Livestock and poultry breeding wastewater CC-HBDP treatment process
A technology of livestock and poultry breeding wastewater and treatment process, which is applied in the fields of animal husbandry wastewater treatment, multi-stage water treatment, water/sewage treatment, etc., and can solve the problem of influent COD not being too high.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0027] Example 1: The coagulant in the coagulation tank in step (1) is polyaluminum chloride, the dosage is 50 mg / L, the stirring speed is 50 r / min, and the residence time is 5 min; by controlling the dosage of the coagulant , so that the C / N ratio of the sewage entering the mixed denitrification tank is 1:1.
[0028] In this example, the hydraulic retention time in the clarifier in step (2) is 1 h, and the pore size of the first solid-liquid separation device is 25 μm; the captured carbon source is discharged through the vent valve 8 below the clarifier 5 for collection.
[0029] In this embodiment, in step (3), the dissolved oxygen in the mixed denitrification tank is controlled at 0.2 mg / L and the pH is controlled at 7.8 by controlling the aeration rate of the aeration device 10; Type packing 11, braid type packing 11 density is to hang 50 per square meter.
Embodiment 2
[0030] Example 2: Polyaluminum chloride is selected as the coagulant in the coagulation tank in step (1), the dosage is 400 mg / L, the stirring speed is 300 r / min, and the residence time is 20 min; by controlling the dosage of the coagulant , so that the C / N ratio of the sewage entering the mixed denitrification tank is 3:1.
[0031] In this example, the hydraulic retention time in the clarifier in step (2) is 3 h, and the pore size of the first solid-liquid separation equipment is 150 μm; the captured carbon source is discharged through the vent valve 8 below the clarifier 5 for collection.
[0032] In this embodiment, in step (3), the dissolved oxygen in the mixed denitrification tank is controlled at 0.5 mg / L and the pH is controlled at 8.2 by controlling the aeration rate of the aeration device 10; Type packing 11, braid type packing 11 density is to hang 100 per square meter.
Embodiment 3
[0033] Example 3: Polyaluminum chloride is selected as the coagulant in the coagulation tank in step (1), the dosage is 200 mg / L, the stirring speed is 300 r / min, and the residence time is 5 min; by controlling the coagulant dosing amount, so that the C / N ratio of the sewage entering the mixed denitrification tank is 2:1.
[0034] In this example, the hydraulic retention time in the clarifier in step (2) is 3 h, and the pore size of the first solid-liquid separation equipment is 70 μm; the captured carbon source is discharged through the vent valve 8 below the clarifier 5 for collection.
[0035]In this embodiment, in step (3), the dissolved oxygen in the mixed denitrification tank is controlled at 0.2 mg / L and the pH is controlled at 8.0 by controlling the aeration rate of the aeration device 10; Type packing 11, braid type packing 11 density is to hang 70 per square meter.
[0036] The influent COD concentration of livestock and poultry breeding wastewater in a rural area i...
PUM
Property | Measurement | Unit |
---|---|---|
pore size | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com