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• W3202066327 abstract "Electrodialysis (ED) was integrated into the desalination unit of an ethylene glycol (EG) recovery system for combustible ice mining in order to alleviate the energy-intensive investment of conventional thermal desalination processes. Bench- and pilot-scale ED experiments were conducted. In bench-scale experiments, the effects of applied voltage, circulating flow rate, and EG content were investigated. Bench-scale ED achieved a 90% desalination ratio within 60 min requiring 9.8 kWh/m3 energy consumption and exhibiting a 0.58% EG leakage ratio under 24 V applied voltage, 20 L/h circulating flow rate, and 40-wt% EG. These results indicated that the desalination performance was more sensitive to the applied voltage and the EG content. Moreover, when treating saline-EG solutions with 40 and 60-wt% EG at 130 V, three-stage pilot-scale ED process generated continuous desalted EG solution (lean-EG) with total dissolved solids corresponding to 2.55 and 9.22 g/L, respectively. The corresponding desalination ratios (90% and 65%) required energy consumptions of 16.19 and 10.41 kWh/m3, respectively. Furthermore, economic estimations predicted that the costs were $3.82 or $3.30 per cubic meter of lean-EG. These results highlighted the fact that ED represents a prospective technology for saline-EG desalination, thus offering a practical design scheme and empirical support for large-scale industrial applications." @default.
• W3202066327 created "2021-10-11" @default.
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• W3202066327 date "2021-12-01" @default.
• W3202066327 modified "2023-09-26" @default.
• W3202066327 title "Comprehensive bench and pilot-scale study of electrodialysis for ethylene glycol waste fluid desalination during combustible ice mining" @default.
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• W3202066327 doi "https://doi.org/10.1016/j.desal.2021.115369" @default.
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