Nonequilibrium modeling of three-phase distillation

A nonequilibrium (NEQ) model for a complete three-phase distillation in tray columns is described. The model consists of a set of mass and energy balances for each of the three possible phases present. Mass and heat transfer between these phases is modeled using the Maxwell

• Type: Journal
• Year: 2004
• Where: CCE
• Authors: A. Higler, R. Chande, R. Taylor, R. Baur, R. Krishna
• Keywords: CCE 2004, CCE 2007, Liquid Phase, Model, Three-phase Distillation