This study investigates the effect of stirring and freezing termination conditions on the performance of a batch Freeze Desalination (FD) system operating with brackish water (15,000 ppm) and seawater (40,000 ppm). To provide a comprehensive assessment of process efficiency, a new Composite Performance Index (CPI) is introduced, which integrates Recovery Ratio (RR), Salt Rejection (SR), and Specific Energy Consumption (SEC) into a single performance metric. A vapor compression refrigeration cycle was employed, and experiments were conducted under both static conditions and with mechanical stirring at 10, 20, and 30 rpm. At 30 rpm, brackish water achieved a maximum RR of 38.6 %, SR of 90.9 %, and a CPI of 12.2, compared to 35.5 %, 79.7 %, and 9.8 under static conditions, respectively. For seawater, stirring at 30 rpm increased RR from 23.8 % to 27.9 % and reduced product salinity from 1857 ppm to 1253 ppm, while SEC dropped from 908.1 to 432.4 kWh/m3. Additionally, the freezing process was extended in some cases until the brine reached twice the feed salinity, which further improved performance. At 30 rpm, increasing the cutoff salinity from 1.5× to 2× raised RR from 38.6 % to 51.6 % and CPI from 12.2 to 21.2, while SEC decreased from 286.5 to 221.4 kWh/m3. These results demonstrate that both stirring and extended freezing can significantly enhance system performance and water quality, offering practical strategies to improve FD efficiency under varying salinity conditions.
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