Process for treating high-concentration organic wastewater in tobacco sheet industry
A technology for organic wastewater and tobacco flakes, applied in multi-stage water treatment, water/sewage treatment, water/sewage multi-stage treatment, etc., can solve the problems of high operating costs, wastewater failing to meet the first-level discharge standard, and high chromaticity of effluent. , to reduce operating costs, improve biochemical capacity, and reduce load
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Embodiment 1
[0024] A domestic coastal tobacco flake company produces 5,000 tons of tobacco flakes annually, and produces 60m of high-concentration organic wastewater per day 3 , Take 2 m3 of high-concentration organic wastewater every day. After testing, the range of COD is 120,000~180,000mg / l, the range of PH value is 5~6, and the chromaticity is more than 2000 times. Using the processing method of the present invention:
[0025] Step 1. The high-concentration organic wastewater enters the coagulation tank through the collection device, and the coagulant and flocculant are added to the coagulation tank for coagulation treatment. The coagulant is polyaluminum chloride and the flocculant is cationic polyacrylamide. , The sludge produced by the reaction is discharged into the sludge treatment system;
[0026] Step 2. The supernatant in step 1 enters the electrocoagulation reaction cell, and the current density is controlled to 40 mA / cm 2 , Reaction for 10 minutes, the sludge produced by the reac...
Embodiment 2
[0030] In the laboratory, the production process of the tobacco flake factory is simulated, and 0.5m3 of high-concentration wastewater is prepared every day, the COD varies from 70,000 to 80,000 mg / l, the PH value is from 5 to 6, and the color is greater than 2000 times. Using the treatment method of the present invention: the high-concentration organic wastewater enters the coagulation tank through the collection device, and the coagulant and flocculant are added to the coagulation tank for coagulation treatment. The coagulant adopts polyferric sulfate and the flocculant adopts cation Polyacrylamide, the supernatant enters the electrocoagulation reaction cell, and the current density is controlled to 20 mA / cm 2 , The reaction is 8min, other processes are the same as in Example 1.
[0031] Tested: COD removal rate is 88~91%, chroma is less than 30 times.
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