Method for treating waste water of antibiotic production
A technology for the production of waste water and treatment methods, applied in biological water/sewage treatment, multi-stage water treatment, water/sewage treatment, etc., can solve the problems of high operating cost, blockage, pollution, etc., and achieve low treatment cost, simple process, The effect of high processing efficiency
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Embodiment 1
[0041] An antibiotic factory produces mixed wastewater produced by lincomycin, rifamycin, etc. The wastewater quality is: COD (Cr method, the same below) 15000mg / L, salt content 1.2wt%, suspended solids 5000mg / L, ammonia nitrogen 200mg / L, pH 7.5.
[0042] The waste water is treated by the method of the present invention. First, air is dissolved in water at 0.35MPa, and then the dissolved air is sent to the air flotation tank. The formed microbubbles bring some pollutants to the water surface and are removed. The concentration of suspended solids in the effluent Reduced to below 1500mg / L. The flotation water enters the ozone reactor. The ozone oxidant is provided by the ozone generator. The dosage of the ozone oxidant is 40mg / L wastewater, the ozone oxidant gas inlet concentration is 100mg / L, and the hydraulic retention time of the wastewater in the reactor is 30min. Ozone oxidation effluent BOD 5 / COD≥0.6. The oxidized effluent is coagulated and precipitated, the dosage of pol...
Embodiment 2
[0044] A certain antibiotic factory produces mixed wastewater produced by nalidixic acid. The wastewater quality is: COD (Cr method, the same below): 12000mg / L, salt content 1.5wt%, suspended solids 10000mg / L, ammonia nitrogen 200mg / L, pH 7.5 .
[0045] The waste water is treated by the method of the present invention. First, air is dissolved in water at 0.35MPa, and then the dissolved air is sent to the air flotation tank. The formed microbubbles bring some pollutants to the water surface and are removed. The concentration of suspended solids in the effluent Reduced to below 2000mg / L. The flotation water enters the ozone reactor. The ozone oxidant is provided by the ozone generator. The dosage of the ozone oxidant is 35mg / L wastewater, the ozone oxidant gas inlet concentration is 100mg / L, and the hydraulic retention time of the wastewater in the reactor is 30min. Ozone oxidation effluent BOD 5 / COD≥0.4. The oxidized effluent is coagulated and precipitated. The dosage of polyac...
Embodiment 3
[0047] An antibiotic factory produces mixed wastewater produced by lincomycin, rifamycin, etc. The wastewater quality is: COD (Cr method, the same below) 15000mg / L, salt content 1.2wt%, suspended solids 5000mg / L, ammonia nitrogen 200mg / L, pH 7.5.
[0048] The waste water is treated by the method of the present invention. First, air is dissolved in water at 0.35MPa, and then the dissolved air is sent to the air flotation tank. The formed microbubbles bring some pollutants to the water surface and are removed. The concentration of suspended solids in the effluent Reduced to below 1500mg / L. The flotation water enters the ozone reactor. The ozone oxidant is provided by the ozone generator. The dosage of the ozone oxidant is 40mg / L wastewater, the ozone oxidant gas inlet concentration is 100mg / L, and the hydraulic retention time of the wastewater in the reactor is 30min. Ozone oxidation effluent BOD 5 / COD≥0.4. The oxidized effluent is coagulated and precipitated, the dosage of pol...
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