Treatment method for ammonia nitrogen and COD (Chemical Oxygen Demand) in surface treatment waste water
A treatment method and surface treatment technology, which is applied in the field of surface treatment wastewater with low concentration of ammonia nitrogen and COD, can solve the problems that hinder the popularization and application of biochemical methods, complex operation, frequent replacement of activated carbon, etc.
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Embodiment 1
[0056] Select the electroplating wastewater from an electroplating factory after chemical precipitation treatment, and firstly use the method of iron-carbon to treat the wastewater. Iron shavings are used as raw materials for iron-carbon reaction. The mixture was reacted for 1 hour, and then the pH was adjusted to 10 for coagulation and precipitation. The raw water quality and the results after iron-carbon treatment are shown in Table 2.
[0057] Table 2. Water quality indicators of an electroplating wastewater
[0058]
[0059]
[0060] In Table 2, BOD is biochemical oxygen demand, and B / C is the ratio of BOD and COD. It can be seen from the data in the above table that the iron-carbon micro-electrolysis reaction can reduce the concentration of metal ions and increase the B / C ratio.
Embodiment 2
[0062] The chemically treated wastewater from an electroplating enterprise basically does not contain metal ions, and directly enters the hydrolytic acidification tank. The residence time in the hydrolysis acidification tank is 5-6 hours, and the residence time in the MBR reactor is 4 hours. The treated wastewater can be discharged directly. , the treatment effect is shown in Table 3, COD and ammonia nitrogen can be removed well at the same time.
[0063] Table 3. Wastewater treatment effect of an electroplating enterprise
[0064]
[0065] It can be seen from the data in the above table that the residence time of wastewater in the hydrolysis tank is 5-6h, and the residence time in the MBR reactor is 4h, and the COD of the effluent can be reduced to 20mg·L -1 , Ammonia nitrogen can be removed simultaneously with COD at a ratio of 1:15.
Embodiment 3
[0067] The B / C of most electroplating wastewater is lower than 0.3, and the total nitrogen content of some electroplating wastewater is high. The way of adding domestic sewage from enterprises can be used as an auxiliary carbon source to appropriately increase the B / C ratio and COD load. The biodegradability of domestic sewage is high, which can improve the biodegradability of mixed sewage, increase the sludge load, improve sludge activity, and obtain better treatment effects. At the same time, it provides sufficient carbon sources for the decomposition of ammonia nitrogen and improves ammonia nitrogen treatment. Efficiency, and finally achieve the standard discharge of COD and ammonia nitrogen in the electroplating wastewater.
[0068] The wastewater after chemical precipitation treatment of an electroplating enterprise is treated with iron carbon + hydrolytic acidification + MBR, so that various indicators of raw water can meet the discharge standards, as shown in Table 4. T...
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