The design and control of extractive dividing-wall columns
(EDWCs)
have not yet been investigated, whereas those of dividing-wall columns
(DWCs) and conventional extractive distillation columns (CEDCs) have
been studied by many researchers. The control of EDWCs is more difficult
than that of CEDCs and somewhat different from that of DWCs because
of differences in the inner structure and interactions among control
loops in EDWCs. In this work, the design and control of an EDWC for
methylal/methanol separation are investigated using commercial chemical
simulators (Aspen Plus and Aspen Dynamics). The optimum EDWC design
based on the total annual cost (TAC) is screened first; then, the
interaction between design and control is observed; and finally, two
control structures for the EDWC are presented. The first proposed
basic control structure featuring four composition controllers and
an adjustable vapor split ratio αV can handle all
disturbances well with small offsets in product purities, except for
a 20% decrease in feed flow rate with a large deviation in methanol
product purity. Then, an improved control structure with the QR/F ratio is established. The
large deviation is effectively suppressed, and all of the disturbances
are well rejected with small offsets in product purities. It is also
revealed that the vapor split ratio αV at the bottom
edge of dividing wall must be adjusted at least for composition disturbances
of key feed components.