Secondary Effluent Disinfection
Destroys pathogens in the effluent that survive the secondary treatment process.
Chlorination:
Chlorine (Cl) is added until a free chlorine residual is attained.
A chlorine contact basin with baffles slows down water flow to ensure sufficient contact time between the effluent and free Cl.
Example: 0.5Lmg$$0.5 \frac{mg}{L}$$ free Cl for 15 minutes.
Dechlorination is needed to remove Cl and prevent fish kills.
Example: add sodium thiosulfate.
UV Light Radiation Disinfection:
Leaves no residual.
UV lamps need periodic cleaning and replacement.
No hazardous Cl gas storage.
Cost is comparable to a Cl system.
Secondary Treatment removes 85-95% of BOD (Biochemical Oxygen Demand) & TSS (Total Suspended Solids) but may not be sufficient to protect sensitive aquatic ecosystems.
Example: eutrophic algal bloom caused by excess nutrients.
Tertiary Treatment involves taking secondary treated effluent and applying additional treatment that:
Removes additional BOD and/or TSS.
Additional Activated Sludge (AS) treatment for additional BOD removal (e.g., membrane bioreactor).
Rapid mixed media filtration for additional TSS removal.
Removes additional nutrients (Nitrogen (N) and/or Phosphorus (P)).
It is not used in every STP (Sewage Treatment Plant) and can be very expensive.
Tertiary Treatment to Remove N
Up to 85% N removal by Biological Nitrification-Denitrification.
Nitrification (1st step): An aerobic process.
Uses methods such as AS, trickling filter, or rotating biological contractor.
Encourages the growth of nitrifying bacteria to convert ammonia to nitrite and then nitrite to nitrate:
$$NH3 \rightarrow NO2^- \rightarrow NO_3^-$$
Denitrification (2nd step): An anaerobic process.
Encourages the growth of denitrifying bacteria to convert nitrate to N2 (nitrogen gas), which is lost to the atmosphere.
Requires a source of Carbon (C) for cell synthesis.
Example: methanol (CH3OH$$CH_3OH$$) is often added since most carbonaceous material was oxidized by secondary treatment.
Internal recirculation from the nitrification (aerobic) tank to the denitrification (anaerobic) tank can result in loss of N2$$N_2$$ gas to the atmosphere.
Tertiary Treatment to Remove P
Enhanced Biological Phosphorus Removal (EBPR):
Uses cycling from an anaerobic tank to an aerated AS tank to enhance P uptake by bacteria.
Bacterial cells normally contain 1-2% P.
Some bacteria are stimulated by being in an anaerobic environment to take up excess phosphates (= luxury uptake).
Those bacteria are then sent to an aerobic phase where they store P as polyphosphate (up to 20% of their mass is P).
The cells are settled using a clarifier, and wasting the sludge removes the cells with excess P.
Chemical precipitation of P:
Alum coagulant is added prior to the aeration tank for floc formation and precipitation to remove 90% of P.
Each person generates approximately 4 gallons of sludge per week.
Accounts for > 1/2 of total typical STP costs.
Sludge comes from the bottom of clarifiers.
Sludge is treated prior to disposal or use to:
Reduce the volume by increasing the solids concentration (reduce the water content).
Reduces costs of handling, treatment, and disposal.
Stabilize the organics.
Less odor.
Less attractive to disease vectors.
Fewer pathogens.
Safer to handle.
Potential beneficial use.
Sludge Treatment
Sludge Thickening:
Increases solid concentration of the sludge, preps sludge for dewatering.
Gravity settling heavy concentrated sludge or air floating the lighter sludge upward; either way, the lighter sludge is removed from the surface to go back to headworks, and the heavier sludge is dewatered or digested.
Sludge dewatering to produce dewatered sludge cake, by:
Centrifuge, press, or drying bed.
Dried to contain < 70% water.
Dewatered sludge may be incinerated, landfilled, or composted.
2-stage Anaerobic Sludge Digestion
Biodegradation of sludge (organic solids) from clarifiers.
Digested sludge may be land applied or dewatered & landfilled.
Time = 15 – 40 days.
1st in covered tank, sludge is mixed & heated to 95oF$$95^o F$$, has two of three digestion phases:
1st digestion phase = hydrolysis (by bacteria) of polymers.
Example: proteins, fats to monomers i.e. amino acids, fatty acids.
2nd digestion phase = acid-forming bacteria metabolize fatty acids to organic acids, flows to 2nd tank.
2nd tank has a floating cover:
Sludge settles, and supernatant is pumped back to headworks.
3rd digestion phase = methanogenic-bacteria convert organic acids to methane gas.
Methane production raises the floating cover.
Stored methane may be flared or burned for heating the 1st tank.
Digested sludge is dewatered if composted.
May not be dewatered prior to land application
Lime stabilization of digested sludge
Mixing quicklime (CaO) or hydrated lime (Ca(OH)2$$Ca(OH)_2$$) with digested sludge.
Raise pH to 12 for at least 2 hours.
Kills microorganisms (pathogens).
Aids to further stabilize & dewater digested sludge.
Digested & limed sludge may be land applied.
Land Application of Sludge:
The primary method of biosolids used in the U.S.
Benefits of sludge spread on fields:
Macronutrients for plant growth:
Typical sludge NPK ratio (% by wt.) = 2.5 : 1.6 : 0.4
Typical inorganic fertilizer NPK ratio = 10 : 10 : 10
Micronutrients for plant growth:
Iron, manganese, copper, chromium, selenium, zinc.
Organic matter is added to soil.
Improves soil structure, tilth, water-holding capacity, water infiltration, soil aeration, biological diversity in soil.
Improves CEC (Cation Exchange Capacity) that allows the soil to retain potassium, calcium, magnesium.
Dangers:
Over fertilization:
With N, potential excess nitrate in groundwater & possible methemoglobinemia (blue-baby syndrome).
Runoff to surface waters leads to eutrophication.
Pathogens, vector attractiveness & odors must be reduced prior to application.
Heavy metal concentrations may accumulate in the soil.
Typical sludge heavy metal concentrations:
Mercury: 5 mg/kg$$mg/kg$$
Arsenic: 10 mg/kg$$mg/kg$$
Cadmium: 16 mg/kg$$mg/kg$$
Lead: 500 mg/kg$$mg/kg$$
Chromium: 890 mg/kg$$mg/kg$$
Zinc: 1740 mg/kg$$mg/kg$$
Preventing heavy metal pollution is critical because cleaning contaminated soils is extremely expensive and difficult.
Applicators of industrial waste or sludge must abide by the regulatory limits set by the U.S. Environmental Protection Agency (EPA).
Use of Digested Sludge
Code of Federal Regulations 40, Part 503, EPA Regulated.
Management practices:
Bulk sewage sludge cannot be applied:
In such a way as it enters a wetland.
Within 10 meters of U.S. waters.
To harm a threatened or endangered species or adversely modify the species critical habitat.
Greater than the agronomic rate (nutrients needed for plant production) for the site.
Bagged sewage sludge:
May be sold or given away if properly labeled:
Name & address of producer.
Identifies the annual sludge application rate (that is not to be exceeded).
Class A Sludge Restrictions & Uses
No site restrictions due to pathogens.
Less than 1,000 MPN fecal coliforms/g dry solids.
Salmonella sp. less than 3 MPN / g dry solids.
Is like a fertilizer; may be bagged.
Common aerated compost pile process to produce Class A is:
Composting with a min. 40°C heat for 5 days, with 4 hours at 55°C.
Class B Sludge Restrictions & Uses
Sludge digestion may produce class B sludge:
< 2,000,000 MPN fecal coliforms/g dry solids.
Site use restricted due to pathogen content.
Site Restrictions for Class B Sludge, after sludge application:
Animals not to graze for 30 days.
Food or feed crops with edible part not touching sludge are not harvested for 30 days.
Land with low public exposure is not accessed for 30 days (i.e., private farmland).
Turf grown for high public exposure areas is not harvested for 1 year.
Land with high public exposure is not accessed for 1 year (i.e., park, ballpark).
Water Quality Management: Wastewater & Sludge Treatment