Wastewater treatment is essential as freshwater becomes scarce due to increasing industrialization. However, the current centralized wastewater treatment technologies are suitable for large-scale applications. There is a pressing need to develop small-scale decentralized wastewater treatment techniques. Towards this goal, a new sweeping gas membrane distillation system (SGMD) integrated with a multistage bubble column dehumidifier (BCD) was designed, built and tested to treat metalworking fluid (MWF)-contaminated wastewater. The performance of the SGMD-BCD system was first optimized using deionized water experiments. The results showed that feed water temperature significantly affected permeate flux, while air and feed water mass flow rates of 10kg/hr and 90kg/hr were identified as optimum since permeate flux and gain output ratio were insignificant above these flow rates. The simulation results of the developed system-scale mathematical model revealed that multi-staging is a more preferable option for improving effectiveness compared to increasing the condensing area in a single-stage BCD. Additionally, in long-term experiments, about 35.5% and 47.7% drops in permeate flux were observed when the MWF concentration in wastewater increased from 5 to 25 wt% at feed water temperatures of 70°C and 80°C, respectively.
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