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In this study, we propose a new distillation system,
which is constituted by the combination of many evaporators
and condensers, as shown in Figure 1. The mass
and heat transfer processes are quite different from
those for the conventional distillation system. In the
conventional distillation system (Figure 2a), the mass
and heat transfer occurs by the vapor-liquid contact
in each rectifying stage and these transport rates are
affected strongly by the mechanical structure of the
rectifying stage. On the other hand, in the proposed
system (Figure 2b), a rectifying stage is divided into an
evaporator and a condenser. Then, the mass and heat
transfer are carried out by the internal flows between
the evaporator and the condenser. Note that these
internal flow rates can be controlled by the supply of
external heat to the evaporators and the release of heat
from the condensers and that the separation performance<

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