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- W2289590905 abstract "In this work we have developed a software for the simulation of the number of theoretical plates in a continuous distillation column, based on the equations of vapor-liquid equilibrium and mass balance in the different sections of the column, by an iterative calculation tray by tray. Using an interactive graphical interface, the software can determine the compositions of the vapor and liquid fractions and temperature on each plate, and the liquid and vapor flow rates in the two sections of the column, it can even represent these balances graphically to determine the number of theoretical stages using the McCabe and Thiele method. The compilation results for the distillation of a binary mixture of benzene - toluene (F = 11.84 Kmol/h; Xf = 0.444, Tm = 91.5 ° C) seems 16 theoretical stages, benzene (most volatile compound) is obtained at the head of the column with vapor molar fraction 98,63% and a bottoms fraction of 35% while the toluene is obtained with 1,37% and 26,31% at the head and bottom of the column, respectively. The graduating temperature prevailing in the column increases upwards of 103.06 ° C (first tray) to 80.86 ° C (16th tray). The results of the number of theoretical stages estimated by our software coincide well with those determined graphically by the McCabe and Thiele method." @default.
- W2289590905 created "2016-06-24" @default.
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- W2289590905 date "2014-01-01" @default.
- W2289590905 modified "2023-09-27" @default.
- W2289590905 title "Elaboration d'un logiciel de simulation du nombre de plateaux théoriques dans une colonne de distillation continue ( Development of simulation software of the number of theoretical plates in a continuous distillation column )" @default.
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