We
present a hybrid osmotic heat engine (OHE) system that uses
draw solutions with an organic solvent for enhanced thermal separation
efficiency. The hybrid OHE system produces sustainable energy by combining
pressure-retarded osmosis (PRO) as a power generation stage and membrane
distillation (MD) utilizing low-grade heat as a separation stage.
While previous OHE systems employed aqueous electrolyte draw solutions,
using methanol as a solvent is advantageous because methanol is highly
volatile and has a lower heat capacity and enthalpy of vaporization
than water. Hence, the thermal separation efficiency of a draw solution
with methanol would be higher than that of an aqueous draw solution.
In this study, we evaluated the performance of LiCl–methanol
as a potential draw solution for a PRO–MD hybrid OHE system.
The membrane transport properties as well as performance with LiCl–methanol
draw solution were evaluated using thin-film composite (TFC) PRO membranes
and compared to the results obtained with a LiCl–water draw
solution. Experimental PRO methanol flux and maximum projected power
density of 47.1 L m–2 h–1 and
72.1 W m–2, respectively, were achieved with a 3
M LiCl–methanol draw solution. The overall efficiency of the
hybrid OHE system was modeled by coupling the mass and energy flows
between the thermal separation (MD) and power generation (PRO) stages
under conditions with and without heat recovery. The modeling results
demonstrate higher OHE energy efficiency with the LiCl–methanol
draw solution compared to that with the LiCl–water draw solution
under practical operating conditions (i.e., heat recovery <90%).
We discuss the implications of the results for converting low-grade
heat to power.