本研究以化學混凝程序,利用鐵作為混凝劑,去除煙氣脫硫廢水中 的硼。處理了來自於火力發電廠的廢水,並分析了會影響煙氣脫硫廢水 中硼的去除效率的因素。 使用三氯化鐵作為混凝劑的處理結果顯示,最適合的pH環境是8,且混凝劑對硼的摩爾比越大,硼的去除效率越高。初始廢水中硼的濃度越大,硼的去除效率越高。通過硼去除效率和廢水初始硼濃度之間的模型曲線將實驗數據整理,設計三階段處理程序以針對較高濃度硼的去除。結果顯示,即使處理初始硼濃度為1600mg/L 的煙氣脫硫廢水,也能達到80%以上的去除效率。在本系統中,鈣離子和鎂離子也獲得了與硼相似的去除效率趨勢。鈣離子和鎂離子分別在其初始廢水濃度為750mg/L和5000mg/L的三階段處理程序中,達到78%和60%以上的去除效率。在本研究程序中使用氫氧化鈣作為pH調節試劑,在不降低硼的去除效率的同時可以使得污泥更易沈降。
In this study, a chemical coagulation (CC) process was used to remove boron (B) from flue gas desulfurization (FGD) wastewater using Fe(III) as a coagulant. In the treatment of FGD wastewater from coal-fired power plants, the factors affecting the boron treatment process in the FGD wastewater were analyzed. The experimental results show that the most suitable pH environment is 8 when using ferric chloride (FeCl3) as coagulant, and the higher the molar ratio of Fe(III) to B, the higher the removal efficiency of B. The higher the initial concentration of B in the wastewater, the higher the removal efficiency of B. The experimental data were compiled and fitted with a model to correlate B removal efficiency and initial B concentration in wastewater for various Fe(III)/B molar ratios, and a three-stage treatment process was proposed to target the removal of higher concentrations of B. The results show that the removal efficiency of more than 80% can be achieved even with the FGD wastewater with an initial B concentration of 1600 mg/L. The removal efficiencies of calcium (Ca2+) and magnesium (Mg2+) were over 78% and 60% in the three-stage treatment process with their initial Ca2+ and Mg2+ wastewater concentrations of 750 mg/L and 5000 mg/L, respectively. The use of calcium hydroxide (Ca(OH)2) as a pH adjustment reagent in the coagulation process can make the sludge easier to settle without reducing the B removal efficiency.