Method for removing haloacetic acids from water
A haloacetic acid, water removal technology, applied in chemical instruments and methods, water pollutants, water/sewage multi-stage treatment, etc., can solve problems such as human health threats, carcinogenicity, teratogenicity and mutagenicity, and achieve investment Low cost and operating cost, short hydraulic retention time, small temperature effect
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Embodiment 1
[0050] The average concentration of trichloroacetic acid in the raw water tank is about 185 μg / L; the EBCT of Fe-column and BAC-column is 2.5 minutes; the reaction temperature is 19°C. The average removal effect of nine samples of haloacetic acid under this condition is as follows image 3 .
[0051] image 3 It shows that TCAA in the raw water bucket becomes DCAA and MCAA after passing through the Fe-column, and the concentration of DCAA and MCAA decreases after passing through the BAC-column. Biodegradation occurs in the column. It shows that this method can effectively reduce the concentration of haloacetic acid in water.
Embodiment 2
[0053] The average concentration of trichloroacetic acid in the raw water tank is about 175 μg / L; the EBCT of Fe-column and BAC-column is 4 minutes; the reaction temperature is 15°C. The average removal effect of nine samples of haloacetic acid under this condition is as follows Figure 5 shown.
[0054] Figure 4 It shows that when the EBCT is 4 minutes, most of the TCAA in the raw water bucket is transformed into DCAA and MCAA after passing through the Fe-column. EBCT is beneficial to improve the dehalogenation efficiency of Fe-column to polyhaloacetic acid and the biodegradation effect of BAC-column to low-haloacetic acid, indicating that this method can efficiently treat haloacetic acid in water.
Embodiment 3
[0056] The average concentration of trichloroacetic acid in the raw water tank is about 165 μg / L; the EBCT of Fe-column and BAC-column is 10 minutes; the reaction temperature is 25°C.
[0057] Figure 5 It shows that TCAA in the raw water bucket is almost completely transformed into DCAA and MCAA after passing through the Fe-column, and no haloacetic acid is detected in the effluent after passing through the BAC-column. It can be seen that polyhaloacetic acid is almost completely dehalogenated into less haloacetic acid in the Fe-column , less haloacetic acids are fully biodegraded in the BAC-column. It shows that the method of the present invention can completely and rapidly remove haloacetic acid in water.
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