Method for treating middle section water of alkaline straw pulp
A treatment method and water treatment technology, applied in the direction of processing wastewater treatment, oxidized water/sewage treatment, water/sewage multi-stage treatment, etc., can solve the problems of deep color and failure to achieve, and achieve mature process routes and large buffer space , the treatment effect is remarkable
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example 1
[0026]Example 1: A large paper industry group has three straw pulp production lines of 50,000 tons per year, using wheat straw as the main raw material, using AQ-NaOH pulping process, and the water production in the middle section is 50,000 cubic meters per day. The water quality is as follows: PH: 85-9.0, COD: 3500-4000mg / L, SS: 2500-3000mg / L, the color is brown. The enterprise invested 70 million yuan to treat the middle water with the process of the present invention. The specific process is as follows: the middle water from the pulping workshop first enters the pre-sedimentation treatment system, and the effluent SS is reduced to 800-1000mg / L, and the COD is reduced to 2800-3000mg / L ; The supernatant enters the hydrolysis acidification system, the net residence time is 24 hours, the pH value is reduced to 6.5-7.0, and it is subjected to physical and chemical treatment. When the input amount of PAFC is 0.02%-0.03%, and the amount of anion PAM is 0.00005 %, the COD of the su...
example 3
[0027] Example 3: An alkaline pulping and papermaking enterprise uses rice straw as the raw material for pulping. The annual pulping scale is 50,000 tons, and the middle section of water is 20,000 cubic meters per day. The water quality is: COD: 3800-4200mg / L, SS: 3500-3700mg / L, PH: 9.0-9.5, dark gray in color. The method of the present invention is used in the middle stage water treatment of this paper mill, and its trial operation is as follows: the middle stage water from the pulping workshop first enters the pre-sedimentation treatment system, and after sedimentation and separation, the COD of the effluent is reduced to 3200-3500mg / L, SS Reduce to 1200-1500mg / L; the supernatant enters the hydrolysis acidification system, and enters the physical and chemical treatment system after the net residence time reaches 30 hours. When the addition of PAFC and anion PAM is controlled at 0.03% and 0.00015% respectively, the supernatant COD reaches 1500-1700mg / L, SS drops to 300-400mg / ...
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