Method and device for purifying high-concentration high polymer in organic wastewater
A technology of organic waste water and high polymer, which is applied in chemical instruments and methods, water pollutants, mining waste water treatment, etc., can solve the problems of restricting large-scale use, large amount of oxidant consumption, high cost, etc., to improve power utilization efficiency, remove Good effect, fast processing effect
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Embodiment 1
[0045] Containing 500mg / L polyacrylamide (molecular weight 1600×10 4 ) Oilfield operation waste liquid, enters into the electrochemical oxidation tank, the oxidant is hydrogen peroxide, the dosage is 10mg L -1 ;The mechanical shearer rotates and shears, the rotation speed is 12000rpm, the positive electrode plate of the electrochemical oxidation cell is made of A3 steel sheet, the negative electrode plate is made of flake graphite electrode, the current intensity is 2.0A, and the reaction time is 10min before entering the electrocoagulation cell , where the positive electrode plate (that is, the anode) is made of A3 steel sheet (the iron ions released by the anode are transformed into hydroxides to realize the adsorption and encapsulation of particles), the negative electrode plate is made of flake graphite electrode, and the current intensity is 15A m -2 , The reaction time is 5.0min. The effluent enters the air flotation tank, and its operating conditions are: the air-water...
Embodiment 2
[0047] Contains 1200mg·L -1 Polyacrylamide (molecular weight 1200×10 4 ) Oilfield production fluid enters the electrochemical oxidation tank, the oxidant is ozone, and the dosage is 30mg L -1 The stirring speed of the mechanical shearer is 15000rpm, the positive electrode plate of the electrochemical oxidation cell adopts A3 steel sheet, the negative electrode plate adopts flake graphite electrode, the current intensity is 1.5A, and the reaction time is 20min, then enters the electrocoagulation cell, wherein the positive The electrode plate is made of A3 steel sheet, the negative electrode plate is made of flake graphite, and the current intensity is 10A m -2 , the reaction time is 10min. The effluent enters the air flotation tank, and its operating conditions are: the air-water ratio is 6.5:1. After the effluent is filtered through the filter tank (the filter tank of the prior art), the concentration of polyacrylamide is reduced to 140mg L -1 , the molecular weight is red...
Embodiment 3
[0049] Contains 1500mg·L -1 Polyacrylamide (molecular weight 800×10 4 ) Industrial organic waste water enters the electrochemical oxidation pool, the oxidizing agent is sodium hypochlorite, and the dosage is 20mg L -1 The stirring speed of the mechanical shearer is 12000rpm, the electrochemical oxidation cell anode (positive pole plate) adopts A3 steel sheet, and the cathode (negative pole plate) adopts flake graphite electrode, the current intensity is 1.8A, and the reaction time is 30min after entering the electrode Flocculation tank, in which the anode (positive electrode plate) is made of A3 steel sheet, the cathode (negative electrode plate) is made of flake graphite electrode, and the current intensity is 30A m -2 , The reaction time is 8min. The effluent enters the air flotation tank, and its operating conditions are: the air-water ratio is 6.0:1. After the effluent is filtered by the filter tank, the concentration of polyacrylamide is reduced to 150mg·L -1 , the mo...
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