Glyphosate-producing wastewater treatment integration technology
A technology for glyphosate wastewater and production wastewater, applied in natural water treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve problems such as limited oxidation degree, waste of resources, incompleteness, etc., and achieve Blends quickly and evenly
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Embodiment 1
[0040] Implementation example 1: get glyphosate waste water (COD cr =12020mg / L, pH=2-3, TP=96mg / L, formaldehyde=5362mg / L) 1L, directly into the micro-electrolysis filler, aeration reaction for 2h, after adjusting the pH to 3-4, adding 2mL of hydrogen peroxide reagent, exposure Gas reaction for 2 hours, adjust the pH to about 9 with milk of lime, and effluent COD after flocculation and precipitation cr 49.17% reduction, formaldehyde reduction 82.56%. After the effluent enters the anaerobic reaction tank and stays for 48 hours, it enters the specific contact oxidation tank and aeration tank for treatment. After the effluent is tested, the COD cr It is 89.6mg / L.
Embodiment 2
[0041] Implementation example 2: A glyphosate production enterprise in Sichuan discharges wastewater (COD cr =10000-13000mg / L, pH=2-3, TP3 / d, the design flow rate is about 5m 3 / h. The waste water is lifted to the micro-electrolysis tower through the regulating tank, and the residence time is about 2 hours. The effluent is added with acid to adjust the pH to 3-4, and hydrogen peroxide is added, and enters the Fenton reactor for reaction. The residence time is about 2 hours. Aluminum), PAM (polyacrylamide), adjusted to pH = 8-9, enters the sedimentation tank, after sedimentation, it is lifted to the UASB reactor by the pump, and the residence time is 48h. After that, it enters the fourth-stage contact oxidation tank for treatment, and then enters the aeration tank. Add PAC (polyaluminum chloride) phosphorus removal agent. The average dosing amount per ton of wastewater in the whole process is about 16kg of liquid PAC (polyaluminum chloride), 10kg of lime, 2kg of PAM (polyacr...
Embodiment 3
[0042] Implementation example 3: A chemical company in Sichuan discharges glyphosate production wastewater (COD cr =5000-16281mg / L, pH=2-4, TP3 / d, take 1L of water sample, directly enter the micro-electrolysis filler, aerate for 2 hours, then adjust the pH to 3-4, add 2mL hydrogen peroxide reagent, aerate for 2 hours, adjust the pH to about 9 with lime milk, flocculate and settle COD cr 47.45% reduction, formaldehyde reduction 84.67%, chloride ion reduction 36.43%. After the effluent enters the anaerobic reaction tank and stays for 48 hours, it enters a specific aerobic reactor (four-stage contact oxidation tank and one-stage aeration tank) for reaction, and the effluent is tested, and the COD cr It is 75.32mg / L.
[0043] Since the control conditions involved in the present invention are relatively high, especially for the aerobic biochemical system, the technical quality of the users is high, and automatic programming assistance is required.
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