Treatment method of concentrated solution produced from landfill leachate by membrane method
A landfill leachate and treatment method technology, applied in the field of landfill leachate treatment, can solve the problems of low biodegradability of pollutants, high operating costs, membrane pollution, etc., and achieve the goal of improving treatment efficiency, improving treatment effect, and high treatment efficiency Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0033] Typical leachate treatment and nanofiltration, reverse osmosis concentrate production process see figure 1 . The leachate enters the conditioning tank through the grid pretreatment system, and then enters the UBF anaerobic system. The anaerobic effluent enters the intermediate tank, and the effluent from the intermediate tank enters the denitrification tank and the two-stage aerobic nitrification tank in turn. The effluent from the nitrification tank enters the tubular ultrafiltration membrane system. The ultrafiltration concentrate is returned to the denitrification tank. The ultrafiltration liquid enters the clear liquid tank and then enters the nanofiltration system to generate nanofiltration concentrate and clear liquid. The nanofiltration liquid can be directly discharged, or collected in the nanofiltration liquid tank and then injected into the reverse osmosis system to generate Reverse osmosis concentrate and reverse osmosis clear liquid.
[0034] In this proc...
Embodiment 2
[0036] The landfill leachate membrane concentrate obtained in Example 1 was first passed through a composite softening coagulation sedimentation tank. The composite softening coagulation sedimentation tank was composed of a three-level reaction tank and a sedimentation tank. The first-level reaction tank was filled with sodium carbonate, and the sodium carbonate The total number of moles added is 1 times the total number of moles of calcium and magnesium ions in the wastewater, 200mg / L polyaluminum chloride is added to the second-stage reaction pool, and 2mg / L polyacrylamide polymer flocculant is added to the third-stage reaction pool PAM, the total reaction time is 30min, and then enters the sedimentation tank for precipitation, reduces the hardness of the wastewater and removes COD, and the total residence time of the wastewater in the composite softening coagulation sedimentation tank is 3h.
[0037] The effluent from the sedimentation tank enters the ozone oxidation reactor...
Embodiment 3
[0043] The landfill leachate membrane concentrate obtained in Example 1 is first passed through a composite softening coagulation sedimentation tank, which consists of a 4-level reaction tank and a sedimentation tank, and sodium hydroxide is added to the first to second-level reaction tanks. The total number of moles of sodium hydroxide added is 0.8 times the total number of moles of calcium and magnesium ions in the wastewater, 500mg / L of polymeric ferric sulfate is added to the second-stage reaction pool, and 2mg / L of polyacrylamide is added to the third-stage reaction pool. Molecular flocculant PAM, the total reaction time is 60min, and then enters the sedimentation tank for precipitation to reduce the hardness of the wastewater and remove COD. The total residence time of the wastewater in the composite softening coagulation sedimentation tank is 5h.
[0044] The effluent from the sedimentation tank enters the ozone oxidation reactor for treatment. The ozone oxidation reacto...
PUM
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