Combination method of coal chemical industry wastewater treatment
A technology of coal chemical wastewater and water holding capacity, applied in chemical instruments and methods, multi-stage water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problem of low biochemical degradation efficiency, poor effluent quality, and low treatment efficiency problems, to achieve the effects of fast biochemical degradation, reduced biochemical treatment load, and high treatment efficiency
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specific Embodiment approach 1
[0022] Specific embodiment one: a kind of combined method of coal chemical industry wastewater treatment in this embodiment is carried out according to the following steps:
[0023] 1. The coal chemical industry wastewater is first degreased through the grease trap, and the hydraulic retention time is 20~30min; among them, the grease trap adopts a sloping plate type grease trap, and the sloping plate material is made of polyester fiberglass;
[0024] 3. The coal chemical wastewater treated by the grease trap is passed into the hydrolysis acidification tower, the hydraulic retention time is controlled at 1.5~3h, the pH value is controlled at 5.0~6.5, and the water temperature is controlled at 25~35°C; among them, the hydrolysis acidification tower is made of steel system structure;
[0025] 3. The coal chemical wastewater treated by the hydrolysis and acidification tower is passed into the anaerobic fluidized bed, the temperature is controlled at 20-35°C, and the carrier in the...
specific Embodiment approach 2
[0035] Specific embodiment two: the difference between this embodiment and specific embodiment one is: the microbial load in the anaerobic fluidized bed described in step 3 is 18g / L~28g / L, and the carrier loading is 11%~by volume percentage 14%. Other steps and parameters are the same as in the first embodiment.
specific Embodiment approach 3
[0036] Embodiment 3: This embodiment differs from Embodiment 1 in that: the microbial load in the anaerobic fluidized bed described in step 3 is 23 g / L, and the loading amount of the carrier is 13% by volume. Other steps and parameters are the same as in the first embodiment.
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