Multistage counter-current liquid–liquid
extraction (MCCE)
is a common unit operation in the chemical industry, but the technique
is often difficult to use at laboratory and small production scales,
because most MCCE systems are gravity-driven and require a large volume
(∼100 mL). We present a new MCCE design that integrates segmented
flow mixing and membrane-based phase separators to achieve equilibrium
extraction at each stage. Multichannel peristaltic pumps transfer
fluids from stage to stage in a counter-current manner, rather than
dedicated pumps at each stage. A self-tuning pressure control element
incorporated into each separator allows robust operation, even in
the presence of variation between stages and imprecise pumping. Experimental
data from two classical ternary case studies (toluene–acetone–water
and ethyl acetate–acetic acid–water) compare well to
ASPEN Plus simulations, showing that the extraction efficiency is
∼100%, regardless of the number of stages. Finally, we demonstrate
the efficiency of the small-scale MCCE system (∼2 mL/stage)
with an industrial example of recovery of THF and ethyl acetate from
methanol, ethanol, iso-butanol, and tert-butanol
mixtures.