Continuous treatment method of 1,4-butanediol (BDO) oxidized wastewater
A technology for oxidizing wastewater and treatment methods, applied in 1 field, to achieve the effect of simple process and energy saving
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0019] Example 1: The BDO oxidation wastewater 13 to be treated has a COD value of 21,000 and a dibutyl phthalate content of 0.3% (wt). Waste water 13 is continuously added in the precipitation tank 3 at 8t / hr, and the precipitation agent 11 calcium hydroxide stored in the precipitation agent storage tank 1 is continuously added in the precipitation tank 3 at a speed of 80kg / hr through the feeder 2, and the pH in the precipitation tank 3 is controlled From 8 to 12, a small amount of compressed air 12 is continuously introduced for stirring. The resulting precipitated liquid 14 continuously enters the clarification tank 4 for solid-liquid separation, and the clear liquid 15 enters the subsequent homogeneous tank 5, and the treated wastewater is added to adjust the COD value of the incoming water to about 1200, and the adjusted water enters the Anaerobic treatment is carried out in the anaerobic oxidation reactor 6, and the water after the anaerobic treatment enters the aerobic ...
Embodiment 2
[0020] Example 2: roughly the same as Example 1, the difference is: the COD value of the BDO oxidation wastewater to be treated is 24000, the content of dibutyl phthalate is 0.8% (wt), and the precipitant 11 calcium oxide is passed through the feeder 2 It is continuously added to the sedimentation tank 3 at a rate of 120kg / hr. The amount of the precipitant 11 is added so that the pH value of the wastewater 13 is controlled within the range of 9-13, and mechanical stirring is adopted at the same time. The resulting precipitated liquid 14 continuously enters the clarification tank 4 for solid-liquid separation, and the clear liquid 15 enters the subsequent homogeneous tank 5, and adds the treated and discharged wastewater to adjust the COD value of the incoming water to about 800, and the adjusted water enters the Anaerobic treatment is performed in the anaerobic oxidation reactor 6, and the water after the anaerobic treatment enters the aerobic treatment unit 7 for aerobic treat...
Embodiment 3
[0021] Embodiment 3: roughly the same as Example 1, the difference is: the clear liquid 15 that precipitant 11 calcium hydroxide separates solid-liquid with clarifier 4 is mixed with the slurry that mass fraction is 20%, with 600kg / hr speed Continuously added to the sedimentation tank 3. Finally, the COD of the wastewater reaching the discharge standard is 40, and the content of dibutyl phthalate is 0.11ppm.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 