在工業廢水中,其中重金屬離子並不一定只呈現單一金屬之污染,總是會含有多種重金屬離子同時存在。本論文研究之目的在於探討利用螯合交換樹脂在何種操作條件下,可將重金屬自廢水中移除,然後再將重金屬從樹脂中脫除,以回收廢水中的重金屬。實驗將螯合交換樹脂加入重金屬廢水中,採批次反應及固定床實驗方式,藉由改變金屬濃度、溫度、脫除劑濃度、流速、床高及pH值加以探討。 由實驗結果得知,螯合樹脂交換Cu2+、Ni2+的能力隨著pH值、溫度與金屬濃度比例的增加而增加;IRC 748螯合樹脂交換Cu2+、Ni2+的反應過程為吸熱反應,可由改變溫度升高時其吸附量增加證明。此外,本研究使用EDTA、HCl、及CA水溶液做為脫除劑,以回收螯合交換樹脂中的Cu2+、Ni2+,並由實驗結果得知,脫除劑的效果以EDTA>HCl>CA。 在固定床交換方面,藉由改變重金屬廢水的流速、濃度、pH值及床高等參數進行實驗。並可由貫穿曲線得知貫穿所需時間隨著流速、濃度、pH值的增加成反比,而與床高成正比;在藉由處理效益對實廠應用做出成本評估。
Many heavy metals exist at the same time in pollution that don’t occur by the single metal in industrial wastewater . The objective of this study that determined the optimal conditions , under which the heavy metals be removed from the wastewater by the chelating resins , and the heavy metals can be removed effectively from the loading chelating resins . Put the chelating resins in wastewater of heavy metals , and changed the concentration of metals and eluent , temperature , velocity , bed height , and pH value by the experiment of batch and fixed-bed . The experimental results showed that the exchange capacities of Cu2+ and Ni2+ increased with increasing the ratio of Cu2+/Ni2+ concentration , temperature and pH value . The process of Cu2+ , Ni2+ exchange by IRC-748 chelating resins was endothermic reaction . That be proofed by exchange capacity increased with increasing temperature . Besides , this study used citric acid , EDTA and HCl solutions as the eluents to recover the Cu2+ and Ni2+ loaded in the chelating resins . EDTA solution was found to the most effectively than HCl than CA for this purpose . Fixed-bed experiments were carried out as a function of velocity , feed concentration , and bed height . The experimental results showed that breakthrough time was inverse ratio with velocity , feed concentration and pH , and was direct ratio with bed height in breakthrough curves . Finally , use the results to evaluate the realistic becefit .