It should also be noted that when β = 0 , the reactor temperature was maintained at its nominal value TR and all dynamical and stationary control efforts were executed by the second column distillation controller.
Obsérvese que cuando β= 0 la temperatura del reactor se mantiene en su valor nominal TR y los esfuerzos de control dinámicos y estacionarios son ejecutados por el controlador de la segunda columna de destilación.