the molecular distillation process in separating heavy petroleum residues. As the results show, the inlet variables such as the temperature and the feed flow rate largely influence the final composition of the condensate flow. Keywords: Molecular distillation; Simulation; Heavy petroleum residues; Physico-chemical properties.