AbstractThe first stage in the production of potash from the Dead Sea involves removal of water from Dead Sea Brine by solar evaporation. The pond function can be supplemented by osmosis, utilizing as a dewatering agent End Brine, a high osmotic pressure solution, available in large quantities as a waste stream from the solar evaporation process. For this osmosis service, asymmetric membranes, i.e. those possessing a dense skin surmounting a porous substructure, were examined. These were tubular membranes 16 mm in diameter. The membranes were of cellulose acetate, fabricated by the Loeb‐Sourirajan technique. The principle objective was to obtain a water permeation flux (permeation rate per unit area) sufficiently high for economic operation. Parameters examined included (1) casting solution composition; (2) temperature to which the membrane was heated in the casting process; (3) circulating brine flow characteristics; (4) effect of using diluted End Brine; (5) influence of reinforcing sleeve; (6) total membrane thickness. Of these parameters the last was found to be most important. At 70 microns, the minimum practical thickness, the flux was still too low. The experimental results were supported by a transport analysis of osmotic flow through an asymmetric membrane. This analysis indicated that any asymmetric membrane of the same thickness, regardless of its chemical composition would also have such low flux because flux is limited by the necessary back diffusion rate of dissolved salt in the porous substructure and by the high salt concentrations within it.
Read full abstract