Fig. 8From: 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 temperature. Conditions: Qf = Qos = 18 L h−1, For (a): osmotic solution concentration, Cos,in = 300 g L−1; For (b): feed concentration Cf,in = 150 g L−1Back to article page