Ammonia nitrogen removal and ammonium salt enrichment method for high-concentration ammonia-nitrogen wastewater through membrane method
A high-concentration technology for ammonia nitrogen wastewater, applied in chemical instruments and methods, water pollutants, water/sewage treatment, etc., can solve the problems of lower concentration of absorption liquid, lower absorption capacity, complex process, etc., to save energy and avoid fog The effects of foam entrainment and simple process flow
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Embodiment 1
[0036] After a certain zeolite absorbs ammonia nitrogen, the ammonia nitrogen concentration of the regenerated liquid with high concentration of ammonia nitrogen is 1580mg / L. The pH value is adjusted to 10.5 with 0.2moL / L NaOH solution, and it is filtered through a 4μm filter as the raw material liquid. Add 5% NaCl electrolyte to the raw material solution, and then enter the polytetrafluoroethylene hollow fiber hydrophobic membrane module for deamination. The porosity of the membrane module is 65%, the outer diameter of the membrane filament is 1.2mm, the inner diameter is 0.8mm, the pore diameter is 0.2μm, the packing density is 45%, and the effective length of the membrane module is 100mm. Using 30% (W / W, ie mass concentration) dilute sulfuric acid as the absorbent, the flow rate of the absorbent circulation pump is controlled to 10L / h, the flow rate of the membrane absorption circulation pump is controlled to 10L / h, and the cycle absorption deamination time is 3h. The tempe...
Embodiment 2
[0038] A high-concentration ammonia-nitrogen industrial wastewater, with an ammonia-nitrogen concentration of 2170mg / L, was filtered and used as wastewater raw material. Adjust the pH value to 11 with 1moL / L NaOH solution, and then enter the polytetrafluoroethylene hollow fiber hydrophobic membrane module for deamination. The porosity of the membrane module is 60%, the outer diameter of the membrane filament is 1.0mm, the inner diameter is 0.6mm, the pore diameter is 0.4μm, the packing density is 50%, and the effective length of the membrane module is 250mm. 20% dilute nitric acid is used as the absorbent, the flow rate of the absorbent circulation pump is controlled at 20L / h, the flow rate of the membrane absorption circulation pump is controlled at 20L / h, and the cycle absorption deamination time is 4h. The temperature difference between the two sides of the membrane is controlled to be 20°C, the ammonia nitrogen value of the wastewater is reduced from 2170mg / L to 52.80mg / L,...
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