Environment-friendly process for improving treatment capacity of EMBR system by utilizing volume synergistic effect of homogenizing tank and inlet and return water flow diversion design
A technology of synergistic effect and processing capacity, applied in the field of chemical wastewater treatment, can solve the problems of high MLSS of sewage, abnormal metabolism and swelling, malnutrition of sludge, etc., to improve membrane treatment efficiency, reduce treatment pressure, and reduce sludge discharge and the effect of environmental treatment costs
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0033] 1. After the production sewage and domestic sewage are combined, they enter the homogenization tank through the sewage collection tank. The homogenization time is about 5 days, the pH is controlled between 5.5-8.5, the average COD is 3500-5000mg / L, and the ammonia nitrogen is 250-350mg / L.
[0034] 2. After homogenization, the sewage enters the anoxic tank at a constant rate every day for denitrification treatment, then enters the contact oxidation tank for oxidation and decomposition, and finally enters the biological aeration tank, where it is filtered and drained through the biofilm tank.
[0035] 3. The daily sewage treatment capacity is 360-400m³, the membrane flux is 16-20m³ / h, the membrane regeneration frequency is 10min per hour, the membrane regeneration water consumption is 48m³ per day, the actual operation time is 20h, and the effluent COD is between 400-550mg / L Between, the ammonia nitrogen is between 40-60mg / L.
Embodiment 2
[0037] 1. Production drainage diversion design:
[0038] 1) Double-high sewage with a solid content greater than 0.4% and ammonia nitrogen greater than 100mg / L enters the homogenization tank with an inflow of 350m 3 / d.
[0039] 2) Double-low sewage with a solid content of less than 0.4% and ammonia nitrogen less than 100mg / L directly enters the biological aeration tank with an inflow of 100mgm 3 / d.
[0040] 3) Production drainage includes: raw material medicine and preparation workshop production sewage of kasugamycin, polyoxin, and Zhongshengmycin, and a small amount of domestic sewage.
[0041]2. EMBR processing system:
[0042] 1) The production double-high drainage enters the double-high wastewater collection tank, and the sewage is pumped into the homogenization tank, the pH balance reaches 5.0-7.0, and 300-400m³ / d is continuously pumped into the anoxic tank for denitrification treatment, and the anoxic tank is controlled The pH is 7.0-8.0, then enters the contact o...
Embodiment 3
[0050] 1. Production drainage diversion design:
[0051] 1) The double-high sewage with COD greater than 2000mg / L and ammonia nitrogen greater than 100mg / L enters the homogenization tank, and the water inflow is 450m³ / d.
[0052] 2) The double-low sewage with COD less than 2000mg / L and ammonia nitrogen less than 100mg / L directly enters the biological aeration tank, and the water inflow is 200m³ / d.
[0053] 3) Production drainage includes: raw material medicine and preparation workshop production sewage of kasugamycin, polyoxin and Zhongshengmycin, and a small amount of domestic sewage.
[0054] 2. EMBR processing system:
[0055] 1) The production drainage enters the double-high wastewater collection tank, and is pumped into the homogenization tank through the sewage, the pH balance reaches between 5.0-7.0, and 600-700m³ / d is continuously pumped into the anoxic tank for denitrification treatment, and the pH of the anoxic tank is controlled at 7.0-8.0, then enter the contact ...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
