Treatment method for wastewater containing small-molecular organic matter
A treatment method and small molecule technology, applied in water/sewage treatment, oxidized water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of difficult treatment, low efficiency of organic amine treatment, multiple treatment processes, etc. Achieving a good treatment effect
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Embodiment 1
[0047] Pyridine wastewater quality: COD=65615mg / L, TOC (total organic carbon)=25380mg / L, NH 3 -N=5381 mg / L, TN (total nitrogen)=10500 mg / L, pH=11.7.
[0048] (1) Catalytic wet oxidation: adjust the pH of pyridine wastewater to 5.6, transfer it to a titanium reactor, increase the reaction pressure from 1.1MPa (normal temperature) to 6MPa (260°C), feed air, the reaction pressure is 6MPa, and maintain the reaction temperature 260°C, based on the quality of pyridine wastewater, add a homogeneous catalyst CuSO with a mass fraction of 1% 4 , using a batch reactor to react in stages, each stage reacted for 1.5h, and the total reaction was 3h.
[0049] After catalytic wet oxidation treatment, the water quality of the wastewater discharged from the kettle: COD=2784mg / L, TOC=1120mg / L, NH 3 -N=8100 mg / L, TN=9200 mg / L, pH=6.5.
[0050] (2) Deamination membrane: Catalytic wet oxidation effluent is added with liquid caustic soda to adjust the pH to 12.2, cooled to 40°C, flow rate is 0.19...
Embodiment 2
[0053] Two kinds of pyridine ring wastewater, the water quality is as follows:
[0054] Wastewater 1: COD=77510mg / L, TOC=176900mg / L, TN=38500mg / L.
[0055] Wastewater 2: COD=33110mg / L, TOC=14600mg / L, TN=10150mg / L.
[0056] (1) Alkali analysis: add liquid caustic soda in waste water 1 and adjust the pH of waste water to 12.8, stratification occurs after standing for a few minutes, the upper layer is the oil phase, the lower layer is the water phase, the oil phase volume accounts for 25% of the total volume, and the water phase The phase volume accounts for 75% of the total volume.
[0057] After liquid separation, the purity of triethylamine in the oil phase was determined by spectrophotometry, and the water quality of the water phase: COD=40480mg / L, TOC=21680mg / L, TN=13100mg / L.
[0058] Before catalytic wet oxidation, the oil phase is removed, which reduces the risk of high temperature and high pressure explosion in wet oxidation when the concentration of organic amine is hi...
Embodiment 3
[0065] The step (1) of embodiment 2 is followed by the membrane distillation step. The water phase in step (1) was heated to 40°C, the flow rate was 0.16m / s, and the organic amine was recovered by air cooling. The COD=36790mg / L, TOC=18160mg / L, TN=10020mg / L of the treatment liquid were measured in 1h.
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