This work focuses on design, dynamics and control of an extended dividing wall distillation column, referred to as a satellite column, and its comparison to the performance of a Kaibel column and to a direct distillation sequence for the separation of BTX mixtures.
In this study, the mass transfer performance of a PDD column was measured under pulsing and non-pulsing conditions using a 72.5 mm diameter disc and doughnut column.
A comprehensive study has been carried out to numerically investigate the performance of a three column bridge bent retrofitted with different options.
In this work we study the performance of a bubble column equipped with metal porous sparger when the liquid phase is a shear-thinning non-Newtonian fluid.
It can predict the unsteady- and steady-state performance of a bubble column reactor for photo-Fenton degradation of toluene in a waste gas.
The dispersion model was used to account for the effect of backmixing in the liquid phase on the performance of a bubble column reactor.
The results from optimized designs for these distillation structures show that the satellite column is the most energy-efficient configuration, with savings of 24.5% compared to the conventional direct sequence, and 11.8% to the performance of a Kaibel column.
The thermal performance of a standing column well system is sensitive to geological and hydrogeological conditions and is maximized in the conditions of stable groundwater temperature, high well yield, and shallow water level.
