本實驗將探討運用電透析程序於高濃度硫酸根離子電鍍廠廢水中回收醋酸的可能性。其中將使用並比較三種陰離子膜的性能：常規陰離子交換膜（MA-3475）和一價陰離子交換膜（A-192, ASV）。電解質、電流密度、液體流速和膜對數的影響將被探討。其中，使用更強的電流密度、流速和高的膜對數將會有更好的回收表現，而電解質的影響則非常細小。硫酸根離子的影響非常顯著，因為二價陰離子的硫酸根會較一價的醋酸根透過膜來得更有優先性。一價陰離子交換膜（ASV）可有效的阻擋硫酸根並分離醋酸根和硫酸根。用ASV膜處理后的工廠廢水其COD值將在兩小時內低於800mg/L。

A study was carried out on the feasibility of recovery acetic acid from an electroplating wastewater that contained high concentration of sulfate and acetate by using electrodialysis (ED) process. In this work, synthetic wastewater was used for experiments in which conventional membrane (MA-3475) and monovalent anion selective membranes (A-192, ASV) were used. Effects of electrolyte solution, current density, flow rate and number of cell pair were examined. Higher current density, flow rate, and number of cell pair resulted in better recovery, while electrolyte solution had insignificant effect. Interference of sulfate was significant since divalent ion has higher priority to migrate than monovalent acetate. The monovalent-anion selective membrane (ASV) was effective in blocking sulfate ion and showed high efficiency in separation of acetate and sulfate. The final COD in the diluate in treated wastewater using ASV membrane decreased to below 800 mg/L in 2 hours.

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