Ma. Gaubert et al., Analysis and multiple steady states of an industrial heterogeneous azeotropic distillation, IND ENG RES, 40(13), 2001, pp. 2914-2924
A study of an industrial multicomponent heterogeneous azeotropic distillati
on is presented. The process concerns an organic acid dehydration using an
immiscible entrainer. First, a validation of the MESH and thermodynamic mod
els through a comparison between pilot-plant experimental reconciled data a
nd simulation results is conducted. A four-component mixture is considered
for the simulation. Case studies of the boiler heat duty are automatically
generated by an operating path tool. An infinity/infinity analysis is perfo
rmed for the heterogeneous azeotropic pilot column and an industrial column
with a decanter. Because of practical constraints, the pilot and the indus
trial columns do not have the same reflux policies. This leads the infinity
/infinity analysis to predict multiple steady states for the industrial uni
t but not for the pilot column. However, multiple steady states are found b
y simulation both for the pilot and for the industrial unit. Multiple stead
y states are confirmed by simulation and experimental data for the industri
al unit. Because of the positive infinity/infinity analysis, they are attri
buted to the phase equilibrium properties of the quaternary system. For the
pilot column, multiple steady states are found by the simulation and linke
d to experimental observations. The multiplicity is not caused by the phase
equilibrium properties; rather, it is attributed to interactions between t
he material and energy balances. An analysis of the simulation results help
s explain the behavior of the industrial unit: the temperature of the sensi
tive tray gives rise to a peak in heat. This peak is located very close to
the industrial temperature set point and is correlated with an impurity con
tent minimum in the main product stream. An impurity minimum is also eviden
ced by the simulation for the pilot column. This complex behavior can expla
in observed difficulties in controlling the process at the industrial set p
oint.