Constituent | Effect | Critical concentration ( mg / L ) |
Suspended solids | May cause sludge deposits or interfere with receiving water clarity | Variable |
Biodegradable organics | May deplete oxygen resources | Variable |
Priority pollutants |
- Toxic to humans and carcinogenic - Toxic to aquatic environment |
- Varies by individual constituent - Varies based on presence in water column, biota, or sediment |
Volatile organic compounds | Toxic to humans, carcinogenic, form photochemical oxidants ( smog ) | Varies by individual constituent |
Ammonia |
- Increases chlorine demand, can be converted to nitrates and, in the process, can deplete oxygen resources, with
phosphorus, can lead to the development of undesirable aquatic growths - Toxic to fish |
- Any amount - Variable |
Nitrate |
- Stimulates algal and aquatic growth - Can cause methemoglobinemia in infants ( blue babies ) |
- 0.3 - 45 |
Phosphorus |
- Stimulates algal and aquatic growth - Interferes with coagulation - Interferes with lime - soda softening |
- 0.015 - 0.2 - 0.4 - 0.3 |
Calcium and magnesium | Increase hardness and total dissolved solids | Variable |
Chloride |
- Imparts salty taste - Interferes with agricultural and industrial processes |
- 250 - 75 - 200 |
Sulfate | Cathartic action | 600 - 1,000 |
Surfactants | Cause foaming and may interfere with coagulation | 1.0 - 3.0 |
Principal removal function | Description of operation or process | Type of wastewater treated |
Suspended solids removal | - Filtration - Microstrainers |
- EPT, EST - EST |
Ammonia oxidation | Biological nitrification | EPT, EBT, EST |
Nitrogen removal | Biological nitrification / denitrification | EPT, EST |
Nitrate removal | Separate stage biological denitrification | EST + nitrification |
Biological phosphorus removal |
- Mainstream phosphorus removal - Sidestream phosphorus removal |
- RW, EPT - RAS |
Combined nitrogen and phosphorus removal by biological methods | Biological nitrification / denitrification and phosphorus removal | RW, EPT |
Nitrogen removal by physical or chemical methods |
- Air stripping - Breakpoint chlorination - Ion exchange |
- EST - EST + filtration - EST + filtration |
Phosphorus removal by chemical addition |
- Chemical precipitation with metal salts - Chemical precipitation with lime |
- RW, EPT, EBT, EST - RW, EPT, EBT, EST |
Toxic compounds and refractory organics removal |
- Carbon adsorption - Activated sludge + powdered activated carbon - Chemical oxidation |
- EST + filtration - EPT - EST + filtration |
Dissolved inorganic solids removal |
- Chemical precipitation - Ion exchange - Ultrafiltration - Reverse osmosis - Electrodialysis |
- RW, EPT, EBT, EST - EST + filtration - EST + filtration - EST + filtration - EST + filtration + carbon adsorption |
Volatile organic compounds | Volatilization and gas stripping | RW, EPT |
EPT : Effluent from primary treatment EBT : Effluent from biological treatment ( before clarification ) EST : Effluent from secondary treatment ( after clarification ) RW : Raw ( untreated ) wastewater RAS : Return activated sludge |
A : Air |
Ae : Aerobic tank |
Al : Alum |
An : Anaerobic tank |
Ao : Anoxic tank |
AS : Activated sludge |
ASN : Activated sludge nitrification |
C : Chlorine |
CA : Carbon absorver |
CT : Contact tank |
DT : Denitrification tank |
F : Filter |
FE : Final effluent |
IC : Intermediate clarifier |
M : Methanol |
MS : Metal salt |
P : Polymer |
PC : Primary clarifier |
RAS : Return activated sludge |
RW : Raw wastewater |
S : Sludge |
SC : Secondary clarifier |
WAS : Waste activated sludge |
WW : Washwater |
Treatment operation or process | Organic nitrogen | NH3/NH4+ | NO3- | Removal of total nitrogen entering process ( % ) |
Conventional treatment | ||||
Primary | 10 - 20 % removed | No effect | No effect | 5 - 10 |
Secondary |
15 - 50 % removed urea====>NH3/NH4+ |
< 10 % removed | Slight effect | 10 - 30 |
Biological processes | ||||
Bacterial assimilation | No effect | 40 - 70 % removed | Slight effect | 30 - 70 |
Denitrification | No effect | No effect | 80 - 90 % removed | 70 - 95 |
Harvesting algae | Partial transformation to NH3/NH4+ | ====>Cells | ====>Cells | 50 - 80 |
Nitrification | Limited effect | ====>NO3- | No effect | 5 - 20 |
Oxidation ponds | Partial transformation to NH3/NH4+ | Partial removal by stripping | Partial removal by nitrification - denitrification | 20 - 90 |
Chemical processes | ||||
Breakpoint chlorination | Uncertain | 90 - 100 % removed | No effect | 80 - 95 |
Chemical coagulation | 50 - 70 % removed | Slight effect | Slight effect | 20 - 30 |
Carbon adsorption | 30 - 50 % removed | Slight effect | Slight effect | 10 - 20 |
Selective ion exchange for ammonium | Slight, uncertain | 80 - 97 % removed | No effect | 70 - 95 |
Selective ion exchange for nitrate | Slight effect | Slight effect | 75 - 90 % removed | 70 - 90 |
Physical operations | ||||
Filtration | 30-95 % of suspended organic N removed | Slight effect | Slight effect | 20 - 40 |
Air stripping | No effect | 60 - 95 % removed | No effect | 50 - 90 |
Electrodialysis | 100 % of suspended organic N removed | 30 - 50 % removed | 30 - 50 % removed | 40 - 50 |
Reverse osmosis | 60 - 90 % removed | 60 - 90 % removed | 60 - 90 % removed | 80 - 90 |
Treatment process | Typical effluent quality | ||||||
SS (mg/L) | BOD5 (mg/L) | COD (mg/L) | Total N (mg/L) | NH3-N (mg/L) | PO4-P (mg/L) | Turbidity (NTU) | |
Activated sludge + granular medium filtration | 4-6 | <5-10 | 30-70 | 15-35 | 15-25 | 4-10 | 0.3-5 |
Activated sludge + granular medium filtration + carbon adsorption | <3 | <1 | 5-15 | 15-30 | 15-25 | 4-10 | 0.3-3 |
Activated sludge / nitrification, single stage | 10-25 | 5-15 | 20-45 | 20-30 | 1-5 | 6-10 | 5-15 |
Activated sludge / nitrification - denitrification, separate stages | 10-25 | 5-15 | 20-35 | 5-10 | 1-2 | 6-10 | 5-15 |
Metal salt addition to activated sludge | 10-20 | 10-20 | 30-70 | 15-30 | 15-25 | <2 | 5-10 |
Metal salt addition to activated sludge + nitrification - denitrification + filtration | 5-10 | 5-10 | 20-30 | 3-5 | 1-2 | <1 | 0.3-3 |
Mainstream biological phosphorus removal | 10-20 | 5-15 | 20-35 | 15-25 | 5-10 | <2 | 5-10 |
Mainstream biological nitrogen and phosphorus removal + filtration | <10 | <5 | 20-30 | <5 | <2 | <1 | 0.3-3 |
Treatment operation or process | Removal of phosphorus entering system ( % ) |
Conventional treatment | |
Primary | 10 - 20 |
Activated sludge | 10 - 25 |
Trickling filter | 8 - 12 |
Rotating biological contactors | 8 - 12 |
Biological phosphorus only | |
Mainstream treatment | 70 - 90 |
Sidestream treatment | 70 - 90 |
Combined biological nitrogen and phosphorus removal | 70 - 90 |
Chemical removal | |
Precipitation with metal salt | 70 - 90 |
Precipitation with lime | 70 - 90 |
Physical removal | |
Filtration | 20 - 50 |
Reverse osmosis | 90 - 100 |
Carbon adsorption | 10 - 30 |