Technology for treating waste water containing ammonia nitrogen
An ammonia nitrogen wastewater and a treatment process technology, which is applied in the field of ammonia nitrogen-containing wastewater treatment technology, can solve problems such as inability to timely and accurately determine, ammonia nitrogen concentration exceeding the standard, low reuse value, etc., and achieves reduced monitoring workload, fewer regeneration times, and convenient desorption. Effect
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Embodiment 1
[0020] Embodiment 1: ion exchange column Φ 40 * 300mm, built-in 001 * 7 (strongly acidic styrene series cation exchange resin) dry resin 275g, the waste water that ammonia nitrogen concentration is 810mg / L enters from the exchange column top with 50mL / min flow rate, when When the feed reaches 14.1L, it is detected that the pH value of the effluent is 7, that is, the feed is stopped, and the remaining liquid is ejected with deionized water, and the total volume of the effluent is 15.6L, of which the volume of the first part of the effluent is 5.2L. After analysis, the concentration of ammonia nitrogen is 10mg / L (in line with the first-class emission standard of 15mg / L), and the discharge meets the standard. The volume of the latter part of the effluent is 10.2L. After analysis, the concentration of ammonia nitrogen is 87mg / L. This effluent enters another exchange column (the same specification is Φ40×300mm, and contains 275g of 001×7 dry resin) at the same flow rate. 10.2L of th...
Embodiment 2
[0022] Embodiment 2: The ion exchange column is the same as Example 1. Firstly, 0.4L of wastewater with an ammonia nitrogen concentration of 31400mg / L was introduced from the top of the exchange column at 30mL / min, and then deionized water was used to push out the remaining liquid, so that the total volume of the effluent was 0.7L, of which the volume of the first part of the effluent was It is 100mL, and the concentration of ammonia nitrogen after analysis is 12mg / L (in line with the first-class discharge standard of 15mg / L), and the discharge meets the standard. The volume of the latter part of the effluent is 600mL, and the ammonia nitrogen concentration is 105mg / L after analysis. The effluent enters another exchange column at the same flow rate (the same specification is Φ40×300mm, and contains 275g of 001×7 dry resin). After the 600mL solution enters , the effluent (600mL) was analyzed for an ammonia nitrogen concentration of 13mg / L. Continue to quantitatively enter 0.4L...
Embodiment 3
[0024] Embodiment 3: with embodiment 1. The difference is that the two exchange columns are connected in series and fed continuously, that is, the wastewater with an ammonia nitrogen concentration of 810mg / L enters from the top of the first exchange column at a flow rate of 50mL / min, and the effluent directly enters the top of the second exchange column and After being adsorbed by the resin, it flows out from the bottom of the column. When the first exchange column was fed to 15L, the feed was stopped, and deionized water was used to push the remaining liquid into the second exchange column. At this moment, the first exchange column is transferred to the desorption (regeneration) operation, and the second exchange column continues to enter the waste water with an ammonia nitrogen concentration of 810mg / L from the top at a flow rate of 40mL / min. The effluent with a volume of 15L in the front part flowing out from the second exchange column, after analysis, the concentration of...
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