A new design method for liquid extractors is developed using the geome
tric properties of the composition profiles in a multistage countercur
rent arrangement. These profiles are found by solving the extractor mo
del equations in the form of an initial value problem. An analysis of
the fixed points or pinches in the profiles gives the minimum solvent
flow requirement. Profiles at solvent flows above the minimum are guar
anteed to be feasible and are to be used to find the equilibrium stage
requirements and product distributions. The fixed points of the extra
ctor model equations can be determined without performing stage-to-sta
ge balances, and a comprehensive picture of the solutions and trade-of
fs in extractor design can thus be determined efficiently. This approa
ch differs from the more classical techniques in that it is applicable
to mixtures with mofe than three components, as illustrated in an exa
mple.