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In the direct contact membrane distillation (DCMD) system, the temperature polarization due to boundary layer formation limits the system performance. This study presents the experimental results and heat transfer analysis of a DCMD module coupled with a salinity gradient solar pond (SGSP) under three different flow channel configurations. In the first case, the feed and permeate channels were both empty, while in the next two cases, the feed and permeate channels were filled with a porous spacer material. Two different spacer geometries are examined: 1.5 mm thick with a filament angle of 65°, and 2 mm thick with a filament angle of 90°. The study considers only the heat transfer due to conduction by replacing the hydrophobic membrane normally used in a DCMD module with a thin polypropylene sheet so that no mass transfer can occur between the feed and permeate channels. The Reynolds number for all three configurations was found to be between 1000 and 2000, indicating the flow regime was laminar. The flow rate through both the feed and permeate sides was the same, and experiments were conducted for flow rates of 5 L/min and 3 L/min. It has been found that the highest overall heat transfer coefficient was obtained with the spacer of 2 mm thickness and filament angle of 90°. [ABSTRACT FROM AUTHOR]

This study examines the effect of spacers and operating conditions (feed inlet temperature, velocity, and feed concentration) on mass transfer characteristics in direct contact membrane distillation (DCMD) systems. The experimental results showed that velocity of the feed and permeate influenced the mass transfer properties more significantly than the temperature and concentration factors. Among the five investigated spacers, the plastic spacer (PL4) had the most influence on mass transfer characteristics, which was proven through analysing the mass transfer coefficient (k s), boundary layer thickness (δ), shear stress (τ) as well as flow property in DCMD spacer-filled channels. Moreover, the mass transfer correlation for each spacer and a general mass transfer correlation for all spacers were determined. Through comparisons between theoretical and experimental Sherwood numbers, the mass transfer correlation developed by Grober for empty channels could be used to describe the mass transfer characteristic in spacer-filled channels in this study. • Propose a new methodology to describe adequately mass transfer properties in spacer-filled DCMD channels. • Identify the mass transfer correlation for all investigated spacers in direct contact membrane distillation module. • Determine the most appropriate spacer for the best improvement in mass transfer property and permeate flux. [ABSTRACT FROM AUTHOR]