Dewatering highly saline aqueous
streams, from mining and geothermal
leachates to industrial wastewater, is essential for effective resource
recovery and safe disposal. Membraneless water extraction (MWE) uses
a low-polarity solvent to separate water from concentrated aqueous
solutions. In this study, we design a new MWE that uses dimethyl ether
(DME) to selectively extract water from high-salinity brines, leveraging
the volatility of DME to achieve rapid solvent recovery. By separating
water and dissolved salts at a liquid–liquid interface, MWE
minimizes the deleterious effects of scaling on vulnerable membrane
and heat exchanger surfaces, reducing the need for extensive pretreatment
and expensive materials. We begin by developing a computational framework
for a multistage counterflow liquid–liquid contactor, which
extracts water into DME, coupled with a multistage solvent regenerator
that uses vapor compression to efficiently separate the desalinated
water from the DME extractant. Excess Gibbs free energy and equation
of state frameworks are used to model fluid phase equilibria in water–DME–sodium
chloride (NaCl) mixtures, with interaction parameters estimated from
experimental data. Incorporating equilibrium calculations into a system-scale
computational model, we examine the performance of MWE using DME for
the first time. Our analysis demonstrates that MWE can concentrate
seawater desalination brine (>1.0 molNaCl kg–1) to zero-liquid discharge salinities, with an energy consumption
of under 50 kW h per m3 of water extracted with a solvent
recovery ratio greater than 99.9%. We highlight the importance of
staging the vapor compression process to simultaneously minimize energy
consumption while enabling brine concentration and product water solvent
contamination. The thermodynamic framework developed here allows for
the robust evaluation of new MWE solvents and systems for critical
brine concentration and fractional precipitation applications