Prepositive denitrification bio-filter processing method for municipal sewage
A pre-denitrification and urban sewage technology, applied in the field of sewage treatment, can solve the problems of high sewage treatment cost, long treatment process, and large floor area, so as to improve water treatment efficiency, reduce operating costs, and reduce floor space Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
specific Embodiment approach 1
[0011] Specific Embodiment 1: In this embodiment, a treatment method of a pre-denitrification biological filter for urban sewage is carried out in accordance with the following steps: 1. Urban sewage passes through the coarse grid, the middle grid, the drum type fine grid, and the swirling flow in sequence. The grit chamber and the hydrolytic acidification sedimentation tank are pretreated; 2. The effluent after pretreatment and the nitrification liquid returned from the clear water tank enter the anoxic biofilter together, and the TN volume load of the anoxic biofilter is controlled to be 1 to 2.5kg / m 3 d, the ascending flow rate is 10-12m / h, the hydraulic retention time is 0.2-0.8h, the reflux ratio of the nitrifying liquid is 100-150%, the filter material in the anoxic biological filter is biological ceramsite, and the particle size of the filter material is The diameter is 6-8mm, and the thickness of the filter material layer is 2-2.5m; 3. The effluent of the anoxic biolo...
specific Embodiment approach 2
[0013] Specific embodiment 2: The difference between this embodiment and specific embodiment 1 is that the gap of the coarse grid in step 1 is 10cm; the water depth in front of the grid of the middle grid is 0.8m, the gap is 5cm, and the flow rate through the grid is 0.57m / s ; The volume of the swirl sedimentation tank is 118m 3 , the surface load is 116.38m 3 / m 2 h, the hydraulic retention time is 40s. Other steps and processes are the same as those in Embodiment 1.
specific Embodiment approach 3
[0014] Specific embodiment three: the difference between this embodiment and specific embodiment one or two is that in step one, the maximum hydraulic load of the hydrolytic acidification sedimentation tank is controlled to be 4.7-5.8m 3 / m 2 h, the sludge concentration is 12-23g / L, and the hydraulic retention time is 2.6-2.9h. Other steps and processes are the same as those in Embodiment 1 or 2.
PUM
Property | Measurement | Unit |
---|---|---|
particle diameter | aaaaa | aaaaa |
thickness | aaaaa | aaaaa |
particle diameter | 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