Integrated electrochemical coupled membrane aerated biofilm reactor and its application
An aerated biological and electrochemical technology, applied in chemical instruments and methods, biological water/sewage treatment, water pollutants, etc., can solve problems such as accumulation and impact on effluent water quality, and achieve improved removal efficiency, efficient oxidation degradation and high efficiency The effect of mineralization removal
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0028] An integrated electrochemically coupled membrane aerated biofilm reactor, including water inlet pipe 1, water inlet pump 11, reactor shell 2, tubular iridium tantalum titanium anode 5, titanium wire mesh cathode 3, PVDF bubble-free aeration hollow Fiber membrane 6, aeration system, regulated DC power supply 8 and water outlet pipe 9; one end of the water inlet pipe 1 is placed in a perforated water tank 21 arranged on the top of the reactor shell 2, and the water inlet pipe 1 is provided with an inlet pump 11 ; The titanium mesh cathode 3 is located in the reactor housing 2, the titanium mesh cathode 3 is columnar, and the titanium mesh cathode 3 is connected to the negative pole of the power supply 8 through a wire; the tubular iridium tantalum titanium anode 5 is placed in the titanium The inner side of the wire mesh cathode 3, the distance between the outer side of the tubular iridium tantalum titanium anode 5 and the titanium mesh cathode 3 is 5 mm, and the tubular i...
Embodiment 2
[0032] The same integrated electrochemically coupled membrane aerated biofilm reactor as in Example 1 was used to treat simulated surface water containing sulfadiazine, and the experimental conditions were set as: influent COD 45mg / L, NH4 + -N 2mg / L, sulfadiazine 100μg / L, aeration pressure 0.02MPa, regulated DC power supply voltage 1.5V, influent flow rate 1.7L / d, hydraulic retention time in electrolysis zone 5h, hydraulic retention time in biological zone It is 7.2h. Other conditions were the same, and the reactor without external electric field was set as the blank control group. Running in the continuous flow mode for 40 days, the results showed that the effluent COD of the two reactors was lower than 5mg / L, and the removal rate of sulfadiazine in the blank group was about 30%. The removal rate of sulfadiazine in the coupled membrane aerated biofilm reactor can reach more than 90%.
Embodiment 3
[0034] The same integrated electrochemically coupled membrane aerated biofilm reactor as in Example 1 was used to treat simulated surface water containing sulfadiazine, and the experimental conditions were set as: influent COD 45mg / L, NH4 + -N 2mg / L, sulfadiazine 100μg / L, aeration pressure 0.02MPa, regulated DC power supply voltage 1.0V, influent flow rate 1.7L / d, electrolysis zone hydraulic retention time 7h, biological zone hydraulic retention time for 10h. Other conditions were the same, and the reactor without external electric field was set as the blank control group. Running in the continuous flow mode, running continuously for 40 days, the results show that the COD of the effluent of the two reactors is lower than 5mg / L, and the removal rate of sulfadiazine in the blank group is about 35%. The removal rate of sulfadiazine in the coupled membrane aerated biofilm reactor can reach more than 90%.
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