Additional separation can be achieved in flash distillation by separat
ing the liquid feed into two parts, vaporizing only one part, and feed
ing these (now) two feeds to the top and bottom of a column. The drivi
ng force for the additional separation is the difference in chemical p
otential between liquid and vapor feeds with the same composition. Thi
s idea of using two feeds with the same composition but different enth
alpies (herein called two-enthalpy feed) is applied to stripping and e
nriching columns and fractional distillation. Two-enthalpy-feed distil
lation, a new method for using waste heat effectively, should be usefu
l in heat-integrated plants. When an ordinary distillation column has
a two-phase feed, the use of two-enthalpy feed increases separation (s
ame N and L/D), or decreases the number of stages (same L/D, x(D), and
x(B)), or decreases the reflux ratio (same N, x(D), and x(B)). The tw
o-enthalpy-feed system has a lower minimum reflux ratio than ordinary
distillation with a two-phase feed. For other types of feed, two-entha
lpy-feed distillation requires either less energy or energy at a less
extreme temperature (i.e., lower temperature for reboilers or higher t
emperature for condensers) than ordinary distillation. Examples are pr
esented for constant relative volatilities, hydrocarbon systems, and e
thanol-water.