Método McCabe-Thile

Universidad Autónoma del Estado de México[pic 1][pic 2]

FACULTAD DE QUÍMICA

Ingeniería Química

Operaciones de Separación

Dr. César Pérez Alonso

CATEDRÁTICO

EQUIPO

García Valdez Luis Evaristo

Garfias González Erika

González Ortega Anai

Morales Morales Daniel Omar

Ortega Perea David Gustavo

ALUMNOS

IQU 76

Patria, Ciencia y Trabajo.

Toluca de Lerdo, México; a 18 de octubre del 2017. 

A mixture of ethane and propane has the equilibrium data given below. Five hundred  kgmol/h of a mixture containing 30 mol % ethane is to be separated into a destillate containing 2 mol % propane and a bottoms containing 5 mol % ethane. A partial condenser and a partial reboiler Will be utilized. A column pressure of 19.0 atm has been decided on. The reflux ratio R will be 6.0. From the standpoint of equilibrium stages only, would it be better to introduce the feed as a saturated liquid or a saturated vapor? A quantitative comparison is required. In either case, estimate the condenser and reboiler temperatures.

[pic 3][pic 4][pic 5]

                                                        D=[pic 6][pic 7][pic 8][pic 9]

                                                        XDetha=0.98[pic 10]

                                                        XDprop=0.02[pic 11]

[pic 12]

F=500 kgmol/h                                                [pic 14][pic 13]

XFethane=0.3

XFpropane=0.7                                                [pic 15]

[pic 16][pic 17]

                                                        B=[pic 18][pic 19]

                                                        XB=0.05[pic 20][pic 21][pic 22][pic 23][pic 24][pic 25][pic 26][pic 27][pic 28]

                                                        XBprop=0.95

Del balance de Materia para el Etano

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