A bench-scale forward osmosis−membrane distillation (FO−MD) system was applied to flue gas desulfurization (FGD) wastewater generated at coal-fired power plants (CFPPs) focusing on water recovery, salt rejection, thermal energy demands, and potential for harvesting low-grade waste heat. With the use of flat-sheet cellulose triacetate (CTA) and polytetrafluoroethylene (PTFE) membranes, treatment of synthetic and collected FGD wastewater was evaluated across a range of applicable temperatures (43.3−65.5 °C) and draw solutions (NaCl, CaCl 2 , PAA-Na). Highest water fluxes were observed at the highest NaCl and CaCl 2 draw solution concentrations (3.4 M) and temperatures (65.5 °C) evaluated, with FO and MD fluxes reaching 37 and 25 LMH, respectively. The FO−MD system achieved over 99.8% rejection of all surveyed components (Na, K, Ca, Mg, B, Cl − , SO 4 2− ), producing permeate with conductivities below 105 μS/cm. An 89% water recovery occurred using a 3.4 M sodium chloride draw solution. While the FO−MD process is capable of treating FGD wastewater, basic osmotic backwashing was insufficient at restoring the FO membrane water flux. Further investigation of membrane fouling and scaling is warranted. Investigation of the required heat for MD indicates that adequate low-grade waste heat sources are available on-site, suggesting the FO−MD process can be an effective, energy efficient, and sustainable treatment technology for FGD wastewater.