Fig. 7From: Development of mass and heat transfer coupled model of hollow fiber membrane for salt recovery from brine via osmotic membrane distillationWater transport flux as a function of feed and osmotic solution flow rate. Conditions: for a osmotic solution concentration, Cos,in = 300 g L−1; For b feed concentration, Cos,in = 150 g L−1; Tf = 303 K ± 1, Tos = 293 K ± 1Back to article page