Device and method for coupling efficient biological treatment and sludge reduction of trademark fabric production wastewater
A technology for production wastewater and biological treatment, which is applied in the field of environmental protection and can solve the problems of large dosage of chemicals, difficulty in meeting discharge standards, and low treatment efficiency.
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Embodiment 1
[0031] A method for high-efficiency biological treatment of wastewater from trademark fabric production coupled with sludge reduction, comprising the following steps:
[0032] (1) A trademark cloth production enterprise produces 450 t / d of finishing waste water during the production process, with a COD of about 4000 mg / L and a pH of 12, and produces 400 t / d of coating waste water with a COD of about 2700 mg / L , pH 6.8, total antimony concentration 2 mg / L. Such as figure 1 As shown, the finishing wastewater and coating wastewater are fully mixed in the neutralization tank. The COD of the effluent from the neutralization tank is about 3388 mg / L, and the pH is 10.5. Waste water is discharged into the regulating tank, and FeCl is added to the influent water of the regulating tank every day2 800 kg, or 0.94 kg FeCl 2 / t waste water, the pH of the waste water drops to 9.2. The effective pool volumes of the neutralization pool, regulating pool, and aerobic pool are respectively 8...
Embodiment 2
[0038] A method for high-efficiency biological treatment of wastewater from trademark fabric production coupled with sludge reduction, comprising the following steps:
[0039] A trademark fabric manufacturer discharges 350 tons of coating wastewater and 300 tons of finishing wastewater every day. Such as figure 1 As shown, the COD concentration of the two types of wastewater mixed in the neutralization tank is 4300 mg / L, the pH is 11, and FeCl is added to the water in the adjustment tank 2 650t / d, that is, the dosage is 1.0 kg FeCl 2 / t waste water, the pH of the waste water drops to 9.0. The hydraulic retention times of the neutralization tank, regulating tank and facultative tank are 20 h, 30 h and 40 h, respectively. The pH of the wastewater at the outlet of the adjustment tank is 8.0. 45% of the sludge in the first-stage sedimentation tank is returned to the adjustment tank, 20% is returned to the facultative tank, and 35% is discharged to the sludge thickening tank. ...
Embodiment 3
[0041] use as figure 1 The processing device for biological treatment, the method of high-efficiency biological treatment of waste water from trademark fabric production coupled with sludge reduction, which includes the following steps: Step 1): the finishing waste water and the coating waste water are reacted in the neutralization tank, the adjustment tank and the facultative tank, Then enter the first-level sedimentation tank for sedimentation, and add an appropriate amount of FeCl to the water in the adjustment tank 2 ; Step 2): Part of the sludge in the first-stage sedimentation tank is returned to the regulating tank, part of it is returned to the facultative tank, and a small part is discharged into the sludge thickening tank, and the sludge is dehydrated and then transported for disposal; Step 3): the The effluent from the first-level sedimentation tank is discharged into the aerobic tank. The aerobic tank adopts the operation mode of combining aeration and static sedim...
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