Name
Abstract | ||
|---|---|---|
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–Stefan equations. Equilibrium is only assumed at the phase boundary between two phases. The equilibrium stage model is a special case of the general model. |
Year | DOI | Venue |
|---|---|---|
2004 | 10.1016/j.compchemeng.2004.04.008 | Computers & Chemical Engineering |
Keywords | DocType | Volume |
Three-phase distillation,Nonequilibrium model,Rate-based model,Maxwell–Stefan | Journal | 28 |
Issue | ISSN | Citations |
10 | 0098-1354 | 0 |
PageRank | References | Authors |
0.34 | 0 | 5 |