Treatment method of polyacrylonitrile fiber production sewage
A polyacrylonitrile fiber, sewage production technology, applied in the direction of water/sewage multi-stage treatment, water/sludge/sewage treatment, flocculation/sedimentation water/sewage treatment, etc., can solve the problem of large flocculants, etc.
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Embodiment 1
[0027] This example is used to illustrate the treatment method of the polyacrylonitrile fiber production sewage of the present invention.
[0028] The waste water (containing 0.009% by mass of polyacrylonitrile) produced in the polymerization process in the production process of polyacrylonitrile fibers is passed into the reaction tank, the pH of the material in the reaction tank is adjusted to 9, the temperature is controlled at 170 ° C, and the pressure The control is 1MPa, and the reaction is kept at this temperature and pressure for about 3h. Then, the waste water (COD is 781mg / L, BOD is 781mg / L, BOD 5 280mg / L, NH 3 -N is 60 mg / L) were mixed at a mass ratio of 1:1, and after uniform mixing, the resulting mixture was allowed to stand for 1 h. Afterwards, the supernatant obtained after standing still was subjected to biochemical treatment by activated sludge method. The specific operating conditions included: temperature 35°C, sludge age 3 days, sludge load 0.3kg BOD 5 / (...
Embodiment 2
[0036] This example is used to illustrate the treatment method of the polyacrylonitrile fiber production sewage of the present invention.
[0037] The waste water (containing 0.001% by mass of polyacrylonitrile) produced in the polymerization process in the production process of polyacrylonitrile fibers is passed into the reaction tank, the pH of the material in the reaction tank is adjusted to 8, the temperature is controlled at 200 ° C, and the pressure The control is 2MPa, and the reaction is kept at this temperature and pressure for about 5h. Then, the waste water (COD is 1030mg / L, BOD is 1030mg / L, BOD 5 370mg / L, NH 3 -N is 50mg / L) mixed with a mass ratio of 1:2, and 0.05 mass parts of polyaluminum chloride (purchased from Gongyi City Fuyuan Water Purification Materials Co., Ltd.), after uniform mixing, the resulting mixture was left to stand for 0.5 h. After that, the supernatant liquid obtained after standing still is subjected to biochemical treatment by biological c...
Embodiment 3
[0042] This example is used to illustrate the treatment method of the polyacrylonitrile fiber production sewage of the present invention.
[0043] The waste water (containing 0.002% by mass of polyacrylonitrile) produced in the polymerization process in the production process of polyacrylonitrile fibers is passed into the reaction tank, the pH of the material in the reaction tank is adjusted to 10, the temperature is controlled at 190 ° C, and the pressure The control is 0.5MPa, and the reaction is kept at this temperature and pressure for about 8h. Then, the reaction product in the reaction tank is mixed with the waste water (COD is 568mg / L, BOD is 568mg / L, BOD 5 150mg / L, NH 3 -N is 34mg / L) mixed with a mass ratio of 1:5, and added 0.03 mass parts of polyaluminum sulfate (purchased from Gongyi Shengshi Water Purification Material Co., Ltd. company), after uniform mixing, the resulting mixture was left to stand for 2h. Then adopt the anaerobic biological filter method to ca...
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