Abstract
As production of LCD increases, it has become necessary to find an economically efficient way of treating LCD wastewater with high concentration of fluoride. This study focuses on the calcium sources : $CaCl_2$, $Ca(OH)_2$ and $CaCO_3$ for the treatment of the LCD wastewater including high concentration of fluoride. Of course considering removal efficiency and economical aspect, study is continued. Then this study have objective giving aid to field. Consequently, each calcium source's removal efficiency was measured in various pH, calcium dosage, reaction time, and mixing intensity. The optimum operational conditions for $CaCl_2$ were found to be pH of 7, calcium dosage of 0.4[Ca]/[F] (mol / mol), 1 hr of operation and 200 rpm of mixing intensity. For $Ca(OH)_2$, they were pH of 7, calcium dosage of 30 mL/L, 1 hr of operation, and 200 rpm of mixing intensity. While $CaCO_3$ had operational conditions of pH of 4, calcium dosage of 30 mL/L, 1 hr operation and 200 rpm of mixing intensity. But it is recommended to use calcium sources according to various field conditions.
본 연구는 고농도의 불소가 함유된 LCD 폐수를 처리하는데 있어, 칼슘원에 따른 제거 효율과 경제성에 부합되는 조건을 도출하여 실제 현장에 적용하는데 목적이 있다. 이를 위하여 칼슘원으로 $CaCl_2$, $Ca(OH)_2$ 및 $CaCO_3$를 이용하여 각각 pH, 칼슘주입량, 반응시간 및 교반속도의 변화에 따른 특성을 관찰하였다. 그 결과 $CaCl_2$의 경우 pH 7, 칼슘주입량 0.4[Ca]/[F] (mol / mol), 1시간, 200 rpm으로 결정되었고, $Ca(OH)_2$의 경우 pH 7, 칼슘주입량 30 mL/L, 1시간, 200 rpm으로 결정하였으며, $CaCO_3$의 경우 pH 4, 칼슘주입량 30 mL/L, 1시간, 200 rpm으로 적용하는 것이 최적조건이라고 판단되었다. 그러나 현장의 상황에 따라 적용 조건의 변경이 가능하다.