**Static Experiment:**
**Required Equipment:** A 1-liter beaker, a small aeration device, micro-electrolytic filler, acid, alkali, and coagulant.
Place 1 kg of the micro-electrolytic filler into the beaker, and position an aeration stone at the bottom to create an aeration system. Then, fill the beaker with the wastewater to be tested (not completely full), turn on the aeration, and adjust the air flow to match the desired process conditions.
**Time Adjustment:** The experiment can be conducted in different time intervals such as 30, 45, 60, or 90 minutes, depending on the treatment goals.
**pH Adjustment:** Adjust the pH to values like 2, 3, 4, 5, or 6, and measure the pH of the effluent after the reaction is complete.
After the reaction, pour out the wastewater, adjust the pH to between 8 and 9 using lime or liquid alkali, and add a small amount of coagulant (such as PAC) to promote flocculation and precipitation. Finally, collect the supernatant for further analysis.
**Dynamic Experiment:**
The dynamic test simulates the operation of a reactor on-site for continuous wastewater treatment. The reactor design can be tailored based on the type of wastewater and site conditions. To calculate the performance, consider that the specific gravity of the filler is 1 ton per cubic meter, with a microporosity of 65%. Based on this, if the micro-electrolysis treatment time is 60 minutes, one cubic meter of filler can treat 0.6 cubic meters of water per hour. If the test is run for 30 minutes, the processing capacity becomes 60/30 × 0.6 = 1.2 cubic meters per hour. Similar calculations apply for other time periods.
**Iron-Carbon Filler Experiment – Summary of Wastewater Treatment Technologies!** – Contact: 186-63-64-04-92
1. **Printing and Dyeing Wastewater:** The micro-current and magnetic field effects between iron and carbon can break down chromophores, effectively decolorizing the wastewater.
2. **Electroplating and PCB Wastewater, Heavy Metal Complex Wastewater:** The newly generated ecological iron ions from the anode reduce heavy metal complexes. Combined with electrophoretic effects and iron hydroxide co-precipitation, this reduces heavy metals and COD in the wastewater.
3. **Nitrobenzene, Aniline, Coking, Petrochemical, Hydrogen Peroxide, Rubber Auxiliary, and Benzene Ring Wastewater:** A 1.2V potential difference between iron and carbon generates a magnetic field, causing electron movement that breaks down carbon chains and rings, reducing COD and improving biodegradability, making refractory wastewater easier to degrade.
4. **Pharmaceutical Wastewater:** The micro-current effect converts stable compounds into more degradable forms, lowering COD and eliminating pathogens in hospital wastewater.
5. **Papermaking Wastewater:** Micro-electrolysis, magnetic fields, and redox reactions convert long-chain polysaccharides into simpler sugars, greatly improving biodegradability and allowing complete removal via Fenton oxidation.
6. **Livestock and High-Concentration Organic Wastewater:** Micro-electrolysis breaks down organic chains and destroys color-forming groups, significantly reducing COD, ammonia nitrogen, and phosphorus levels.
**Iron Micro-Electrolysis Filler Experiment – Detailed Data on Various Wastewaters!** – Contact: 186-63-64-04-92
1. **Pig Farm Wastewater:** Initial COD: 12,163.05 mg/L, Ammonia Nitrogen: 1,080.16 mg/L; After small-scale denitrification tower: COD: 1,790.43 mg/L, Ammonia Nitrogen: 13.28 mg/L; After micro-electrolysis: COD: 384.27 mg/L.
2. **Electroplating Wastewater:** Raw Water COD: 945 mg/L; After micro-electrolysis: COD: 135 mg/L.
3. **Nitrobenzene Wastewater:** Raw Water COD: 3,800 mg/L, Nitrobenzene: 82.5 mg/L; After Iron-Carbon Micro-Electrolysis + Fenton: COD: 107 mg/L, Nitrobenzene: 0.26 mg/L.
4. **Aniline Wastewater:** Raw Water COD: 5,035 mg/L; After two-stage micro-electrolysis + Fenton: COD: 113 mg/L.
5. **Modified Starch Wastewater:** Raw Water COD: 12,000 mg/L; After two-stage micro-electrolysis: COD: 5,875 mg/L.
6. **Cattle Wastewater:** Raw Water COD: 11,034 mg/L; After two-stage micro-electrolysis: COD: 1,416 mg/L; After two-stage micro-electrolysis + Fenton: COD: 857 mg/L.
7. **Chemical Wastewater:** Raw Water COD: 20,000 mg/L; After two-stage micro-electrolysis + Fenton: COD: 1,600 mg/L.
---186--63-64-04-92
**Required Equipment:** A 1-liter beaker, a small aeration device, micro-electrolytic filler, acid, alkali, and coagulant.
Place 1 kg of the micro-electrolytic filler into the beaker, and position an aeration stone at the bottom to create an aeration system. Then, fill the beaker with the wastewater to be tested (not completely full), turn on the aeration, and adjust the air flow to match the desired process conditions.
**Time Adjustment:** The experiment can be conducted in different time intervals such as 30, 45, 60, or 90 minutes, depending on the treatment goals.
**pH Adjustment:** Adjust the pH to values like 2, 3, 4, 5, or 6, and measure the pH of the effluent after the reaction is complete.
After the reaction, pour out the wastewater, adjust the pH to between 8 and 9 using lime or liquid alkali, and add a small amount of coagulant (such as PAC) to promote flocculation and precipitation. Finally, collect the supernatant for further analysis.
**Dynamic Experiment:**
The dynamic test simulates the operation of a reactor on-site for continuous wastewater treatment. The reactor design can be tailored based on the type of wastewater and site conditions. To calculate the performance, consider that the specific gravity of the filler is 1 ton per cubic meter, with a microporosity of 65%. Based on this, if the micro-electrolysis treatment time is 60 minutes, one cubic meter of filler can treat 0.6 cubic meters of water per hour. If the test is run for 30 minutes, the processing capacity becomes 60/30 × 0.6 = 1.2 cubic meters per hour. Similar calculations apply for other time periods.
**Iron-Carbon Filler Experiment – Summary of Wastewater Treatment Technologies!** – Contact: 186-63-64-04-92
1. **Printing and Dyeing Wastewater:** The micro-current and magnetic field effects between iron and carbon can break down chromophores, effectively decolorizing the wastewater.
2. **Electroplating and PCB Wastewater, Heavy Metal Complex Wastewater:** The newly generated ecological iron ions from the anode reduce heavy metal complexes. Combined with electrophoretic effects and iron hydroxide co-precipitation, this reduces heavy metals and COD in the wastewater.
3. **Nitrobenzene, Aniline, Coking, Petrochemical, Hydrogen Peroxide, Rubber Auxiliary, and Benzene Ring Wastewater:** A 1.2V potential difference between iron and carbon generates a magnetic field, causing electron movement that breaks down carbon chains and rings, reducing COD and improving biodegradability, making refractory wastewater easier to degrade.
4. **Pharmaceutical Wastewater:** The micro-current effect converts stable compounds into more degradable forms, lowering COD and eliminating pathogens in hospital wastewater.
5. **Papermaking Wastewater:** Micro-electrolysis, magnetic fields, and redox reactions convert long-chain polysaccharides into simpler sugars, greatly improving biodegradability and allowing complete removal via Fenton oxidation.
6. **Livestock and High-Concentration Organic Wastewater:** Micro-electrolysis breaks down organic chains and destroys color-forming groups, significantly reducing COD, ammonia nitrogen, and phosphorus levels.
**Iron Micro-Electrolysis Filler Experiment – Detailed Data on Various Wastewaters!** – Contact: 186-63-64-04-92
1. **Pig Farm Wastewater:** Initial COD: 12,163.05 mg/L, Ammonia Nitrogen: 1,080.16 mg/L; After small-scale denitrification tower: COD: 1,790.43 mg/L, Ammonia Nitrogen: 13.28 mg/L; After micro-electrolysis: COD: 384.27 mg/L.
2. **Electroplating Wastewater:** Raw Water COD: 945 mg/L; After micro-electrolysis: COD: 135 mg/L.
3. **Nitrobenzene Wastewater:** Raw Water COD: 3,800 mg/L, Nitrobenzene: 82.5 mg/L; After Iron-Carbon Micro-Electrolysis + Fenton: COD: 107 mg/L, Nitrobenzene: 0.26 mg/L.
4. **Aniline Wastewater:** Raw Water COD: 5,035 mg/L; After two-stage micro-electrolysis + Fenton: COD: 113 mg/L.
5. **Modified Starch Wastewater:** Raw Water COD: 12,000 mg/L; After two-stage micro-electrolysis: COD: 5,875 mg/L.
6. **Cattle Wastewater:** Raw Water COD: 11,034 mg/L; After two-stage micro-electrolysis: COD: 1,416 mg/L; After two-stage micro-electrolysis + Fenton: COD: 857 mg/L.
7. **Chemical Wastewater:** Raw Water COD: 20,000 mg/L; After two-stage micro-electrolysis + Fenton: COD: 1,600 mg/L.
---186--63-64-04-92
Square Bath Spout,Floor Mounted Square Bath Spout,Tub Spout,Floor Mounted Bathroom Bath
JANGMEN MOON SHOWER SANITARYWARE CO.,LTD , https://www.moonshowerglobal.com