Advanced treatment process of biochemical tail water of percolate of city consumption residue
A technology for advanced treatment of municipal solid waste, which is applied in the field of biochemical treatment of tail water of municipal solid waste leachate, which can solve the problems of high treatment cost, high investment and operation cost of nanofiltration, and large energy consumption.
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Embodiment 1
[0018] The biochemical treatment process of landfill leachate is an external membrane bioreactor, and the tail water is discharged from it, COD Cr The concentration of ammonia nitrogen is 515mg / L, the concentration of ammonia nitrogen is 60mg / L, and the concentration of total nitrogen is 150mg / L. Add a small amount of Ca(OH) to the leachate raw water 2 Adjust the pH to about 10 to produce flocs. After stirring for half an hour to fully mix, take the supernatant and add acid to adjust the pH to 4.5. COD at this time Cr The concentration of ammonia nitrogen is 162mg / L, the concentration of ammonia nitrogen is 30mg / L, and the concentration of total nitrogen is 75mg / L.
[0019] Put 20ml of composite functional adsorption resin NDA-66 into a jacketed glass adsorption column (Φ20×350mm). At room temperature (20-25°C), the pretreated biochemical tail water is passed through the resin bed at a flow rate of 40mL / h, and the wastewater treatment capacity is 2000mL / batch. Adsorbed wate...
Embodiment 2
[0022] Other operating conditions are the same as in Example 1. The landfill leachate biochemical treatment process is membrane bioreactor + nanofiltration membrane interception, and the tail water is nanofiltration discharge water, COD Cr The concentration of ammonia nitrogen is 156mg / L, the concentration of ammonia nitrogen is 34.3mg / L, and the concentration of total nitrogen is 96.2mg / L. The pH is adjusted to 4.0 with acid.
[0023] Put 20ml of composite functional adsorption resin NDA-66 into a jacketed glass adsorption column (Φ20×350mm). At room temperature (20-25°C), the pretreated biochemical tail water is passed through the resin bed at a flow rate of 40mL / h, and the wastewater treatment capacity is 2000mL / batch. Adsorbed water COD Cr The nitrogen concentration is 72mg / L, the ammonia nitrogen is 2.44mg / L, and the total nitrogen concentration is 10.06mg / L. Whole process COD Cr The removal rate of ammonia nitrogen is 53.8%, the removal rate of ammonia nitrogen is 92....
Embodiment 3
[0026] Other operating conditions are the same as in Example 1. The landfill leachate biochemical treatment process is pretreatment-UASB-combined aerobic biological treatment, and the tail water is discharged from aerobic biological treatment. COD Cr The concentration of ammonia nitrogen is 486mg / L, the concentration of ammonia nitrogen is 28.6mg / L, and the concentration of total nitrogen is 75.4mg / L. The pH is adjusted to 4.5 with acid.
[0027] Put 20ml of composite functional adsorption resin NDA-66 into a jacketed glass adsorption column (Φ20×350mm). At room temperature (20-25°C), the pretreated biochemical tail water is passed through the resin bed at a flow rate of 40mL / h, and the wastewater treatment capacity is 1000mL / batch. Adsorbed water CODCr The concentration of ammonia nitrogen is 92mg / L, the concentration of ammonia nitrogen is 1.52mg / L, and the concentration of total nitrogen is 17.28mg / L. Whole process COD Cr The removal rate of ammonia nitrogen is 81.1%, the...
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