Electrocoagulation advanced treatment system and method for biochemically treating effluent of waste water of diosgenin saponins
A technology for turmeric saponin and advanced treatment, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problem of high operating costs and unstable removal of activated carbon adsorption and membrane methods Organic matter, high cost of chemicals, etc., to achieve stable treatment effect, easy transformation, and low energy consumption
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0037] Such as figure 2 As shown, an electric coagulation advanced treatment system for turmeric saponin wastewater biochemical treatment effluent, including an electric coagulation tank 1, an inclined plate sedimentation tank 2 and a coal sand filter tank 3;
[0038] The electric coagulation tank 1 is provided with a water inlet perforated pipe 4, the water inlet end of the water inlet perforated pipe 4 is connected with the water inlet pump 5, and the water outlet of the electric coagulation tank 1 adopts the first overflow weir 6, and the first overflow weir There is a first scum baffle in front of 6, and the electric coagulation tank 1 is connected to the inclined plate sedimentation tank 2 through the first connecting pipe 7, and one end of the first connecting pipe 7 is connected to the first overflow weir 6 on the water outlet side. A sump 8 is connected, and the other end is connected with the water inlet of the inclined plate sedimentation tank 2. There is a branch p...
Embodiment 2
[0053] The difference between this example and Example 1 is that the flow rate of the turmeric saponin wastewater biochemical treatment effluent in step (1) is 0.73m 3 / h, the pH value is 6.9-7.1, the COD is 223-310mg / L, and the chromaticity is 100 times. The hypochlorite solution described in step (2) is a KClO solution with a mass concentration of 30%. The amount is: add 2 milliliters of the KClO solution to every liter of turmeric saponin wastewater biochemical treatment effluent, run continuously for 8 hours, and carry out dynamic monitoring. The chromaticity is 50 times, and both COD and chromaticity reach the standard stably.
Embodiment 3
[0055] The difference between this example and Example 1 is that the flow rate of the turmeric saponin wastewater biochemical treatment effluent in step (1) is 0.73m 3 / h, pH value is 6.9~7.0, COD is 318~432mg / L, chromaticity is 100 times, and the hypochlorite solution described in step (2) is the Ca(ClO) that mass concentration is 10% 2 Solution, its dosage is: add the described Ca(ClO) of 8 milliliters in every liter of turmeric saponin wastewater biochemical treatment effluent water 2 Solution, continuous operation for 8 hours, dynamic monitoring, system effluent water quality: pH value is 6.9-7.0, COD is 120-240mg / L, chromaticity is 50 times, COD and chromaticity are stable up to the standard.
PUM
| Property | Measurement | Unit |
|---|---|---|
| particle diameter | aaaaa | aaaaa |
| thickness | aaaaa | aaaaa |
| particle diameter | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 